The Editorial Committee of Offshore Oil Engineering Design Guide(海洋石油工程设计指南编委会).Design Introduction and Process Design of Offshore Oil Engineering:1st volume(海洋石油工程设计概论与工艺设计:第一册)[M].Beijing:Petroleum Industry Press,2007:100.
[2]
Gu Anzhong(顾安忠).Natural Gas Liquefaction Technology(液化天然气技术)[M].Beijing:China Machine Press,2004.
[3]
Chang H,Chung M J,Park S B.Cryogenic heat-exchanger design for freeze-out removal of carbon dioxide from landfill gas[J].J.Therm.Sci. & Tech.,2009,4:362-371.
[4]
Eggman T,Chafin S.Beware the pitfalls of CO2 freezing prediction[J].Chem.Eng.Prog.,2005,101:39-44.
[5]
Pikaar M J.A study of phase equilibrium in hydrocarbon-CO2 systems[D].London:Department of Chemical Engineering,Imperical College of Science and Techno-logy,1959.
[6]
Agrawal G M,Laverman R J.Phase behavior of the methane carbon dioxide system in the solid-vapor region[J].Adv.Cryo.Eng.,1974, 19:327-338.
[7]
Zhang Longman,Burgass R,Chapoy A,Tohidi B,Solbraa E.Measurement and modeling of CO2 frost points in the CO2-methane systems[J].J.Chem.Eng.Data,2011,56(6):2971-2975
[8]
Le T T,Trebble M A.Measurement of carbon dioxide free-zing in mixtures of methane,ethane,and nitrogen in the solid-vapor equilibrium region[J].J.Chem.Eng.Data,2007,52(3):683-686.
[9]
ZareNezhad B,Eggeman T.Application of Peng-Rabinson equation of state for CO2 freezing prediction of hydrocarbon mixtures at cryogenic conditions of gas plants[J].Cryogenics,2006,46:840-845.
[10]
Xiong Xiaojun(熊晓俊),Lin Wensheng(林文胜),Gu Anzhong(顾安忠).Prediction of CO2 frosting temperature in CH4-CO2 binary system[J].Chem.Eng.Oil & Gas(石油与天然气化工),2012,(2):176-178.
[11]
Jiang Hong(蒋洪),He Yuxin(何愈歆),Zhu Cong(朱聪).Prediction of solid CO2 formation condition in CH4-CO2 system[J].Nat.Gas Ind.(天然气工业),2011,31(9):112-115.
[12]
Peng Dingyu,Robinson D B.A new tow-constant equation of state[J].Ind.Eng.Chem.Fundam.,1976,15:59-64.
[13]
Kwak T Y,Mansoori G A.van der Waals mixing rules for cubic equations of state.Applications for supercritical fluid extraction modeling[J].Chem.Eng.Sci.,1986,41(5):1303-1309.
[14]
Kidnay A J,Miller R C,Parrish W R,Hiza M J.Liquid-vapor phase equilibrium in the N2-CH4 system from 130 to 180 K[J].Cryogenics,1975,15(9):531-540.
[15]
Mazzoccoli M,Bosio B,Arato E,Brandani S.Comparison of equations-of-state with p-ρ-T experimental data of binary mixtures rich in CO2 under the conditions of pipeline transport[J].J.Supercrit.Fluids,2014,95:474-490.
[16]
Kordas A,Tsoutsouras K,Stamataki S,Tassios D.A gen-eralized correlation for the interaction coefficients of CO2-hydrocarbon binary mixtures[J].Fluid Phase Equilib.,1994,93:141-166.
[17]
Bian Xiaoqiang,Du Zhimin,Tang Yong.Experimental de-termination and prediction of the compressibility factor of high CO2 content natural gas with and without water vapor[J].J.Nat.Gas Chem.,2011,20:364-371.
[18]
Gao Ting,Lin Wensheng,Gu Anzhong,Gu Min.Coalbed methane liquefaction adopting a nitrogen expansion process with propane pre-cooling[J].Appl.Energy,2010,87:2142-2147.
[19]
Aspelund A,Gundersen T,Myklebust J,Nowak M P,Tomasgard A.An optimization-simulation model for a simple LNG process[J].Comp.Chem.Eng.,2010,34:1606-1617.
[20]
Hu Xiaochen(胡晓晨),Gao Ting(高婷),Lin Wensheng(林文胜).Preliminary research on CO2 freeze-out in PLNG process[J].Cryo.& Supercond.(低温与超导),2009,37(6):15-18.
[21]
Xiong Xiaojun,Lin Wensheng,Jia R,Song Yang.Mea-surement and calculation of CO2 frost data in CH4+CO2/CH4+CO2+N2/CH4+CO2+C2H6 mixtures at low temperatures[J]. J.Chem.Eng.Data,(in press).