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| bbl/stb | p ≤ pb | LaTeX Math Inline |
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body | --uriencoded--\displaystyle B_o(p, T) = 1 + |
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c_1 \, R_s(p, T) + (T-60) \, \left( \frac%7B\gamma_%7BAPI%7D%7D%7B\gamma_g%7D \right) \, \big[ |
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LaTeX Math Inline |
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body | --uriencoded--\gamma_%7BAPI%7D \leq 30 \ %7B\rm API%7D : \quad c_1 = 4.677 · 10%5e%7B-4%7D, \, c_2 = 1.751· 10%5e%7B-5%7D, \ c_3 = -1.811· 10%5e%7B-8%7D |
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LaTeX Math Inline |
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body | --uriencoded--\gamma_%7BAPI%7D > 30 \ %7B\rm API%7D : \quad c_1 = 4.670 · 10%5e%7B-4%7D, \, c_2 = 1.100 · 10%5e%7B-5%7D, \ c_3 = 1.337 · 10%5e%7B-9%7D |
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where
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LaTeX Math Inline |
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body | --uriencoded--\gamma_%7BAPI%7D \leq 30 \ %7B\rm API%7D |
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LaTeX Math Inline |
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body | --uriencoded--\gamma_%7BAPI%7D > 30 \ %7B\rm API%7D |
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See Also
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Petroleum Industry / Upstream / Petroleum Engineering / Subsurface E&P Disciplines / Reservoir Engineering (RE) / PVT correlations / Oil correlations
[ Vasquez-Beggs (1980) oil correlations ]
References
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Vasquez, M., and H.D. Beggs. "Correlations for Fluid Physical Property Prediction." J Pet Technol 32 (1980): 968–970, doi.org/10.2118/6719-PA