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位阻胺混合甘氨酸盐溶液吸收CO_2的研究 被引量:4

Absorption of carbon dioxide with aqueous blends of 2-amino-2-methyl-1-propanol and sodium glycinate.
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摘要 在双搅拌反应釜中研究了位阻胺2-氨基-2-甲基-1-丙醇(AMP)与甘氨酸钠(SG)混合溶液吸收CO2的性能.实验温度293~313K,混合溶液的浓度为AMP(1.5kmol/m3)+SG(0.2,0.4,0.6,0.8kmol/m3),SG浓度每增加0.2kmol/m3,200min内的平均吸收速率分别提高11.47%,10.07%,9.18%和5.33%.与AMP单一溶液相比,混合溶液在200 min时的吸收容量增加了11.5%~41.1%.在293~313K,吸收速率随温度上升而提高.使用加热的方法进行再生实验,得到1.5 kmol/m3 AMP+0.6 kmol/m3 SG混合液的最适再生温度为378K.AMP+SG混合溶液的再生效率高于单一SG溶液及AMP+MEA/DEA混合溶液. The absorption of carbon dioxide into aqueous blends of 2-amino-2-methyl-1-propanol(AMP) and sodium glycinate(SG) was investigated from 293k to 313k in a double stirred-cell contactor.Five systems of which 1.5 kmol/m3AMP mixed with various SG concentrations(0.2,0.4,0.6 and 0.8 kmol/m3) were studied.The average CO2 absorption rates increased(11.47%,10.07%,9.18% and 5.33%) with an increase of SG concentrations(0.2 kmol/m3 SG at a time).Compared to 1.5 kmol/m3 AMP,the blends had an increase of absorption capacity of 11.5%~41.1% within 200 min.The absorption rates increased with an increase of temperature within the temperature range of 293k to 313k.The regenerating performance was also done by heating.The optimum regeneration temperature was 378 K for the mixture of 1.5 kmol/m3 AMP + 0.6 kmol/m3 SG.The aqueous blends of AMP + SG had a higher regenerating efficiency than either single SG or blends of AMP+MEA/DEA.
出处 《中国环境科学》 EI CAS CSCD 北大核心 2011年第5期729-733,共5页 China Environmental Science
基金 国家自然科学基金资助项目(20976159)
关键词 CO2 吸收 再生 2-氨基-2-甲基-1-丙醇(AMP) 甘氨酸钠(SG) carbon dioxidea bsorption regeneration 2-amino-2-methyl-1-propanol(AMP) sodium glycinate(SG)
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  • 1Sheng H L,Ching T S,1999.Performance characteristics and modeling of carbon dioxide absorption by amines in a packed column.Waste Manage,19:255-262.
  • 2Shi Y,Huang H,Chang S G,1997.Kinetic of NO absorption in aqueous Iron(Ⅱ) thiochelate solutions.Environ Prog,16:301-306.
  • 3Shi Y,Zhong Z T,2005.A rigorous model for absorption of carbon dioxide into aqueous N-methyldiethanolamine solution.Chem Eng Commun,192:1180-1193.
  • 4Winyu T,Amornvadee V,Bryce M,2006.Electrochemical investigation on the effect of heat-stable salts on corrosion in CO2 capture plants using aqueous solution of MEA.Ind Eng Chem Res,45:2586-2593.
  • 5Xu S,Wang Y W,Otto F D et al.,1995.Kinetics of the reaction of carbon dioxide with 2-amino-1-methyl-1-propanol solutions.Chem Eng Sci,51:841-850.
  • 6Yeh J T,Resnik K P,Rygle K et al.,2005.Semi-batch absorption and regeneration studies for CO2 capture by aqueous ammonia.Fuel Processing Technology,86:1533-1546.
  • 7Yoon S J,Lee H,Yoon J H et al.,2002.Kinetics of absorption of carbon dioxide into aqueous 2-amino-2-ethyl-1,3-propanediol solutions.Ind Eng Chem Res,41:3651-3656.
  • 8Zhang K,Hawrylak B,Papepu R et al.,2002.Thermodynamics of aqueous amines:excess molar heat capacities,volumes,and expansibilities of (water + methyldiethanolamine (MDEA)) and (water + 2-amino-2-methyl-1-propanol (AMP)).J Chem Thermodynamics,34:679-710.
  • 9Hook R J,1997.An investigation of some sterically hindered amines as potential carbon dioxide scrubbing compounds.Ind Eng Chem Res,36:1779-1790.
  • 10Huang H,Chang S G,2002.Method to regenerate ammonia for the capture of carbon dioxide.Energy & Fuels,16:904-910.

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