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	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Vogel%27s_IPR&amp;diff=7838</id>
		<title>Vogel's IPR</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Vogel%27s_IPR&amp;diff=7838"/>
				<updated>2025-04-07T12:03:35Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* See also */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&amp;lt;div style='text-align: right;'&amp;gt;By Mikhail Tuzovskiy on {{REVISIONTIMESTAMP}}&amp;lt;/div&amp;gt;&lt;br /&gt;
==Vogel's Inflow Performance Relationship==&lt;br /&gt;
[[File:Vogel's.png|thumb|right|300px| Vogel's IPR&amp;lt;ref name=Vogel /&amp;gt;]]&lt;br /&gt;
&lt;br /&gt;
[[Vogel's IPR]] is an empirical two-phase (oil + gas) inflow performance relationship correlation published in '''1968'''  &amp;lt;ref name=Vogel /&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
[[Vogel's IPR]] is based on computer simulations to several solution gas drive reservoirs for different fluid and reservoir relative permeability properties.&lt;br /&gt;
&lt;br /&gt;
[[Vogel's IPR]] is the default [[IPR]] correlation to calculate oil wells performance in the [[:Category:PQplot|PQplot]] nodal analysis software which is available online at petroleum engineering site [https://www.pengtools.com www.pengtools.com].&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
===[[Vogel's IPR]] equation===&lt;br /&gt;
:&amp;lt;math&amp;gt; \frac{q_o}{q_{o_{max}}} = 1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2&amp;lt;/math&amp;gt; &amp;lt;ref name=Vogel /&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===[[Darcy's law]] + [[Vogel's IPR]]===&lt;br /&gt;
Combination single phase liquid constant PI equation and [[Vogel's IPR]]:&lt;br /&gt;
&lt;br /&gt;
[[File:Constant PI and Vogel's IPR.png|300px| Combination Constant PI and Vogel's IPR]]&amp;lt;ref name=KermitBrown1984 /&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; q_{ob} = J (\bar{P} - P_b) &amp;lt;/math&amp;gt;&amp;lt;ref name=KermitBrown1984 /&amp;gt; , oil flow rate at the bubble point.&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; q_{o_{max}} = q_{ob} + \frac{J P_b}{1.8} &amp;lt;/math&amp;gt; &amp;lt;ref name= Neely /&amp;gt; , maximum oil rate or absolute open flow (AOF).&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; q_o = q_{ob} + (q_{o_{max}} - q_{ob})  \left (1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2 \right )&amp;lt;/math&amp;gt;&amp;lt;ref name=KermitBrown1984 /&amp;gt; , oil rate at given flowing bottomhole pressure.&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; J = \frac{q_o}{\bar{P}-P_b + \frac{P_b}{1.8} \left (1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2 \right ) } &amp;lt;/math&amp;gt;&amp;lt;ref name=KermitBrown1984 /&amp;gt; , productivity index for test below the bubble point pressure.&lt;br /&gt;
&lt;br /&gt;
==Discussion ==&lt;br /&gt;
&lt;br /&gt;
Why [[Vogel's IPR]]?&lt;br /&gt;
&lt;br /&gt;
{{Quote| text = Vogel's IPR solution has been found to be very good and is widely used in prediction of IPR curves. | source = Kermit Brown et al&amp;lt;ref name=KermitBrown1984 /&amp;gt;}}&lt;br /&gt;
&lt;br /&gt;
==[[Vogel's IPR]] calculation workflow==&lt;br /&gt;
===1. Calculate the Productivity Index, J:===&lt;br /&gt;
:1.1 J from the flow test:&lt;br /&gt;
::* Test is above the bubble point: &lt;br /&gt;
::&amp;lt;math&amp;gt;J=\frac{q_{o_{test}}}{\bar{P}-P_{wf}}&amp;lt;/math&amp;gt;&lt;br /&gt;
::* Test is below the bubble point: &lt;br /&gt;
::&amp;lt;math&amp;gt; J = \frac{q_{o_{test}}}{\bar{P}-P_b + \frac{P_b}{1.8} \left (1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2 \right ) }&amp;lt;/math&amp;gt;&lt;br /&gt;
:1.2 J from kh and [[JD]]:&lt;br /&gt;
:: &amp;lt;math&amp;gt;J = \frac{kh\ J_D}{141.2 B \mu}&amp;lt;/math&amp;gt;&lt;br /&gt;
:1.3 J from kh  and skin:&lt;br /&gt;
:: &amp;lt;math&amp;gt;J = \frac{kh\ \frac{1}{1 / 0.13 + S}}{141.2 B \mu}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===2. Calculate the flowing rates, q&amp;lt;sub&amp;gt;o&amp;lt;/sub&amp;gt;:===&lt;br /&gt;
For each P&amp;lt;sub&amp;gt;wf&amp;lt;/sub&amp;gt; from &amp;lt;math&amp;gt;\bar{P}&amp;lt;/math&amp;gt; to 0:&lt;br /&gt;
:2.1 Calculate oil flow rate at the bubble point:&lt;br /&gt;
::&amp;lt;math&amp;gt; q_{ob} = J (\bar{P} - P_b) &amp;lt;/math&amp;gt; &lt;br /&gt;
:2.2 Calculate maximum oil rate:&lt;br /&gt;
::&amp;lt;math&amp;gt; q_{o_{max}} = q_{ob} + \frac{J P_b}{1.8} &amp;lt;/math&amp;gt;&lt;br /&gt;
:2.3 Calculate oil rate at given flowing bottomhole pressure, P&amp;lt;sub&amp;gt;wf&amp;lt;/sub&amp;gt;:&lt;br /&gt;
::&amp;lt;math&amp;gt; q_o = q_{ob} + (q_{o_{max}} - q_{ob})  \left (1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2 \right )&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==[[Vogel's IPR]] calculation example==&lt;br /&gt;
[[File:Vogel's IPR calculation example.png|thumb|right|400px| Figure.1 [https://www.pengtools.com/pqPlot?paramsToken=e9d7a7fc72e7264858153a4a9099bcf7 Vogel's IPR calculation example]]]&lt;br /&gt;
Following the example problem #6, page 15 &amp;lt;ref name=KermitBrown1984 /&amp;gt;:&lt;br /&gt;
===Given:===&lt;br /&gt;
:&amp;lt;math&amp;gt;\bar{P}&amp;lt;/math&amp;gt;=4200 psi&lt;br /&gt;
:J=2 b/d/psi&lt;br /&gt;
:P&amp;lt;sub&amp;gt;b&amp;lt;/sub&amp;gt;=3000 psi&lt;br /&gt;
===Calculate:===&lt;br /&gt;
:(1) q&amp;lt;sub&amp;gt;ob&amp;lt;/sub&amp;gt;&lt;br /&gt;
:(2) q&amp;lt;sub&amp;gt;max&amp;lt;/sub&amp;gt;&lt;br /&gt;
:(3) q for P&amp;lt;sub&amp;gt;wf&amp;lt;/sub&amp;gt;=1500 psi&lt;br /&gt;
===Solution:===&lt;br /&gt;
:(1) &amp;lt;math&amp;gt; q_{ob} = J (\bar{P} - P_b) = 2 \times (4200 - 3000) = 2400\ b/d&amp;lt;/math&amp;gt;&lt;br /&gt;
:(2) &amp;lt;math&amp;gt; q_{o_{max}} = q_{ob} + \frac{J P_b}{1.8} = 2400 + \frac{2 \times 3000}{1.8} = 2400 + 3333 = 5733\ b/d&amp;lt;/math&amp;gt;&lt;br /&gt;
:(3 )&amp;lt;math&amp;gt; q_o = q_{ob} + (q_{o_{max}} - q_{ob})  \left (1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2 \right ) &amp;lt;/math&amp;gt;&lt;br /&gt;
::&amp;lt;math&amp;gt; q_o = 2400 + (5733 - 2400)  \left (1-0.2 \frac{1500}{4200} - 0.8 \left ( \frac{1500}{4200} \right )^2 \right )&amp;lt;/math&amp;gt;&lt;br /&gt;
::&amp;lt;math&amp;gt; q_o = 2400 + 3333 \times 0.7 = 4733\ b/d&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
With the help of the [[:Category:PQplot|PQplot]] software, other values of flowing pressure has been assumed, and the corresponding values of flow rate were determined. From these, the IPR cure was plotted ('''Fig.1''').&lt;br /&gt;
&lt;br /&gt;
The  [[:Category:PQplot|PQplot]] model from this example is available online by the following link: [https://www.pengtools.com/pqPlot?paramsToken=e9d7a7fc72e7264858153a4a9099bcf7 Vogel's IPR calculation example]&lt;br /&gt;
&lt;br /&gt;
== Nomenclature  ==&lt;br /&gt;
:&amp;lt;math&amp;gt; B &amp;lt;/math&amp;gt; = formation volume factor, bbl/stb&lt;br /&gt;
:&amp;lt;math&amp;gt; J &amp;lt;/math&amp;gt; = productivity index, stb/d/psia&lt;br /&gt;
:&amp;lt;math&amp;gt; J_D &amp;lt;/math&amp;gt; = dimensionless productivity index, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; kh&amp;lt;/math&amp;gt; = permeability times thickness, md*ft&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P} &amp;lt;/math&amp;gt; = average reservoir pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; q &amp;lt;/math&amp;gt; = flowing rate, stb/d&lt;br /&gt;
:&amp;lt;math&amp;gt; S &amp;lt;/math&amp;gt; = skin factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
===Greek symbols===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu &amp;lt;/math&amp;gt; = viscosity, cp&lt;br /&gt;
&lt;br /&gt;
===Subscripts===&lt;br /&gt;
&lt;br /&gt;
:b = at bubble point pressure&amp;lt;BR/&amp;gt;&lt;br /&gt;
:max = maximum&amp;lt;BR/&amp;gt;&lt;br /&gt;
:o = oil&amp;lt;BR/&amp;gt;&lt;br /&gt;
:test = well test&amp;lt;BR/&amp;gt;&lt;br /&gt;
:wf = well flowing bottomhole pressure&amp;lt;BR/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Vogel&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Vogel |first1=J. V.&lt;br /&gt;
 |title=Inflow Performance Relationships for Solution-Gas Drive Wells&lt;br /&gt;
 |journal=Journal of Petroleum Technology &lt;br /&gt;
 |volume=20&lt;br /&gt;
 |number=SPE-1476-PA&lt;br /&gt;
 |date=1968&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Neely &amp;gt;{{cite book&lt;br /&gt;
 |last1= Neely |first1=  A.B.&lt;br /&gt;
 |title=Use of IPR Curves&lt;br /&gt;
 |publisher=Shell Oil Co&lt;br /&gt;
 |place=Houston, Texas&lt;br /&gt;
 |date=1976&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==See also==&lt;br /&gt;
:[[IPR]]&lt;br /&gt;
:[[Composite IPR]]&lt;br /&gt;
:[[3 Phase IPR]]&lt;br /&gt;
:[[Darcy's law]]&lt;br /&gt;
:[[JD]]&lt;br /&gt;
:[[141.2 derivation]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Vogel's Inflow Performance Relationship&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Inflow Performance Relationship, nodal analysis, IPR curve, IPR calculator, Vogel's IPR&lt;br /&gt;
|description=Vogel IPR curve equation for well performance analysis.&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:PQplot]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Vogel%27s_IPR&amp;diff=7837</id>
		<title>Vogel's IPR</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Vogel%27s_IPR&amp;diff=7837"/>
				<updated>2025-04-07T12:03:16Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* See also */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
&amp;lt;div style='text-align: right;'&amp;gt;By Mikhail Tuzovskiy on {{REVISIONTIMESTAMP}}&amp;lt;/div&amp;gt;&lt;br /&gt;
==Vogel's Inflow Performance Relationship==&lt;br /&gt;
[[File:Vogel's.png|thumb|right|300px| Vogel's IPR&amp;lt;ref name=Vogel /&amp;gt;]]&lt;br /&gt;
&lt;br /&gt;
[[Vogel's IPR]] is an empirical two-phase (oil + gas) inflow performance relationship correlation published in '''1968'''  &amp;lt;ref name=Vogel /&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
[[Vogel's IPR]] is based on computer simulations to several solution gas drive reservoirs for different fluid and reservoir relative permeability properties.&lt;br /&gt;
&lt;br /&gt;
[[Vogel's IPR]] is the default [[IPR]] correlation to calculate oil wells performance in the [[:Category:PQplot|PQplot]] nodal analysis software which is available online at petroleum engineering site [https://www.pengtools.com www.pengtools.com].&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
===[[Vogel's IPR]] equation===&lt;br /&gt;
:&amp;lt;math&amp;gt; \frac{q_o}{q_{o_{max}}} = 1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2&amp;lt;/math&amp;gt; &amp;lt;ref name=Vogel /&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===[[Darcy's law]] + [[Vogel's IPR]]===&lt;br /&gt;
Combination single phase liquid constant PI equation and [[Vogel's IPR]]:&lt;br /&gt;
&lt;br /&gt;
[[File:Constant PI and Vogel's IPR.png|300px| Combination Constant PI and Vogel's IPR]]&amp;lt;ref name=KermitBrown1984 /&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; q_{ob} = J (\bar{P} - P_b) &amp;lt;/math&amp;gt;&amp;lt;ref name=KermitBrown1984 /&amp;gt; , oil flow rate at the bubble point.&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; q_{o_{max}} = q_{ob} + \frac{J P_b}{1.8} &amp;lt;/math&amp;gt; &amp;lt;ref name= Neely /&amp;gt; , maximum oil rate or absolute open flow (AOF).&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; q_o = q_{ob} + (q_{o_{max}} - q_{ob})  \left (1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2 \right )&amp;lt;/math&amp;gt;&amp;lt;ref name=KermitBrown1984 /&amp;gt; , oil rate at given flowing bottomhole pressure.&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; J = \frac{q_o}{\bar{P}-P_b + \frac{P_b}{1.8} \left (1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2 \right ) } &amp;lt;/math&amp;gt;&amp;lt;ref name=KermitBrown1984 /&amp;gt; , productivity index for test below the bubble point pressure.&lt;br /&gt;
&lt;br /&gt;
==Discussion ==&lt;br /&gt;
&lt;br /&gt;
Why [[Vogel's IPR]]?&lt;br /&gt;
&lt;br /&gt;
{{Quote| text = Vogel's IPR solution has been found to be very good and is widely used in prediction of IPR curves. | source = Kermit Brown et al&amp;lt;ref name=KermitBrown1984 /&amp;gt;}}&lt;br /&gt;
&lt;br /&gt;
==[[Vogel's IPR]] calculation workflow==&lt;br /&gt;
===1. Calculate the Productivity Index, J:===&lt;br /&gt;
:1.1 J from the flow test:&lt;br /&gt;
::* Test is above the bubble point: &lt;br /&gt;
::&amp;lt;math&amp;gt;J=\frac{q_{o_{test}}}{\bar{P}-P_{wf}}&amp;lt;/math&amp;gt;&lt;br /&gt;
::* Test is below the bubble point: &lt;br /&gt;
::&amp;lt;math&amp;gt; J = \frac{q_{o_{test}}}{\bar{P}-P_b + \frac{P_b}{1.8} \left (1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2 \right ) }&amp;lt;/math&amp;gt;&lt;br /&gt;
:1.2 J from kh and [[JD]]:&lt;br /&gt;
:: &amp;lt;math&amp;gt;J = \frac{kh\ J_D}{141.2 B \mu}&amp;lt;/math&amp;gt;&lt;br /&gt;
:1.3 J from kh  and skin:&lt;br /&gt;
:: &amp;lt;math&amp;gt;J = \frac{kh\ \frac{1}{1 / 0.13 + S}}{141.2 B \mu}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===2. Calculate the flowing rates, q&amp;lt;sub&amp;gt;o&amp;lt;/sub&amp;gt;:===&lt;br /&gt;
For each P&amp;lt;sub&amp;gt;wf&amp;lt;/sub&amp;gt; from &amp;lt;math&amp;gt;\bar{P}&amp;lt;/math&amp;gt; to 0:&lt;br /&gt;
:2.1 Calculate oil flow rate at the bubble point:&lt;br /&gt;
::&amp;lt;math&amp;gt; q_{ob} = J (\bar{P} - P_b) &amp;lt;/math&amp;gt; &lt;br /&gt;
:2.2 Calculate maximum oil rate:&lt;br /&gt;
::&amp;lt;math&amp;gt; q_{o_{max}} = q_{ob} + \frac{J P_b}{1.8} &amp;lt;/math&amp;gt;&lt;br /&gt;
:2.3 Calculate oil rate at given flowing bottomhole pressure, P&amp;lt;sub&amp;gt;wf&amp;lt;/sub&amp;gt;:&lt;br /&gt;
::&amp;lt;math&amp;gt; q_o = q_{ob} + (q_{o_{max}} - q_{ob})  \left (1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2 \right )&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==[[Vogel's IPR]] calculation example==&lt;br /&gt;
[[File:Vogel's IPR calculation example.png|thumb|right|400px| Figure.1 [https://www.pengtools.com/pqPlot?paramsToken=e9d7a7fc72e7264858153a4a9099bcf7 Vogel's IPR calculation example]]]&lt;br /&gt;
Following the example problem #6, page 15 &amp;lt;ref name=KermitBrown1984 /&amp;gt;:&lt;br /&gt;
===Given:===&lt;br /&gt;
:&amp;lt;math&amp;gt;\bar{P}&amp;lt;/math&amp;gt;=4200 psi&lt;br /&gt;
:J=2 b/d/psi&lt;br /&gt;
:P&amp;lt;sub&amp;gt;b&amp;lt;/sub&amp;gt;=3000 psi&lt;br /&gt;
===Calculate:===&lt;br /&gt;
:(1) q&amp;lt;sub&amp;gt;ob&amp;lt;/sub&amp;gt;&lt;br /&gt;
