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		<updated>2026-05-15T23:55:51Z</updated>
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	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Dranchuk_correlation&amp;diff=2550</id>
		<title>Dranchuk correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Dranchuk_correlation&amp;diff=2550"/>
				<updated>2017-06-30T09:49:18Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Dranchuk correlation]] is the fitting equation of the classic '''Standing and Katz''' &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt; gas compressibility factor correlation.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
A1 = 0.3265&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = –1.0700&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = –0.5339&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 0.01569&amp;lt;br/&amp;gt;&lt;br /&gt;
A5 = –0.05165&amp;lt;br/&amp;gt;&lt;br /&gt;
A6 = 0.5475&amp;lt;br/&amp;gt;&lt;br /&gt;
A7 = –0.7361&amp;lt;br/&amp;gt;&lt;br /&gt;
A8 = 0.1844&amp;lt;br/&amp;gt;&lt;br /&gt;
A9 = 0.1056&amp;lt;br/&amp;gt;&lt;br /&gt;
A10 = 0.6134&amp;lt;br/&amp;gt;&lt;br /&gt;
A11 = 0.7210&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z =  1-z+&lt;br /&gt;
\left(A_1&lt;br /&gt;
 +\frac{A_2}{T_{pr}}&lt;br /&gt;
 +\frac{A_3}{T^3_{pr}}&lt;br /&gt;
 +\frac{A_4}{T^4_{pr}}&lt;br /&gt;
 +\frac{A_5}{T^5_{pr}}&lt;br /&gt;
\right)\  \rho_r+&lt;br /&gt;
\left(A_6&lt;br /&gt;
 +\frac{A_7}{T_{pr}}&lt;br /&gt;
 +\frac{A_8}{T^2_{pr}}&lt;br /&gt;
\right)\ \rho^2_r&lt;br /&gt;
-A_9\ \left(\frac{A_7}{T_{pr}}+\frac{A_8}{T^2_{pr}}\right) \rho^5_r&lt;br /&gt;
+A_{10}\ \left(1+A_{11}\ \rho^2_r\right)\ \frac{\rho^2_r}{T^3_{pr}}&lt;br /&gt;
\ e^{(-A_{11}\ \rho^2_r)}&lt;br /&gt;
&amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho_r = \frac{0.27\ P_{pr}}{{z\ T_{pr}}}  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pr} =  \frac{P}{P_{pc}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  T_{pr} =  \frac{T}{T_{pc}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Dranchuk correlation]]?&lt;br /&gt;
&lt;br /&gt;
{{Quote| text = It's classics! | source = www.pengtools.com}}&lt;br /&gt;
&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
To solve the [[Dranchuk correlation| Dranchuk]] equation use the iterative secant method.&lt;br /&gt;
&lt;br /&gt;
To find the pseudo critical properties from the gas specific gravity &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt;:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pc} =  ( 4.6+0.1\ SG_g-0.258\ SG^2_g ) \times 10.1325 \times 14.7&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  T_{pc} =  ( 99.3+180\ SG_g-6.94\ SG^2_g ) \times 1.8 &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  0.2 \le P_{pr} &amp;lt; 30 ; 1.0 &amp;lt; T_{pr} \le 3.0 &amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
and&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pr} &amp;lt; 1.0 ; 0.7 &amp;lt; T_{pr} \le 1.0&amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{11} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_r &amp;lt;/math&amp;gt; = reduced density, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pc} &amp;lt;/math&amp;gt; = pseudo critical pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pr} &amp;lt;/math&amp;gt; = pseudoreduced pressure, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pc} &amp;lt;/math&amp;gt; = pseudo critical temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pr} &amp;lt;/math&amp;gt; = pseudoreduced temperature, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Standing&amp;amp;Katz&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Standing |first1=M. B.&lt;br /&gt;
 |last2= Katz |first2=D. L.&lt;br /&gt;
 |title=Density of Natural Gases&lt;br /&gt;
 |journal=Transactions of the AIME&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-942140-G&lt;br /&gt;
 |date=December 1942&lt;br /&gt;
 |volume=146&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-942140-G&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dranchuk &amp;gt;{{cite journal&lt;br /&gt;
 |last1= Dranchuk |first1=P. M.&lt;br /&gt;
 |last2= Abou-Kassem |first2=H.&lt;br /&gt;
 |title=Calculation of Z Factors For Natural Gases Using Equations of State&lt;br /&gt;
 |journal=The Journal of Canadian Petroleum&lt;br /&gt;
 |number=PETSOC-75-03-03&lt;br /&gt;
 |date=July 1975&lt;br /&gt;
 |volume=14&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/PETSOC-75-03-03&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Beggs_and_Robinson_Oil_Viscosity_correlation&amp;diff=2547</id>
		<title>Beggs and Robinson Oil Viscosity correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Beggs_and_Robinson_Oil_Viscosity_correlation&amp;diff=2547"/>
				<updated>2017-06-14T05:14:04Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Beggs - Robinson correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
Dead oil viscosity:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\mu_{od} = 10^X-1&amp;lt;/math&amp;gt;&amp;lt;ref name= {Beggs - Robinson}/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -1.163&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 13.108&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 6.591&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;X = T^{A_0} \times e^{A_1-A_2/SG_{o}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Saturated oil viscosity:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\mu_{os} =  \alpha1 \mu^{\alpha2}_{od}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
B0 = 10.715&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 5.615&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 0.515&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 = B_0 * (B_1 * R + 100)^B2) &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 5.44&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 5.615&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 0.338&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = C_0 * pow(C_1 * R + 150, -C_3) &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_0..A_{2} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_0..B_{2} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_0..C_{2} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name={Beggs - Robinson}&amp;gt;&lt;br /&gt;
{{cite journal&lt;br /&gt;
 |last1= Vazquez |first1=M.&lt;br /&gt;
 |last2= Beggs |first2=H.D.&lt;br /&gt;
 |title=Correlations for Fluid Physical Property Prediction.&lt;br /&gt;
 |journal=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-6719-PA&lt;br /&gt;
 |date=1980&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-6719-PA&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Beggs_and_Robinson_Oil_Viscosity_correlation&amp;diff=2546</id>
		<title>Beggs and Robinson Oil Viscosity correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Beggs_and_Robinson_Oil_Viscosity_correlation&amp;diff=2546"/>
				<updated>2017-06-14T05:12:40Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: Created page with &amp;quot;__TOC__  === Brief ===  Beggs - Robinson correlation is ...  === Math &amp;amp; Physics ===  Dead oil viscosity:  :&amp;lt;math&amp;gt;\mu_{od} = 10^X-1&amp;lt;/math&amp;gt;&amp;lt;ref name= {Beggs - Robinson}/&amp;gt;  w...&amp;quot;&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Beggs - Robinson correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
Dead oil viscosity:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\mu_{od} = 10^X-1&amp;lt;/math&amp;gt;&amp;lt;ref name= {Beggs - Robinson}/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -1.163&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 13.108&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 6.591&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;X = T^{A_0} \times e^{A_1-A_2/SG_{o}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Saturated oil viscosity:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\mu_{os} =  \alpha1 \mu^{\alpha2}_{od}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
B0 = 10.715&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 5.615&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 0.515&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 = B_0 * (B_1 * R + 100)^B2) &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 5.44&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 5.615&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 0.338&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = C_0 * pow(C_1 * R + 150, -C_3) &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_0..A_{2} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_0..B_{2} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_0..C_{2} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name={Beggs - Robinson}&amp;gt;&lt;br /&gt;
{{cite journal&lt;br /&gt;
 |last1= Vazquez |first1=M.&lt;br /&gt;
 |last2= Beggs |first2=H.D.&lt;br /&gt;
 |title=Correlations for Fluid Physical Property Prediction.&lt;br /&gt;
 |journal=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-6719-PA&lt;br /&gt;
 |date=1980&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-6719-PA&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Farshad_Oil_Compressibility_correlation&amp;diff=2545</id>
		<title>Farshad Oil Compressibility correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Farshad_Oil_Compressibility_correlation&amp;diff=2545"/>
				<updated>2017-06-14T03:26:36Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
A1 = 0.1982&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.6685&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = –0.21435&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.0116&amp;lt;br/&amp;gt;&lt;br /&gt;
A5 = 0.1616&amp;lt;br/&amp;gt;&lt;br /&gt;
A6 = –5.4531&amp;lt;br/&amp;gt;&lt;br /&gt;
A7 = –5.03 * 1e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A8 = 3.5 * 1e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; C_o = 10^{A6 + A7 \times X - A8 \times X^2}&amp;lt;/math&amp;gt;&amp;lt;ref name= Farshad/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  X = R^{A1}_s \times T^{A2} \times SG^{A3}_g \times Y^{A4}_{oil_API} \times P^{A5}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{8} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Farshad&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Frashad |first1=F.&lt;br /&gt;
 |last2= LeBlanc |first2=J.L.&lt;br /&gt;
 |last3= Garber |first3=J.D.&lt;br /&gt;
 |title=Empirical PVT Correlations For Colombian Crude Oils&lt;br /&gt;
 |journal=SPE Latin America/Caribbean Petroleum Engineering Conference, 23-26 April, Port-of-Spain, Trinidad&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-36105-MS&lt;br /&gt;
 |date=1996&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/SPE-36105-MS&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2544</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2544"/>
				<updated>2017-06-14T03:25:45Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Valco - McCain correlation|Valco - McCain]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Velarde correlation|Velarde]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[McCain correlation| McCain]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Beggs - Robinson correlation|Beggs - Robinson]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Farshad correlation|Farshad]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2543</id>
		<title>Velarde solution gas oil ratio correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2543"/>
				<updated>2017-06-14T03:22:05Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Velarde correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
:&amp;lt;math&amp;gt;R_s = \frac{R_{sr}}{R_{sb}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;R_{sr} = \alpha1 \times P^{\alpha2}_r + (1 - \alpha1) \times P^{\alpha3}_r&amp;lt;/math&amp;gt;&amp;lt;ref name= Velarde/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;P_r = \frac{P}{P_{bp}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
A0 = 1.8653e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 1.672608&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.929870&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.247235&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.056052&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 = A_0 \times SG^{A_1}_g \times Y^{A_2}_{oil_API} \times {(T- 459.67)}^{A_3} \times P^{A_3}_{bp} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 0.1004&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = -1.00475&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 0.337711&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 0.132795&amp;lt;br/&amp;gt;&lt;br /&gt;
