研究生: |
鄭仲恩 Chung-En Cheng |
---|---|
論文名稱: |
以超重力技術自排放氣體中移除二氧化碳 Removal of Carbon Dioxide from Waste Air by Higee Process |
指導教授: |
談駿嵩
Chung-Sung Tan |
口試委員: | |
學位類別: |
碩士 Master |
系所名稱: |
工學院 - 化學工程學系 Department of Chemical Engineering |
論文出版年: | 2004 |
畢業學年度: | 92 |
語文別: | 中文 |
論文頁數: | 75 |
中文關鍵詞: | 二氧化碳 、旋轉床 、醇胺 、超重力 |
外文關鍵詞: | Carbon dioxide, Rotating Packed Bed, ethanolamine, higee |
相關次數: | 點閱:2 下載:0 |
分享至: |
查詢本校圖書館目錄 查詢臺灣博碩士論文知識加值系統 勘誤回報 |
摘 要
隨著對能源需求的增加及高度工業化,燃燒大量化石燃料的結果,使得CO2排放量大增,造成全球暖化的現象,對氣候變遷影響頗鉅。如何有效率地自排放氣中回收CO2一直是各國致力追求的方向。
有別於傳統利用填充塔吸收CO2的方式,本研究探討一種新發展的技術-Higee(High Gravity)Technology。Higee技術即是在高速旋轉床(Rotating Packed Bed, RPB)中,吸收液與CO2採Counter-Current的方式,進行化學吸收。
本研究使用PZ(Piperazine)、MEA(Monoethanolamine)、AMP(2-Amino-2-Methyl-1-Propanol)、MDEA(Methyldiethanolamine)等吸收劑,在不同的氣體流量、液體流量、吸收液種類、及吸收液比例等操作條件下,探討對CO2吸收效果的影響。實驗結果顯示當氣體流量為10 L/min,液體流量為90 cc/min,旋轉床轉速為1300 rpm時,無論單一成份的吸收劑(0.7M PZ),或混合吸收液(0.5M PZ+0.5M MEA)均可使高濃度的CO2(10% CO2 Vol%)出口濃度降至1%以下。
在低濃度CO2(1000 ppm Vol%)部分,當氣體流量為18 L/min,液體流量為20 cc/min,旋轉床轉速為1300 rpm時,總濃度為0.3M的0.2MPZ+0.1M MEA,在120 min的操作下,出口CO2的濃度可維持在50 ppm以下。
參考文獻
[1]. Adisorn, A.; Paitoon, T. High-Efficiency Strctured Packing for CO2 Separation Using 2-Amino-2-Methyl-1-Propanol (AMP). Separation and Purification Technology 1997, 12, 67.
[2]. Adisorn, A.; Amornvadee, V.; Paitoon, T. Behavior of the Mass-Transfer Coefficient of Structured Packings CO2 Absorbers with Chemical Reactions. Ind. Eng. Chem. Res. 1999, 38, 2044.
[3]. Adisorn, A.; Paitoon, T. Mass Transfer Coefficients and Correlation for CO2 Absorption into 2-Amino-2-Methyl-1-Propanol (AMP) Using Structured Packing. Ind. Eng. Chem. Res. 1998, 37, 569.
[4]. Amit, C. CO2 Capture Processes-Opportunities for Improved Energy Efficiencies. Energy Convers. Mgmt. 1997, 38, S51.
[5]. Browning, J. G.; Weiland, H. R. Physical Solubility of Carbon Dioxide in Aqueous Alkanolamines via Nitrous Oxide Analogy. J. Chem. Eng. Data, 1994, 39, 817.
[6]. Danckwerts, V. P. Gas-Liquid Reactions. McGraw-Hill, 1970.
[7]. Hydrocarbon Processing Gas Process Handbook. McGraw-Hill, 1990, 69.