:(2) q&amp;lt;sub&amp;gt;max&amp;lt;/sub&amp;gt;&lt;br /&gt;
:(3) q for P&amp;lt;sub&amp;gt;wf&amp;lt;/sub&amp;gt;=1500 psi&lt;br /&gt;
===Solution:===&lt;br /&gt;
:(1) &amp;lt;math&amp;gt; q_{ob} = J (\bar{P} - P_b) = 2 \times (4200 - 3000) = 2400\ b/d&amp;lt;/math&amp;gt;&lt;br /&gt;
:(2) &amp;lt;math&amp;gt; q_{o_{max}} = q_{ob} + \frac{J P_b}{1.8} = 2400 + \frac{2 \times 3000}{1.8} = 2400 + 3333 = 5733\ b/d&amp;lt;/math&amp;gt;&lt;br /&gt;
:(3 )&amp;lt;math&amp;gt; q_o = q_{ob} + (q_{o_{max}} - q_{ob})  \left (1-0.2 \frac{P_{wf}}{\bar{P}} - 0.8 \left ( \frac{P_{wf}}{\bar{P}} \right )^2 \right ) &amp;lt;/math&amp;gt;&lt;br /&gt;
::&amp;lt;math&amp;gt; q_o = 2400 + (5733 - 2400)  \left (1-0.2 \frac{1500}{4200} - 0.8 \left ( \frac{1500}{4200} \right )^2 \right )&amp;lt;/math&amp;gt;&lt;br /&gt;
::&amp;lt;math&amp;gt; q_o = 2400 + 3333 \times 0.7 = 4733\ b/d&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
With the help of the [[:Category:PQplot|PQplot]] software, other values of flowing pressure has been assumed, and the corresponding values of flow rate were determined. From these, the IPR cure was plotted ('''Fig.1''').&lt;br /&gt;
&lt;br /&gt;
The  [[:Category:PQplot|PQplot]] model from this example is available online by the following link: [https://www.pengtools.com/pqPlot?paramsToken=e9d7a7fc72e7264858153a4a9099bcf7 Vogel's IPR calculation example]&lt;br /&gt;
&lt;br /&gt;
== Nomenclature  ==&lt;br /&gt;
:&amp;lt;math&amp;gt; B &amp;lt;/math&amp;gt; = formation volume factor, bbl/stb&lt;br /&gt;
:&amp;lt;math&amp;gt; J &amp;lt;/math&amp;gt; = productivity index, stb/d/psia&lt;br /&gt;
:&amp;lt;math&amp;gt; J_D &amp;lt;/math&amp;gt; = dimensionless productivity index, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; kh&amp;lt;/math&amp;gt; = permeability times thickness, md*ft&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P} &amp;lt;/math&amp;gt; = average reservoir pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; q &amp;lt;/math&amp;gt; = flowing rate, stb/d&lt;br /&gt;
:&amp;lt;math&amp;gt; S &amp;lt;/math&amp;gt; = skin factor, dimensionless&lt;br /&gt;
&lt;br /&gt;
===Greek symbols===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu &amp;lt;/math&amp;gt; = viscosity, cp&lt;br /&gt;
&lt;br /&gt;
===Subscripts===&lt;br /&gt;
&lt;br /&gt;
:b = at bubble point pressure&amp;lt;BR/&amp;gt;&lt;br /&gt;
:max = maximum&amp;lt;BR/&amp;gt;&lt;br /&gt;
:o = oil&amp;lt;BR/&amp;gt;&lt;br /&gt;
:test = well test&amp;lt;BR/&amp;gt;&lt;br /&gt;
:wf = well flowing bottomhole pressure&amp;lt;BR/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Vogel&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Vogel |first1=J. V.&lt;br /&gt;
 |title=Inflow Performance Relationships for Solution-Gas Drive Wells&lt;br /&gt;
 |journal=Journal of Petroleum Technology &lt;br /&gt;
 |volume=20&lt;br /&gt;
 |number=SPE-1476-PA&lt;br /&gt;
 |date=1968&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Neely &amp;gt;{{cite book&lt;br /&gt;
 |last1= Neely |first1=  A.B.&lt;br /&gt;
 |title=Use of IPR Curves&lt;br /&gt;
 |publisher=Shell Oil Co&lt;br /&gt;
 |place=Houston, Texas&lt;br /&gt;
 |date=1976&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==See also==&lt;br /&gt;
:[[IPR]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
:[[Composite IPR]]&lt;br /&gt;
:[[3 Phase IPR]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
:[[Darcy's law]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
:[[JD]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
:[[141.2 derivation]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Vogel's Inflow Performance Relationship&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Inflow Performance Relationship, nodal analysis, IPR curve, IPR calculator, Vogel's IPR&lt;br /&gt;
|description=Vogel IPR curve equation for well performance analysis.&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:PQplot]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=JD&amp;diff=7836</id>
		<title>JD</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=JD&amp;diff=7836"/>
				<updated>2025-04-07T11:53:07Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* See Also */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;==Brief==&lt;br /&gt;
&lt;br /&gt;
[[JD]] - dimensionless productivity index&amp;lt;ref name = pushing/&amp;gt;, inverse of dimensionless pressure (based on average pressure) which contains the type of flow regime, boundary condition, drainage shape and stimulation &amp;lt;ref name = DW/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math &amp;amp; Physics==&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D} = \frac{1}{\bar{P}_D} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
From the [[Darcy's law]] for the unfractured well the [[JD]] is: &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;&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Well in circular drainage area&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Well in a drainage area with the shape factor &amp;lt;math&amp;gt; {C_A}&amp;lt;/math&amp;gt;&amp;lt;ref name = DW/&amp;gt;&amp;lt;/th&amp;gt;&lt;br /&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;Steady state&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt; {J_D} = \frac{1}{ln{\frac{r_e}{r_w}-\frac{1}{2}+S}} &amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt;{J_D} = \frac{1}{\frac{1}{2}ln{\frac{4.5A}{C_A{r_w}^2}+S}}&amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&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;Pseudo steady state&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt; {J_D} = \frac{1}{ln{\frac{r_e}{r_w}-\frac{3}{4}+S}} &amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt;{J_D} = \frac{1}{\frac{1}{2}ln{\frac{2.25A}{C_A{r_w}^2}+S}}&amp;lt;/math&amp;gt;&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;
Some typical &amp;lt;math&amp;gt; {C_A}&amp;lt;/math&amp;gt; values: circle 31.6, square 30.88 &amp;lt;ref name = Dietz/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
===Oil===&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D} = \frac{141.2 B \mu}{kh} \frac{q}{\bar{P} - P_{wf}} = \frac{141.2 B \mu}{kh} J&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {q} = \frac{kh}{141.2 B \mu} (\bar{P} - P_{wf}) J_D = (\bar{P} - P_{wf}) J&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Gas===&lt;br /&gt;
:&amp;lt;math&amp;gt;J_D=\frac{1422 \times 10^3\ T_R}{kh} \frac{q_g}{P_{\bar{P}}-P_{P_{wf}}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==Maximum &amp;lt;math&amp;gt;J_D&amp;lt;/math&amp;gt;==&lt;br /&gt;
&lt;br /&gt;
The undamaged unstimulated vertical well potential in a pseudo steady radial flow in a circular drainage area:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D}_{max} \approx \frac{1}{ln{\frac{500}{0.1}-\frac{3}{4}+0}} \approx 0.1287&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
The maximum possible stimulated well potential for pseudo steady linear flow is:&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;{J_D}_{max}= \frac{6}{\pi} \approx 1.91 &amp;lt;/math&amp;gt; , see [[6/π stimulated well potential]]&lt;br /&gt;
&lt;br /&gt;
The maximum possible stimulated well potential for steady state linear flow is:&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;{J_D}_{max}= \frac{4}{\pi} \approx 1.27 &amp;lt;/math&amp;gt; , see [[4/π stimulated well potential]]&lt;br /&gt;
&lt;br /&gt;
== Nomenclature  ==&lt;br /&gt;
:&amp;lt;math&amp;gt; B &amp;lt;/math&amp;gt; = formation volume factor, bbl/stb&lt;br /&gt;
:&amp;lt;math&amp;gt; C_A &amp;lt;/math&amp;gt; = Dietz shape factor, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; J &amp;lt;/math&amp;gt; = productivity index, stb/psia&lt;br /&gt;
:&amp;lt;math&amp;gt; J_D &amp;lt;/math&amp;gt; = dimensionless productivity index, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; kh&amp;lt;/math&amp;gt; = permeability times thickness, md*ft&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P} &amp;lt;/math&amp;gt; = average reservoir pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P}_D&amp;lt;/math&amp;gt; = dimensionless pressure (based on average pressure), dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{\bar{P}} &amp;lt;/math&amp;gt; = average reservoir pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{wf} &amp;lt;/math&amp;gt; = well flowing pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{P_{wf}} &amp;lt;/math&amp;gt; = average well flowing pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; q &amp;lt;/math&amp;gt; = flowing rate, stb/d&lt;br /&gt;
:&amp;lt;math&amp;gt; q_g &amp;lt;/math&amp;gt; = gas rate, MMscfd&lt;br /&gt;
:&amp;lt;math&amp;gt; r_w &amp;lt;/math&amp;gt; = wellbore radius, ft&lt;br /&gt;
:&amp;lt;math&amp;gt; r_e &amp;lt;/math&amp;gt; = drainage radius, ft&lt;br /&gt;
:&amp;lt;math&amp;gt; S &amp;lt;/math&amp;gt; = skin factor, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
&lt;br /&gt;
===Greek symbols===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu &amp;lt;/math&amp;gt; = viscosity, cp&lt;br /&gt;
&lt;br /&gt;
==See Also==&lt;br /&gt;
&lt;br /&gt;
* [[Darcy's law]]&lt;br /&gt;
* [[IPR]]&lt;br /&gt;
* [[Productivity index|J]]&lt;br /&gt;
* [[Production Potential]]&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= pushing &amp;gt;{{cite journal&lt;br /&gt;
 |last1=Rueda|first1=J.I.&lt;br /&gt;
 |last2=Mach|first2=J.&lt;br /&gt;
 |last3=Wolcott|first3=D.&lt;br /&gt;
 |title=Pushing Fracturing Limits to Maximize Producibility in Turbidite Formations in Russia&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-91760-MS&lt;br /&gt;
 |date=2004&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/SPE-91760-MS&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name=DW&amp;gt;&lt;br /&gt;
{{cite book&lt;br /&gt;
 |last1= Wolcott |first1=Don&lt;br /&gt;
 |title=Applied Waterflood Field Development&lt;br /&gt;
 |date=2009&lt;br /&gt;
 |publisher=Energy Tribune Publishing Inc&lt;br /&gt;
 |place=Houston&lt;br /&gt;
 |url=https://www.amazon.com/Applied-Waterflood-Field-Development-Wolcott/dp/0578023946/ref=sr_1_1?ie=UTF8&amp;amp;qid=1481788841&amp;amp;sr=8-1&amp;amp;keywords=Don+wolcott&lt;br /&gt;
 |url-access=subscription&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dietz &amp;gt;{{cite journal&lt;br /&gt;
 |last1=Dietz|first1=D.N.&lt;br /&gt;
 |title=Determination of Average Reservoir Pressure From Build-Up Surveys&lt;br /&gt;
 |publisher=J Pet Technol&lt;br /&gt;
 |number=SPE-1156-PA&lt;br /&gt;
 |date=1965&lt;br /&gt;
 |url=https://doi.org/10.2118/1156-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:optiFrac]]&lt;br /&gt;
[[Category:optiFracMS]]&lt;br /&gt;
[[Category:fracDesign]]&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:E&amp;amp;P Portal]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Dimensionless Productivity Index&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=hydraulic fracturing, hydraulic fracturing formulas, well potential, productivity index&lt;br /&gt;
|description=JD dimensionless productivity index&lt;br /&gt;
}}&lt;br /&gt;
&amp;lt;div style='text-align: right;'&amp;gt;By Mikhail Tuzovskiy on {{REVISIONTIMESTAMP}}&amp;lt;/div&amp;gt;&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=IPR&amp;diff=7835</id>
		<title>IPR</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=IPR&amp;diff=7835"/>
				<updated>2025-04-07T10:08:51Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* See also */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Inflow Performance Relationship==&lt;br /&gt;
[[File:Inflow Performance Relationship.png|thumb|right|400px|link=https://www.pengtools.com/pqPlot|Inflow Performance Relationship Curve]]&lt;br /&gt;
&lt;br /&gt;
[[IPR | Inflow Performance Relationship]] is a curve of producing rates plotted against well bottomhole pressures for oil, water and gas wells&amp;lt;ref name= Vogel/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
[[IPR]] curve shows productive capacity and well performance.&lt;br /&gt;
&lt;br /&gt;
[[IPR]] curve is used in [[Well Nodal Analysis]] for production systems design, analysis and optimization.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
===Oil well IPR equation===&lt;br /&gt;
*[[Darcy's law]] equation for the single-phase flow of incompressible liquid:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; q = \frac{kh}{141.2 B \mu}\ (\bar{P} - P_{wf}) J_D&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
*[[Vogel's IPR]] two-phase flow equation (oil + gas) and it's combination with single phase liquid.&lt;br /&gt;
*[[Composite IPR]] curve for oil wells producing water.&lt;br /&gt;
*[[3 Phase IPR]] three-phase flow equation (oil + gas + water).&lt;br /&gt;
&lt;br /&gt;
===Gas well IPR equation ===&lt;br /&gt;
*[[Darcy's law]] gas inflow equation:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;q_g=\frac{kh}{1422 \times 10^3\ T_R}\ (P_{\bar{P}} - P_{P_{wf}})\ J_D &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
*C and n equation&lt;br /&gt;
&lt;br /&gt;
==IPR calculator software==&lt;br /&gt;
*[[:Category:PQplot | PQplot]] nodal analysis software is used to calculate the [[IPR]] curves. [[:Category:PQplot | PQplot]]  is available online at [https://www.pengtools.com www.pengtools.com].&lt;br /&gt;
*Excel&lt;br /&gt;
*other&lt;br /&gt;
&lt;br /&gt;
== Nomenclature  ==&lt;br /&gt;
:&amp;lt;math&amp;gt; B &amp;lt;/math&amp;gt; = formation volume factor, bbl/stb&lt;br /&gt;
:&amp;lt;math&amp;gt; J_D &amp;lt;/math&amp;gt; = dimensionless productivity index, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; kh&amp;lt;/math&amp;gt; = permeability times thickness, md*ft&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P} &amp;lt;/math&amp;gt; = average reservoir pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{\bar{P}} &amp;lt;/math&amp;gt; = average reservoir pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{wf} &amp;lt;/math&amp;gt; = well flowing pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{P_{wf}} &amp;lt;/math&amp;gt; = average well flowing pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; q &amp;lt;/math&amp;gt; = flowing rate, stb/d&lt;br /&gt;
:&amp;lt;math&amp;gt; q_g &amp;lt;/math&amp;gt; = gas rate, MMscfd&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
&lt;br /&gt;
===Greek symbols===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu &amp;lt;/math&amp;gt; = viscosity, cp&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Vogel&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Vogel |first1=J. V.&lt;br /&gt;
