[1] SLOAN E D.Clathrate hydrates of natural gases[M].3th ed.New York:Marcel Dekker,2007.[2] 樊栓狮.天然气水合物储存与运输技术[M].北京:化学工业出版社,2005.[3] 陈光进,孙长宇,马庆兰.气体水合物科学与技术[M].北京:化学工业出版社,2008.[4] SEOL Y,MYSHAKIN E.Experimental and numerical observations of hydrate reformation during depressurization in a core-scale reactor[J].Energy&Fuels,2011,25(3):1099-1110.[5] LEE J,PARK S,SUNG W.An experimental study on the productivity of dissociated gas from gas hydrate by depressurization scheme[J].Energy Conversion and Management,2010,51(12):2510-2515.[6] HE S,LIANG D Q,LI D L,et al.Decomposition characteristics of ethane hydrate and propane hydrate by microwave heating[J].Acta Phys.Chim.Sin.,2010,26(6):1473-1480.[7] YANG X,SUN C Y,YUAN Q,et al.Experimental study on gas production from methane hydrate-bearing sand by hot-water cyclic injection[J].Energy&Fuels,2010,24:5912-5920.[8] YUAN Q,SUN CY,YANG X,et al.Gas production from methane-hydrate-bearing sands by ethylene glycol injection using a three-dimensional reactor[J].Energy&Fuels,2011,25(7):3108-3115.[9] 宋光春,李玉星,王武昌.温度和压力对CO2置换甲烷水合物的影响[J].油气储运,2016,35(3):295-301.[10] KAWAMURA T,OHTAKE M,YAMAMOTO Y,et al.Dissociation behavior of hydrate core sample using thermodynamic inhibitor——part 3.Inhibitor or steam injection combined with depressurization and high-concentration inhibitor injection[J].Int.J.Offshore Polar Eng.,2010,20(2):125-131.[11] 李淑霞,李杰,靳玉容.不同饱和度的天然气水合物降压分解实验[J].化工学报,2014,65(4):1411-1415.[12] 李淑霞,李杰,徐新华,等.天然气水合物藏注热水开采敏感因素试验研究[J].中国石油大学学报(自然科学版),2014,38(2):99-102.[13] 吴西顺,张百忍,张炜,等.天然气水合物开采技术进展[J].新能源进展,2015,3(3):218-225.[14] 孙志高,郭开华,王如竹,等.甲烷水合物形成促进技术实验研究[J].工程热物理学报,2005,26(2):205-207.[15] FAN S S,LIANG D Q,GUO K H.Hydrate equilibrium conditions for cyclopentane and a quaternary cyclopentane-rich mixture[J].Journal of Chemical and Engineering Data,2001,46:930-932.[16] TAKEYA S,OHMURA R.Phase equilibrium for structure Ⅱ hydrates formed with krypton co-existing with cyclopentane,cyclopentene,or tetrahydropyran[J].Journal of Chemical and Engineering Data,2006,51(5):1880-1883.[17] ZHONG D L, DING K,YAN J,et al.Influence of cyclopentane and SDS on methane separation from coal mine gas by hydrate crystallization[J].Energy&Fuels,2013,27:7252-7258.[18] ZHONG D L,DARABOINA N,ENGLEZOS P.Recovery of CH4 from coal mine model gas mixture (CH4/N2) by hydrate crystallization in the presence of cyclopentane[J].Fuel,2013,106:425-430.[19] CAI L C,PETHICAL B A,DEBENEDETTI P G,et al.Formation of cyclopentane methane binary clathrate hydrate in brine solutions[J].Chem.Eng.Sci.,2016,141:125-132.[20] HASHEMI S,MACCHI A,SERVIO P.Gas-liquid mass transfer in a slurry bubble column operated at gas hydrate forming conditions[J].Chem.Eng.Sci.,2009,64(16):3709-3716.[21] 王东雷,李栋梁,梁德清,等.甲烷-叔丁胺-水体系中水合物的生成过程[J].过程工程学报,2008,8(2):274-279.[22] YANG D,LE L A,MARTINEZ R J,et al.Heat transfer during CO2 hydrate formation in a continuous flow reactor[J].Energy&Fuel,2008,22(4):2649-2659.[23] 罗艳托,朱建华,陈光进.甲烷-四氢呋喃-水体系水合物生成动力学的实验和模型化研究[J].化工学报,2006,57(5):1153-1158.[24] LUO X,LEE D J,LAU R,et al.Maximum stable bubble size and gas holdup in high-pressure slurry bubble columns[J].AIChE Journal,1999,45(4):665-680.[25] TAKAHASHI M,KAWAMURA T,YAMAMOTO T,et al.Effect of shrinking microbubble on gas hydrate formation[J].J.Phys.Chem.B,2003,107(10):2171-2173.[26] 罗艳托,朱建华,陈光进.鼓泡塔中甲烷水合物生成现象的观测[J].石油学报,2006,22(1):84-89. |