B4 = 0.302065&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha2 = B_0 \times SG^{B_1}_g \times Y^{B_2}_{oil_API} \times {(T - 459.67)}^{B_3} \times P^{B_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 0.9167&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = -1.48548&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = -0.164741&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = -0.09133&amp;lt;br/&amp;gt;&lt;br /&gt;
C4 = 0.047094&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha3 = C_0 \times SG^{C_1}_g \times Y^{C_2}_{oil_API} \times {(T - 459.67)}^{C_3} \times P^{C_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Velarde correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_1..B_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_1..C_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Velarde&amp;gt;&lt;br /&gt;
{{cite journal&lt;br /&gt;
 |last1= Velarde |first1=J.&lt;br /&gt;
 |last2= Blasingame |first2=T. A.&lt;br /&gt;
 |last3= McCain Jr. |first3=W. D.&lt;br /&gt;
 |title=Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach&lt;br /&gt;
 |journal=Presented at the Annual Technical Meeting of CIM, Calgary, Alberta&lt;br /&gt;
 |publisher=Petroleum Society of Canada&lt;br /&gt;
 |number=PETSOC-97-93&lt;br /&gt;
 |date=1997&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/PETSOC-97-93&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2542</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2542"/>
				<updated>2017-06-14T03:21:39Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 \alpha + 0.0075 \alpha^2}&amp;lt;/math&amp;gt;&amp;lt;ref name= {Valco - McCain}/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -4.814074834&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 0.7480913&lt;br /&gt;
A2 = 0.1743556&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.0206&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 =  A_0+ A_1 log(R_{sb}) + A_2 log^2(R_{sb}) - A_3 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 1.27&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 0.0449&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 4.36e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 4.76e-6&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = B_0 - B_1  Y_{oil_API}+ B_2 Y^2_{oil_API}  - B_3 Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 4.51&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 10.84&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 8.39&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = 2.34&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha3 = C_0 - C_1 SG_{g} + C_2 SG^2_{g} - C_3 SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
D0 = -7.2254661&amp;lt;br/&amp;gt;&lt;br /&gt;
D1 = 0.043155&amp;lt;br/&amp;gt;&lt;br /&gt;
D2 = 8.55e-5&amp;lt;br/&amp;gt;&lt;br /&gt;
D3 = 6.00696e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha4 = D_0 + D_1 T - D_2 T^2 + D_4 T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha = \alpha1 + \alpha2 + \alpha3 + \alpha4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_0..A_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_0..B_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_0..C_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; D_0..D_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name={Valco - McCain}&amp;gt;&lt;br /&gt;
{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2541</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2541"/>
				<updated>2017-06-14T03:21:00Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 \alpha + 0.0075 \alpha^2}&amp;lt;/math&amp;gt;&amp;lt;ref name= Valco/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -4.814074834&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 0.7480913&lt;br /&gt;
A2 = 0.1743556&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.0206&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 =  A_0+ A_1 log(R_{sb}) + A_2 log^2(R_{sb}) - A_3 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 1.27&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 0.0449&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 4.36e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 4.76e-6&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = B_0 - B_1  Y_{oil_API}+ B_2 Y^2_{oil_API}  - B_3 Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 4.51&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 10.84&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 8.39&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = 2.34&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha3 = C_0 - C_1 SG_{g} + C_2 SG^2_{g} - C_3 SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
D0 = -7.2254661&amp;lt;br/&amp;gt;&lt;br /&gt;
D1 = 0.043155&amp;lt;br/&amp;gt;&lt;br /&gt;
D2 = 8.55e-5&amp;lt;br/&amp;gt;&lt;br /&gt;
D3 = 6.00696e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha4 = D_0 + D_1 T - D_2 T^2 + D_4 T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha = \alpha1 + \alpha2 + \alpha3 + \alpha4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_0..A_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_0..B_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_0..C_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; D_0..D_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Valco&amp;gt;&lt;br /&gt;
{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2540</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2540"/>
				<updated>2017-06-14T03:20:20Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 \alpha + 0.0075 \alpha^2}&amp;lt;/math&amp;gt;&amp;lt;ref name= Valco - McCain correlation/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -4.814074834&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 0.7480913&lt;br /&gt;
A2 = 0.1743556&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.0206&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 =  A_0+ A_1 log(R_{sb}) + A_2 log^2(R_{sb}) - A_3 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 1.27&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 0.0449&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 4.36e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 4.76e-6&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = B_0 - B_1  Y_{oil_API}+ B_2 Y^2_{oil_API}  - B_3 Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 4.51&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 10.84&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 8.39&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = 2.34&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha3 = C_0 - C_1 SG_{g} + C_2 SG^2_{g} - C_3 SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
D0 = -7.2254661&amp;lt;br/&amp;gt;&lt;br /&gt;
D1 = 0.043155&amp;lt;br/&amp;gt;&lt;br /&gt;
D2 = 8.55e-5&amp;lt;br/&amp;gt;&lt;br /&gt;
D3 = 6.00696e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha4 = D_0 + D_1 T - D_2 T^2 + D_4 T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha = \alpha1 + \alpha2 + \alpha3 + \alpha4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_0..A_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_0..B_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_0..C_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; D_0..D_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Valco - McCain correlation|Valco - McCain&amp;gt;&lt;br /&gt;
{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2539</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2539"/>
				<updated>2017-06-14T03:18:39Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 \alpha + 0.0075 \alpha^2}&amp;lt;/math&amp;gt;&amp;lt;ref name= Valco - McCain/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -4.814074834&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 0.7480913&lt;br /&gt;
A2 = 0.1743556&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.0206&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 =  A_0+ A_1 log(R_{sb}) + A_2 log^2(R_{sb}) - A_3 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 1.27&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 0.0449&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 4.36e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 4.76e-6&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = B_0 - B_1  Y_{oil_API}+ B_2 Y^2_{oil_API}  - B_3 Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 4.51&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 10.84&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 8.39&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = 2.34&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha3 = C_0 - C_1 SG_{g} + C_2 SG^2_{g} - C_3 SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
D0 = -7.2254661&amp;lt;br/&amp;gt;&lt;br /&gt;
D1 = 0.043155&amp;lt;br/&amp;gt;&lt;br /&gt;
D2 = 8.55e-5&amp;lt;br/&amp;gt;&lt;br /&gt;
D3 = 6.00696e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha4 = D_0 + D_1 T - D_2 T^2 + D_4 T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha = \alpha1 + \alpha2 + \alpha3 + \alpha4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_0..A_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_0..B_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_0..C_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; D_0..D_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Valco - McCain&amp;gt;&lt;br /&gt;
{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2538</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2538"/>
				<updated>2017-06-14T03:10:55Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 \alpha + 0.0075 \alpha^2}&amp;lt;/math&amp;gt;&amp;lt;ref name= Valco - McCain/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -4.814074834&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 0.7480913&lt;br /&gt;
A2 = 0.1743556&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.0206&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 =  A_0+ A_1 log(R_{sb}) + A_2 log^2(R_{sb}) - A_3 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 1.27&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 0.0449&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 4.36e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 4.76e-6&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = B_0 - B_1  Y_{oil_API}+ B_2 Y^2_{oil_API}  - B_3 Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 4.51&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 10.84&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 8.39&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = 2.34&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha3 = C_0 - C_1 SG_{g} + C_2 SG^2_{g} - C_3 SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
D0 = -7.2254661&amp;lt;br/&amp;gt;&lt;br /&gt;
D1 = 0.043155&amp;lt;br/&amp;gt;&lt;br /&gt;
D2 = 8.55e-5&amp;lt;br/&amp;gt;&lt;br /&gt;
D3 = 6.00696e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha4 = D_0 + D_1 T - D_2 T^2 + D_4 T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha = \alpha1 + \alpha2 + \alpha3 + \alpha4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_0..A_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_0..B_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_0..C_{3} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; D_0..D_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Valco - McCain&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2537</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2537"/>
				<updated>2017-06-13T10:00:11Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 \alpha + 0.0075 \alpha^2}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -4.814074834&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 0.7480913&lt;br /&gt;
A2 = 0.1743556&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.0206&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 =  A_0+ A_1 log(R_{sb}) + A_2 log^2(R_{sb}) - A_3 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 1.27&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 0.0449&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 4.36e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 4.76e-6&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = B_0 - B_1  Y_{oil_API}+ B_2 Y^2_{oil_API}  - B_3 Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 4.51&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 10.84&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 8.39&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = 2.34&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha3 = C_0 - C_1 SG_{g} + C_2 SG^2_{g} - C_3 SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
