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Dissociation behavior of (CH4 + C2H4) hydrate in the presence of sodium dodecyl sulfate
引用本文:Peng Baozi,Sun Changyu,Chen Guangjin,Tang Xulong,Liu Peng,Chen Jun,Zhang Yanqin. Dissociation behavior of (CH4 + C2H4) hydrate in the presence of sodium dodecyl sulfate[J]. 石油科学(英文版), 2010, 7(1): 112-117. DOI: 10.1007/s12182-010-0014-z
作者姓名:Peng Baozi  Sun Changyu  Chen Guangjin  Tang Xulong  Liu Peng  Chen Jun  Zhang Yanqin
作者单位:[1]State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China [2]High Pressure Fluid Phase Behavior & Property Research Laboratory, China University of Petroleum, Beijing 102249, China
基金项目:The financial support received from the National Nature Science Foundation of China,the National Basic Research Program of China (973 program),the Hi-Tech Research and Development Program of China,New Century Excellent Talents in University,National Science and Technology Major Projects,Foundation for the Authors of National Excellent Doctoral Dissertation of the People's Republic of China (No. 200447) is gratefully acknowledged 
摘    要:Separation of a mixture of CH4+C2H4 gas by forming hydrate in ethylene production has become of interest,and the dissociation behavior of(CH4+C2H4) hydrate is of great importance for this process. The hydrate formation rate could be increased by adding a small amount of sodium dodecyl sulfate(SDS) into water. In this work,the kinetic data of CH4(18.5 mol%) +C2H4(81.5 mol%) hydrate decomposition in the presence of 1000 mg·L-1 SDS at different temperatures and pressures were measured with the depressurizing m...

关 键 词:十二烷基硫酸钠  水合物形成  乙烯气体  分解行为  甲烷  混合气体水合物  动力学模型  离解
收稿时间:2009-05-26

Dissociation behavior of (CH4 + C2H4) hydrate in the presence of sodium dodecyl sulfate
Baozi Peng,Changyu Sun,Guangjin Chen,Xulong Tang,Peng Liu,Jun Chen,Yanqin Zhang. Dissociation behavior of (CH4 + C2H4) hydrate in the presence of sodium dodecyl sulfate[J]. Petroleum Science, 2010, 7(1): 112-117. DOI: 10.1007/s12182-010-0014-z
Authors:Baozi Peng  Changyu Sun  Guangjin Chen  Xulong Tang  Peng Liu  Jun Chen  Yanqin Zhang
Affiliation:1. State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China
2. High Pressure Fluid Phase Behavior & Property Research Laboratory, China University of Petroleum, Beijing 102249,China
Abstract:Separation of a mixture of CH4+C2H4 gas by forming hydrate in ethylene production has become of interest, and the dissociation behavior of (CH4+C2H4) hydrate is of great importance for this process. The hydrate formation rate could be increased by adding a small amount of sodium dodecyl sulfate (SDS) into water. In this work, the kinetic data of CH4(18.5 mol%)+C2H4(81.5 mol%) hydrate decomposition in the presence of 1000 mg·L−1 SDS at different temperatures and pressures were measured with the depressurizing method using a sapphire cell apparatus. The experimental results show that the dissociation rate of (CH4+C2H4) mixed gas hydrate was large at high temperature and low pressure, and temperature had great influence on the dissociation rate at high pressure. A kinetic model for hydrate dissociation was proposed and the calculated results from the kinetic model were in good agreement with the experimental data. The activation energy for dissociation of the (CH4+C2H4) mixed gas hydrate was determined to be 43.9 kJ·mol−1, which is lower than that of methane (81.0 kJ·mol−1) and ethane (104.0 kJ·mol−1) hydrate in water (Clarke and Bishnoi, 2004). As the similar molecular dimensions between ethane and ethylene, the close activation energy need to be provided for ethylene hydrate dissociation. The obtained activation energy of the (CH4+C2H4) mixed gas hydrate dissociation indicates that the dissociation of the (CH4+C2H4) mixed gas hydrate is easier than that of pure CH4 or C2H4 gas hydrate.
Keywords:Methane  ethylene  hydrate  dissociation  SDS
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