A water droplet size distribution dependent modeling of hydrate formation in water/oil emulsion

被引:50
|
作者
Lv, Yi-Ning [1 ,2 ]
Sun, Chang-Yu [1 ,2 ]
Liu, Bei [2 ]
Chen, Guang-Jin [2 ]
Gong, Jing [1 ]
机构
[1] China Univ Petr, Natl Engn Lab Pipeline Safety, MOE Key Lab Petr Engn, Beijing Key Lab Urban Oil & Gas Distribut Technol, Beijing 102249, Peoples R China
[2] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
基金
中国国家自然科学基金;
关键词
hydrates; mass transfer; particle measurements; mathematical modeling; reaction kinetics; IN-OIL EMULSION; REACTION-RATE CONSTANT; CARBON-DIOXIDE; MASS-TRANSFER; INTRINSIC KINETICS; ANTI-AGGLOMERANT; PARTICLE-SIZE; SHELL-MODEL; GAS; METHANE;
D O I
10.1002/aic.15436
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Experimental data on chord length distributions and growth rate during methane hydrate formation in water-in-oil emulsions were obtained in a high pressure stirring reactor using focused beam reflectance measurement and particle video microscope. The experiments were carried out at 274.2 K for 10-30% water cuts and agitation rates ranging from 200 to 500 rpm initially at 7.72 MPa. Rapid growth was accompanied by gradually decrease in rate. Free water was observed to become depleted during rapid growth while some water remained encapsulated inside hydrate layers constituting a mass transfer barrier. The apparent kinetic constants of methane hydrate formation and free-water fractions were determined using a newly developed kinetic model independent of the dissolution rate at the gas-oil interface. It was illustrated that continued growth depends on distribution and transfer of water in oil-dominated systems. This perception accords with observations of hydrate film growth on suspended water droplet in oil and clarifies transfer limits in kinetics. (c) 2016 American Institute of Chemical Engineers AIChE J, 63: 1010-1023, 2017
引用
收藏
页码:1010 / 1023
页数:14
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