D0 = -7.2254661&amp;lt;br/&amp;gt;&lt;br /&gt;
D1 = 0.043155&amp;lt;br/&amp;gt;&lt;br /&gt;
D2 = 8.55e-5&amp;lt;br/&amp;gt;&lt;br /&gt;
D3 = 6.00696e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha4 = -7.2254661 + 0.043155 T - 8.5548e-5 T^2 + 6.00696e-8 T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha = \alpha1 + \alpha2 + \alpha3 + \alpha4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_1..B_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_1..C_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; D_1..D_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Valco - McCain&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2536</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2536"/>
				<updated>2017-06-13T09:56:54Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 \alpha + 0.0075 \alpha^2}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -4.814074834&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 0.7480913&lt;br /&gt;
A2 = 0.1743556&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.0206&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 =  A_0+ A_1 log(R_{sb}) + A_2 log^2(R_{sb}) - A_3 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 1.27&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 0.0449&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 4.36e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 4.76e-6&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = B_0 - B_1  Y_{oil_API}+ B_2 Y^2_{oil_API}  - B_3 Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 4.51&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 10.84&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 8.39&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = 2.34&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha3 = C_0 - C_1 SG_{g} + C_2 SG^2_{g} - C_3 SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
D0 = -7.2254661&amp;lt;br/&amp;gt;&lt;br /&gt;
D1 = 0.043155&amp;lt;br/&amp;gt;&lt;br /&gt;
D2 = 8.55e-5&amp;lt;br/&amp;gt;&lt;br /&gt;
D3 = 6.00696e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha4 = -7.2254661 + 0.043155 T - 8.5548e-5 T^2 + 6.00696e-8 T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha = \alpha1 + \alpha2 + \alpha3 + \alpha4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_1..B_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_1..C_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; D_1..D_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Valco - McCain&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2535</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2535"/>
				<updated>2017-06-13T09:55:57Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 \alpha + 0.0075 \alpha^2}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -4.814074834&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 0.7480913&lt;br /&gt;
A2 = 0.1743556&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.0206&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 =  A_0+ A_1 log(R_{sb}) + A_2 log^2(R_{sb}) - A_3 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 1.27&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 0.0449&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 4.36e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 4.76e-6&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = B_0 - B_1  Y_{oil_API}+ B_2 Y^2_{oil_API}  - B_3 Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 4.51&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 10.84&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 8.39&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = 2.34&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha3 = C_0 - C_1 SG_{g} + C_2 SG^2_{g} - C_3 SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
D0 = -7.2254661&amp;lt;/br&amp;gt;&lt;br /&gt;
D1 = 0.043155&amp;lt;/br&amp;gt;&lt;br /&gt;
D2 = 8.55e-5&amp;lt;/br&amp;gt;&lt;br /&gt;
D3 = 6.00696e-8&amp;lt;/br&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha4 = -7.2254661 + 0.043155 T - 8.5548e-5 T^2 + 6.00696e-8 T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha = \alpha1 + \alpha2 + \alpha3 + \alpha4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_1..B_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_1..C_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; D_1..D_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Valco - McCain&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2534</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2534"/>
				<updated>2017-06-13T09:55:19Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 z + 0.0075 z^2}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = -4.814074834&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 0.7480913&lt;br /&gt;
A2 = 0.1743556&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.0206&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 =  A_0+ A_1 log(R_{sb}) + A_2 log^2(R_{sb}) - A_3 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 1.27&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = 0.0449&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 4.36e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 4.76e-6&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha2 = B_0 - B_1  Y_{oil_API}+ B_2 Y^2_{oil_API}  - B_3 Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 4.51&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = 10.84&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = 8.39&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = 2.34&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha3 = C_0 - C_1 SG_{g} + C_2 SG^2_{g} - C_3 SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
D0 = -7.2254661&amp;lt;/br&amp;gt;&lt;br /&gt;
D1 = 0.043155&amp;lt;/br&amp;gt;&lt;br /&gt;
D2 = 8.55e-5&amp;lt;/br&amp;gt;&lt;br /&gt;
D3 = 6.00696e-8&amp;lt;/br&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha4 = -7.2254661 + 0.043155 T - 8.5548e-5 T^2 + 6.00696e-8 T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha = \alpha1 + \alpha2 + \alpha3 + \alpha4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_1..B_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_1..C_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; D_1..D_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Valco - McCain&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2533</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2533"/>
				<updated>2017-06-13T09:35:10Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 z + 0.0075 z^2}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z1 = -4.814074834 + 0.7480913 log(R_{sb}) + 0.1743556 log^2(R_{sb}) - 0.0206 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z2 = 1.27 - 0.0449  Y_{oil_API}+ 0.000436  Y^2_{oil_API}  - 0.00000476  Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z3 = 4.51 - 10.84 \times SG_{g} + 8.39 \times SG^2_{g} - 2.34 \times SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z4 = -7.2254661 + 0.043155 \times T - 8.5548e-5 \times T^2 + 6.00696e-8 \times T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z = z1 + z2 + z3 + z4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Valco - McCain&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2532</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2532"/>
				<updated>2017-06-13T09:34:41Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 z + 0.0075 z^2}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z1 = -4.814074834 + 0.7480913 log(R_{sb}) + 0.1743556 log^2(R_{sb}) - 0.0206 log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z2 = 1.27 - 0.0449 Y_{oil_API}+ 0.000436 Y^2_{oil_API}  - 0.00000476 Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z3 = 4.51 - 10.84 \times SG_{g} + 8.39 \times SG^2_{g} - 2.34 \times SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z4 = -7.2254661 + 0.043155 \times T - 8.5548e-5 \times T^2 + 6.00696e-8 \times T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z = z1 + z2 + z3 + z4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, m3/m3&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Valco - McCain&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2531</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2531"/>
				<updated>2017-06-13T08:48:05Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco - McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} = e^{2.498 + 0.713 z + 0.0075 z^2}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z1 = -4.814074834 + 0.7480913 \times log(R_{sb}) + 0.1743556 \times log^2(R_{sb}) - 0.0206 \times log^3(R_{sb})&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z2 = 1.27 - 0.0449 \times Y_{oil_API}+ 0.000436 \times Y^2_{oil_API}  - 0.00000476 \times Y^3_{oil_API}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z3 = 4.51 - 10.84 * SG_{g} + 8.39 \times SG^2_{g} - 2.34 \times SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z4 = -7.2254661 + 0.043155 \times T - 8.5548e-5 \times T^2 + 6.00696e-8 \times T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z = z1 + z2 + z3 + z4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Valco - McCain&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Valkó |first1=P. P.&lt;br /&gt;
 |last2= McCain |first2=W.D.&lt;br /&gt;
 |title=Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities.&lt;br /&gt;
 |journal=J. Pet. Sci. Eng. 37 (3–4): 153-169&lt;br /&gt;
 |date=2003&lt;br /&gt;
 |url=http://dx.doi.org/10.1016/S0920-4105(02)00319-4&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Farshad_Oil_Compressibility_correlation&amp;diff=2530</id>
		<title>Farshad Oil Compressibility correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Farshad_Oil_Compressibility_correlation&amp;diff=2530"/>
				<updated>2017-06-13T08:43:56Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
A1 = 0.1982&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.6685&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = –0.21435&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.0116&amp;lt;br/&amp;gt;&lt;br /&gt;
A5 = 0.1616&amp;lt;br/&amp;gt;&lt;br /&gt;
A6 = –5.4531&amp;lt;br/&amp;gt;&lt;br /&gt;
A7 = –5.03 * 1e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A8 = 3.5 * 1e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; C_o = 10^{A6 + A7 \times X - A8 \times X^2}&amp;lt;/math&amp;gt;&amp;lt;ref name= Farshad/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  X = R^{A1}_s \times T^{A2} \times SG^{A3}_g \times Y^{A4}_{oil_API} \times P^{A5}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{8} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration &lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Farshad&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Frashad |first1=F.&lt;br /&gt;
 |last2= LeBlanc |first2=J.L.&lt;br /&gt;
 |last3= Garber |first3=J.D.&lt;br /&gt;
 |title=Empirical PVT Correlations For Colombian Crude Oils&lt;br /&gt;
 |journal=SPE Latin America/Caribbean Petroleum Engineering Conference, 23-26 April, Port-of-Spain, Trinidad&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-36105-MS&lt;br /&gt;
 |date=1996&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/SPE-36105-MS&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Farshad_Oil_Compressibility_correlation&amp;diff=2529</id>
		<title>Farshad Oil Compressibility correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Farshad_Oil_Compressibility_correlation&amp;diff=2529"/>
				<updated>2017-06-13T08:36:19Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
A1 = 0.1982&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.6685&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = –0.21435&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.0116&amp;lt;br/&amp;gt;&lt;br /&gt;
A5 = 0.1616&amp;lt;br/&amp;gt;&lt;br /&gt;
A6 = –5.4531&amp;lt;br/&amp;gt;&lt;br /&gt;
A7 = –5.03 * 1e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A8 = 3.5 * 1e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; C_o = 10^{A6 + A7 \times X - A8 \times X^2}&amp;lt;/math&amp;gt;&amp;lt;ref name= Farshad/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  X = R^{A1}_s \times T^{A2} \times SG^{A3}_g \times Y^{A4}_{oil_API} \times P^{A5}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{8} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; R_s &amp;lt;/math&amp;gt; =  oil gas ration, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Farshad&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Frashad |first1=F.&lt;br /&gt;