 |title=Inflow Performance Relationships for Solution-Gas Drive Wells&lt;br /&gt;
 |journal=Journal of Petroleum Technology &lt;br /&gt;
 |volume=20&lt;br /&gt;
 |number=SPE-1476-PA&lt;br /&gt;
 |date=1968&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;
==See also==&lt;br /&gt;
:[[Well Nodal Analysis]]&lt;br /&gt;
:[[141.2 derivation]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
:[[Darcy's law]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
:[[JD]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
:[[Production Potential]]&lt;br /&gt;
:[[Vogel's IPR]]&lt;br /&gt;
:[[Composite IPR]]&lt;br /&gt;
:[[3 Phase IPR]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Inflow Performance Relationship&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Inflow Performance Relationship, nodal analysis, IPR curve, IPR calculator&lt;br /&gt;
|description=IPR curve formula for well performance.&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:PQplot]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Well_Nodal_Analysis&amp;diff=7834</id>
		<title>Well Nodal Analysis</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Well_Nodal_Analysis&amp;diff=7834"/>
				<updated>2025-04-07T10:08:18Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* See also */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;==Brief==&lt;br /&gt;
[[File:Well Nodal Analysis.png|thumb|right|400px| Well Nodal Analysis]]&lt;br /&gt;
&lt;br /&gt;
[[Well Nodal Analysis]] is the fundamental [[Petroleum Engineering|petroleum engineering]] technique published in '''1979''' by Joe Mach &amp;lt;ref name=JoeMach/&amp;gt;. For his invention Joe Mach was [https://youtu.be/xArtxcT5joc?t=2749 honored] as a JPT Legend of Production and Operations in 2009&amp;lt;ref name=Legends/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
[[Well Nodal Analysis]] is used to predict the well rate and performance by combining the reservoir inflow with the wellbore lift capacity by intersecting the [[IPR]] and [[VLP]] curves on a pressure vs rate plot.&lt;br /&gt;
&lt;br /&gt;
For the given reservoir [[Well Nodal Analysis]] calculates how much oil, water and gas can be produced by the given well.&lt;br /&gt;
&lt;br /&gt;
[[:Category:PQplot | PQplot]] is a [[Well Nodal Analysis]] software available online at [https://www.pengtools.com/pqPlot www.pengtools.com].&lt;br /&gt;
&lt;br /&gt;
==The Power of Well Nodal Analysis==&lt;br /&gt;
[[File:Location of various nodes.png|thumb|right|400px| Location of various nodes &amp;lt;ref name=JoeMach/&amp;gt;]]&lt;br /&gt;
&lt;br /&gt;
[[Well Nodal Analysis]] is the cornerstone of [[Petroleum Engineering| petroleum engineering]]. It allows to:&lt;br /&gt;
&lt;br /&gt;
# Calculate the well [[Production Potential | production potential]] and identify the performance gaps to maximize oil and gas production.&lt;br /&gt;
# Evaluate the various well nodes impact on production. Nodes: reservoir, perforation, tubing string, restrictions, downhole safety valves, the surface chokes, the surface flow lines and separator.&lt;br /&gt;
&lt;br /&gt;
==Typical Applications==&lt;br /&gt;
* Estimation of well [[Production Potential | production potential]] and absolute open flow (AOF)&lt;br /&gt;
* Tubing sizing&lt;br /&gt;
* Selection of the operating wellhead pressures&lt;br /&gt;
* Artificial lift design. Gas lift. [[ESP]] sizing.&lt;br /&gt;
* Sensitivity studies&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
[[Well Nodal Analysis]] is done on a pressure vs rate plot. [[IPR]] and [[VLP]] curves intersect at well operating point.&lt;br /&gt;
&lt;br /&gt;
Well [[IPR]] curve: [[Darcy's law]], [[Vogel's IPR]], [[Composite IPR]].&lt;br /&gt;
&lt;br /&gt;
Well [[VLP]] curve: [[Hagedorn and Brown]] multiphase flow correlation&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
Given data&amp;lt;ref name=JoeMach/&amp;gt;:&lt;br /&gt;
 SG&amp;lt;sub&amp;gt;g&amp;lt;/sub&amp;gt;=0.65, SG&amp;lt;sub&amp;gt;o&amp;lt;/sub&amp;gt;=35 API, P&amp;lt;sub&amp;gt;r&amp;lt;/sub&amp;gt;=2200 psi, P&amp;lt;sub&amp;gt;b&amp;lt;/sub&amp;gt;=1800 psi, T&amp;lt;sub&amp;gt;r&amp;lt;/sub&amp;gt;=140 F, depth = 5000ft, tubing size = 2 3/8 in OD, GOR=400 scf/stb, WOR=0&lt;br /&gt;
 Productivity index J = 1 bbl/d/psi&lt;br /&gt;
&lt;br /&gt;
It's required to find the well flowing rate at the wellhead pressure of 230 psi. Surface flow line and separator are not in question.&lt;br /&gt;
===Solution at bottom of well ===&lt;br /&gt;
In order to solve for the flow rate at bottomhole (node position 6), the entire system  is divided into two components, the reservoir or well capability component, [[IPR]] and the piping system component, [[VLP]] &amp;lt;ref name= KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
:First, [[Vogel's IPR | Vogel's equation]] is used to calculate the [[IPR]] curve. The AOF = 1400 bbl/d&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table 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;&amp;lt;th&amp;gt;Rate, bbl/d&amp;lt;/th&amp;gt;&amp;lt;th&amp;gt;Pwf, psi&amp;lt;/th&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;0&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;2200&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;200&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;2000&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;400&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1800&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;600&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1590&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;800&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1350&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;1000&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1067&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;1400&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;0&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
:Second, [[Hagedorn and Brown]] multiphase flow correlation is used to calculate the required tubing intake pressures at the given wellhead pressure, [[VLP]] curve.&lt;br /&gt;
&lt;br /&gt;
&amp;lt;table 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;&amp;lt;th&amp;gt;Rate, bbl/d&amp;lt;/th&amp;gt;&amp;lt;th&amp;gt;Pwf, psi&amp;lt;/th&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;0&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1929&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;200&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1065&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;400&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1125&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;600&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1181&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;800&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1235&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;1000&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1289&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
 &amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;1400&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;1399&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
:Third, [[IPR]] and [[VLP]] curves are plotted on the pressure vs rate plot. The intersection of these two curves shows the flow rate to be 872 bbl/d.&lt;br /&gt;
&lt;br /&gt;
[[File:Well Nodal Analysis Example.png | link=https://www.pengtools.com/pqPlot?paramsToken=7db370789c234c0949337f8b1978fa3c | Solution at Bottom of Well]]&lt;br /&gt;
&lt;br /&gt;
{{Quote| text = This is &amp;quot;the rate&amp;quot; possible for this system. It is not a maximum, minimum, or optimum but is the rate at which this well will produce for the piping system installed. The rate can be changed only by changing something in the system - that is, pipe sizes, choke or by shifting the [[IPR]] curve through simulation treatment. | source = Kermit Brown et al &amp;lt;ref name= KermitBrown1984/&amp;gt;}}&lt;br /&gt;
&lt;br /&gt;
== See also ==&lt;br /&gt;
*[[IPR]]&lt;br /&gt;
*[[VLP]]&lt;br /&gt;
*[[Petroleum Engineering]]&lt;br /&gt;
*[[Hydraulic fracturing]]&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= JoeMach&amp;gt;&lt;br /&gt;
{{cite journal&lt;br /&gt;
 |last1= Mach |first1=Joe&lt;br /&gt;
 |last2= Proano |first2=Eduardo&lt;br /&gt;
 |last3= Brown |first3=Kermit E.&lt;br /&gt;
 |title=A Nodal Approach For Applying Systems Analysis To The Flowing And Artificial Lift Oil Or Gas Well&lt;br /&gt;
 |date=1979&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-8025-MS&lt;br /&gt;
 |url=https://www.onepetro.org/general/SPE-8025-MS&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Legends&amp;gt;&lt;br /&gt;
{{cite journal&lt;br /&gt;
 |last1= JPT |first1=staff&lt;br /&gt;
 |title=Legends of Production and Operation&lt;br /&gt;
 |date=2009&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |journal=Journal of Petroleum Technology&lt;br /&gt;
 |number=SPE-1209-0033-JPT&lt;br /&gt;
 |url=https://www.onepetro.org/journal-paper/SPE-1209-0033-JPT&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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:Technology]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Well Nodal Analysis&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Well Nodal Analysis, Petroleum Engineering, petroleum technology&lt;br /&gt;
|description=Well Nodal Analysis is the fundamental petroleum engineering technique published in 1979 by Joe Mach.&lt;br /&gt;
}}&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=JD&amp;diff=7833</id>
		<title>JD</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=JD&amp;diff=7833"/>
				<updated>2025-04-07T09:43:15Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Oil */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;==Brief==&lt;br /&gt;
&lt;br /&gt;
[[JD]] - dimensionless productivity index&amp;lt;ref name = pushing/&amp;gt;, inverse of dimensionless pressure (based on average pressure) which contains the type of flow regime, boundary condition, drainage shape and stimulation &amp;lt;ref name = DW/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math &amp;amp; Physics==&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D} = \frac{1}{\bar{P}_D} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
From the [[Darcy's law]] for the unfractured well the [[JD]] is: &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;&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Well in circular drainage area&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Well in a drainage area with the shape factor &amp;lt;math&amp;gt; {C_A}&amp;lt;/math&amp;gt;&amp;lt;ref name = DW/&amp;gt;&amp;lt;/th&amp;gt;&lt;br /&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;Steady state&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt; {J_D} = \frac{1}{ln{\frac{r_e}{r_w}-\frac{1}{2}+S}} &amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt;{J_D} = \frac{1}{\frac{1}{2}ln{\frac{4.5A}{C_A{r_w}^2}+S}}&amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&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;Pseudo steady state&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt; {J_D} = \frac{1}{ln{\frac{r_e}{r_w}-\frac{3}{4}+S}} &amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt;{J_D} = \frac{1}{\frac{1}{2}ln{\frac{2.25A}{C_A{r_w}^2}+S}}&amp;lt;/math&amp;gt;&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;
Some typical &amp;lt;math&amp;gt; {C_A}&amp;lt;/math&amp;gt; values: circle 31.6, square 30.88 &amp;lt;ref name = Dietz/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
===Oil===&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D} = \frac{141.2 B \mu}{kh} \frac{q}{\bar{P} - P_{wf}} = \frac{141.2 B \mu}{kh} J&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {q} = \frac{kh}{141.2 B \mu} (\bar{P} - P_{wf}) J_D = (\bar{P} - P_{wf}) J&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Gas===&lt;br /&gt;
:&amp;lt;math&amp;gt;J_D=\frac{1422 \times 10^3\ T_R}{kh} \frac{q_g}{P_{\bar{P}}-P_{P_{wf}}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==Maximum &amp;lt;math&amp;gt;J_D&amp;lt;/math&amp;gt;==&lt;br /&gt;
&lt;br /&gt;
The undamaged unstimulated vertical well potential in a pseudo steady radial flow in a circular drainage area:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D}_{max} \approx \frac{1}{ln{\frac{500}{0.1}-\frac{3}{4}+0}} \approx 0.1287&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
The maximum possible stimulated well potential for pseudo steady linear flow is:&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;{J_D}_{max}= \frac{6}{\pi} \approx 1.91 &amp;lt;/math&amp;gt; , see [[6/π stimulated well potential]]&lt;br /&gt;
&lt;br /&gt;
The maximum possible stimulated well potential for steady state linear flow is:&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;{J_D}_{max}= \frac{4}{\pi} \approx 1.27 &amp;lt;/math&amp;gt; , see [[4/π stimulated well potential]]&lt;br /&gt;
&lt;br /&gt;
== Nomenclature  ==&lt;br /&gt;
:&amp;lt;math&amp;gt; B &amp;lt;/math&amp;gt; = formation volume factor, bbl/stb&lt;br /&gt;
:&amp;lt;math&amp;gt; C_A &amp;lt;/math&amp;gt; = Dietz shape factor, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; J &amp;lt;/math&amp;gt; = productivity index, stb/psia&lt;br /&gt;
:&amp;lt;math&amp;gt; J_D &amp;lt;/math&amp;gt; = dimensionless productivity index, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; kh&amp;lt;/math&amp;gt; = permeability times thickness, md*ft&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P} &amp;lt;/math&amp;gt; = average reservoir pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P}_D&amp;lt;/math&amp;gt; = dimensionless pressure (based on average pressure), dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{\bar{P}} &amp;lt;/math&amp;gt; = average reservoir pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{wf} &amp;lt;/math&amp;gt; = well flowing pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{P_{wf}} &amp;lt;/math&amp;gt; = average well flowing pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; q &amp;lt;/math&amp;gt; = flowing rate, stb/d&lt;br /&gt;
:&amp;lt;math&amp;gt; q_g &amp;lt;/math&amp;gt; = gas rate, MMscfd&lt;br /&gt;
:&amp;lt;math&amp;gt; r_w &amp;lt;/math&amp;gt; = wellbore radius, ft&lt;br /&gt;
:&amp;lt;math&amp;gt; r_e &amp;lt;/math&amp;gt; = drainage radius, ft&lt;br /&gt;
:&amp;lt;math&amp;gt; S &amp;lt;/math&amp;gt; = skin factor, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
&lt;br /&gt;
