Joule-Thomson expansion of high-pressure-high-temperature gas condensates

被引:34
作者
Kortekaas, WG [1 ]
Peters, CJ [1 ]
Arons, JD [1 ]
机构
[1] Delft Univ Technol, Fac Chem Technol & Mat Sci, Lab Appl Thermodynam & Phase Equilibria, NL-2628 BL Delft, Netherlands
关键词
model; equation of state; enthalpy; method of calculation; application;
D O I
10.1016/S0378-3812(97)00183-0
中图分类号
O414.1 [热力学];
学科分类号
摘要
This paper presents calculations of Joule-Thomson inversion effects in high-pressure-high-temperature gas condensates. Isenthalpic expansions were modelled for several gas condensate mixtures reported in literature using the Soave-Redlich-Kwong and the Peng-Robinson equations of state. The calculations confirmed qualitatively the heating of gas condensates at expansion. Although reservoir temperatures are in the region where cooling occurs, i.e., inside the inversion curve, it was shown that reservoir pressures lie outside this region, and that the temperature will increase until the inversion curve is reached. The calculated temperature increases are not very large. Although exact values depend on fluid composition, reservoir conditions, and pressure drop, typical calculated temperature increases are in the range of 10-30 degrees C for reservoir pressures of 1000 bar. A sensitivity study showed that both reservoir pressure and fluid composition greatly affect the temperature increase. With increasing pressures and increasing amounts of heavy constituents present in gas condensate mixtures, the maximum possible temperature effect will also increase. Unfortunately, due to lack of experimental information, the calculated results could not be verified on their reliability. (C) 1997 Elsevier Science B.V.
引用
收藏
页码:205 / 218
页数:14
相关论文
共 29 条
[1]   PREDICTION OF THERMODYNAMIC PROPERTIES OF OIL AND GAS CONDENSATE MIXTURES [J].
AASBERGPETERSEN, K ;
STENBY, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (01) :248-254
[2]   VERSATILE ALGORITHM FOR CALCULATING VAPOR-LIQUID-EQUILIBRIA [J].
ASSELINEAU, L ;
BOGDANIC, G ;
VIDAL, J .
FLUID PHASE EQUILIBRIA, 1979, 3 (04) :273-290
[3]  
BAKER AC, 1990, SPE EUR PETR C 21 24, P217
[4]  
CAVETT RH, 1964, API DIVISION REFININ
[5]   The Joule Thomson inversion curves of recent equations of state. [J].
Corner, J .
TRANSACTIONS OF THE FARADAY SOCIETY, 1939, 35 (01) :0784-0791
[6]   CALCULATION OF JOULE-THOMSON INVERSION CURVES FROM EQUATIONS OF STATE [J].
DILAY, GW ;
HEIDEMANN, RA .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1986, 25 (01) :152-158
[7]  
EDMINSTER WC, 1988, APPL HYDROCARBON THE, V2
[8]  
Fredenslund Aa., 1988, AICHE SPRING NAT M N
[9]   CALCULATION OF JOULE-THOMSON INVERSION CURVES FROM A GENERAL CUBIC EQUATION OF STATE [J].
GEANA, D ;
FEROIU, V .
FLUID PHASE EQUILIBRIA, 1992, 77 :121-132
[10]   INVERSION TEMPERATURES AND PRESSURES FOR CRYOGENIC GASES AND THEIR MIXTURES [J].
GUNN, RD ;
CHUEH, PL ;
PRAUSNITZ, JM .
CRYOGENICS, 1966, 6 (06) :324-+