 |last2= LeBlanc |first2=J.L.&lt;br /&gt;
 |last3= Garber |first3=J.D.&lt;br /&gt;
 |title=Empirical PVT Correlations For Colombian Crude Oils&lt;br /&gt;
 |journal=SPE Latin America/Caribbean Petroleum Engineering Conference, 23-26 April, Port-of-Spain, Trinidad&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-36105-MS&lt;br /&gt;
 |date=1996&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/SPE-36105-MS&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2528</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2528"/>
				<updated>2017-06-13T05:45:19Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco- McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
:&amp;lt;math&amp;gt; z1 = -4.814074834 + 0.7480913 \times log(R_{sb}) + 0.1743556 \times (log(R_{sb}))^2 - 0.0206 \times (log(R_{sb}))^3 &lt;br /&gt;
&amp;lt;/math&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; z2 = 1.27 - 0.0449 * $API + 0.000436 * pow($API, 2) - 0.00000476 * pow($API, 3)&amp;lt;/math&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; z3 = 4.51 - 10.84 * SG_{g} + 8.39 \times SG^2_{g} - 2.34 * SG^3_{g}&amp;lt;/math&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; z4 = -7.2254661 + 0.043155 \times T - 8.5548e-5 \times T^2 + 6.00696e-8 * T^3&amp;lt;/math&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; z = z1 + z2 + z3 + z4&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
lnPb = 2.498 + 0.713 * $z + 0.0075 * pow($z, 2);&lt;br /&gt;
&lt;br /&gt;
Bubblepoint_Valko_McCainSI = exp($lnPb);&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{11} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_r &amp;lt;/math&amp;gt; = reduced density, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pc} &amp;lt;/math&amp;gt; = pseudo critical pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pr} &amp;lt;/math&amp;gt; = pseudoreduced pressure, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pc} &amp;lt;/math&amp;gt; = pseudo critical temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pr} &amp;lt;/math&amp;gt; = pseudoreduced temperature, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Standing&amp;amp;Katz&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Standing |first1=M. B.&lt;br /&gt;
 |last2= Katz |first2=D. L.&lt;br /&gt;
 |title=Density of Natural Gases&lt;br /&gt;
 |journal=Transactions of the AIME&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-942140-G&lt;br /&gt;
 |date=December 1942&lt;br /&gt;
 |volume=146&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-942140-G&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dranchuk &amp;gt;{{cite journal&lt;br /&gt;
 |last1= Dranchuk |first1=P. M.&lt;br /&gt;
 |last2= Abou-Kassem |first2=H.&lt;br /&gt;
 |title=Calculation of Z Factors For Natural Gases Using Equations of State&lt;br /&gt;
 |journal=The Journal of Canadian Petroleum&lt;br /&gt;
 |number=PETSOC-75-03-03&lt;br /&gt;
 |date=July 1975&lt;br /&gt;
 |volume=14&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/PETSOC-75-03-03&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2527</id>
		<title>Valko - McCain bubble point pressure correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Valko_-_McCain_bubble_point_pressure_correlation&amp;diff=2527"/>
				<updated>2017-06-13T05:34:29Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: Created page with &amp;quot;__TOC__  === Brief ===  Valco- McCain correlation is ...  === Math &amp;amp; Physics === :&amp;lt;math&amp;gt; z1 = -4.814074834 + 0.7480913 * log(R_{sb}) + 0.1743556 * (log(R_{sb}))^2 - 0.0206...&amp;quot;&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Valco- McCain correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
:&amp;lt;math&amp;gt; z1 = -4.814074834 + 0.7480913 * log(R_{sb}) + 0.1743556 * (log(R_{sb}))^2 - 0.0206 * (log($Rsb_m3m3))^3 &lt;br /&gt;
&amp;lt;/math&amp;gt;&lt;br /&gt;
z2 = 1.27 - 0.0449 * $API + 0.000436 * pow($API, 2) - 0.00000476 * pow($API, 3);&lt;br /&gt;
z3 = 4.51 - 10.84 * $sgGas + 8.39 * pow($sgGas, 2) - 2.34 * pow($sgGas, 3);&lt;br /&gt;
z4 = -7.2254661 + 0.043155 * $tKel - 8.5548e-5 * pow($tKel, 2) + 6.00696e-8 * pow($tKel, 3);&lt;br /&gt;
z = $z1 + $z2 + $z3 + $z4;&lt;br /&gt;
&lt;br /&gt;
lnPb = 2.498 + 0.713 * $z + 0.0075 * pow($z, 2);&lt;br /&gt;
&lt;br /&gt;
Bubblepoint_Valko_McCainSI = exp($lnPb);&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; z =  1-z+&lt;br /&gt;
\left(A_1&lt;br /&gt;
 +\frac{A_2}{T_{pr}}&lt;br /&gt;
 +\frac{A_3}{T^3_{pr}}&lt;br /&gt;
 +\frac{A_4}{T^4_{pr}}&lt;br /&gt;
 +\frac{A_5}{T^5_{pr}}&lt;br /&gt;
\right)\  \rho_r+&lt;br /&gt;
\left(A_6&lt;br /&gt;
 +\frac{A_7}{T_{pr}}&lt;br /&gt;
 +\frac{A_8}{T^2_{pr}}&lt;br /&gt;
\right)\ \rho^2_r&lt;br /&gt;
-A_9\ \left(\frac{A_7}{T_{pr}}+\frac{A_8}{T^2_{pr}}\right)&lt;br /&gt;
+A_{10}\ \left(1+A_{11}\ \rho^2_r\right)\ \frac{\rho^2_r}{T^3_{pr}}&lt;br /&gt;
\ e^{(-A_{11}\ \rho^2_r)}&lt;br /&gt;
&amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho_r = \frac{0.27\ P_{pr}}{{z\ T_{pr}}}  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pr} =  \frac{P}{P_{pc}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  T_{pr} =  \frac{T}{T_{pc}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Dranchuk correlation]]?&lt;br /&gt;
&lt;br /&gt;
{{Quote| text = It's classics! | source = www.pengtools.com}}&lt;br /&gt;
&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
To solve the [[Dranchuk correlation| Dranchuk]] equation use the iterative secant method.&lt;br /&gt;
&lt;br /&gt;
To find the pseudo critical properties from the gas specific gravity &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt;:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pc} =  ( 4.6+0.1\ SG_g-0.258\ SG^2_g ) \times 10.1325 \times 14.7&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  T_{pc} =  ( 99.3+180\ SG_g-6.94\ SG^2_g ) \times 1.8 &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  0.2 \le P_{pr} &amp;lt; 30 ; 1.0 &amp;lt; T_{pr} \le 3.0 &amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
and&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pr} &amp;lt; 1.0 ; 0.7 &amp;lt; T_{pr} \le 1.0&amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{11} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_r &amp;lt;/math&amp;gt; = reduced density, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pc} &amp;lt;/math&amp;gt; = pseudo critical pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pr} &amp;lt;/math&amp;gt; = pseudoreduced pressure, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pc} &amp;lt;/math&amp;gt; = pseudo critical temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pr} &amp;lt;/math&amp;gt; = pseudoreduced temperature, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Standing&amp;amp;Katz&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Standing |first1=M. B.&lt;br /&gt;
 |last2= Katz |first2=D. L.&lt;br /&gt;
 |title=Density of Natural Gases&lt;br /&gt;
 |journal=Transactions of the AIME&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-942140-G&lt;br /&gt;
 |date=December 1942&lt;br /&gt;
 |volume=146&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-942140-G&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dranchuk &amp;gt;{{cite journal&lt;br /&gt;
 |last1= Dranchuk |first1=P. M.&lt;br /&gt;
 |last2= Abou-Kassem |first2=H.&lt;br /&gt;
 |title=Calculation of Z Factors For Natural Gases Using Equations of State&lt;br /&gt;
 |journal=The Journal of Canadian Petroleum&lt;br /&gt;
 |number=PETSOC-75-03-03&lt;br /&gt;
 |date=July 1975&lt;br /&gt;
 |volume=14&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/PETSOC-75-03-03&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2526</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2526"/>
				<updated>2017-06-13T05:27:16Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Valco - McCain correlation|Valco - McCain]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Velarde correlation|Velarde]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[McCain correlation| McCain]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Farshad correlation|Farshad]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Farshad_Oil_Compressibility_correlation&amp;diff=2525</id>
		<title>Farshad Oil Compressibility correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Farshad_Oil_Compressibility_correlation&amp;diff=2525"/>
				<updated>2017-06-09T08:58:53Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
A1 = 0.1982&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.6685&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = –0.21435&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.0116&amp;lt;br/&amp;gt;&lt;br /&gt;
A5 = 0.1616&amp;lt;br/&amp;gt;&lt;br /&gt;
A6 = –5.4531&amp;lt;br/&amp;gt;&lt;br /&gt;
A7 = –5.03 * 1e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A8 = 3.5 * 1e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; C_o = 10^{A6 + A7 \times X - A8 \times X^2}&amp;lt;/math&amp;gt;&amp;lt;ref name= Farshad/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  X = R^{A1}_s \times T^{A2} \times SG^{A3}_g \times Y^{A4}_{oil_API} \times P^{A5}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{8} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Farshad&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Frashad |first1=F.&lt;br /&gt;
 |last2= LeBlanc |first2=J.L.&lt;br /&gt;
 |last3= Garber |first3=J.D.&lt;br /&gt;
 |title=Empirical PVT Correlations For Colombian Crude Oils&lt;br /&gt;
 |journal=SPE Latin America/Caribbean Petroleum Engineering Conference, 23-26 April, Port-of-Spain, Trinidad&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-36105-MS&lt;br /&gt;
 |date=1996&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/SPE-36105-MS&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2524</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2524"/>
				<updated>2017-06-09T08:24:12Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valco - McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Velarde correlation|Velarde]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[McCain correlation| McCain]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Farshad correlation|Farshad]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2523</id>
		<title>Velarde solution gas oil ratio correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2523"/>
				<updated>2017-06-08T08:22:25Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Velarde correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
:&amp;lt;math&amp;gt;R_s = \frac{R_{sr}}{R_{sb}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;R_{sr} = \alpha1 \times P^{\alpha2}_r + (1 - \alpha1) \times P^{\alpha3}_r&amp;lt;/math&amp;gt;&amp;lt;ref name= Velarde/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;P_r = \frac{P}{P_{bp}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
A0 = 1.8653e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 1.672608&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.929870&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.247235&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.056052&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 = A_0 \times SG^{A_1}_g \times Y^{A_2}_{oil_API} \times {(T- 459.67)}^{A_3} \times P^{A_3}_{bp} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 0.1004&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = -1.00475&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 0.337711&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 0.132795&amp;lt;br/&amp;gt;&lt;br /&gt;
B4 = 0.302065&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha2 = B_0 \times SG^{B_1}_g \times Y^{B_2}_{oil_API} \times {(T - 459.67)}^{B_3} \times P^{B_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 0.9167&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = -1.48548&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = -0.164741&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = -0.09133&amp;lt;br/&amp;gt;&lt;br /&gt;
C4 = 0.047094&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha3 = C_0 \times SG^{C_1}_g \times Y^{C_2}_{oil_API} \times {(T - 459.67)}^{C_3} \times P^{C_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Velarde correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_1..B_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_1..C_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{bp} &amp;lt;/math&amp;gt; = bubble point pressure, MPA&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Velarde&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Velarde |first1=J.&lt;br /&gt;
