Difference between revisions of "Velarde solution gas oil ratio correlation"
From wiki.pengtools.com
| Line 8: | Line 8: | ||
:<math>R_s = \frac{R_{sr}}{R_{sb}}</math> | :<math>R_s = \frac{R_{sr}}{R_{sb}}</math> | ||
| − | :<math>R_{sr} = \alpha1 \times P^{\alpha2}_r + (1 - \alpha1) \times P^{\alpha3}_r</math | + | :<math>R_{sr} = \alpha1 \times P^{\alpha2}_r + (1 - \alpha1) \times P^{\alpha3}_r</math> |
where: | where: | ||
| Line 14: | Line 14: | ||
:<math>P_r = \frac{P-0.101}{P_b}</math> | :<math>P_r = \frac{P-0.101}{P_b}</math> | ||
| − | A0 = 1.8653e-4<br/> | + | A0 = 1.8653e-4<br/><ref name= PracticalPVT/> |
A1 = 1.672608<br/> | A1 = 1.672608<br/> | ||
A2 = 0.929870<br/> | A2 = 0.929870<br/> | ||
| Line 22: | Line 22: | ||
:<math> \alpha1 = A_0 \times SG^{A_1}_g \times Y^{A_2}_{oil_API} \times {(1.8 T- 459.67)}^{A_3} \times P^{A_3}_b </math> | :<math> \alpha1 = A_0 \times SG^{A_1}_g \times Y^{A_2}_{oil_API} \times {(1.8 T- 459.67)}^{A_3} \times P^{A_3}_b </math> | ||
| − | B0 = 0.1004<br/> | + | B0 = 0.1004<br/><ref name= PracticalPVT/> |
B1 = -1.00475<br/> | B1 = -1.00475<br/> | ||
B2 = 0.337711<br/> | B2 = 0.337711<br/> | ||
| Line 30: | Line 30: | ||
:<math>\alpha2 = B_0 \times SG^{B_1}_g \times Y^{B_2}_{oil_API} \times {(1.8 T - 459.67)}^{B_3} \times P^{B_4}_b</math> | :<math>\alpha2 = B_0 \times SG^{B_1}_g \times Y^{B_2}_{oil_API} \times {(1.8 T - 459.67)}^{B_3} \times P^{B_4}_b</math> | ||
| − | C0 = 0.9167<br/> | + | C0 = 0.9167<br/><ref name= PracticalPVT/> |
C1 = -1.48548<br/> | C1 = -1.48548<br/> | ||
C2 = -0.164741<br/> | C2 = -0.164741<br/> | ||
| Line 67: | Line 67: | ||
|url=https://www.onepetro.org/conference-paper/PETSOC-97-93 | |url=https://www.onepetro.org/conference-paper/PETSOC-97-93 | ||
|url-access=registration | |url-access=registration | ||
| + | }}</ref> | ||
| + | <ref name=PracticalPVT> | ||
| + | {{cite journal | ||
| + | |last1= Afanasyev |first1=Vitaliy | ||
| + | |last2= Moskvin |first2=Igor | ||
| + | |last3= Wolcott |first3=Ken | ||
| + | |last4= McCain |first4=W.D. | ||
| + | |title=Practical PVT Calculations for black oils | ||
| + | |journal=YUKOS publication | ||
| + | |date=2004 | ||
| + | }}</ref> | ||
| + | <ref name=DW> | ||
| + | {{cite book | ||
| + | |last1= Wolcott |first1=Don | ||
| + | |title=Applied Waterflood Field Development | ||
| + | |date=2009 | ||
| + | |publisher=Energy Tribune Publishing Inc | ||
| + | |place=Houston | ||
| + | |url=https://www.amazon.com/Applied-Waterflood-Field-Development-Wolcott/dp/0578023946/ref=sr_1_1?ie=UTF8&qid=1481788841&sr=8-1&keywords=Don+wolcott | ||
| + | |url-access=subscription | ||
}}</ref> | }}</ref> | ||
</references> | </references> | ||
Revision as of 08:28, 28 September 2020
Brief
Velarde correlation is an empirical correlation for the solution gas oil ratio published in 1997. [1]
Math & Physics
where:
A0 = 1.8653e-4
[2]
A1 = 1.672608
A2 = 0.929870
A3 = 0.247235
A4 = 1.056052
B0 = 0.1004
[2]
B1 = -1.00475
B2 = 0.337711
B3 = 0.132795
B4 = 0.302065
C0 = 0.9167
[2]
C1 = -1.48548
C2 = -0.164741
C3 = -0.09133
C4 = 0.047094
Discussion
Why the Velarde correlation?
Application range
Nomenclature
= coefficients
= coefficients
= coefficients
= pressure, MPA
= bubble point pressure, MPA
= gas specific gravity, dimensionless
= temperature, °R
= oil API gravity, dimensionless
References
- ↑
Velarde, J.; Blasingame, T. A.; McCain Jr., W. D. (1997). "Correlation of Black Oil Properties At Pressures Below Bubble Point Pressure - A New Approach"
. Presented at the Annual Technical Meeting of CIM, Calgary, Alberta. Petroleum Society of Canada (PETSOC-97-93).
- ↑ 2.0 2.1 2.2 Afanasyev, Vitaliy; Moskvin, Igor; Wolcott, Ken; McCain, W.D. (2004). "Practical PVT Calculations for black oils". YUKOS publication.
Cite error: <ref> tag with name "DW" defined in <references> is not used in prior text.