[8]. Li, M. H.; Xiao, J.; Li, C. W. Kinetics of Absorption of Carbon Dioxide into Aqueous Solutions of 2-Amino-2-Methyl-1-Propanol + Monoethanolamine. Chem. Eng. Sci. 2000, 55, 161.
[9]. Li, M. H.; Liao, C. H. Kinetics of Absorption of Carbon Dioxide into Aqueous Solutions of Monoethanolamine + N-Methyldiethanolamine. Chem. Eng. Sci. 2002, 57, 4569.
[10]. Liu, H. S.; Lin, C. C.; Wu, S. C.; Hsu, S. W. Characteristics of a Rotating Packed Bed. Ind. Eng. Chem. Res. 1996, 35, 3590.
[11]. Liu, H. S.; Chen, Y. S. Absorption of VOCs in a Rotating Packed Bed. Ind. Eng. Chem. Res. 2002, 41, 1583.
[12]. Munjal, S.; Dudukovic, M. P.; Ramachandran, P. A. Mass Transfer in Rotating Packed Beds: I. Development of Gas-Liquid and Liquid-Solid Mass-Transfer Coefficients. Chem. Eng. Sci. 1989a, 44, 2245.
[13]. Paitoon, T.; Meisen, A.; Lim, C. J. CO2 Absorption by NaOH, Monoethanolamine and 2-Amino-2-Methyl-1-Propanol Solutions in a Packed Column, Chem. Eng. Sci. 1992, 47, 381.
[14]. Ramshaw, C.; Mallinson, R. H. Mass Transfer Process. U.S. Patent 4, 383, 255, 1981.
[15]. Reid, C. R.; Prausnitz, M. J.; Poling, E. B. The Properties of Gases and Liquids. McGraw Hill, 4th Edition 1988.
[16]. Rochelle, T. G.; Bishnoi, S. Absorption of Carbon Dioxide in Aqueous Piperazine/Methyldiethanolamine. AIChE Journal, 2002, 48, 2788.
[17]. Rochelle, T.G.; Dang, H. CO2 Absorption Rate and Solubility in Monoethanolamine/Piperazine/Water. Separation and Purification Technology, 2003, 38, 337.
[18]. Rochelle, T. G.; Bishnoi, S. Absorption of Carbon Dioxide into Aqueous Piperazine: Reaction Kinetics, Mass Transfer and Solubility. Chem. Eng. Sci. 2000, 55, 5531.
[19]. Tan, C. S.; Lin, C. C.; Liu, W. T. Removal of Carbon Dioxide by Absorption in a Rotating Packed Bed. Ind. Eng. Chem. Res. 2003, 42, 2381.
[20]. Trevour, K.; James, R. F. Distillation Studies in a High-Gravity Contactor. Ind. Eng. Chem. Res. 1996, 35, 4646.
[21]. Tung, H. H.; Mah, R. S. H. Modeling of Liquid Mass Transfer in HIGEE Separation Process. Chem. Eng. Commun. 1985, 39, 147.
[22]. Xu, S.; Wang, Y. W.; Frederick, O. D.; Alan, M. E. Rate of Absorption of CO2 in a Mixed Solvent. Ind. Eng. Chem. Res. 1991, 30, 1213.
[23]. Xu, Z.; Zhang, C. F.; Qin, S. J.; Zheng, Z. S. A Kinetics Study on the Absorption of Carbon Dioxide into a Mixed Aqueous Solution of Methyldiethanolamine and Piperazine. Ind. Eng. Chem. Res. 2001, 40, 3785.
[24]. 潘守保,以混合醇胺溶液(MEA+AMP)吸收二氧化碳溫室效應氣體之可行性研究,交通大學環境工程所碩士論文,民國87年
[25]. 曾映棠,化學溶劑吸收再生法回收廢氣中二氧化碳之溶劑使用成本分析,交通大學環境工程所碩士論文,民國91年。
[26]. 經濟部工業局,以吸收法回收二氧化碳之技術手冊,九十一年十一月。
[27]. 林佳璋;劉文宗,二氧化碳回收技術,工研院化工所。