 |last2= Blasingame |first2=T. A.&lt;br /&gt;
 |last3= McCain Jr. |first3=W. D.&lt;br /&gt;
 |title=Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach&lt;br /&gt;
 |journal=Presented at the Annual Technical Meeting of CIM, Calgary, Alberta&lt;br /&gt;
 |publisher=Petroleum Society of Canada&lt;br /&gt;
 |number=PETSOC-97-93&lt;br /&gt;
 |date=1997&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/PETSOC-97-93&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2522</id>
		<title>Velarde solution gas oil ratio correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2522"/>
				<updated>2017-06-08T08:04:54Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Velarde correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
:&amp;lt;math&amp;gt;R_s = \frac{R_{sr}}{R_{sb}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;R_{sr} = \alpha1 \times Pr^{\alpha2} + (1 - \alpha1) \times Pr^{\alpha3}&amp;lt;/math&amp;gt;&amp;lt;ref name= Velarde/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = 1.8653e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 1.672608&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.929870&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.247235&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.056052&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 = A_0 \times SG^{A_1}_{gas} \times Y^{A_2}_{oil_API} \times {(T- 459.67)}^{A_3} \times P^{A_3}_{bp} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 0.1004&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = -1.00475&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 0.337711&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 0.132795&amp;lt;br/&amp;gt;&lt;br /&gt;
B4 = 0.302065&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha2 = B_0 \times SG^{B_1}_{gas} \times Y^{B_2}_{oil_API} \times {(T - 459.67)}^{B_3} \times P^{B_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 0.9167&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = -1.48548&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = -0.164741&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = -0.09133&amp;lt;br/&amp;gt;&lt;br /&gt;
C4 = 0.047094&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha3 = C_0 \times SG^{C_1}_{gas} \times Y^{C_2}_{oil_API} \times {(T - 459.67)}^{C_3} \times P^{C_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Velarde correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_1..B_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_1..C_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_r &amp;lt;/math&amp;gt; = reduced density, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pc} &amp;lt;/math&amp;gt; = pseudo critical pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pr} &amp;lt;/math&amp;gt; = pseudoreduced pressure, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pc} &amp;lt;/math&amp;gt; = pseudo critical temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pr} &amp;lt;/math&amp;gt; = pseudoreduced temperature, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Velarde&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Velarde |first1=J.&lt;br /&gt;
 |last2= Blasingame |first2=T. A.&lt;br /&gt;
 |last3= McCain Jr. |first3=W. D.&lt;br /&gt;
 |title=Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach&lt;br /&gt;
 |journal=Presented at the Annual Technical Meeting of CIM, Calgary, Alberta&lt;br /&gt;
 |publisher=Petroleum Society of Canada&lt;br /&gt;
 |number=PETSOC-97-93&lt;br /&gt;
 |date=1997&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/PETSOC-97-93&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2521</id>
		<title>Velarde solution gas oil ratio correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2521"/>
				<updated>2017-06-08T05:34:33Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Velarde correlation]] is ...&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
:&amp;lt;math&amp;gt;R_s = \frac{R_{sr}}{R_{sb}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;R_{sr} = \alpha1 \times Pr^{\alpha2} + (1 - \alpha1) \times Pr^{\alpha3}&amp;lt;/math&amp;gt;&amp;lt;ref name= Velarde/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = 1.8653e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 1.672608&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.929870&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.247235&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.056052&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 = A_0 \times SG^{A_1}_{gas} \times Y^{A_2}_{oil_API} \times {(T- 459.67)}^{A_3} \times P^{A_3}_{bp} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 0.1004&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = -1.00475&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 0.337711&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 0.132795&amp;lt;br/&amp;gt;&lt;br /&gt;
B4 = 0.302065&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha2 = B_0 \times SG^{B_1}_{gas} \times Y^{B_2}_{oil_API} \times {(T - 459.67)}^{B_3} \times P^{B_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 0.9167&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = -1.48548&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = -0.164741&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = -0.09133&amp;lt;br/&amp;gt;&lt;br /&gt;
C4 = 0.047094&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha3 = C_0 \times SG^{C_1}_{gas} \times Y^{C_2}_{oil_API} \times {(T - 459.67)}^{C_3} \times P^{C_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Velarde correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; B_1..B_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; C_1..C_{4} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_r &amp;lt;/math&amp;gt; = reduced density, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pc} &amp;lt;/math&amp;gt; = pseudo critical pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pr} &amp;lt;/math&amp;gt; = pseudoreduced pressure, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pc} &amp;lt;/math&amp;gt; = pseudo critical temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pr} &amp;lt;/math&amp;gt; = pseudoreduced temperature, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Standing&amp;amp;Katz&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Standing |first1=M. B.&lt;br /&gt;
 |last2= Katz |first2=D. L.&lt;br /&gt;
 |title=Density of Natural Gases&lt;br /&gt;
 |journal=Transactions of the AIME&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-942140-G&lt;br /&gt;
 |date=December 1942&lt;br /&gt;
 |volume=146&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-942140-G&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dranchuk &amp;gt;{{cite journal&lt;br /&gt;
 |last1= Dranchuk |first1=P. M.&lt;br /&gt;
 |last2= Abou-Kassem |first2=H.&lt;br /&gt;
 |title=Calculation of Z Factors For Natural Gases Using Equations of State&lt;br /&gt;
 |journal=The Journal of Canadian Petroleum&lt;br /&gt;
 |number=PETSOC-75-03-03&lt;br /&gt;
 |date=July 1975&lt;br /&gt;
 |volume=14&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/PETSOC-75-03-03&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2520</id>
		<title>Velarde solution gas oil ratio correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2520"/>
				<updated>2017-06-08T05:19:40Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Velarde correlation]] is the fitting equation of the classic '''Standing and Katz''' &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt; gas compressibility factor correlation.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
:&amp;lt;math&amp;gt;R_s = \frac{R_{sr}}{$R_{sb}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;R_{sr} = (\alpha1 * Pr^{\alpha2}) + (1 - \alpha1) * Pr^\alpha3))&amp;lt;/math&amp;gt;&amp;lt;ref name= Velarde/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = 1.8653e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 1.672608&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.929870&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.247235&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.056052&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 = A0 * SG^{A_1}_{gas} Y^{A_2}_{oil_API} {(T- 459.67)}^{A_3} P^{A_3}_{bp} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 0.1004&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = -1.00475&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 0.337711&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 0.132795&amp;lt;br/&amp;gt;&lt;br /&gt;
B4 = 0.302065&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha2 = B_0 SG^{B_1}_{gas} Y^{B_2}_{oil_API} {(T - 459.67)}^{B_3} P^{B_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 0.9167&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = -1.48548&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = -0.164741&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = -0.09133&amp;lt;br/&amp;gt;&lt;br /&gt;
C4 = 0.047094&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha3 = C_0 SG^{C_1}_{gas} Y^{C_2}_{oil_API} *{(T - 459.67)}^{C_3} P^{C_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Velarde correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
To solve the [[Dranchuk correlation| Dranchuk]] equation use the iterative secant method.&lt;br /&gt;
&lt;br /&gt;
To find the pseudo critical properties from the gas specific gravity &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt;:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pc} =  ( 4.6+0.1\ SG_g-0.258\ SG^2_g ) \times 10.1325 \times 14.7&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  T_{pc} =  ( 99.3+180\ SG_g-6.94\ SG^2_g ) \times 1.8 &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  0.2 \le P_{pr} &amp;lt; 30 ; 1.0 &amp;lt; T_{pr} \le 3.0 &amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
and&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pr} &amp;lt; 1.0 ; 0.7 &amp;lt; T_{pr} \le 1.0&amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{11} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_r &amp;lt;/math&amp;gt; = reduced density, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pc} &amp;lt;/math&amp;gt; = pseudo critical pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pr} &amp;lt;/math&amp;gt; = pseudoreduced pressure, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pc} &amp;lt;/math&amp;gt; = pseudo critical temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pr} &amp;lt;/math&amp;gt; = pseudoreduced temperature, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Standing&amp;amp;Katz&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Standing |first1=M. B.&lt;br /&gt;
 |last2= Katz |first2=D. L.&lt;br /&gt;
 |title=Density of Natural Gases&lt;br /&gt;
 |journal=Transactions of the AIME&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-942140-G&lt;br /&gt;
 |date=December 1942&lt;br /&gt;
 |volume=146&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-942140-G&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dranchuk &amp;gt;{{cite journal&lt;br /&gt;
 |last1= Dranchuk |first1=P. M.&lt;br /&gt;
 |last2= Abou-Kassem |first2=H.&lt;br /&gt;
 |title=Calculation of Z Factors For Natural Gases Using Equations of State&lt;br /&gt;
 |journal=The Journal of Canadian Petroleum&lt;br /&gt;
 |number=PETSOC-75-03-03&lt;br /&gt;
 |date=July 1975&lt;br /&gt;
 |volume=14&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/PETSOC-75-03-03&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2519</id>
		<title>Velarde solution gas oil ratio correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2519"/>
				<updated>2017-06-08T05:18:40Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Velarde correlation]] is the fitting equation of the classic '''Standing and Katz''' &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt; gas compressibility factor correlation.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
