By K S Pedersen; Aage Fredenslund; P Thomassen
ISBN-10: 0872015882
ISBN-13: 9780872015883
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Sample text
Volumetric and Thermodynamic Properties of Fluids. 1. Theoretical Basis and Virial Coefficíents," ]. Am. Chem. , 77, 1955, pp. 3427-3433. Redlich, O. and Kwong, J. N. , "The Thermodynamics of Solutions. V. An Equation of State. Fugacities of Gaseous Solutíons," Chem. , 44, 1949, pp. 233-244. Reid, R. , Prausnitz, J. , and Sherwood, T. , New York, McGraw-Hill, 1977. , "Equilíbrium Constants from a Modified Redlich-Kwong Equation of State," Chem. Eng. , 27, 1972, pp. 1197-1203. Spencer, C. F. and Danner, R.
E ea ea al ea ~ ~ >0 ~ ";" - o el) _CII -o CII e~a ea Q. ' "'O e ea O 5 tU ~~ ~ (f) f! : E ~ ~ü~ ~ 'O-e III el) Cl ea I '" N 00 ! 00 C/) ID.... ~ ea O,D~ ID - Injection pressure Saturation pressure Vs - Vi - LiQuid volume at injection pressure Saturation volume A V - Swelling volume &. ~ 8 g s QJ e ~ ~ t~ I el tl M (/)a. 17 Ps - Ci>~~ üCl •.. 30 a. "'" Ol . 49 (") a. ~.. a. >< e '" tU ~ ID . 1 000 U) . , e •... 11: U O CD o ea E-o •.. ~~* >-~ •... o t5 -;jctS el:: cu ctI •... 2 ~ l;o~~~~C> o U tU Ps '~~§~oca~~ ~o~~~o8g Ci5CñEñi~x(/)'; cu cu o 0- Q) c: ea (1) o ce e s o s ISfiff ~ §:§: p¡ Pressure Figure 3-13.
Calculation of the unknown density from the equatión: p = p¡(C¡/C2) (5-88) where the CI and C2 are the density correlation factors (Equation 5-86) at standard conditions, and at the actual conditions, respectively. 96 Properties 01 Oils and Natural Gases Equations 01 State Table 5-6 Coefficients of Equation 5-87 for Calculation of Liquid Denslties Using the API-Method B, B2 B. 1812(10-6) A. 5841 B3 - Source: API (1982). The API-density method is only applicable to liquid phases. Results for vapor and liquid phase den sities using each of the correlations mentioned previously are given in Chapter 9.
Properties of oils and natural gases by K S Pedersen; Aage Fredenslund; P Thomassen
by Thomas
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