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MA水溶液吸收CO2的实验研究

高升 刘学军 王广全 李育敏 艾宁 吴杰 计建炳

天然气化工2011,Vol.36Issue(6):8-10,24,4.
天然气化工2011,Vol.36Issue(6):8-10,24,4.

MA水溶液吸收CO2的实验研究

Study on absorption of carbon dioxide in MA aqueous solution

高升 1刘学军 1王广全 1李育敏 1艾宁 1吴杰 1计建炳1

作者信息

  • 1. 浙江工业大学化学工程与材料学院,浙江杭州310014
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摘要

Abstract

Absorption of carbon dioxide in MA (a mixture of MDEA and the hindered amine) aqueous solution was studied in a packed column filled with triangular spiral packing. The influences of experimental conditions including MA concentration, absorption temperature and flow rates of absorbent and feed gas on absorption rate of carbon dioxide were investigated. The results showed that the absorption rate of carbon dioxide reached 0.01028mol'm'2-s"' under the conditions of MA mass fraction of 40% in absorbent solution, absorption temperature of 40^, absorbent solution flow rate of lOL/h and feed gas flow rate of 80L/h, and the volume fraction of carbon dioxide in feed gas decreased to 0.1% from 35%.

关键词

MA/N-甲基二乙醇胺/二氧化碳脱除/沼气净化

Key words

MA/ MDEA/ carbon dioxide removal/ biogas purification

分类

化学化工

引用本文复制引用

高升,刘学军,王广全,李育敏,艾宁,吴杰,计建炳..MA水溶液吸收CO2的实验研究[J].天然气化工,2011,36(6):8-10,24,4.

基金项目

浙江省自然科学基金资助项目(Y4110364) (Y4110364)

天然气化工

OA北大核心CSCDCSTPCD

1001-9219

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