:&amp;lt;math&amp;gt;R_s = \frac{R_{sr}}{$R_{sb}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;R_{sr} = (\alpha1 * Pr^{\alpha2}) + (1 - \alpha1) * Pr^\alpha3))&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = 1.8653e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 1.672608&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.929870&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.247235&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.056052&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 = A0 * SG^{A_1}_{gas} Y^{A_2}_{oil_API} {(T- 459.67)}^{A_3} P^{A_3}_{bp} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 0.1004&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = -1.00475&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 0.337711&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 0.132795&amp;lt;br/&amp;gt;&lt;br /&gt;
B4 = 0.302065&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha2 = B_0 SG^{B_1}_{gas} Y^{B_2}_{oil_API} {(T - 459.67)}^{B_3} P^{B_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 0.9167&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = -1.48548&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = -0.164741&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = -0.09133&amp;lt;br/&amp;gt;&lt;br /&gt;
C4 = 0.047094&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha3 = C_0 SG^{C_1}_{gas} Y^{C_2}_{oil_API} *{(T - 459.67)}^{C_3} P^{C_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Velarde correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
To solve the [[Dranchuk correlation| Dranchuk]] equation use the iterative secant method.&lt;br /&gt;
&lt;br /&gt;
To find the pseudo critical properties from the gas specific gravity &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt;:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pc} =  ( 4.6+0.1\ SG_g-0.258\ SG^2_g ) \times 10.1325 \times 14.7&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  T_{pc} =  ( 99.3+180\ SG_g-6.94\ SG^2_g ) \times 1.8 &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  0.2 \le P_{pr} &amp;lt; 30 ; 1.0 &amp;lt; T_{pr} \le 3.0 &amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
and&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pr} &amp;lt; 1.0 ; 0.7 &amp;lt; T_{pr} \le 1.0&amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{11} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_r &amp;lt;/math&amp;gt; = reduced density, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pc} &amp;lt;/math&amp;gt; = pseudo critical pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pr} &amp;lt;/math&amp;gt; = pseudoreduced pressure, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pc} &amp;lt;/math&amp;gt; = pseudo critical temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pr} &amp;lt;/math&amp;gt; = pseudoreduced temperature, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Standing&amp;amp;Katz&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Standing |first1=M. B.&lt;br /&gt;
 |last2= Katz |first2=D. L.&lt;br /&gt;
 |title=Density of Natural Gases&lt;br /&gt;
 |journal=Transactions of the AIME&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-942140-G&lt;br /&gt;
 |date=December 1942&lt;br /&gt;
 |volume=146&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-942140-G&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dranchuk &amp;gt;{{cite journal&lt;br /&gt;
 |last1= Dranchuk |first1=P. M.&lt;br /&gt;
 |last2= Abou-Kassem |first2=H.&lt;br /&gt;
 |title=Calculation of Z Factors For Natural Gases Using Equations of State&lt;br /&gt;
 |journal=The Journal of Canadian Petroleum&lt;br /&gt;
 |number=PETSOC-75-03-03&lt;br /&gt;
 |date=July 1975&lt;br /&gt;
 |volume=14&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/PETSOC-75-03-03&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2518</id>
		<title>Velarde solution gas oil ratio correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Velarde_solution_gas_oil_ratio_correlation&amp;diff=2518"/>
				<updated>2017-06-08T05:17:26Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: Created page with &amp;quot;__TOC__  === Brief ===  Velarde correlation is the fitting equation of the classic '''Standing and Katz''' &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt; gas compressibility factor correlatio...&amp;quot;&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Velarde correlation]] is the fitting equation of the classic '''Standing and Katz''' &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt; gas compressibility factor correlation.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
:&amp;lt;math&amp;gt;R_s = \frac{R_{sr}}{$R_{sb}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;R_{sr} = (\alpha1 * Pr^{\alpha2}) + (1 - \alpha1) * Pr^\alpha3))&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
A0 = 1.8653e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A1 = 1.672608&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.929870&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = 0.247235&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.056052&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \alpha1 = A0 * SG^{A_1}_{gas} * Y^{A_2}_{oil_API} * {(T- 459.67)}^{A_3} * P^{A_3}_{bp} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
B0 = 0.1004&amp;lt;br/&amp;gt;&lt;br /&gt;
B1 = -1.00475&amp;lt;br/&amp;gt;&lt;br /&gt;
B2 = 0.337711&amp;lt;br/&amp;gt;&lt;br /&gt;
B3 = 0.132795&amp;lt;br/&amp;gt;&lt;br /&gt;
B4 = 0.302065&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\alpha2 = B_0 SG^{B_1}_{gas}  * Y^{B_2}_{oil_API} {(T - 459.67)}^{B_3} * P^{B_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
C0 = 0.9167&amp;lt;br/&amp;gt;&lt;br /&gt;
C1 = -1.48548&amp;lt;br/&amp;gt;&lt;br /&gt;
C2 = -0.164741&amp;lt;br/&amp;gt;&lt;br /&gt;
C3 = -0.09133&amp;lt;br/&amp;gt;&lt;br /&gt;
C4 = 0.047094&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;\a3 = C_0 SG^{C_1}_{gas} * Y^{C_2}_{oil_API} *{(T - 459.67)}^{C_3} P^{C_4}_{bp}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Velarde correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Workflow  ===&lt;br /&gt;
To solve the [[Dranchuk correlation| Dranchuk]] equation use the iterative secant method.&lt;br /&gt;
&lt;br /&gt;
To find the pseudo critical properties from the gas specific gravity &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt;:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pc} =  ( 4.6+0.1\ SG_g-0.258\ SG^2_g ) \times 10.1325 \times 14.7&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  T_{pc} =  ( 99.3+180\ SG_g-6.94\ SG^2_g ) \times 1.8 &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  0.2 \le P_{pr} &amp;lt; 30 ; 1.0 &amp;lt; T_{pr} \le 3.0 &amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
and&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pr} &amp;lt; 1.0 ; 0.7 &amp;lt; T_{pr} \le 1.0&amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{11} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_r &amp;lt;/math&amp;gt; = reduced density, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pc} &amp;lt;/math&amp;gt; = pseudo critical pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pr} &amp;lt;/math&amp;gt; = pseudoreduced pressure, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pc} &amp;lt;/math&amp;gt; = pseudo critical temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pr} &amp;lt;/math&amp;gt; = pseudoreduced temperature, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Standing&amp;amp;Katz&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Standing |first1=M. B.&lt;br /&gt;
 |last2= Katz |first2=D. L.&lt;br /&gt;
 |title=Density of Natural Gases&lt;br /&gt;
 |journal=Transactions of the AIME&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-942140-G&lt;br /&gt;
 |date=December 1942&lt;br /&gt;
 |volume=146&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-942140-G&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dranchuk &amp;gt;{{cite journal&lt;br /&gt;
 |last1= Dranchuk |first1=P. M.&lt;br /&gt;
 |last2= Abou-Kassem |first2=H.&lt;br /&gt;
 |title=Calculation of Z Factors For Natural Gases Using Equations of State&lt;br /&gt;
 |journal=The Journal of Canadian Petroleum&lt;br /&gt;
 |number=PETSOC-75-03-03&lt;br /&gt;
 |date=July 1975&lt;br /&gt;
 |volume=14&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/PETSOC-75-03-03&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2517</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2517"/>
				<updated>2017-06-08T04:14:26Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valco - McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Velarde correlation|Velarde]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Farshad correlation|Farshad]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2516</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2516"/>
				<updated>2017-06-08T04:14:05Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valco - McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde correlation|Velarde&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Farshad correlation|Farshad]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Farshad_Oil_Compressibility_correlation&amp;diff=2512</id>
		<title>Farshad Oil Compressibility correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Farshad_Oil_Compressibility_correlation&amp;diff=2512"/>
				<updated>2017-06-07T04:57:20Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: Created page with &amp;quot;__TOC__  === Brief ===  === Math &amp;amp; Physics === A1 = 0.1982&amp;lt;br/&amp;gt; A2 = 0.6685&amp;lt;br/&amp;gt; A3 = –0.21435&amp;lt;br/&amp;gt; A4 = 1.0116&amp;lt;br/&amp;gt; A5 = 0.1616&amp;lt;br/&amp;gt; A6 = –5.4531&amp;lt;br/&amp;gt; A7 = –5.03 * 1e-4...&amp;quot;&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
A1 = 0.1982&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = 0.6685&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = –0.21435&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 1.0116&amp;lt;br/&amp;gt;&lt;br /&gt;
A5 = 0.1616&amp;lt;br/&amp;gt;&lt;br /&gt;
A6 = –5.4531&amp;lt;br/&amp;gt;&lt;br /&gt;
A7 = –5.03 * 1e-4&amp;lt;br/&amp;gt;&lt;br /&gt;
A8 = 3.5 * 1e-8&amp;lt;br/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; C_o = 10^{A6 + A7 * X - A8 * X^2}&amp;lt;/math&amp;gt;&amp;lt;ref name= Farshad/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  X = R^{A1}_s * T^{A2} * SG^{A3}_g * Y^{A4}_{oil_API} * P^{A5}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
=== Application range === &lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{8} &amp;lt;/math&amp;gt; = coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; Y_{oil_API} &amp;lt;/math&amp;gt; = oil API gravity, dimensionless&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Farshad&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Frashad |first1=F.&lt;br /&gt;
 |last2= LeBlanc |first2=J.L.&lt;br /&gt;
 |last3= Garber |first3=J.D.&lt;br /&gt;
 |title=Empirical PVT Correlations For Colombian Crude Oils&lt;br /&gt;
 |journal=SPE Latin America/Caribbean Petroleum Engineering Conference, 23-26 April, Port-of-Spain, Trinidad&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-36105-MS&lt;br /&gt;
 |date=1996&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/SPE-36105-MS&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2511</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2511"/>
				<updated>2017-06-07T04:56:48Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valco - McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Farshad correlation|Farshad]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2501</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2501"/>
				<updated>2017-06-06T04:02:33Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valco - McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Farshad]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2500</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2500"/>
				<updated>2017-06-05T09:29:59Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valco - McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Farshad&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2499</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2499"/>
				<updated>2017-06-05T09:11:25Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valco - McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Farshad&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Real Gas law]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Real Gas law]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2498</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2498"/>
				<updated>2017-06-05T07:56:33Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valco - McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Farshad&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Standard equation]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Standard equation]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2275</id>
