接触器
传质
传质系数
气泡
鼓泡塔反应器
水溶液
化学
工作(物理)
吸收(声学)
分析化学(期刊)
二氧化碳
色谱法
化学工程
热力学
材料科学
气泡
机械
有机化学
复合材料
功率(物理)
物理
工程类
作者
José M. Navaza,Diego Gómez‐Díaz,M. Dolores La Rubia
标识
DOI:10.1016/j.cej.2008.04.040
摘要
Present work analyses the behaviour and mass transfer of N-methyldiethanolamine (MDEA) in the removal process of carbon dioxide using a bubble column reactor (BCR) as gas–liquid contactor. The use of this type of equipment requires the interfacial area determination for the following mass transfer coefficient calculation based on absorption kinetics. In this work, a photographic method based on the bubble diameter determination, has been employed. The effect of contactor, operation conditions, liquid-phase nature and chemical reaction upon the mass transfer coefficient and interfacial areas have been analysed.
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