Determination of the intrinsic rate of ethane gas hydrate decomposition

被引:150
作者
Clarke, M [1 ]
Bishnoi, PR [1 ]
机构
[1] Univ Calgary, Dept Chem & Petr Engn, Calgary, AB T2N 1N4, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
gas hydrates; kinetics; crystallisation; particulate; population balance;
D O I
10.1016/S0009-2509(00)00137-8
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The kinetics of ethane hydrate decomposition was studied using an isothermal/isobaric semibatch stirred-tank reactor. The experimental set-up and procedure used was similar to that used by Kim, Bishnoi, Heidemann and Rizvi (1987), Chemical Engineering Science, 42, (1645-1653) with one major modification; the addition of an on-line particle size analyser. The experiments were conducted at temperatures ranging from 274.15 to 281.15 K and at pressures between 5 and 11 bar. A new mathematical model is developed to determine the rate constant of decomposition. The model accounts for the distribution of particle sizes in the hydrate phase when determining the intrinsic rate constant of decomposition. The effect of the rate of stirring on the rate constant was also investigated to establish the regime where mass and heat transfer effects were negligible. The data were then obtained to determine the intrinsic rate constant. It was found that the activation energy for ethane hydrate decomposition is 104 kJ/mol and the intrinsic rate constant of decomposition is 2.56 x 10(8) mol/m(2) Pa s. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:4869 / 4883
页数:15
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