		<title>Lee correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2275"/>
				<updated>2017-05-02T09:04:09Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: /* Math &amp;amp; Physics */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
Lee correlation for viscosity of natural gases.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g = K\ e^{X\ \rho^Y} &amp;lt;/math&amp;gt;&amp;lt;ref name= Lee/&amp;gt;&lt;br /&gt;
where&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho = 0.00149406\ P\ \frac{\ M_g}{z\ T}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  K = \frac{(0.00094+2\times10^-6\ M_g)\ T^{1.5}}{(209+19M_g+T)}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; X = 3.5+\frac{986}{T}+0.001M_g &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; Y = 2.4-0.203\ X &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g = 28.967\ SG_g  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the Lee correlation?&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  560 \le T &amp;lt; 800R\   or\  100 \le T &amp;lt; 340F&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; 100 &amp;lt; P \le 8000 psia &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_g &amp;lt;/math&amp;gt; = gas density, g/cm3&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g &amp;lt;/math&amp;gt; = gas viscosity, cp&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g &amp;lt;/math&amp;gt; = gas molecular weight&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Lee&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Lee |first1=A. B.&lt;br /&gt;
 |last2= Gonzalez |first2=M. H.&lt;br /&gt;
 |last3= Eakin |first3=B. E.&lt;br /&gt;
 |title=The Viscosity of Natural Gases&lt;br /&gt;
 |journal=J Pet Technol &lt;br /&gt;
 |number=SPE-1340-PA&lt;br /&gt;
 |date=1966&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2274</id>
		<title>Lee correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2274"/>
				<updated>2017-05-02T06:28:22Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
Lee correlation for viscosity of natural gases.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g = K\ e^{X\ \rho^Y} &amp;lt;/math&amp;gt;&amp;lt;ref name= Lee/&amp;gt;&lt;br /&gt;
where&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho = 0.00149496\ P\ \frac{\ M_g}{z\ T}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  K = \frac{(0.00094+2\times10^-6\ M_g)\ T^{1.5}}{(209+19M_g+T)}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; X = 3.5+\frac{986}{T}+0.001M_g &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; Y = 2.4-0.203\ X &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g = 28.967\ SG_g  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the Lee correlation?&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  560 \le T &amp;lt; 800R\   or\  100 \le T &amp;lt; 340F&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; 100 &amp;lt; P \le 8000 psia &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_g &amp;lt;/math&amp;gt; = gas density, g/cm3&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g &amp;lt;/math&amp;gt; = gas viscosity, cp&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g &amp;lt;/math&amp;gt; = gas molecular weight&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Lee&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Lee |first1=A. B.&lt;br /&gt;
 |last2= Gonzalez |first2=M. H.&lt;br /&gt;
 |last3= Eakin |first3=B. E.&lt;br /&gt;
 |title=The Viscosity of Natural Gases&lt;br /&gt;
 |journal=J Pet Technol &lt;br /&gt;
 |number=SPE-1340-PA&lt;br /&gt;
 |date=1966&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2273</id>
		<title>Lee correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2273"/>
				<updated>2017-05-02T05:53:10Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
Lee correlation for viscosity of natural gases.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g = K\ e^{X\ \rho^Y} &amp;lt;/math&amp;gt;&amp;lt;ref name= Lee/&amp;gt;&lt;br /&gt;
where&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho = 0.000149496\ P\ \frac{\ M_g}{z\ T}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  K = \frac{(0.00094+2\times10^-6\ M_g)\ T^{1.5}}{(209+19M_g+T)}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; X = 3.5+\frac{986}{T}+0.001M_g &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; Y = 2.4-0.203\ X &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g = 28.967\ SG_g  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the Lee correlation?&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  560 \le T &amp;lt; 800R\   or\  100 \le T &amp;lt; 340F&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; 100 &amp;lt; P \le 8000 psia &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_g &amp;lt;/math&amp;gt; = gas density, g/cm3&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g &amp;lt;/math&amp;gt; = gas viscosity, cp&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g &amp;lt;/math&amp;gt; = gas molecular weight&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Lee&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Lee |first1=A. B.&lt;br /&gt;
 |last2= Gonzalez |first2=M. H.&lt;br /&gt;
 |last3= Eakin |first3=B. E.&lt;br /&gt;
 |title=The Viscosity of Natural Gases&lt;br /&gt;
 |journal=J Pet Technol &lt;br /&gt;
 |number=SPE-1340-PA&lt;br /&gt;
 |date=1966&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2272</id>
		<title>Lee correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2272"/>
				<updated>2017-04-27T04:16:56Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
Lee correlation for viscosity of natural gases.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g = K\ e^{X\ \rho^Y} &amp;lt;/math&amp;gt;&amp;lt;ref name= Lee/&amp;gt;&lt;br /&gt;
where&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho = 0.000149496\ \frac{\ M_g}{z\ T}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  K = \frac{(0.00094+2\times10^-6\ M_g)\ T^{1.5}}{(209+19M_g+T)}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; X = 3.5+\frac{986}{T}+0.001M_g &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; Y = 2.4-0.203\ X &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g = 28.967\ SG_g  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the Lee correlation?&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  560 \le T &amp;lt; 800R\   or\  100 \le T &amp;lt; 340F&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; 100 &amp;lt; P \le 8000 psia &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_g &amp;lt;/math&amp;gt; = gas density, g/cm3&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g &amp;lt;/math&amp;gt; = gas viscosity, cp&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g &amp;lt;/math&amp;gt; = gas molecular weight&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Lee&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Lee |first1=A. B.&lt;br /&gt;
 |last2= Gonzalez |first2=M. H.&lt;br /&gt;
 |last3= Eakin |first3=B. E.&lt;br /&gt;
 |title=The Viscosity of Natural Gases&lt;br /&gt;
 |journal=J Pet Technol &lt;br /&gt;
 |number=SPE-1340-PA&lt;br /&gt;
 |date=1966&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2271</id>
		<title>Lee correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2271"/>
				<updated>2017-04-27T04:16:25Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
Lee correlation for viscosity of natural gases.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g = K\ e^{X\ \rho^Y} &amp;lt;/math&amp;gt;&amp;lt;ref name= Lee/&amp;gt;&lt;br /&gt;
where&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho = 0.000149496\ \frac{\ M_g}{z\ T}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  K = \frac{(0.00094+2\times10^-6\ M_g)\ T^{1.5}}{(209+19M_g+T)}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; X = 3.5+\frac{986}{T}+0.001M_g &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; Y = 2.4-0.203\ X &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g = 28.967\ SG_g  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Lee correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  560 \le T &amp;lt; 800R\   or\  100 \le T &amp;lt; 340F&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; 100 &amp;lt; P \le 8000 psia &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_g &amp;lt;/math&amp;gt; = gas density, g/cm3&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g &amp;lt;/math&amp;gt; = gas viscosity, cp&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g &amp;lt;/math&amp;gt; = gas molecular weight&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Lee&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Lee |first1=A. B.&lt;br /&gt;
 |last2= Gonzalez |first2=M. H.&lt;br /&gt;
 |last3= Eakin |first3=B. E.&lt;br /&gt;
 |title=The Viscosity of Natural Gases&lt;br /&gt;
 |journal=J Pet Technol &lt;br /&gt;
 |number=SPE-1340-PA&lt;br /&gt;
 |date=1966&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2270</id>
		<title>Lee correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2270"/>
				<updated>2017-04-27T04:15:09Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
Lee correlation for viscosity of natural gases.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g = K\ e^{X\ \rho^Y} &amp;lt;/math&amp;gt;&lt;br /&gt;
where&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho = 0.000149496\ \frac{\ M_g}{z\ T}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  K = \frac{(0.00094+2\times10^-6\ M_g)\ T^{1.5}}{(209+19M_g+T)}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; X = 3.5+\frac{986}{T}+0.001M_g &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; Y = 2.4-0.203\ X &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g = 28.967\ SG_g  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Lee correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  560 \le T &amp;lt; 800R\   or\  100 \le T &amp;lt; 340F&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; 100 &amp;lt; P \le 8000 psia &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_g &amp;lt;/math&amp;gt; = gas density, g/cm3&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g &amp;lt;/math&amp;gt; = gas viscosity, cp&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g &amp;lt;/math&amp;gt; = gas molecular weight&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Lee&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Lee |first1=A. B.&lt;br /&gt;
 |last2= Gonzalez |first2=M. H.&lt;br /&gt;
 |last3= Eakin |first3=B. E.&lt;br /&gt;
 |title=The Viscosity of Natural Gases&lt;br /&gt;
 |journal=J Pet Technol &lt;br /&gt;
 |number=SPE-1340-PA&lt;br /&gt;
 |date=1966&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2269</id>
		<title>Lee correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2269"/>
				<updated>2017-04-27T04:09:32Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
Lee correlation for viscosity of natural gases.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g = K\ e^{X\ \rho^Y} &amp;lt;/math&amp;gt;&lt;br /&gt;
where&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho = 0.000149496\ \frac{\ M_g}{z\ T}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  K = \frac{(0.00094+2\times10^-6\ M_g)\ T^{1.5}}{(209+19M_g+T)}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; X = 3.5+\frac{986}{T}+0.001M_g &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; Y = 2.4-0.203\ X &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g = 28.967\ SG_g  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Lee correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  560 \le T &amp;lt; 800R\   or\  100 \le T &amp;lt; 340F&lt;br /&gt;
&lt;br /&gt;
100 &amp;lt; P \le 8000 psia &lt;br /&gt;
&lt;br /&gt;
&amp;lt;/math&amp;gt;&amp;lt;ref name= Lee/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_g &amp;lt;/math&amp;gt; = gas density, g/cm3&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g &amp;lt;/math&amp;gt; = gas viscosity, cp&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g &amp;lt;/math&amp;gt; = gas molecular weight&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Lee&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Lee |first1=A. B.&lt;br /&gt;
 |last2= Gonzalez |first2=M. H.&lt;br /&gt;
 |last3= Eakin |first3=B. E.&lt;br /&gt;
 |title=The Viscosity of Natural Gases&lt;br /&gt;
 |journal=J Pet Technol &lt;br /&gt;
 |number=SPE-1340-PA&lt;br /&gt;
