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Vasquez-Beggs Solution Gas-Oil Ratio Calculator

Rs=C1γgpC2exp(C3APIT+460)R_s=C_1\gamma_g p^{C_2}\exp\left(\frac{C_3API}{T+460}\right)

Enter pressure, reservoir temperature, oil API gravity, gas specific gravity, and the Vasquez-Beggs coefficient set for the applicable API range. The output is solution gas-oil ratio in scf/STB.

Tabular solver

Inputs

Defaults provide a quick field-unit example for the equation.

7 variables

Your input values and calculation stay in this browser.

Engineering reference summary

Calculation context and source notes

The Vasquez-Beggs correlation estimates solution gas-oil ratio from pressure, temperature, oil API gravity, gas specific gravity, and the coefficient set selected for the oil-gravity range.

Use the correlation for black-oil PVT screening when laboratory differential-liberation data or a calibrated PVT model are unavailable. Select the API-gravity coefficient range deliberately and compare the estimate with regional fluid data whenever possible.

Solves for

R_s (SCF/STB)

Related source-backed guides

Formula reference

Formula, variables, and default calculation

Rs=C1γgpC2exp(C3APIT+460)R_s=C_1\gamma_g p^{C_2}\exp\left(\frac{C_3API}{T+460}\right)

Reproducible default result

With the default values shown below, the calculation returns R_s = 569.164106 SCF/STB. Defaults demonstrate the implementation; they are not recommended field values.

ppsi

2500

T°F

180

APIAPI

35

gamma_gfraction

0.8

C_rs1dimensionless

0.0178

C_rs2dimensionless

1.187

C_rs3dimensionless

23.931

Input definitions

p

psi

Pressure

T

°F

Reservoir Temperature

API

API

Oil API Gravity

gamma_g

fraction

Gas Specific Gravity

C_rs1

dimensionless

Vasquez-Beggs C1 Coefficient (0.0178 if API > 30; 0.0362 if API <= 30)

C_rs2

dimensionless

Vasquez-Beggs C2 Coefficient (1.1870 if API > 30; 1.0937 if API <= 30)

C_rs3

dimensionless

Vasquez-Beggs C3 Coefficient (23.931 if API > 30; 25.724 if API <= 30)

Output definitions

R_s

SCF/STB

Solution Gas-Oil Ratio

p

psi

Pressure

gamma_g

fraction

Gas Specific Gravity

Engineering use, assumptions, and limits

Use the correlation for black-oil PVT screening when laboratory differential-liberation data or a calibrated PVT model are unavailable. Select the API-gravity coefficient range deliberately and compare the estimate with regional fluid data whenever possible.

Assumptions

  • Pressure, temperature, API gravity, and gas specific gravity use the field-unit basis of the published correlation.
  • The input condition is within the black-oil behavior represented by the correlation.
  • The coefficient set matches the selected oil API-gravity range.

Limitations

  • An empirical correlation is not a substitute for representative laboratory PVT data.
  • Accuracy can degrade for fluids and conditions outside the data range used to develop the correlation.

Common mistakes

  • Using gauge pressure where the implementation or comparison requires absolute pressure.
  • Selecting the wrong API-gravity coefficient set.
  • Using separator gas gravity without applying the source correlation's gas-gravity basis or correction.

Source and record status

Source metadata identifies the relationship implemented by the calculator. Check the cited edition, unit basis, and scope against the engineering case before operational use.

reviewedguidance published

Vasquez and Beggs 1980 oil PVT correlations, as summarized in IHS Harmony / WellTest documentation and PIPESIM fluid-property documentation.

Open source reference

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