===Greek symbols===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu &amp;lt;/math&amp;gt; = viscosity, cp&lt;br /&gt;
&lt;br /&gt;
==See Also==&lt;br /&gt;
&lt;br /&gt;
* [[Darcy's law]]&lt;br /&gt;
* [[JD]]&lt;br /&gt;
* [[Productivity index|J]]&lt;br /&gt;
* [[Production Potential]]&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= pushing &amp;gt;{{cite journal&lt;br /&gt;
 |last1=Rueda|first1=J.I.&lt;br /&gt;
 |last2=Mach|first2=J.&lt;br /&gt;
 |last3=Wolcott|first3=D.&lt;br /&gt;
 |title=Pushing Fracturing Limits to Maximize Producibility in Turbidite Formations in Russia&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-91760-MS&lt;br /&gt;
 |date=2004&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/SPE-91760-MS&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name=DW&amp;gt;&lt;br /&gt;
{{cite book&lt;br /&gt;
 |last1= Wolcott |first1=Don&lt;br /&gt;
 |title=Applied Waterflood Field Development&lt;br /&gt;
 |date=2009&lt;br /&gt;
 |publisher=Energy Tribune Publishing Inc&lt;br /&gt;
 |place=Houston&lt;br /&gt;
 |url=https://www.amazon.com/Applied-Waterflood-Field-Development-Wolcott/dp/0578023946/ref=sr_1_1?ie=UTF8&amp;amp;qid=1481788841&amp;amp;sr=8-1&amp;amp;keywords=Don+wolcott&lt;br /&gt;
 |url-access=subscription&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dietz &amp;gt;{{cite journal&lt;br /&gt;
 |last1=Dietz|first1=D.N.&lt;br /&gt;
 |title=Determination of Average Reservoir Pressure From Build-Up Surveys&lt;br /&gt;
 |publisher=J Pet Technol&lt;br /&gt;
 |number=SPE-1156-PA&lt;br /&gt;
 |date=1965&lt;br /&gt;
 |url=https://doi.org/10.2118/1156-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:optiFrac]]&lt;br /&gt;
[[Category:optiFracMS]]&lt;br /&gt;
[[Category:fracDesign]]&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:E&amp;amp;P Portal]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Dimensionless Productivity Index&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=hydraulic fracturing, hydraulic fracturing formulas, well potential, productivity index&lt;br /&gt;
|description=JD dimensionless productivity index&lt;br /&gt;
}}&lt;br /&gt;
&amp;lt;div style='text-align: right;'&amp;gt;By Mikhail Tuzovskiy on {{REVISIONTIMESTAMP}}&amp;lt;/div&amp;gt;&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=JD&amp;diff=7832</id>
		<title>JD</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=JD&amp;diff=7832"/>
				<updated>2025-04-07T09:41:56Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Oil */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;==Brief==&lt;br /&gt;
&lt;br /&gt;
[[JD]] - dimensionless productivity index&amp;lt;ref name = pushing/&amp;gt;, inverse of dimensionless pressure (based on average pressure) which contains the type of flow regime, boundary condition, drainage shape and stimulation &amp;lt;ref name = DW/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math &amp;amp; Physics==&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D} = \frac{1}{\bar{P}_D} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
From the [[Darcy's law]] for the unfractured well the [[JD]] is: &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;&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Well in circular drainage area&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Well in a drainage area with the shape factor &amp;lt;math&amp;gt; {C_A}&amp;lt;/math&amp;gt;&amp;lt;ref name = DW/&amp;gt;&amp;lt;/th&amp;gt;&lt;br /&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;Steady state&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt; {J_D} = \frac{1}{ln{\frac{r_e}{r_w}-\frac{1}{2}+S}} &amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt;{J_D} = \frac{1}{\frac{1}{2}ln{\frac{4.5A}{C_A{r_w}^2}+S}}&amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&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;Pseudo steady state&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt; {J_D} = \frac{1}{ln{\frac{r_e}{r_w}-\frac{3}{4}+S}} &amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt;{J_D} = \frac{1}{\frac{1}{2}ln{\frac{2.25A}{C_A{r_w}^2}+S}}&amp;lt;/math&amp;gt;&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;
Some typical &amp;lt;math&amp;gt; {C_A}&amp;lt;/math&amp;gt; values: circle 31.6, square 30.88 &amp;lt;ref name = Dietz/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
===Oil===&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D} = \frac{141.2 B \mu}{kh} \frac{q}{\bar{P} - P_{wf}} = \frac{141.2 B \mu}{kh} J&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {q} = (\bar{P} - P_{wf}) J = \frac{kh}{141.2 B \mu} (\bar{P} - P_{wf}) J_D&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Gas===&lt;br /&gt;
:&amp;lt;math&amp;gt;J_D=\frac{1422 \times 10^3\ T_R}{kh} \frac{q_g}{P_{\bar{P}}-P_{P_{wf}}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==Maximum &amp;lt;math&amp;gt;J_D&amp;lt;/math&amp;gt;==&lt;br /&gt;
&lt;br /&gt;
The undamaged unstimulated vertical well potential in a pseudo steady radial flow in a circular drainage area:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D}_{max} \approx \frac{1}{ln{\frac{500}{0.1}-\frac{3}{4}+0}} \approx 0.1287&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
The maximum possible stimulated well potential for pseudo steady linear flow is:&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;{J_D}_{max}= \frac{6}{\pi} \approx 1.91 &amp;lt;/math&amp;gt; , see [[6/π stimulated well potential]]&lt;br /&gt;
&lt;br /&gt;
The maximum possible stimulated well potential for steady state linear flow is:&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;{J_D}_{max}= \frac{4}{\pi} \approx 1.27 &amp;lt;/math&amp;gt; , see [[4/π stimulated well potential]]&lt;br /&gt;
&lt;br /&gt;
== Nomenclature  ==&lt;br /&gt;
:&amp;lt;math&amp;gt; B &amp;lt;/math&amp;gt; = formation volume factor, bbl/stb&lt;br /&gt;
:&amp;lt;math&amp;gt; C_A &amp;lt;/math&amp;gt; = Dietz shape factor, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; J &amp;lt;/math&amp;gt; = productivity index, stb/psia&lt;br /&gt;
:&amp;lt;math&amp;gt; J_D &amp;lt;/math&amp;gt; = dimensionless productivity index, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; kh&amp;lt;/math&amp;gt; = permeability times thickness, md*ft&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P} &amp;lt;/math&amp;gt; = average reservoir pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P}_D&amp;lt;/math&amp;gt; = dimensionless pressure (based on average pressure), dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{\bar{P}} &amp;lt;/math&amp;gt; = average reservoir pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{wf} &amp;lt;/math&amp;gt; = well flowing pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{P_{wf}} &amp;lt;/math&amp;gt; = average well flowing pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; q &amp;lt;/math&amp;gt; = flowing rate, stb/d&lt;br /&gt;
:&amp;lt;math&amp;gt; q_g &amp;lt;/math&amp;gt; = gas rate, MMscfd&lt;br /&gt;
:&amp;lt;math&amp;gt; r_w &amp;lt;/math&amp;gt; = wellbore radius, ft&lt;br /&gt;
:&amp;lt;math&amp;gt; r_e &amp;lt;/math&amp;gt; = drainage radius, ft&lt;br /&gt;
:&amp;lt;math&amp;gt; S &amp;lt;/math&amp;gt; = skin factor, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
&lt;br /&gt;
===Greek symbols===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu &amp;lt;/math&amp;gt; = viscosity, cp&lt;br /&gt;
&lt;br /&gt;
==See Also==&lt;br /&gt;
&lt;br /&gt;
* [[Darcy's law]]&lt;br /&gt;
* [[JD]]&lt;br /&gt;
* [[Productivity index|J]]&lt;br /&gt;
* [[Production Potential]]&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= pushing &amp;gt;{{cite journal&lt;br /&gt;
 |last1=Rueda|first1=J.I.&lt;br /&gt;
 |last2=Mach|first2=J.&lt;br /&gt;
 |last3=Wolcott|first3=D.&lt;br /&gt;
 |title=Pushing Fracturing Limits to Maximize Producibility in Turbidite Formations in Russia&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-91760-MS&lt;br /&gt;
 |date=2004&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/SPE-91760-MS&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name=DW&amp;gt;&lt;br /&gt;
{{cite book&lt;br /&gt;
 |last1= Wolcott |first1=Don&lt;br /&gt;
 |title=Applied Waterflood Field Development&lt;br /&gt;
 |date=2009&lt;br /&gt;
 |publisher=Energy Tribune Publishing Inc&lt;br /&gt;
 |place=Houston&lt;br /&gt;
 |url=https://www.amazon.com/Applied-Waterflood-Field-Development-Wolcott/dp/0578023946/ref=sr_1_1?ie=UTF8&amp;amp;qid=1481788841&amp;amp;sr=8-1&amp;amp;keywords=Don+wolcott&lt;br /&gt;
 |url-access=subscription&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dietz &amp;gt;{{cite journal&lt;br /&gt;
 |last1=Dietz|first1=D.N.&lt;br /&gt;
 |title=Determination of Average Reservoir Pressure From Build-Up Surveys&lt;br /&gt;
 |publisher=J Pet Technol&lt;br /&gt;
 |number=SPE-1156-PA&lt;br /&gt;
 |date=1965&lt;br /&gt;
 |url=https://doi.org/10.2118/1156-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:optiFrac]]&lt;br /&gt;
[[Category:optiFracMS]]&lt;br /&gt;
[[Category:fracDesign]]&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:E&amp;amp;P Portal]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Dimensionless Productivity Index&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=hydraulic fracturing, hydraulic fracturing formulas, well potential, productivity index&lt;br /&gt;
|description=JD dimensionless productivity index&lt;br /&gt;
}}&lt;br /&gt;
&amp;lt;div style='text-align: right;'&amp;gt;By Mikhail Tuzovskiy on {{REVISIONTIMESTAMP}}&amp;lt;/div&amp;gt;&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=JD&amp;diff=7831</id>
		<title>JD</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=JD&amp;diff=7831"/>
				<updated>2025-04-07T09:41:22Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Oil */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;==Brief==&lt;br /&gt;
&lt;br /&gt;
[[JD]] - dimensionless productivity index&amp;lt;ref name = pushing/&amp;gt;, inverse of dimensionless pressure (based on average pressure) which contains the type of flow regime, boundary condition, drainage shape and stimulation &amp;lt;ref name = DW/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math &amp;amp; Physics==&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D} = \frac{1}{\bar{P}_D} &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
From the [[Darcy's law]] for the unfractured well the [[JD]] is: &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;&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Well in circular drainage area&amp;lt;/th&amp;gt;&lt;br /&gt;
&amp;lt;th&amp;gt;Well in a drainage area with the shape factor &amp;lt;math&amp;gt; {C_A}&amp;lt;/math&amp;gt;&amp;lt;ref name = DW/&amp;gt;&amp;lt;/th&amp;gt;&lt;br /&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;Steady state&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt; {J_D} = \frac{1}{ln{\frac{r_e}{r_w}-\frac{1}{2}+S}} &amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt;{J_D} = \frac{1}{\frac{1}{2}ln{\frac{4.5A}{C_A{r_w}^2}+S}}&amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&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;Pseudo steady state&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt; {J_D} = \frac{1}{ln{\frac{r_e}{r_w}-\frac{3}{4}+S}} &amp;lt;/math&amp;gt;&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;&amp;lt;math&amp;gt;{J_D} = \frac{1}{\frac{1}{2}ln{\frac{2.25A}{C_A{r_w}^2}+S}}&amp;lt;/math&amp;gt;&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;
Some typical &amp;lt;math&amp;gt; {C_A}&amp;lt;/math&amp;gt; values: circle 31.6, square 30.88 &amp;lt;ref name = Dietz/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
===Oil===&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D} = \frac{141.2 B \mu}{kh} \frac{q}{\bar{P} - P_{wf}} = \frac{141.2 B \mu}{kh} J&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {q} = \frac{kh}{141.2 B \mu} (\bar{P} - P_{wf}) J_D = (\bar{P} - P_{wf}) J&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Gas===&lt;br /&gt;
:&amp;lt;math&amp;gt;J_D=\frac{1422 \times 10^3\ T_R}{kh} \frac{q_g}{P_{\bar{P}}-P_{P_{wf}}}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==Maximum &amp;lt;math&amp;gt;J_D&amp;lt;/math&amp;gt;==&lt;br /&gt;
&lt;br /&gt;
The undamaged unstimulated vertical well potential in a pseudo steady radial flow in a circular drainage area:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; {J_D}_{max} \approx \frac{1}{ln{\frac{500}{0.1}-\frac{3}{4}+0}} \approx 0.1287&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
The maximum possible stimulated well potential for pseudo steady linear flow is:&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;{J_D}_{max}= \frac{6}{\pi} \approx 1.91 &amp;lt;/math&amp;gt; , see [[6/π stimulated well potential]]&lt;br /&gt;
&lt;br /&gt;
The maximum possible stimulated well potential for steady state linear flow is:&lt;br /&gt;
&lt;br /&gt;
&amp;lt;math&amp;gt;{J_D}_{max}= \frac{4}{\pi} \approx 1.27 &amp;lt;/math&amp;gt; , see [[4/π stimulated well potential]]&lt;br /&gt;
&lt;br /&gt;
== Nomenclature  ==&lt;br /&gt;
:&amp;lt;math&amp;gt; B &amp;lt;/math&amp;gt; = formation volume factor, bbl/stb&lt;br /&gt;
:&amp;lt;math&amp;gt; C_A &amp;lt;/math&amp;gt; = Dietz shape factor, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; J &amp;lt;/math&amp;gt; = productivity index, stb/psia&lt;br /&gt;
:&amp;lt;math&amp;gt; J_D &amp;lt;/math&amp;gt; = dimensionless productivity index, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; kh&amp;lt;/math&amp;gt; = permeability times thickness, md*ft&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P} &amp;lt;/math&amp;gt; = average reservoir pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P}_D&amp;lt;/math&amp;gt; = dimensionless pressure (based on average pressure), dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{\bar{P}} &amp;lt;/math&amp;gt; = average reservoir pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{wf} &amp;lt;/math&amp;gt; = well flowing pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{P_{wf}} &amp;lt;/math&amp;gt; = average well flowing pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; q &amp;lt;/math&amp;gt; = flowing rate, stb/d&lt;br /&gt;
:&amp;lt;math&amp;gt; q_g &amp;lt;/math&amp;gt; = gas rate, MMscfd&lt;br /&gt;
:&amp;lt;math&amp;gt; r_w &amp;lt;/math&amp;gt; = wellbore radius, ft&lt;br /&gt;
:&amp;lt;math&amp;gt; r_e &amp;lt;/math&amp;gt; = drainage radius, ft&lt;br /&gt;
:&amp;lt;math&amp;gt; S &amp;lt;/math&amp;gt; = skin factor, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