 |date=1966&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2268</id>
		<title>Lee correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Lee_correlation&amp;diff=2268"/>
				<updated>2017-04-27T04:07:30Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: Created page with &amp;quot;__TOC__  === Brief ===  Lee correlation for viscosity of natural gases.  === Math &amp;amp; Physics ===  :&amp;lt;math&amp;gt; \mu_g = K\ e^{X\ \rho^Y} &amp;lt;/math&amp;gt; where :&amp;lt;math&amp;gt;  \rho = 0.000149496...&amp;quot;&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Lee correlation]] for viscosity of natural gases.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g = K\ e^{X\ \rho^Y} &amp;lt;/math&amp;gt;&lt;br /&gt;
where&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho = 0.000149496\ \frac{\ M_g}{z\ T}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  K = \frac{(0.00094+2\times10^-6\ M_g)\ T^{1.5}}{(209+19M_g+T)}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; X = 3.5+\frac{986}{T}+0.001M_g &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; Y = 2.4-0.203\ X &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g = 28.967\ SG_g  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
Why the [[Lee correlation]]?&lt;br /&gt;
&lt;br /&gt;
=== Application range === &lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  560 \le T &amp;lt; 800R\   or\  100 \le T &amp;lt; 340F&lt;br /&gt;
&lt;br /&gt;
100 &amp;lt; P \le 8000 psia &lt;br /&gt;
&lt;br /&gt;
&amp;lt;/math&amp;gt;&amp;lt;ref name= Lee/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_g &amp;lt;/math&amp;gt; = gas density, g/cm3&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu_g &amp;lt;/math&amp;gt; = gas viscosity, cp&lt;br /&gt;
:&amp;lt;math&amp;gt; M_g &amp;lt;/math&amp;gt; = gas molecular weight&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Lee&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Lee |first1=A. B.&lt;br /&gt;
 |last2= Gonzalez |first2=M. H.&lt;br /&gt;
 |last3= Eakin |first3=B. E.&lt;br /&gt;
 |title=The Viscosity of Natural Gases&lt;br /&gt;
 |journal=J Pet Technol &lt;br /&gt;
 |number=SPE-1340-PA&lt;br /&gt;
 |date=1966&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2267</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2267"/>
				<updated>2017-04-27T04:06:06Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valco - McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Farshad&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee correlation| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2265</id>
		<title>PVT tool</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=PVT_tool&amp;diff=2265"/>
				<updated>2017-04-27T02:18:28Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Brief ==&lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] provides the basic input for any '''Petroleum Engineering''' calculation. &lt;br /&gt;
&lt;br /&gt;
[[PVT tool]] calculates the main properties of oil, gas and water for oil using a set of black-oil correlations.&lt;br /&gt;
&lt;br /&gt;
== Main features ==&lt;br /&gt;
&lt;br /&gt;
* Plots of PVT properties vs pressure at reservoir temperature.&lt;br /&gt;
* Output section contains values under reservoir conditions.&lt;br /&gt;
* Results section contains values under standard conditions and at pressures between surface atmospheric and reservoir at reservoir temperature&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
&lt;br /&gt;
[[File:PVT_i.png|thumb|left|200px|link=http://www.pengtools.com/pvtCalculator|PVT Tool]]&lt;br /&gt;
&amp;lt;div style=&amp;quot;margin-left:220px&amp;quot;&amp;gt;&lt;br /&gt;
*	&amp;quot;Default values&amp;quot; button resets input values to the default values.&lt;br /&gt;
*	Switch between Metric and Field units.&lt;br /&gt;
*	Save/load models to the files and to the user’s cloud.&lt;br /&gt;
*	Export pdf report containing input parameters, calculated values and plots of the PVT properties.&lt;br /&gt;
*	Share models to the public cloud or by using model’s link.&lt;br /&gt;
*	Continue your work from where you stopped: last saved model will be automatically opened.&lt;br /&gt;
*	Download the chart as an image or data and print (upper-right corner chart’s button).&lt;br /&gt;
*	Export results table to Excel or other application.&lt;br /&gt;
&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;div style=&amp;quot;clear:both&amp;quot;&amp;gt;&amp;lt;/div&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table width=&amp;quot;100%&amp;quot; border=&amp;quot;1&amp;quot; cellpadding=&amp;quot;3&amp;quot; cellspacing=&amp;quot;1&amp;quot;&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Property&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Correlation&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Reference&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Bubble point&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valco - McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Valkó, P.P. and McCain, W.D. Jr . 2003. Reservoir oil bubblepoint pressures revisited; solution gas–oil ratios and surface gas specific gravities. J. Pet. Sci. Eng. 37 (3–4): 153-169.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas-oil ratio&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Velarde, J., Blasingame, T.A., and McCain Jr., W.D. 1997. Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta, 8–11 June. PETSOC-97-93.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr, N.C. Hill: Correlations for Liquid Densities and Evolved Gas Specific Gravities for Black Oils during Pressure Depletion, SPE, 30773, 1995.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;W.D. McCain, Jr: The Properties of Petroleum Fluids, Second edition, Tulsa, Oklahoma, 1990.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Beggs - Robinson&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Vazquez, M. and Beggs, H.D. 1980. Correlations for Fluid Physical Property Prediction. J Pet Technol 32 (6): 968-970. SPE-6719-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Farshad&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Frashad, F., LeBlanc, J.L., Garber, J.D. et al. 1996. Empirical PVT Correlations For Colombian Crude Oils. SPE-36105-MS.&lt;br /&gt;
http://petrowiki.org/Calculating_PVT_properties&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Z factor&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Dranchuk correlation| Dranchuk]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dranchuk, P.M. and Abou-Kassem, H. 1975. Calculation of Z Factors For Natural Gases Using Equations of State. J Can Pet Technol 14 (3): 34. PETSOC-75-03-03.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas FVF&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Gas_formation_volume_factor_and_density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas viscosity&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Lee| Lee]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Lee, A.L., Gonzalez, M.H., and Eakin, B.E. 1966. The Viscosity of Natural Gases. J Pet Technol 18 (8): 997–1000. SPE-1340-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Gas compressibility&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Standard equation&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;http://petrowiki.org/Isothermal_compressibility_of_gases&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Water density&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;McCain Jr., W.D. 1991. Reservoir-Fluid Property Correlations-State of the Art. SPE Res Eng 6 (2): 266-272. SPE-18571-PA.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
[[Category:PVT]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Dranchuk_correlation&amp;diff=2226</id>
		<title>Dranchuk correlation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Dranchuk_correlation&amp;diff=2226"/>
				<updated>2017-04-25T09:24:47Z</updated>
		
		<summary type="html">&lt;p&gt;Gprotsykov: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&lt;br /&gt;
=== Brief ===&lt;br /&gt;
&lt;br /&gt;
[[Dranchuk correlation]] is the fitting function of the classic '''Standing and Katz''' &amp;lt;ref name=Standing&amp;amp;Katz /&amp;gt; gas compressibility factor correlation.&lt;br /&gt;
&lt;br /&gt;
=== Math &amp;amp; Physics ===&lt;br /&gt;
A1 = 0.3265&amp;lt;br/&amp;gt;&lt;br /&gt;
A2 = –1.0700&amp;lt;br/&amp;gt;&lt;br /&gt;
A3 = –0.5339&amp;lt;br/&amp;gt;&lt;br /&gt;
A4 = 0.01569&amp;lt;br/&amp;gt;&lt;br /&gt;
A5 = –0.05165&amp;lt;br/&amp;gt;&lt;br /&gt;
A6 = 0.5475&amp;lt;br/&amp;gt;&lt;br /&gt;
A7 = –0.7361&amp;lt;br/&amp;gt;&lt;br /&gt;
A8 = 0.1844&amp;lt;br/&amp;gt;&lt;br /&gt;
A9 = 0.1056&amp;lt;br/&amp;gt;&lt;br /&gt;
A10 = 0.6134&amp;lt;br/&amp;gt;&lt;br /&gt;
A11 = 0.7210&amp;lt;br/&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; z =  1-z+&lt;br /&gt;
\left(A_1&lt;br /&gt;
 +\frac{A_2}{T_{pr}}&lt;br /&gt;
 +\frac{A_3}{T^3_{pr}}&lt;br /&gt;
 +\frac{A_4}{T^4_{pr}}&lt;br /&gt;
 +\frac{A_5}{T^5_{pr}}&lt;br /&gt;
\right)\  \rho_r+&lt;br /&gt;
\left(A_6&lt;br /&gt;
 +\frac{A_7}{T_{pr}}&lt;br /&gt;
 +\frac{A_8}{T^2_{pr}}&lt;br /&gt;
\right)\ \rho^2_r&lt;br /&gt;
-A_9\ \left(\frac{A_7}{T_{pr}}+\frac{A_8}{T^2_{pr}}\right)&lt;br /&gt;
+A_{10}\ \left(1+A_{11}\ \rho^2_r\right)\ \frac{\rho^2_r}{T^3_{pr}}&lt;br /&gt;
\ e^{-A_{11}\ \rho^2_r}&lt;br /&gt;
&amp;lt;/math&amp;gt;&amp;lt;ref name= Dranchuk/&amp;gt;&lt;br /&gt;
where &lt;br /&gt;
:&amp;lt;math&amp;gt;  T_{pc} =  99.3+180\ SG_g-6.94\ SG^2_g&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pc} =  4.6+0.1\ SG_g-0.258\ SG^2_g&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  T_{pr} =  \frac{T}{T_{pc}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  P_{pr} =  \frac{P}{P_{pc}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;  \rho_r = \frac{0.27\ P_{pr}}{({z\ T_{pr}})}  &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
=== Discussion  ===&lt;br /&gt;
To avoid the [[Liquid loading]] the gas velocity should be above the [[Liquid loading]] velocity.&lt;br /&gt;
&lt;br /&gt;
The higher the gas rate the higher the gas velocity.&lt;br /&gt;
&lt;br /&gt;
The lower the wellhead flowing pressure the higher the gas rate.&lt;br /&gt;
&lt;br /&gt;
The bigger the tubing ID the higher the gas rate.&lt;br /&gt;
&lt;br /&gt;
In case when the gas rate is limited by the [[Reservoirs|Reservoir]] deliverability smaller tubing ID will increase the gas velocity.&lt;br /&gt;
&lt;br /&gt;
=== Nomenclature ===&lt;br /&gt;
:&amp;lt;math&amp;gt; A_1..A_{11} &amp;lt;/math&amp;gt; coefficients&lt;br /&gt;
:&amp;lt;math&amp;gt; \rho_r &amp;lt;/math&amp;gt; = reduced density, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = Pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pc} &amp;lt;/math&amp;gt; = pseudo critical pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{pr} &amp;lt;/math&amp;gt; = pseudoreduced pressure, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; SG_g &amp;lt;/math&amp;gt; = gas specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pc} &amp;lt;/math&amp;gt; = pseudo critical temperature, °R&lt;br /&gt;
:&amp;lt;math&amp;gt; T_{pr} &amp;lt;/math&amp;gt; = pseudoreduced temperature, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; z &amp;lt;/math&amp;gt; = gas compressibility factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
=== References ===&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Standing&amp;amp;Katz&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Standing |first1=M. B.&lt;br /&gt;
 |last2= Katz |first2=D. L.&lt;br /&gt;
 |title=Density of Natural Gases&lt;br /&gt;
 |journal=Transactions of the AIME&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-942140-G&lt;br /&gt;
 |date=December 1942&lt;br /&gt;
 |volume=146&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-942140-G&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dranchuk &amp;gt;{{cite journal&lt;br /&gt;
 |last1= Dranchuk |first1=P. M.&lt;br /&gt;
 |last2= Abou-Kassem |first2=H.&lt;br /&gt;
 |title=Calculation of Z Factors For Natural Gases Using Equations of State&lt;br /&gt;
 |journal=The Journal of Canadian Petroleum&lt;br /&gt;
 |number=PETSOC-75-03-03&lt;br /&gt;
 |date=July 1975&lt;br /&gt;
 |volume=14&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/PETSOC-75-03-03&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:PVT]]&lt;/div&gt;</summary>
		<author><name>Gprotsykov</name></author>	</entry>

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