High-Temperature Removal of Hydrogen Sulfide over Mn2O3/γ-Al2O3 Sorbent

碩士 === 國立成功大學 === 環境工程學系碩博士班 === 90 === Most large-scale existing commercial coal-based IGCC plants use wet scrubbers to remove H2S, but there are too much heat losses in the process. Therefore, it is necessary to find out a feasible dry desulfurization process operating under high temperature to ra...

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Main Authors: Lung-Kai Chuang, 莊隆凱
Other Authors: Hsin Chu
Format: Others
Language:zh-TW
Published: 2002
Online Access:http://ndltd.ncl.edu.tw/handle/728p7u
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spelling ndltd-TW-090NCKU55150022018-06-25T06:05:08Z http://ndltd.ncl.edu.tw/handle/728p7u High-Temperature Removal of Hydrogen Sulfide over Mn2O3/γ-Al2O3 Sorbent 以Mn2O3/γ-Al2O3吸著劑高溫去除硫化氫之研究 Lung-Kai Chuang 莊隆凱 碩士 國立成功大學 環境工程學系碩博士班 90 Most large-scale existing commercial coal-based IGCC plants use wet scrubbers to remove H2S, but there are too much heat losses in the process. Therefore, it is necessary to find out a feasible dry desulfurization process operating under high temperature to raise the thermal efficiency and reduce the cost of the IGCC. Desulfurization of hot syngas using homemade Mn2O3/γ-Al2O3 sorbent in a fixed bed reactor was conducted in this study. The explanation of results can be divided into five major parts. 1.The Zinc based sorbent and Copper based sorbent have the highest sorbent utilization among all the metal oxide sorbents supported on the γ-Al2O3 that we have tested. 2.The Manganese based sorbent supported on γ-Al2O3 has higher sorbent utilization than that supported on SiO2 and the Manganese based sorbent supported on TiO2 has the worst performance. 3.The effects of operating factors, such as inlet temperature, space velocity, CO inlet concentration, H2 inlet concentration and H2S inlet concentration on the absorption of H2S were performed. The results show that the sorbent utilization increases with the inlet temperature and CO concentration, and decreases as the H2 concentration increases. H2S concentration and space velocity, however, don’t change the sorbent utilization significantly. 4.The activity of the sorbent decreases significantly while sulfuration is operating after regeneration. Some instruments were employed to determine the characteristics of the sorbents after regeneration, such as BET, EDX, XPS, and XRD. From the results of pore analyses, we infer that sintering happens during regeneration. EDX spectra show that sulfur still exists in the sorbent after regeneration and we find that the forms of sulfur existed in the sorbent are sulfate and sulfite from XPS spectra. The peaks relating to Manganese disappear and only γ-Al2O3 can be identified in the XRD spectra of regenerated sorbents. 5.In the operating range of this study, we can find that Deactivation model typeⅠ is the most suitable model to fit the experimental data. We obtain the activity energy Ea=86.9 KJ/mole. Hsin Chu 朱信 2002 學位論文 ; thesis 151 zh-TW
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language zh-TW
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description 碩士 === 國立成功大學 === 環境工程學系碩博士班 === 90 === Most large-scale existing commercial coal-based IGCC plants use wet scrubbers to remove H2S, but there are too much heat losses in the process. Therefore, it is necessary to find out a feasible dry desulfurization process operating under high temperature to raise the thermal efficiency and reduce the cost of the IGCC. Desulfurization of hot syngas using homemade Mn2O3/γ-Al2O3 sorbent in a fixed bed reactor was conducted in this study. The explanation of results can be divided into five major parts. 1.The Zinc based sorbent and Copper based sorbent have the highest sorbent utilization among all the metal oxide sorbents supported on the γ-Al2O3 that we have tested. 2.The Manganese based sorbent supported on γ-Al2O3 has higher sorbent utilization than that supported on SiO2 and the Manganese based sorbent supported on TiO2 has the worst performance. 3.The effects of operating factors, such as inlet temperature, space velocity, CO inlet concentration, H2 inlet concentration and H2S inlet concentration on the absorption of H2S were performed. The results show that the sorbent utilization increases with the inlet temperature and CO concentration, and decreases as the H2 concentration increases. H2S concentration and space velocity, however, don’t change the sorbent utilization significantly. 4.The activity of the sorbent decreases significantly while sulfuration is operating after regeneration. Some instruments were employed to determine the characteristics of the sorbents after regeneration, such as BET, EDX, XPS, and XRD. From the results of pore analyses, we infer that sintering happens during regeneration. EDX spectra show that sulfur still exists in the sorbent after regeneration and we find that the forms of sulfur existed in the sorbent are sulfate and sulfite from XPS spectra. The peaks relating to Manganese disappear and only γ-Al2O3 can be identified in the XRD spectra of regenerated sorbents. 5.In the operating range of this study, we can find that Deactivation model typeⅠ is the most suitable model to fit the experimental data. We obtain the activity energy Ea=86.9 KJ/mole.
author2 Hsin Chu
author_facet Hsin Chu
Lung-Kai Chuang
莊隆凱
author Lung-Kai Chuang
莊隆凱
spellingShingle Lung-Kai Chuang
莊隆凱
High-Temperature Removal of Hydrogen Sulfide over Mn2O3/γ-Al2O3 Sorbent
author_sort Lung-Kai Chuang
title High-Temperature Removal of Hydrogen Sulfide over Mn2O3/γ-Al2O3 Sorbent
title_short High-Temperature Removal of Hydrogen Sulfide over Mn2O3/γ-Al2O3 Sorbent
title_full High-Temperature Removal of Hydrogen Sulfide over Mn2O3/γ-Al2O3 Sorbent
title_fullStr High-Temperature Removal of Hydrogen Sulfide over Mn2O3/γ-Al2O3 Sorbent
title_full_unstemmed High-Temperature Removal of Hydrogen Sulfide over Mn2O3/γ-Al2O3 Sorbent
title_sort high-temperature removal of hydrogen sulfide over mn2o3/γ-al2o3 sorbent
publishDate 2002
url http://ndltd.ncl.edu.tw/handle/728p7u
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