&lt;br /&gt;
===Greek symbols===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu &amp;lt;/math&amp;gt; = viscosity, cp&lt;br /&gt;
&lt;br /&gt;
==See Also==&lt;br /&gt;
&lt;br /&gt;
* [[Darcy's law]]&lt;br /&gt;
* [[JD]]&lt;br /&gt;
* [[Productivity index|J]]&lt;br /&gt;
* [[Production Potential]]&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= pushing &amp;gt;{{cite journal&lt;br /&gt;
 |last1=Rueda|first1=J.I.&lt;br /&gt;
 |last2=Mach|first2=J.&lt;br /&gt;
 |last3=Wolcott|first3=D.&lt;br /&gt;
 |title=Pushing Fracturing Limits to Maximize Producibility in Turbidite Formations in Russia&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-91760-MS&lt;br /&gt;
 |date=2004&lt;br /&gt;
 |url=https://www.onepetro.org/conference-paper/SPE-91760-MS&lt;br /&gt;
 |url-access=registration &lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name=DW&amp;gt;&lt;br /&gt;
{{cite book&lt;br /&gt;
 |last1= Wolcott |first1=Don&lt;br /&gt;
 |title=Applied Waterflood Field Development&lt;br /&gt;
 |date=2009&lt;br /&gt;
 |publisher=Energy Tribune Publishing Inc&lt;br /&gt;
 |place=Houston&lt;br /&gt;
 |url=https://www.amazon.com/Applied-Waterflood-Field-Development-Wolcott/dp/0578023946/ref=sr_1_1?ie=UTF8&amp;amp;qid=1481788841&amp;amp;sr=8-1&amp;amp;keywords=Don+wolcott&lt;br /&gt;
 |url-access=subscription&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name= Dietz &amp;gt;{{cite journal&lt;br /&gt;
 |last1=Dietz|first1=D.N.&lt;br /&gt;
 |title=Determination of Average Reservoir Pressure From Build-Up Surveys&lt;br /&gt;
 |publisher=J Pet Technol&lt;br /&gt;
 |number=SPE-1156-PA&lt;br /&gt;
 |date=1965&lt;br /&gt;
 |url=https://doi.org/10.2118/1156-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:optiFrac]]&lt;br /&gt;
[[Category:optiFracMS]]&lt;br /&gt;
[[Category:fracDesign]]&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:E&amp;amp;P Portal]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Dimensionless Productivity Index&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=hydraulic fracturing, hydraulic fracturing formulas, well potential, productivity index&lt;br /&gt;
|description=JD dimensionless productivity index&lt;br /&gt;
}}&lt;br /&gt;
&amp;lt;div style='text-align: right;'&amp;gt;By Mikhail Tuzovskiy on {{REVISIONTIMESTAMP}}&amp;lt;/div&amp;gt;&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=IPR&amp;diff=7830</id>
		<title>IPR</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=IPR&amp;diff=7830"/>
				<updated>2025-04-04T15:26:40Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* See also */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Inflow Performance Relationship==&lt;br /&gt;
[[File:Inflow Performance Relationship.png|thumb|right|400px|link=https://www.pengtools.com/pqPlot|Inflow Performance Relationship Curve]]&lt;br /&gt;
&lt;br /&gt;
[[IPR | Inflow Performance Relationship]] is a curve of producing rates plotted against well bottomhole pressures for oil, water and gas wells&amp;lt;ref name= Vogel/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
[[IPR]] curve shows productive capacity and well performance.&lt;br /&gt;
&lt;br /&gt;
[[IPR]] curve is used in [[Well Nodal Analysis]] for production systems design, analysis and optimization.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
===Oil well IPR equation===&lt;br /&gt;
*[[Darcy's law]] equation for the single-phase flow of incompressible liquid:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; q = \frac{kh}{141.2 B \mu}\ (\bar{P} - P_{wf}) J_D&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
*[[Vogel's IPR]] two-phase flow equation (oil + gas) and it's combination with single phase liquid.&lt;br /&gt;
*[[Composite IPR]] curve for oil wells producing water.&lt;br /&gt;
*[[3 Phase IPR]] three-phase flow equation (oil + gas + water).&lt;br /&gt;
&lt;br /&gt;
===Gas well IPR equation ===&lt;br /&gt;
*[[Darcy's law]] gas inflow equation:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;q_g=\frac{kh}{1422 \times 10^3\ T_R}\ (P_{\bar{P}} - P_{P_{wf}})\ J_D &amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
*C and n equation&lt;br /&gt;
&lt;br /&gt;
==IPR calculator software==&lt;br /&gt;
*[[:Category:PQplot | PQplot]] nodal analysis software is used to calculate the [[IPR]] curves. [[:Category:PQplot | PQplot]]  is available online at [https://www.pengtools.com www.pengtools.com].&lt;br /&gt;
*Excel&lt;br /&gt;
*other&lt;br /&gt;
&lt;br /&gt;
== Nomenclature  ==&lt;br /&gt;
:&amp;lt;math&amp;gt; B &amp;lt;/math&amp;gt; = formation volume factor, bbl/stb&lt;br /&gt;
:&amp;lt;math&amp;gt; J_D &amp;lt;/math&amp;gt; = dimensionless productivity index, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt; kh&amp;lt;/math&amp;gt; = permeability times thickness, md*ft&lt;br /&gt;
:&amp;lt;math&amp;gt; \bar{P} &amp;lt;/math&amp;gt; = average reservoir pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{\bar{P}} &amp;lt;/math&amp;gt; = average reservoir pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{wf} &amp;lt;/math&amp;gt; = well flowing pressure, psia&lt;br /&gt;
:&amp;lt;math&amp;gt; P_{P_{wf}} &amp;lt;/math&amp;gt; = average well flowing pseudopressure, psia&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;/cP&lt;br /&gt;
:&amp;lt;math&amp;gt; q &amp;lt;/math&amp;gt; = flowing rate, stb/d&lt;br /&gt;
:&amp;lt;math&amp;gt; q_g &amp;lt;/math&amp;gt; = gas rate, MMscfd&lt;br /&gt;
:&amp;lt;math&amp;gt; T &amp;lt;/math&amp;gt; = temperature, °R&lt;br /&gt;
&lt;br /&gt;
===Greek symbols===&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu &amp;lt;/math&amp;gt; = viscosity, cp&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Vogel&amp;gt;{{cite journal&lt;br /&gt;
 |last1= Vogel |first1=J. V.&lt;br /&gt;
 |title=Inflow Performance Relationships for Solution-Gas Drive Wells&lt;br /&gt;
 |journal=Journal of Petroleum Technology &lt;br /&gt;
 |volume=20&lt;br /&gt;
 |number=SPE-1476-PA&lt;br /&gt;
 |date=1968&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;
==See also==&lt;br /&gt;
:[[141.2 derivation]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
:[[Darcy's law]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
:[[JD]]&amp;lt;BR/&amp;gt;&lt;br /&gt;
:[[Production Potential]]&lt;br /&gt;
:[[Vogel's IPR]]&lt;br /&gt;
:[[Composite IPR]]&lt;br /&gt;
:[[3 Phase IPR]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Inflow Performance Relationship&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Inflow Performance Relationship, nodal analysis, IPR curve, IPR calculator&lt;br /&gt;
|description=IPR curve formula for well performance.&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:PQplot]]&lt;br /&gt;
[[Category:pengtools]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Darcy%27s_law&amp;diff=7829</id>
		<title>Darcy's law</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Darcy%27s_law&amp;diff=7829"/>
				<updated>2025-04-04T15:25:03Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* See Also */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;== Darcy's law ==&lt;br /&gt;
&lt;br /&gt;
[[File:Darcy's law.png|thumb|right|300px| Darcy's law. Equation and notations]]&lt;br /&gt;
&lt;br /&gt;
[[Darcy's law]] is the fundamental '''law''' of fluid motion in porous media published by '''Henry Darcy''' in '''1856''' &amp;lt;ref name=Darcy/&amp;gt;. French engineer '''Henry Darcy''' has earned himself a special place in history as the first experimental reservoir engineer &amp;lt;ref name=DakeF/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
[[Darcy's law]] has been successfully applied to determine the flow through permeable media since the early days of [[Petroleum Engineering]].&lt;br /&gt;
&lt;br /&gt;
The basic form of [[Darcy's law]] is very similar to in form to other physical laws. For example '''Fourier's law''' for heat conduction and '''Ohm's law''' for flow of electricity &amp;lt;ref name=DW/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
[[Darcy's law]] formula:&lt;br /&gt;
:&amp;lt;math&amp;gt;q=\frac{kA}{\mu} \frac{\Delta P}{L}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; A &amp;lt;/math&amp;gt; = cross-sectional area, cm&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; k&amp;lt;/math&amp;gt; = permeability, Darcy&lt;br /&gt;
:&amp;lt;math&amp;gt; L &amp;lt;/math&amp;gt; = length, cm&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt; q &amp;lt;/math&amp;gt; = flow rate, cm&amp;lt;sup&amp;gt;3&amp;lt;/sup&amp;gt;/sec&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu &amp;lt;/math&amp;gt; = fluid viscosity, cp&lt;br /&gt;
&lt;br /&gt;
The permeability of 1 Darcy defined as permeability which allows fluid with viscosity of 1 centipoise flow a distance of 1 cm with velocity of 1 cc/sec through the crossectional area of 1 cm2 with the pressure gradient of 1 atm.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
Determine the water phase permeability given the core lab test data:&lt;br /&gt;
100% water saturation, A=2.5 cm2, L=3 cm, qw=0.6 cm3/sec, dP=2 atm, water viscosity 1 cP.&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;k=\frac{q \mu L}{A \Delta P} = \frac{0.6 *1 *3}{2*2.5}=0.360\ Darcy&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==History ==&lt;br /&gt;
[[File:Darcy's experimental equipment.png|thumb|right|300px| Darcy's experimental equipment]]&lt;br /&gt;
&lt;br /&gt;
'''Henry Darcy''' worked on the design of a filter large enough to process the Dijon towns daily water requirement &amp;lt;ref name=DakeF/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
By flowing water through the sand pack Darcy established that, for any flow rate, the velocity of the flow was directly proportional to the difference in manometric heights&amp;lt;ref name=DakeF/&amp;gt;:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;u=K\frac{h1-h2}{L}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
All the experiments were carried out with water changing the type of sand pack. The effects of fluid density and viscosity on the flow was not investigated&amp;lt;ref name=DakeF/&amp;gt; and therefore accounted for in the constant '''K'''. &lt;br /&gt;
&lt;br /&gt;
Subsequently, others experiments performed with a variety of different liquids revealed the dependence of fluid flow on fluid density and viscosity. &lt;br /&gt;
&lt;br /&gt;
The new constant '''k''' has therefore been isolated as being solely dependent on the nature of sand and is described as the '''permeability'''&amp;lt;ref name=DakeF/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
== Equation ==&lt;br /&gt;
===Differential form ===&lt;br /&gt;
If distance is measured positive in the direction of flow, then the pressure gradient must be negative in the same direction since fluids move from high to low pressure&amp;lt;ref name=DakeF/&amp;gt;. Therefore, Darcy's law is:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; q = -\frac{kA}{\mu} \frac{dP}{dL}&amp;lt;/math&amp;gt;&lt;br /&gt;
===Linear form===&lt;br /&gt;
:&amp;lt;math&amp;gt; q = \frac{k}{\mu} \frac{A}{L} (P_1 - P_2)&amp;lt;/math&amp;gt; [[File:Darcy's Law Linear form equation.png|300px| Darcy's Law Linear form equation notation]]&lt;br /&gt;
&lt;br /&gt;
===Radial form===&lt;br /&gt;
:&amp;lt;math&amp;gt; q = \frac{2 \pi kh (P_e - P_w)}{\mu ln(r_e/r_w)}&amp;lt;/math&amp;gt; [[File:Darcy's Law Radial form equation.png|300px| Darcy's Law Radial form equation notation]]&lt;br /&gt;
&lt;br /&gt;
=== Conditions  ===&lt;br /&gt;
&lt;br /&gt;
*Single fluid&lt;br /&gt;
*Steady stay flow&lt;br /&gt;
*Constant fluid compressibility&lt;br /&gt;
*Constant temperature&lt;br /&gt;
&lt;br /&gt;
== Inflow Equations Derivation ==&lt;br /&gt;
&lt;br /&gt;
Derivation of the Linear and Radial Inflow Equations&lt;br /&gt;
[[File:Darcy's Law mtuz.png|800px]]&lt;br /&gt;
&lt;br /&gt;
==See Also==&lt;br /&gt;
&lt;br /&gt;
* [[IPR]]&lt;br /&gt;
* [[141.2 derivation]] Converting from the Darcy's law units to the field units in the well's inflow equations&lt;br /&gt;
* [[18.41 derivation]] Converting from the Darcy's law units to the metric units in the well's inflow equations&lt;br /&gt;
* Calculating [[Production Potential]] with the [[Darcy's law]]&lt;br /&gt;
* [[Petroleum Engineering]]&lt;br /&gt;
* [[Relative Permeability]]&lt;br /&gt;
* [[JD]]&lt;br /&gt;
* [[Productivity index|J]]&lt;br /&gt;
&lt;br /&gt;
==References==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Darcy&amp;gt;{{cite journal&lt;br /&gt;
 |last1=Darcy|first1= Henry&lt;br /&gt;
 |title=Les Fontaines Publiques de la Ville de Dijon&lt;br /&gt;
 |publisher=Victor Dalmont&lt;br /&gt;
 |date=1856&lt;br /&gt;
 |place=Paris&lt;br /&gt;
 |url=https://books.google.ru/books?id=-FxYAAAAYAAJ&amp;amp;printsec=frontcover&amp;amp;hl=ru&amp;amp;source=gbs_ge_summary_r&amp;amp;cad=0#v=twopage&amp;amp;q&amp;amp;f=false&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=DakeF&amp;gt;{{cite book&lt;br /&gt;
 |last1= Dake |first1=L.P.&lt;br /&gt;
 |title=Fundamentals of Reservoir Engineering&lt;br /&gt;
 |date=1978&lt;br /&gt;
 |publisher=Elsevier Science&lt;br /&gt;
 |place=Amsterdam, Hetherlands&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=DW&amp;gt;&lt;br /&gt;
{{cite book&lt;br /&gt;
 |last1= Wolcott |first1=Don&lt;br /&gt;
 |title=Applied Waterflood Field Development&lt;br /&gt;
 |date=2009&lt;br /&gt;
 |publisher=Energy Tribune Publishing Inc&lt;br /&gt;
 |place=Houston&lt;br /&gt;
 |url=https://www.amazon.com/Applied-Waterflood-Field-Development-Wolcott/dp/0578023946/ref=sr_1_1?ie=UTF8&amp;amp;qid=1481788841&amp;amp;sr=8-1&amp;amp;keywords=Don+wolcott&lt;br /&gt;
 |url-access=subscription&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:E&amp;amp;P Portal]]&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:Mature Water Flood Analysis]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Darcy's law | Equation Formula Examples | Petroleum Engineering&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Darcy's law equation&lt;br /&gt;
|description=Darcy's law equation, history, examples, derivation and applications in petroleum engineering.&lt;br /&gt;
}}&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Darcy%27s_law&amp;diff=7828</id>
		<title>Darcy's law</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Darcy%27s_law&amp;diff=7828"/>
				<updated>2025-04-04T15:24:46Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* See Also */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;== Darcy's law ==&lt;br /&gt;
&lt;br /&gt;
