Effect of reactor geometry on aqueous ammonia-based carbon dioxide capture in bubble column reactors

被引:21
作者
Zhao, Bingtao [1 ]
Su, Yaxin [2 ]
Peng, Yuanchang [1 ]
机构
[1] Shanghai Univ Sci & Technol, Sch Energy & Power Engn, Shanghai 200093, Peoples R China
[2] Donghua Univ, Sch Environm Sci & Engn, Shanghai 201620, Peoples R China
基金
中国国家自然科学基金;
关键词
Carbon dioxide; Capture efficiency; Reactor geometry; Liquid height-to-diameter ratio; Aqueous ammonia; Bubble column reactor; CO2; GREENHOUSE-GAS; VAPOR-LIQUID-EQUILIBRIA; CO2-NH3-H2O SYSTEM; ABSORPTION; BICARBONATE; REMOVAL; NH3-CO2-H2O; SPECIATION; VLE;
D O I
10.1016/j.ijggc.2013.06.009
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Capture of carbon dioxide (CO2) from combustion flue gas by aqueous ammonia has been demonstrated as an effective and promising technology. To examine the effect of reactor geometry on ammonia-based CO2 capture performance, a series of bubble column reactors with same volume of working liquid but varied geometry (liquid height-to-diameter ratios H/D = 0.93, 2.04 and 3.98) were designed to investigate CO2 capture efficiency with ammonia under different reaction conditions. It is found that reactor geometry characterized by liquid height-to-diameter ratio plays an important role in CO2 capture efficiency as it is associated with gas holdup time in reactors. CO2 capture efficiency increases as liquid height-to-diameter ratio increases. Under the same experimental conditions, the maximum CO2 capture efficiency can increase by up to 7%. Besides, CO2 capture efficiency has positive correlation with the ammonia concentration and reaction temperature whereas has negative correlation with the CO2 inlet concentration and flue gas flowrate. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:481 / 487
页数:7
相关论文
共 61 条
[1]   Determination of Ammonium Salt/Ion Speciation in the CO2 Absorption Process Using Ammonia Solution: Modeling and Experimental Approaches [J].
Ahn, C. K. ;
Lee, H. W. ;
Lee, M. W. ;
Chang, Y. S. ;
Han, K. ;
Rhee, C. H. ;
Kim, J. Y. ;
Chun, H. D. ;
Park, J. M. .
10TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, 2011, 4 :541-547
[2]   Modeling of CO2 absorption in membrane contactors [J].
Al-Marzouqi, Mohamed H. ;
El-Naas, Muftah H. ;
Marzouk, Sayed A. M. ;
Al-Zarooni, Mohamed A. ;
Abdullatif, Nadia ;
Faiz, Rami .
SEPARATION AND PURIFICATION TECHNOLOGY, 2008, 59 (03) :286-293
[3]   Simulation of CO2 capture using MEA scrubbing:: a flowsheet decomposition method [J].
Alie, C ;
Backham, L ;
Croiset, E ;
Douglas, PL .
ENERGY CONVERSION AND MANAGEMENT, 2005, 46 (03) :475-487
[5]   Characterization and comparison of the CO2 absorption performance into single and blended alkanolamines in a packed column [J].
Aroonwilas, A ;
Veawab, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (09) :2228-2237
[6]   Removal of CO2 greenhouse gas by ammonia scrubbing [J].
Bai, HL ;
Yeh, AC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (06) :2490-2493
[7]   NH3-CO2-H2O VLE CALCULATION USING AN EXTENDED UNIQUAC EQUATION [J].
BERNARDIS, M ;
CARVOLI, G ;
DELOGU, P .
AICHE JOURNAL, 1989, 35 (02) :314-317
[8]  
Bollinger R., 2010, CCS PROJECT ALSTOMS, P1
[9]   AMMONIUM CARBAMATE [J].
BROOKS, LA ;
AUDRIETH, LF .
INORGANIC SYNTHESES, 1946, 2 :85-86
[10]  
Chen HP, 2007, PROCEEDINGS OF THE 6TH INTERNATIONAL SYMPOSIUM ON COAL COMBUSTION, P767