Difference between revisions of "Velarde solution gas oil ratio correlation"
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− | == | + | == Velarde solution gas oil ratio correlation == |
[[Velarde correlation]] is an empirical correlation for the '''solution gas oil ratio''' published in '''1997'''. <ref name=Velarde /> | [[Velarde correlation]] is an empirical correlation for the '''solution gas oil ratio''' published in '''1997'''. <ref name=Velarde /> | ||
− | + | == Math & Physics == | |
:<math>R_s = \frac{R_{sr}}{R_{sb}}</math> | :<math>R_s = \frac{R_{sr}}{R_{sb}}</math> | ||
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:<math>P_r = \frac{P-0.101}{P_b}</math> | :<math>P_r = \frac{P-0.101}{P_b}</math> | ||
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+ | :<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> | ||
A0 = 1.8653e-4<ref name= PracticalPVT/><br/> | A0 = 1.8653e-4<ref name= PracticalPVT/><br/> | ||
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A4 = 1.056052<br/> | A4 = 1.056052<br/> | ||
− | :<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> |
B0 = 0.1004<ref name= PracticalPVT/><br/> | B0 = 0.1004<ref name= PracticalPVT/><br/> | ||
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B4 = 0.302065<br/> | B4 = 0.302065<br/> | ||
− | :<math>\ | + | :<math>\alpha3 = C_0 \times SG^{C_1}_g \times Y^{C_2}_{oil_API} \times {(1.8 T - 459.67)}^{C_3} \times P^{C_4}_b</math> |
C0 = 0.9167<ref name= PracticalPVT/><br/> | C0 = 0.9167<ref name= PracticalPVT/><br/> | ||
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C4 = 0.047094<br/> | C4 = 0.047094<br/> | ||
− | + | == Application range == | |
− | + | == Nomenclature == | |
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:<math> A_1..A_{4} </math> = coefficients | :<math> A_1..A_{4} </math> = coefficients | ||
:<math> B_1..B_{4} </math> = coefficients | :<math> B_1..B_{4} </math> = coefficients |
Revision as of 08:30, 28 September 2020
Contents
Velarde solution gas oil ratio correlation
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
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.