[[File:Darcy's law.png|thumb|right|300px| Darcy's law. Equation and notations]]&lt;br /&gt;
&lt;br /&gt;
[[Darcy's law]] is the fundamental '''law''' of fluid motion in porous media published by '''Henry Darcy''' in '''1856''' &amp;lt;ref name=Darcy/&amp;gt;. French engineer '''Henry Darcy''' has earned himself a special place in history as the first experimental reservoir engineer &amp;lt;ref name=DakeF/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
[[Darcy's law]] has been successfully applied to determine the flow through permeable media since the early days of [[Petroleum Engineering]].&lt;br /&gt;
&lt;br /&gt;
The basic form of [[Darcy's law]] is very similar to in form to other physical laws. For example '''Fourier's law''' for heat conduction and '''Ohm's law''' for flow of electricity &amp;lt;ref name=DW/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
[[Darcy's law]] formula:&lt;br /&gt;
:&amp;lt;math&amp;gt;q=\frac{kA}{\mu} \frac{\Delta P}{L}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
where&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; A &amp;lt;/math&amp;gt; = cross-sectional area, cm&amp;lt;sup&amp;gt;2&amp;lt;/sup&amp;gt;&lt;br /&gt;
:&amp;lt;math&amp;gt; k&amp;lt;/math&amp;gt; = permeability, Darcy&lt;br /&gt;
:&amp;lt;math&amp;gt; L &amp;lt;/math&amp;gt; = length, cm&lt;br /&gt;
:&amp;lt;math&amp;gt; P &amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt; q &amp;lt;/math&amp;gt; = flow rate, cm&amp;lt;sup&amp;gt;3&amp;lt;/sup&amp;gt;/sec&lt;br /&gt;
:&amp;lt;math&amp;gt; \mu &amp;lt;/math&amp;gt; = fluid viscosity, cp&lt;br /&gt;
&lt;br /&gt;
The permeability of 1 Darcy defined as permeability which allows fluid with viscosity of 1 centipoise flow a distance of 1 cm with velocity of 1 cc/sec through the crossectional area of 1 cm2 with the pressure gradient of 1 atm.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
Determine the water phase permeability given the core lab test data:&lt;br /&gt;
100% water saturation, A=2.5 cm2, L=3 cm, qw=0.6 cm3/sec, dP=2 atm, water viscosity 1 cP.&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;k=\frac{q \mu L}{A \Delta P} = \frac{0.6 *1 *3}{2*2.5}=0.360\ Darcy&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
==History ==&lt;br /&gt;
[[File:Darcy's experimental equipment.png|thumb|right|300px| Darcy's experimental equipment]]&lt;br /&gt;
&lt;br /&gt;
'''Henry Darcy''' worked on the design of a filter large enough to process the Dijon towns daily water requirement &amp;lt;ref name=DakeF/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
By flowing water through the sand pack Darcy established that, for any flow rate, the velocity of the flow was directly proportional to the difference in manometric heights&amp;lt;ref name=DakeF/&amp;gt;:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt;u=K\frac{h1-h2}{L}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
All the experiments were carried out with water changing the type of sand pack. The effects of fluid density and viscosity on the flow was not investigated&amp;lt;ref name=DakeF/&amp;gt; and therefore accounted for in the constant '''K'''. &lt;br /&gt;
&lt;br /&gt;
Subsequently, others experiments performed with a variety of different liquids revealed the dependence of fluid flow on fluid density and viscosity. &lt;br /&gt;
&lt;br /&gt;
The new constant '''k''' has therefore been isolated as being solely dependent on the nature of sand and is described as the '''permeability'''&amp;lt;ref name=DakeF/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
== Equation ==&lt;br /&gt;
===Differential form ===&lt;br /&gt;
If distance is measured positive in the direction of flow, then the pressure gradient must be negative in the same direction since fluids move from high to low pressure&amp;lt;ref name=DakeF/&amp;gt;. Therefore, Darcy's law is:&lt;br /&gt;
&lt;br /&gt;
:&amp;lt;math&amp;gt; q = -\frac{kA}{\mu} \frac{dP}{dL}&amp;lt;/math&amp;gt;&lt;br /&gt;
===Linear form===&lt;br /&gt;
:&amp;lt;math&amp;gt; q = \frac{k}{\mu} \frac{A}{L} (P_1 - P_2)&amp;lt;/math&amp;gt; [[File:Darcy's Law Linear form equation.png|300px| Darcy's Law Linear form equation notation]]&lt;br /&gt;
&lt;br /&gt;
===Radial form===&lt;br /&gt;
:&amp;lt;math&amp;gt; q = \frac{2 \pi kh (P_e - P_w)}{\mu ln(r_e/r_w)}&amp;lt;/math&amp;gt; [[File:Darcy's Law Radial form equation.png|300px| Darcy's Law Radial form equation notation]]&lt;br /&gt;
&lt;br /&gt;
=== Conditions  ===&lt;br /&gt;
&lt;br /&gt;
*Single fluid&lt;br /&gt;
*Steady stay flow&lt;br /&gt;
*Constant fluid compressibility&lt;br /&gt;
*Constant temperature&lt;br /&gt;
&lt;br /&gt;
== Inflow Equations Derivation ==&lt;br /&gt;
&lt;br /&gt;
Derivation of the Linear and Radial Inflow Equations&lt;br /&gt;
[[File:Darcy's Law mtuz.png|800px]]&lt;br /&gt;
&lt;br /&gt;
==See Also==&lt;br /&gt;
&lt;br /&gt;
- [[IPR]]&lt;br /&gt;
* [[141.2 derivation]] Converting from the Darcy's law units to the field units in the well's inflow equations&lt;br /&gt;
* [[18.41 derivation]] Converting from the Darcy's law units to the metric units in the well's inflow equations&lt;br /&gt;
* Calculating [[Production Potential]] with the [[Darcy's law]]&lt;br /&gt;
* [[Petroleum Engineering]]&lt;br /&gt;
* [[Relative Permeability]]&lt;br /&gt;
* [[JD]]&lt;br /&gt;
* [[Productivity index|J]]&lt;br /&gt;
&lt;br /&gt;
==References==&lt;br /&gt;
&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=Darcy&amp;gt;{{cite journal&lt;br /&gt;
 |last1=Darcy|first1= Henry&lt;br /&gt;
 |title=Les Fontaines Publiques de la Ville de Dijon&lt;br /&gt;
 |publisher=Victor Dalmont&lt;br /&gt;
 |date=1856&lt;br /&gt;
 |place=Paris&lt;br /&gt;
 |url=https://books.google.ru/books?id=-FxYAAAAYAAJ&amp;amp;printsec=frontcover&amp;amp;hl=ru&amp;amp;source=gbs_ge_summary_r&amp;amp;cad=0#v=twopage&amp;amp;q&amp;amp;f=false&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=DakeF&amp;gt;{{cite book&lt;br /&gt;
 |last1= Dake |first1=L.P.&lt;br /&gt;
 |title=Fundamentals of Reservoir Engineering&lt;br /&gt;
 |date=1978&lt;br /&gt;
 |publisher=Elsevier Science&lt;br /&gt;
 |place=Amsterdam, Hetherlands&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&amp;lt;ref name=DW&amp;gt;&lt;br /&gt;
{{cite book&lt;br /&gt;
 |last1= Wolcott |first1=Don&lt;br /&gt;
 |title=Applied Waterflood Field Development&lt;br /&gt;
 |date=2009&lt;br /&gt;
 |publisher=Energy Tribune Publishing Inc&lt;br /&gt;
 |place=Houston&lt;br /&gt;
 |url=https://www.amazon.com/Applied-Waterflood-Field-Development-Wolcott/dp/0578023946/ref=sr_1_1?ie=UTF8&amp;amp;qid=1481788841&amp;amp;sr=8-1&amp;amp;keywords=Don+wolcott&lt;br /&gt;
 |url-access=subscription&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:E&amp;amp;P Portal]]&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
[[Category:Mature Water Flood Analysis]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Darcy's law | Equation Formula Examples | Petroleum Engineering&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Darcy's law equation&lt;br /&gt;
|description=Darcy's law equation, history, examples, derivation and applications in petroleum engineering.&lt;br /&gt;
}}&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Category:SPipe&amp;diff=7827</id>
		<title>Category:SPipe</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Category:SPipe&amp;diff=7827"/>
				<updated>2025-02-18T09:40:28Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Pipe pressure drop calulator */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Pipe pressure drop calculator==&lt;br /&gt;
&lt;br /&gt;
[[File:SPIPE_i.png|thumb|300px|link=http://www.pengtools.com/sPipe|sPipe]] &lt;br /&gt;
&lt;br /&gt;
[[:Category:sPipe | sPipe]] is the simple surface pipeline sizing software in the [[:Category: Pengtools | pengtools]].&lt;br /&gt;
&lt;br /&gt;
[[:Category:sPipe | sPipe]] calculates the pressure drop in oil, gas and water flowlines.&lt;br /&gt;
&lt;br /&gt;
[[:Category:sPipe | sPipe]] is available online at [https://www.pengtools.com www.pengtools.com].&lt;br /&gt;
&lt;br /&gt;
== Typical applications ==&lt;br /&gt;
* Estimation of flowrate with defined pressures at inlet and outlet&lt;br /&gt;
* Estimation of inlet and outlet pressures for achieving target flowrate&lt;br /&gt;
* Selection of pipeline size &lt;br /&gt;
* Estimation of mixture velocity&lt;br /&gt;
&lt;br /&gt;
== Main features== &lt;br /&gt;
&lt;br /&gt;
* Plot of pressure profile vs length&lt;br /&gt;
* Result table with pressure, velocity and hold-up&lt;br /&gt;
* Sensitivity analysis&lt;br /&gt;
* Using prepared PVT models&lt;br /&gt;
* Account for elevation&lt;br /&gt;
&lt;br /&gt;
== Interface features ==&lt;br /&gt;
* Save and share references to saved models with colleagues&lt;br /&gt;
* Last saved model on current computer and browser is automatically opened&lt;br /&gt;
* Choose between Metric units and US oilfield units.&lt;br /&gt;
* Save as image and print plot by means of chart context menu (button at the upper-right corner of chart) &lt;br /&gt;
* Download report in pdf format containing input parameters, calculated values and plot&lt;br /&gt;
* Select and copy results to Excel or other application&lt;br /&gt;
&lt;br /&gt;
== Correlations ==&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;Type of problem&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;&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Oil, gas and water flow&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Beggs and Brill correlation|Beggs and Brill]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Brill, J.P. and Mukherjee, H. 1999. Multiphase Flow in Wells. SPE Monograph, Vol. 17, Society of Petroleum Engineers, Richardson, TX.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&amp;lt;tr&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Dry gas flow&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;[[Fanning correlation|Fanning]]&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;td&amp;gt;Cullender, M.H. and Smith, R.V. 1956. Practical Solution of Gas-Flow Equations for Wells and Pipelines with Large Temperature Gradients. Trans., AIME 207: 281.&amp;lt;/td&amp;gt;&lt;br /&gt;
&amp;lt;/tr&amp;gt;&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
[[Category:pengtools]]&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Pipe pressure drop calculator&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=pressure drop pipe calculator, pipeline, pipeline oil, pipeline sizing, gas pipeline sizing, flow rate, fluids flow, gas flow, petroleum engineering&lt;br /&gt;
|description=Petroleum engineering software for pipe pressure drop calculation and pipeline sizing&lt;br /&gt;
}}&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7826</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7826"/>
				<updated>2024-11-08T16:10:31Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Brief */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;&amp;lt;div style='text-align: right;'&amp;gt;By Mikhail Tuzovskiy on {{REVISIONTIMESTAMP}}&amp;lt;/div&amp;gt;&lt;br /&gt;
__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes developed by '''Gilbert''' in 1954&amp;lt;ref name=Gilbert/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; i.e. fluid reach sonic velocity in the throat of the choke&amp;lt;ref name=Economides/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/474.7=0.38 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = liquid flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Economides&amp;gt;{{cite book&lt;br /&gt;
 |last1= Economides |first1=M.J.&lt;br /&gt;
 |last2= Hill |first2=A.D.&lt;br /&gt;
 |last3= Economides |first3=C.E. &lt;br /&gt;
 |last4= Zhu |first4=D.&lt;br /&gt;
 |title=Petroleum Production Systems&lt;br /&gt;
 |edition=2&lt;br /&gt;
 |date=2013&lt;br /&gt;
 |publisher=Prentice Hall&lt;br /&gt;
 |place=Westford, Massachusetts&lt;br /&gt;
 |isbn=978-0-13-703158-0&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7825</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7825"/>
				<updated>2024-11-08T16:10:04Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Brief */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;&amp;lt;div style='text-align: right;'&amp;gt;By Mikhail Tuzovskiy on {{REVISIONTIMESTAMP}}&amp;lt;/div&amp;gt;&lt;br /&gt;
__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes developed by '''Gilbert''' &amp;lt;ref name=Gilbert/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; i.e. fluid reach sonic velocity in the throat of the choke&amp;lt;ref name=Economides/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/474.7=0.38 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = liquid flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Economides&amp;gt;{{cite book&lt;br /&gt;
 |last1= Economides |first1=M.J.&lt;br /&gt;
 |last2= Hill |first2=A.D.&lt;br /&gt;
 |last3= Economides |first3=C.E. &lt;br /&gt;
 |last4= Zhu |first4=D.&lt;br /&gt;
 |title=Petroleum Production Systems&lt;br /&gt;
 |edition=2&lt;br /&gt;
 |date=2013&lt;br /&gt;
 |publisher=Prentice Hall&lt;br /&gt;
 |place=Westford, Massachusetts&lt;br /&gt;
 |isbn=978-0-13-703158-0&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7824</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7824"/>
				<updated>2024-11-08T16:07:50Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Brief */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;&amp;lt;div style='text-align: right;'&amp;gt;By Mikhail Tuzovskiy on {{REVISIONTIMESTAMP}}&amp;lt;/div&amp;gt;&lt;br /&gt;
__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes developed by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; i.e. fluid reach sonic velocity in the throat of the choke&amp;lt;ref name=Economides/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/474.7=0.38 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = liquid flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Economides&amp;gt;{{cite book&lt;br /&gt;
 |last1= Economides |first1=M.J.&lt;br /&gt;
 |last2= Hill |first2=A.D.&lt;br /&gt;
 |last3= Economides |first3=C.E. &lt;br /&gt;
 |last4= Zhu |first4=D.&lt;br /&gt;
 |title=Petroleum Production Systems&lt;br /&gt;
 |edition=2&lt;br /&gt;
 |date=2013&lt;br /&gt;
 |publisher=Prentice Hall&lt;br /&gt;
 |place=Westford, Massachusetts&lt;br /&gt;
 |isbn=978-0-13-703158-0&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7823</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7823"/>
				<updated>2024-11-08T16:05:44Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;&amp;lt;div style='text-align: right;'&amp;gt;By Mikhail Tuzovskiy on {{REVISIONTIMESTAMP}}&amp;lt;/div&amp;gt;&lt;br /&gt;
