A comparison between packed beds and rotating packed beds for CO2 capture using monoethanolamine and dilute aqueous ammonia solutions
暂无分享,去创建一个
[1] Shi-Shang Jang,et al. Aspen Plus rate-based modeling for reconciling laboratory scale and pilot scale CO2 absorption using aqueous ammonia , 2015 .
[2] Bingtao Zhao,et al. Mass transfer performance of CO2 capture in rotating packed bed: Dimensionless modeling and intelligent prediction , 2014 .
[3] Morteza Afkhamipour,et al. Sensitivity analysis of the rate-based CO2 absorber model using amine solutions (MEA, MDEA and AMP) in packed columns , 2014 .
[4] David Shan-Hill Wong,et al. Modeling studies on absorption of CO2 by monoethanolamine in rotating packed bed , 2014 .
[5] Filip Johnsson,et al. The Rate of CO2 Absorption in Ammonia—Implications on Absorber Design , 2014 .
[6] C. Ramshaw,et al. Process analysis of intensified absorber for post-combustion CO2 capture through modelling and simulation , 2014 .
[7] Jialin Liu,et al. Experiment and Modeling Studies on Absorption of CO2 by Dilute Ammonia in Rotating Packed Bed , 2014 .
[8] Thijs J. H. Vlugt,et al. Predicting Aerosol Based Emissions in a Post Combustion CO2 Capture Process Using an Aspen Plus Model , 2014 .
[9] Masoud Mofarahi,et al. Comparison of rate-based and equilibrium-stage models of a packed column for post-combustion CO2 capture using 2-amino-2-methyl-1-propanol (AMP) solution , 2013 .
[10] Chih-Hung Huang,et al. A Review of CO2 Capture by Absorption and Adsorption , 2012 .
[11] Chung-Sung Tan,et al. CO2 capture by alkanolamine solutions containing diethylenetriamine and piperazine in a rotating packed bed , 2012 .
[12] Chau-Chyun Chen,et al. New mass-transfer correlations for packed towers , 2012 .
[13] Ying Zhang,et al. Thermodynamic modeling for CO2 absorption in aqueous MEA solution with electrolyte NRTL model , 2011 .
[14] Chau-Chyun Chen,et al. Thermodynamic Modeling of the NH3–CO2–H2O System with Electrolyte NRTL Model , 2011 .
[15] Hai Yu,et al. Results from trialling aqueous NH3 based post-combustion capture in a pilot plant at Munmorah power station: Absorption , 2011 .
[16] D. V. Krevelen,et al. Kinetics of gas‐liquid reactions part I. General theory , 2010 .
[17] Chung-Sung Tan,et al. CO2 capture from hot stove gas in steel making process , 2010 .
[18] Graeme Puxty,et al. Comparison of the rate of CO2 absorption into aqueous ammonia and monoethanolamine , 2010 .
[19] Meihong Wang,et al. Dynamic modelling of CO2 absorption for post combustion capture in coal-fired power plants , 2009 .
[20] Jianfeng Chen,et al. Simultaneous Absorption of CO2 and NH3 into Water in a Rotating Packed Bed , 2009 .
[21] Gary T. Rochelle,et al. Amine Scrubbing for CO2 Capture , 2009, Science.
[22] Chung-Sung Tan,et al. Carbon dioxide capture by blended alkanolamines in rotating packed bed , 2009 .
[23] E. Stenby,et al. Chilled ammonia process for CO2 capture , 2009 .
[24] Gary T. Rochelle,et al. Effects of the Temperature Bulge in CO2 Absorption from Flue Gas by Aqueous Monoethanolamine , 2008 .
[25] R. B. Slimane,et al. Progress in carbon dioxide separation and capture: a review. , 2008, Journal of environmental sciences.
[26] Colin Ramshaw,et al. Carbon dioxide absorption and desorption in aqueous monoethanolamine solutions in a rotating packed bed , 2007 .
[27] G. Versteeg,et al. CO2 capture from power plants. Part I: A parametric study of the technical performance based on monoethanolamine , 2007 .
[28] Chung-Sung Tan,et al. Reduction of CO2 concentration in a zinc/air battery by absorption in a rotating packed bed , 2006 .
[29] Chung-Sung Tan,et al. Absorption of carbon dioxide with piperazine and its mixtures in a rotating packed bed , 2006 .
[30] Eric Croiset,et al. Techno-economic study of CO2 capture from an existing coal-fired power plant: MEA scrubbing vs. O2/CO2 recycle combustion , 2003 .
[31] Chia-Chang Lin,et al. Removal of carbon dioxide by absorption in a rotating packed bed , 2003 .
[32] Colin Ramshaw,et al. Process intensification: operating characteristics of rotating packed beds - determination of liquid hold-up for a high-voidage structured packing , 2000 .
[33] R. Billet,et al. Prediction of Mass Transfer Columns with Dumped and Arranged Packings , 1999 .
[34] Geert Versteeg,et al. ON THE KINETICS BETWEEN CO2 AND ALKANOLAMINES BOTH IN AQUEOUS AND NON-AQUEOUS SOLUTIONS. AN OVERVIEW , 1996 .
[35] M. J. Lockett,et al. Flooding of rotating structured packing and its application to conventional packed columns : Distillation , 1995 .
[36] R. A. Ashworth,et al. Removal of volatile organic compounds from groundwater using a rotary air stripper , 1992 .
[37] James R. Fair,et al. General model for prediction of pressure drop and capacity of countercurrent gas/liquid packed columns , 1989 .
[38] Richard S.H. Mah,et al. MODELING LIQUID MASS TRANSFER IN HIGEE SEPARATION PROCESS , 1985 .
[39] Hiroshi Takeuchi,et al. MASS TRANSFER COEFFICIENTS BETWEEN GAS AND LIQUID PHASES IN PACKED COLUMNS , 1968 .
[40] L. Pearson,et al. The kinetics of combination of carbon dioxide with ammonia , 1956 .