Mass transfer performance and correlations for CO2 absorption into aqueous blended of DEEA/MEA in a random packed column

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Bin Xu ◽  
Liang Han ◽  
Xiao Luo ◽  
Zhiwu Liang
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Author(s):  
Kaiyun Fu ◽  
Teerawat Sema ◽  
Zhiwu Liang ◽  
Helei Liu ◽  
Yanqing Na ◽  
...  

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pp. 16162-16162 ◽  
Author(s):  
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Zhiwu Liang ◽  
Helei Liu ◽  
Yanqing Na ◽  
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pp. 10788-10793 ◽  
Author(s):  
Miaopeng Sheng ◽  
Chenguang Liu ◽  
Chunyuan Ge ◽  
Moses Arowo ◽  
Yang Xiang ◽  
...  

2021 ◽  
Author(s):  
Sukanya Nakrak ◽  
Tarabordin Yurata ◽  
Benjapon Chalermsinsuwan ◽  
Paitoon Tontiwachwuthikul ◽  
Teerawat Sema

2019 ◽  
Vol 41 (5) ◽  
pp. 820-820
Author(s):  
Pongayi Ponnusamy Selvi and Rajoo Baskar Pongayi Ponnusamy Selvi and Rajoo Baskar

The acidic gas, Carbon dioxide (CO2) absorption in aqueous ammonia solvent was carried as an example for industrial gaseous treatment. The packed column was provided with a novel structured BX-DX packing material. The overall mass transfer coefficient was calculated from the absorption efficiency of the various runs. Due to the high solubility of CO2, mass transfer was shown to be mainly controlled by gas side transfer rates. The effects of different operating parameters on KGav including CO2 partial pressure, total gas flow rates, volume flow rate of aqueous ammonia solution, aqueous ammonia concentration, and reaction temperature were investigated. For a particular system and operating conditions structured packing provides higher mass transfer coefficient than that of commercial random packing.


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