__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; i.e. fluid reach sonic velocity in the throat of the choke&amp;lt;ref name=Economides/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/474.7=0.38 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = liquid flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Economides&amp;gt;{{cite book&lt;br /&gt;
 |last1= Economides |first1=M.J.&lt;br /&gt;
 |last2= Hill |first2=A.D.&lt;br /&gt;
 |last3= Economides |first3=C.E. &lt;br /&gt;
 |last4= Zhu |first4=D.&lt;br /&gt;
 |title=Petroleum Production Systems&lt;br /&gt;
 |edition=2&lt;br /&gt;
 |date=2013&lt;br /&gt;
 |publisher=Prentice Hall&lt;br /&gt;
 |place=Westford, Massachusetts&lt;br /&gt;
 |isbn=978-0-13-703158-0&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7822</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7822"/>
				<updated>2024-11-08T16:03:46Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; i.e. fluid reach sonic velocity in the throat of the choke&amp;lt;ref name=Economides/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/474.7=0.38 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = liquid flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Economides&amp;gt;{{cite book&lt;br /&gt;
 |last1= Economides |first1=M.J.&lt;br /&gt;
 |last2= Hill |first2=A.D.&lt;br /&gt;
 |last3= Economides |first3=C.E. &lt;br /&gt;
 |last4= Zhu |first4=D.&lt;br /&gt;
 |title=Petroleum Production Systems&lt;br /&gt;
 |edition=2&lt;br /&gt;
 |date=2013&lt;br /&gt;
 |publisher=Prentice Hall&lt;br /&gt;
 |place=Westford, Massachusetts&lt;br /&gt;
 |isbn=978-0-13-703158-0&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7821</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7821"/>
				<updated>2024-11-08T16:03:34Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* References */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; i.e. fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/474.7=0.38 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = liquid flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name=Economides&amp;gt;{{cite book&lt;br /&gt;
 |last1= Economides |first1=M.J.&lt;br /&gt;
 |last2= Hill |first2=A.D.&lt;br /&gt;
 |last3= Economides |first3=C.E. &lt;br /&gt;
 |last4= Zhu |first4=D.&lt;br /&gt;
 |title=Petroleum Production Systems&lt;br /&gt;
 |edition=2&lt;br /&gt;
 |date=2013&lt;br /&gt;
 |publisher=Prentice Hall&lt;br /&gt;
 |place=Westford, Massachusetts&lt;br /&gt;
 |isbn=978-0-13-703158-0&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;/references&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7820</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7820"/>
				<updated>2024-11-08T16:02:34Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Nomenclature */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; i.e. fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/474.7=0.38 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = liquid flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7819</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7819"/>
				<updated>2024-11-08T16:02:10Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Math and Physics */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; i.e. fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/474.7=0.38 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7818</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7818"/>
				<updated>2024-11-08T16:01:03Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Example */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; and fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/474.7=0.38 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7817</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7817"/>
				<updated>2024-11-08T16:00:17Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; and fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7816</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7816"/>
				<updated>2024-11-08T15:58:47Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Solution */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; and fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7815</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7815"/>
				<updated>2024-11-08T15:58:35Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Solution */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; and fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig or 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7814</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7814"/>
				<updated>2024-11-08T15:58:17Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; and fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psig = 460 +14.7 = 474.7 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7813</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7813"/>
				<updated>2024-11-08T15:57:04Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Given data */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; and fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psia&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psi&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7812</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7812"/>
				<updated>2024-11-08T15:56:55Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; and fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psi&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psi&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psig&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
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&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7811</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7811"/>
				<updated>2024-11-08T15:55:32Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Brief */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his empirical equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; and fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psi&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psi&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psi&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
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}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7810</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7810"/>
				<updated>2024-11-08T15:54:28Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Math and Physics */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure, i.e. the flow is &amp;quot;critical&amp;quot; and fluid reach sonic velocity in the throat of the choke.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psi&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psi&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psi&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7809</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7809"/>
				<updated>2024-11-08T15:48:09Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Example */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psi&lt;br /&gt;
&lt;br /&gt;
Calculate the well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psi&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psi&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7808</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7808"/>
				<updated>2024-11-08T15:47:12Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psi&lt;br /&gt;
&lt;br /&gt;
Calculate well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psi&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;D&amp;lt;/math&amp;gt; = choke beam diametr, 64th of an inch&lt;br /&gt;
:&amp;lt;math&amp;gt;GLR&amp;lt;/math&amp;gt; = gas liquid ratio, Mscf/bbl or 10^3 scf/bbl&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}&amp;lt;/math&amp;gt; = well head pressure, psi&lt;br /&gt;
:&amp;lt;math&amp;gt;q&amp;lt;/math&amp;gt; = flow rate, bbl/d&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7807</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7807"/>
				<updated>2024-11-08T15:44:37Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Solution */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psi&lt;br /&gt;
&lt;br /&gt;
Calculate well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psi&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Validity check 180/460=0.4 &amp;lt; 0.7 OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7806</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7806"/>
				<updated>2024-11-08T15:44:09Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Example */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psi&lt;br /&gt;
&lt;br /&gt;
Calculate well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psi&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Check validity 180/460=0.4 - OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7805</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7805"/>
				<updated>2024-11-08T15:43:39Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Example */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64 in, Line pressure = 180 psi&lt;br /&gt;
&lt;br /&gt;
Calculate well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Check validity 180/460=0.4 - OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7804</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7804"/>
				<updated>2024-11-08T15:43:28Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Example */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, D=22/64, Line pressure = 180 psi&lt;br /&gt;
&lt;br /&gt;
Calculate well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Check validity 180/460=0.4 - OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7803</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7803"/>
				<updated>2024-11-08T15:43:01Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure.&lt;br /&gt;
&lt;br /&gt;
==Example==&lt;br /&gt;
===Given data===&lt;br /&gt;
Oil rate = 600 bbl/d, GLR=400 scf/bbl, S=22, Line pressure = 180 psi&lt;br /&gt;
&lt;br /&gt;
Calculate well head pressure?&lt;br /&gt;
&lt;br /&gt;
===Solution===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times 0.4^{0.546}}{22^{1.89}} \times 600 = 460 psia&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Check validity 180/460=0.4 - OK&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7802</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7802"/>
				<updated>2024-11-08T15:33:24Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Math and Physics */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that the equation is independent of the downstream pressure and assumes that the downstream pressure is less than 70% of the upstream pressure.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7801</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7801"/>
				<updated>2024-11-08T15:31:41Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Brief */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Gilbert developed his equation from field data in California.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7800</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7800"/>
				<updated>2024-11-08T15:29:46Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Brief */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7799</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7799"/>
				<updated>2024-11-08T15:29:21Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Brief */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common formula used for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Echometer is used to measure the fluid level in the wells.&lt;br /&gt;
&lt;br /&gt;
Fluid level is used to calculate and monitor the bottom hole pressure of the wells.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7798</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7798"/>
				<updated>2024-11-08T15:27:59Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: &lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common used formula for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=Gilbert/&amp;gt;&amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Echometer is used to measure the fluid level in the wells.&lt;br /&gt;
&lt;br /&gt;
Fluid level is used to calculate and monitor the bottom hole pressure of the wells.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7797</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7797"/>
				<updated>2024-11-08T15:27:36Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* References */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common used formula for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Echometer is used to measure the fluid level in the wells.&lt;br /&gt;
&lt;br /&gt;
Fluid level is used to calculate and monitor the bottom hole pressure of the wells.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= Gilbert&amp;gt;{{cite book&lt;br /&gt;
 |last1= Gilbert |first1= W.E.&lt;br /&gt;
 |title=Flowing and Gas-Lift Well Performance&lt;br /&gt;
 |journal=Drilling and Production Practice API&lt;br /&gt;
 |date=1954&lt;br /&gt;
 |page=143&lt;br /&gt;
}}&amp;lt;/ref&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7796</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7796"/>
				<updated>2024-11-08T15:25:27Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Math and Physics */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common used formula for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Echometer is used to measure the fluid level in the wells.&lt;br /&gt;
&lt;br /&gt;
Fluid level is used to calculate and monitor the bottom hole pressure of the wells.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^{0.546}}{D^{1.89}} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7795</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7795"/>
				<updated>2024-11-08T15:25:12Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Math and Physics */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common used formula for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Echometer is used to measure the fluid level in the wells.&lt;br /&gt;
&lt;br /&gt;
Fluid level is used to calculate and monitor the bottom hole pressure of the wells.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \times GLR^0.546}{D^1.89} \times q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7794</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7794"/>
