Modeling Rotating Packed Bed on Absorption of CO2 by Aqueous Amines and Ammonia Solutions

博士 === 國立清華大學 === 化學工程學系 === 105 === The contributions of this dissertation are listed as following: • Developed a model of the carbon dioxide absorption by monoethanolamine and dilute ammonia solutions in a rotating packed bed based on two-film theory. • Found out that temperature bulge can b...

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Main Authors: KANG,JIA-LIN, 康嘉麟
Other Authors: Jang,Shi-Shang
Format: Others
Language:en_US
Published: 2016
Online Access:http://ndltd.ncl.edu.tw/handle/8raac8
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spelling ndltd-TW-105NTHU50630022019-05-15T23:00:46Z http://ndltd.ncl.edu.tw/handle/8raac8 Modeling Rotating Packed Bed on Absorption of CO2 by Aqueous Amines and Ammonia Solutions 醇胺與氨水溶液之超重力旋轉床建模應用於 二氧化碳吸收製程 KANG,JIA-LIN 康嘉麟 博士 國立清華大學 化學工程學系 105 The contributions of this dissertation are listed as following: • Developed a model of the carbon dioxide absorption by monoethanolamine and dilute ammonia solutions in a rotating packed bed based on two-film theory. • Found out that temperature bulge can be found in the rotating packed bed when a large amount of carbon dioxide was removed. • Found out that use of a modified expression for the apparent kinetic constant in the enhancement factor is necessary to predict experiment results using high amine concentrations. • Compared to the traditional packed bed and rotating packed bed by models for different throughput rates, ranging from bench scale to industrial scale. • Found out that the apparent intensification effect of the rotating packed bed is more significant for ammonia than for monoethanolamine solution because of the different operating of CO2 loading. • Found out that the Height of a Transfer Unit is inappropriate to be an indicator for intensification effect of volume. Jang,Shi-Shang 鄭西顯 2016 學位論文 ; thesis 133 en_US
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language en_US
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description 博士 === 國立清華大學 === 化學工程學系 === 105 === The contributions of this dissertation are listed as following: • Developed a model of the carbon dioxide absorption by monoethanolamine and dilute ammonia solutions in a rotating packed bed based on two-film theory. • Found out that temperature bulge can be found in the rotating packed bed when a large amount of carbon dioxide was removed. • Found out that use of a modified expression for the apparent kinetic constant in the enhancement factor is necessary to predict experiment results using high amine concentrations. • Compared to the traditional packed bed and rotating packed bed by models for different throughput rates, ranging from bench scale to industrial scale. • Found out that the apparent intensification effect of the rotating packed bed is more significant for ammonia than for monoethanolamine solution because of the different operating of CO2 loading. • Found out that the Height of a Transfer Unit is inappropriate to be an indicator for intensification effect of volume.
author2 Jang,Shi-Shang
author_facet Jang,Shi-Shang
KANG,JIA-LIN
康嘉麟
author KANG,JIA-LIN
康嘉麟
spellingShingle KANG,JIA-LIN
康嘉麟
Modeling Rotating Packed Bed on Absorption of CO2 by Aqueous Amines and Ammonia Solutions
author_sort KANG,JIA-LIN
title Modeling Rotating Packed Bed on Absorption of CO2 by Aqueous Amines and Ammonia Solutions
title_short Modeling Rotating Packed Bed on Absorption of CO2 by Aqueous Amines and Ammonia Solutions
title_full Modeling Rotating Packed Bed on Absorption of CO2 by Aqueous Amines and Ammonia Solutions
title_fullStr Modeling Rotating Packed Bed on Absorption of CO2 by Aqueous Amines and Ammonia Solutions
title_full_unstemmed Modeling Rotating Packed Bed on Absorption of CO2 by Aqueous Amines and Ammonia Solutions
title_sort modeling rotating packed bed on absorption of co2 by aqueous amines and ammonia solutions
publishDate 2016
url http://ndltd.ncl.edu.tw/handle/8raac8
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