PREDICTING PHASE BEHAVIOR OF CONDENSATE-CRUDE-OIL SYSTEMS USING METHANE INTERACTION COEFFICIENTS

被引：152

作者：

KATZ, DL ^{[1
]}

FIROOZABADI, A ^{[1
]}

机构：

[1] ABADAN INST TECHNOL,ABADAN,IRAN

来源：

JOURNAL OF PETROLEUM TECHNOLOGY | 1978年 / 30卷 / NOV期

关键词：

HYDROCARBONS - Phase Equilibria - PETROLEUM; CRUDE;

D O I：

10.2118/6721-PA

中图分类号：

TE [石油、天然气工业]; TK [能源与动力工程];

学科分类号：

0807 ; 0820 ;

摘要：

This paper reports the extension of the Peng-Robinson-AGA procedure for phase prediction of condensates and natural-gas/crude-oil systems at reservoir conditions. New interaction coefficients were found necessary for methane and C//6** plus constituents so that experimental behavior could be matched by prediction. Steps for developing interaction parameters are presented. Then, agreement between measured and predicted phase behavior up to pressures of 64,121 kPa (9300 psia) is shown for several crude oil and condensate systems.

引用

页码：1649 / 1655

页数：7

共 26 条

[1] Azarnoosh A., 1963, J CHEM ENG DATA, V8, P494, DOI DOI 10.1021/JE60019A005
[2] Bergman D.F., 1975, RETROGRADE CONDENSAT
[3] BERGMAN DF, 1976, THESIS U MICHIGAN AN
[4] CAVETT RH, 1962, 27TH P API MID YEAR, V52, P351
[5] EVANS RB, 1956, IND ENG CHEM, V1, P45
[6] HOFFMANN AE, 1953, T AM I MIN MET ENG, V198, P1
[7] Vaporization equilibrium constants in a crude oil-natural gas system
Katz, DL
Hachmuth, KH
[J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1937, 29 : 1072 - 1077
[8] Kohn J.P., 1964, J CHEM ENG DATA, V9, P5, DOI DOI 10.1021/JE60020A003
[9] A New Two-Constant Equation of State
PENG, D
ROBINSON, DB
[J]. INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1976, 15 (01): : 59 - 64
[10] VAPOR-LIQUID EQUILIBRIUM IN N-HEXANE-NITROGEN SYSTEM
POSTON, RS
MCKETTA, JJ
[J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1966, 11 (03) : 364 - &

← 1 2 3 →