				<updated>2024-11-08T15:24:50Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Math and Physics */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common used formula for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Echometer is used to measure the fluid level in the wells.&lt;br /&gt;
&lt;br /&gt;
Fluid level is used to calculate and monitor the bottom hole pressure of the wells.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 \GLR^0.546}{D^1.89} \q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7793</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7793"/>
				<updated>2024-11-08T15:24:34Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Math and Physics */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common used formula for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Echometer is used to measure the fluid level in the wells.&lt;br /&gt;
&lt;br /&gt;
Fluid level is used to calculate and monitor the bottom hole pressure of the wells.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435/ GLR^0.546}{D^1.89}/q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7792</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7792"/>
				<updated>2024-11-08T15:24:20Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Math and Physics */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common used formula for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Echometer is used to measure the fluid level in the wells.&lt;br /&gt;
&lt;br /&gt;
Fluid level is used to calculate and monitor the bottom hole pressure of the wells.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435\ GLR^0.546}{D^1.89}\q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7791</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7791"/>
				<updated>2024-11-08T15:23:48Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Math and Physics */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common used formula for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Echometer is used to measure the fluid level in the wells.&lt;br /&gt;
&lt;br /&gt;
Fluid level is used to calculate and monitor the bottom hole pressure of the wells.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wh}=\frac{435 GLR^0.546}{D^1.89}q&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7790</id>
		<title>Gilbert choke equation</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Gilbert_choke_equation&amp;diff=7790"/>
				<updated>2024-11-08T15:22:13Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: Created page with &amp;quot;__TOC__ ==Brief== The most common used formula for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=KermitBrown1984/&amp;gt;.  Echometer is used to measure the fluid level...&amp;quot;&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
==Brief==&lt;br /&gt;
The most common used formula for multiphase flow through surface chokes by Gilbert &amp;lt;ref name=KermitBrown1984/&amp;gt;.&lt;br /&gt;
&lt;br /&gt;
Echometer is used to measure the fluid level in the wells.&lt;br /&gt;
&lt;br /&gt;
Fluid level is used to calculate and monitor the bottom hole pressure of the wells.&lt;br /&gt;
&lt;br /&gt;
==Math and Physics==&lt;br /&gt;
The physics is based on the principal hydrostatics law:&lt;br /&gt;
:&amp;lt;math&amp;gt;P=\frac{\rho g h}{101325}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
===Flowing well fluids segregation===&lt;br /&gt;
When the well is flowing with the pump this is how fluids segregate in the well bore:&lt;br /&gt;
*Oil, gas and water are produced through the tubing from the reservoir to the surface  &lt;br /&gt;
*Gas is in the annulus from the surface to the fluid level, Hd&lt;br /&gt;
*Oil and gas are between the fluid level Hd, and the pump setting depth, Hd&lt;br /&gt;
*Water, oil and gas are between pump, Hd and the top of the perforations, Hperfs&lt;br /&gt;
*Water is in the rathole&lt;br /&gt;
&lt;br /&gt;
===Equation to calculate the BHP from the fluid level===&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}=P_{ann}+\frac{(H_{perfs}-H_{pump})(SG_o(1-WCUT)+SG_w WCUT)+(H_{pump}-H_d)SG_o}{10.32}&amp;lt;/math&amp;gt;&lt;br /&gt;
&lt;br /&gt;
Note that for the deviated wells TVD depths should be used.&lt;br /&gt;
&lt;br /&gt;
==Nomenclature==&lt;br /&gt;
:&amp;lt;math&amp;gt;g&amp;lt;/math&amp;gt; = 9.81, m/s^2&lt;br /&gt;
:&amp;lt;math&amp;gt;h&amp;lt;/math&amp;gt; = depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_d&amp;lt;/math&amp;gt; = fluid level, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{perfs}&amp;lt;/math&amp;gt; = top of the perforations, m&lt;br /&gt;
:&amp;lt;math&amp;gt;H_{pump}&amp;lt;/math&amp;gt; = pump setting depth, m&lt;br /&gt;
:&amp;lt;math&amp;gt;P&amp;lt;/math&amp;gt; = pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{ann}&amp;lt;/math&amp;gt; = annulus presssure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;P_{wf}&amp;lt;/math&amp;gt; = well flowing bottomhole pressure, atm&lt;br /&gt;
:&amp;lt;math&amp;gt;\rho&amp;lt;/math&amp;gt; = density, kg/m^3&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_o&amp;lt;/math&amp;gt; = oil specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;SG_w&amp;lt;/math&amp;gt; = water specific gravity, dimensionless&lt;br /&gt;
:&amp;lt;math&amp;gt;WCUT&amp;lt;/math&amp;gt; = well water cut, fraction&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name= KermitBrown1984 &amp;gt;{{cite book&lt;br /&gt;
 |last1= Brown |first1= Kermit&lt;br /&gt;
 |title=The Technology of Artificial Lift Methods. Volume 4. Production Optimization of Oil and Gas Wells by Nodal System Analysis&lt;br /&gt;
 |publisher=PennWellBookss&lt;br /&gt;
 |date=1984&lt;br /&gt;
 |place=Tulsa, Oklahoma&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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Gilbert choke equation&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=Gilbert choke equation&lt;br /&gt;
|description=Gilbert choke equation&lt;br /&gt;
}}&lt;br /&gt;
&lt;br /&gt;
[[Category:Technology]]&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	<entry>
		<id>https://wiki.pengtools.com/index.php?title=Category:PQplot&amp;diff=7789</id>
		<title>Category:PQplot</title>
		<link rel="alternate" type="text/html" href="https://wiki.pengtools.com/index.php?title=Category:PQplot&amp;diff=7789"/>
				<updated>2024-05-10T07:10:24Z</updated>
		
		<summary type="html">&lt;p&gt;MishaT: /* Typical applications */&lt;/p&gt;
&lt;hr /&gt;
&lt;div&gt;__TOC__&lt;br /&gt;
== Well Nodal Analysis Software ==&lt;br /&gt;
&lt;br /&gt;
[[File:PQPLOT_i.png|thumb|300px|link=https://www.pengtools.com/pqPlot| PQplot nodal analysis software]]  &lt;br /&gt;
&lt;br /&gt;
[[:Category:PQplot | PQplot software]] is the core '''petroleum engineering''' engine of the [[:Category: Pengtools | pengtools]].&lt;br /&gt;
&lt;br /&gt;
[[:Category:PQplot | PQplot software]] calculates inflow performance relationship [[IPR]] and vertical lift performance [[VLP]] curves for oil and gas wells.&lt;br /&gt;
&lt;br /&gt;
[[:Category:PQplot | PQplot software]] is available online at [https://www.pengtools.com www.pengtools.com].&lt;br /&gt;
&lt;br /&gt;
== Typical applications ==&lt;br /&gt;
&lt;br /&gt;
* Calculating the [[Well Nodal Analysis]] &amp;lt;ref name= JM8025/&amp;gt; model of the well&lt;br /&gt;
* Matching the [[Well Nodal Analysis]] model to the well test data&lt;br /&gt;
* Calculating and exporting the [[IPR]] curves: [[Vogel's IPR]], [[Composite IPR]]&lt;br /&gt;
* Calculating and exporting the [[VLP]] tables to Excel or reservoir simulator&lt;br /&gt;
* Estimation of well's [[Production Potential]] and absolute open flow (AOF)&lt;br /&gt;
* Tubing sizing&lt;br /&gt;
* Gas lift design&lt;br /&gt;
* Selection of the operating wellhead pressures&lt;br /&gt;
* Estimation of the effects of reservoir pressure depletion &lt;br /&gt;
* Sensitivity studies&lt;br /&gt;
&lt;br /&gt;
== Main features == &lt;br /&gt;
* Multiphase flow correlations&lt;br /&gt;
* Plot of Inflow performance curve [[IPR]] and Vertical lift performance curve [[VLP]]&lt;br /&gt;
* Rate and pressure at intersection point&lt;br /&gt;
* Tubing, annular and tubing+annular flow types&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;
* Share models to the public cloud or by using model’s link&lt;br /&gt;
* Export pdf report containing input parameters, calculated values and plots of the PQplot&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;
&lt;br /&gt;
==Demo==&lt;br /&gt;
The demo is a copy of a training seminar.  This video demonstrates basic functionality of the [[:Category:PVT | PVT Software]] and [[:Category:PQplot | PQplot software]]. It is shown how to create the well nodal analysis model, run sensitivity, save the model.&lt;br /&gt;
&lt;br /&gt;
[[File:PQplot_demo.png|400px|link=https://youtu.be/oioheTV45tU | Watch on youtube]]&lt;br /&gt;
&lt;br /&gt;
In this demo we are solving the homework where it was asked to:&lt;br /&gt;
* Calculate the flowing bottomhole pressure.&lt;br /&gt;
* Construct [[VLP]] curve&lt;br /&gt;
* Construct [[IPR]] and calculate AOF&lt;br /&gt;
* Calculate current production efficiency (production/AOF)&lt;br /&gt;
* What is the production potential and what actions do you propose to close the performance gap?&lt;br /&gt;
* What will be production increment from the proposed actions?&lt;br /&gt;
&lt;br /&gt;
[https://www.pengtools.com/pvtCalculator?paramsToken=b4bd505e0a17a75adb14f0989f89c502 PVT model at www.pengtools.com]&amp;lt;BR/&amp;gt;&lt;br /&gt;
[https://www.pengtools.com/pqPlot?paramsToken=9fba6c3fa125c5e6d8aa101e5cf9b52c PQplot model at www.pengtools.com]&lt;br /&gt;
&lt;br /&gt;
== Correlations ==&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;Type of problem&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;&amp;lt;td&amp;gt;&lt;br /&gt;
Oil well [[VLP]]&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
[[Hagedorn and Brown correlation|Hagedorn and Brown]] + [[Griffith correlation| Griffith]]&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Hagedorn, A. R., &amp;amp; Brown, K. E. (1965). Experimental study of pressure gradients occurring during continuous two-phase flow in small-diameter vertical conduits. Journal of Petroleum Technology, 17(04), 475-484.&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Gas well [[VLP]]&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
[[Gray correlation|Gray]]&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Gray, H. E. (1974). Vertical flow correlation in gas wells. User manual for API14B, subsurface controlled safety valve sizing computer program.&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Dry gas [[VLP]]&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
[[Fanning correlation|Fanning]]&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Cullender, M.H. and Smith, R.V. 1956. Practical Solution of Gas-Flow Equations for Wells and Pipelines with Large Temperature Gradients. Trans., AIME 207: 281.&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Oil well [[IPR]]&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
[[Composite IPR]] – [[Vogel's IPR]] based equations taking into account water&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Kermit E. Brown &amp;quot;The Technology of Artificial Lift&lt;br /&gt;
Methods&amp;quot; Vol. 4 Production Optimization of Oil and Gas&lt;br /&gt;
Wells by Nodal System Analysis, p. 30, section 2.227.1&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Gas well [[IPR]] – backpressure equation&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Rawlins and Schellhardt&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Rawlins, E.L. and Schellhardt, M.A. 1935. Backpressure Data on Natural Gas Wells and Their Application to Production Practices, Vol. 7. Monograph Series, USBM.&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Gas well [[IPR]] – pseudo-pressure equation using Jd and kh values&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Real-gas pseudopressure equation&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
See for example: Ahmed, T., &amp;amp; McKinney, P. (2011). Advanced reservoir engineering. Gulf Professional Publishing.&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
[[Liquid loading]]&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Turner&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Turner, R. G., Hubbard, M. G., and Dukler, A. E. (1969) “Analysis and Prediction of Minimum Flow Rate for the Continuous Removal of Liquids from Gas Wells,” Journal of Petroleum Technology, Nov. 1969. pp. 1475–1482.&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
&amp;lt;tr&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
[[Erosional velocity]]&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Guidelines from API RP14E&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;td&amp;gt;&lt;br /&gt;
Mokhatab S, Poe WA, Speight JG (2006) &amp;quot;Handbook of Natural Gas Transmission and Processing&amp;quot;, Section 11.6 - Design Considerations on sales gas pipelines, subsection 11.6.1 - Line Sizing Criteria, Elsevier, 2006.&lt;br /&gt;
&amp;lt;/td&amp;gt;&amp;lt;/tr&amp;gt;&lt;br /&gt;
&amp;lt;/table&amp;gt;&lt;br /&gt;
&lt;br /&gt;
&lt;br /&gt;
PVT correlations are the same as in [[:Category:PVT|PVT software]].&lt;br /&gt;
&lt;br /&gt;
== References ==&lt;br /&gt;
&amp;lt;references&amp;gt;&lt;br /&gt;
&amp;lt;ref name=JM8025&amp;gt;{{cite journal&lt;br /&gt;
 |last1=Mach|first1=Joe&lt;br /&gt;
 |last2=Proano|first2=Eduardo&lt;br /&gt;
 |last3=E. Brown|first3=Kermit&lt;br /&gt;
 |title=A Nodal Approach For Applying Systems Analysis To The Flowing And Artificial Lift Oil Or Gas Well&lt;br /&gt;
 |publisher=Society of Petroleum Engineers&lt;br /&gt;
 |number=SPE-8025-MS&lt;br /&gt;
 |date=1979&lt;br /&gt;
 |url=https://www.onepetro.org/general/SPE-8025-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;
&lt;br /&gt;
{{#seo:&lt;br /&gt;
|title=Well Nodal Analysis Software&lt;br /&gt;
|titlemode= replace&lt;br /&gt;
|keywords=nodal analysis, nodal analysis software, tubing, reservoir, fluids flow, sensitivity, gas flow, petroleum engineering&lt;br /&gt;
|description=PQplot petroleum engineering software calculates inflow performance relationship and vertical lift performance curves for oil and gas flow for well nodal analysis.&lt;br /&gt;
}}&lt;/div&gt;</summary>
		<author><name>MishaT</name></author>	</entry>

	</feed>