期刊文献+

磷石膏强化氨法CO_2捕集机理与模型 被引量:9

Mechanism and model of ammonia-based carbon dioxide trapping enhanced by gypsum particles
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摘要 基于化学活性颗粒强化气液吸收机理,建立了磷石膏悬浮液强化氨法烟气CO2捕集模型。以液膜内量纲一传质距离λ*为特征参数,增强因子2E1/λqβλ/2**=+。用恒温反应器在不同搅拌转速及磷石膏颗粒固含量下实验测定CO2吸收增强因子对模型进行检验,结果表明:随颗粒固含量由5%增加到30%(质量分数),增强因子由1.69增加到2.10;而随搅拌转速从150 r·min-1增加到300 r·min-1,增强因子仅由1.75略增到1.80,表明磷石膏颗粒固含量及溶解速率是影响增强因子的控制性因素。实验结果与模型预测值吻合良好,偏差小于10%。 Based on reaction plane theory, a mass transfer model of gas-liquid reaction absorption enhanced by reactive particles was established for the absorption of CO2 into aqueous ammonia suspension with gypsum particles. The absorption enhancement factor was derived theoretically as21//2E=λ-+qβλ-with the dimensionless reaction positionλ-as the characteristic parameter. The validation experiments of CO2 absorption into the suspension was carried out in a thermostatic reactor and the enhancement factors were measured with different solids loadings at selected speeds. The results showed that the enhancement factor increased from 1.69 to 2.10 when the solids loadings varied from 5% to 30% (mass); and it changed sparingly from 1.75 to 1.80 as the stirred speed varied from 150 to 300 r·min-1. It revealed that the enhancement factors were controlled by the solids loading and dissolution rate of gypsum particles. The experimental data agreed well with the model prediction, with a maximum deviation of 10%.
出处 《化工学报》 EI CAS CSCD 北大核心 2015年第8期3218-3224,共7页 CIESC Journal
基金 国家自然科学基金项目(21276161) 国家科技支撑计划课题(2013BAC12B01)~~
关键词 吸收 增强因子 传质 磷石膏颗粒 CO2矿化 absorption enhancement factor mass transfer gypsum particles CO2 mineralization
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  • 1Intergovernmental Panel on Climate Change, Working Group Ⅱ. Climate Change 2014: Impacts, Adaptation, and Vulnerability [R]. UN, 2014.
  • 2朱家骅,郭鑫楠,谢和平,夏素兰,梁斌,谢凌志,王子宁.CO_2减排CCS与CCU路线的热力学认识[J].四川大学学报(工程科学版),2013(5):1-7. 被引量:18
  • 3刘畅,陆小华.我国碳减排模式探讨——CCS路线与生物甲烷路线的比较[J].化工学报,2013,64(1):7-10. 被引量:17
  • 4Darde V, Maribo-Mogensen B, van Well W J M, et al. Process simulation of CO2 capture with aqueous ammonia using the extended UNIQUAC model [J]. International Journal of Greenhouse Gas Control, 2012, 10 (1): 74-87.
  • 5Hu Y, Naito S, Kobayashi N, et al. CO2, NOx and SO2 emissions from the combustion of coal with high oxygen concentration gases [J]. Fuel, 2000, 79 (15): 1925-1932.
  • 6Song K, Jang Y N, Kim W, et al. Factors affecting the precipitation of pure calcium carbonate during the direct aqueous carbonation of flue gas desulfurization gypsum [J]. Energy, 2014, 65 (1): 527-532.
  • 7Zhu Jiahua (朱家骅), Xie Heping (谢和平), Xia Sulan (夏素兰), et al. One step clean process to convert flue gas CO2 by phosphogypsum with low energy and water cost [P]: CN, 201210223218.4. 2014-10-15.
  • 8Wang T, Wang J, Jin Y. Slurry reactors for gas-to-liquid processes: a review [J]. Industrial & Engineering Chemistry Research, 2007, 46 (18): 5824-5847.
  • 9Dagaonkar M V, Beenackers A A, Pangarkar V G. Enhancement of gas-liquid mass transfer by small reactive particles at realistically high mass transfer coefficients: absorption of sulfur dioxide into aqueous slurries of Ca(OH)2 and Mg(OH)2 particles [J]. Chemical Engineering Journal, 2001, 81 (1): 203-212.
  • 10Bravo R, Camacho R, Moya V, García L. Desulphurization of SO2-N2 mixtures by limestone slurries [J]. Chemical Engineering Science, 2002, 57 (11): 2047-2058.

二级参考文献62

共引文献61

同被引文献105

  • 1徐国文,张成芳,钦淑均,朱炳辰.填料塔气液传质参数研究(Ⅱ)──气膜传质系数[J].化学工程,1996,24(1):19-21. 被引量:7
  • 2杨敏,钱觉时,王智,黄煜镔.杂质对磷石膏应用性能的影响[J].材料导报,2007,21(6):104-106. 被引量:79
  • 3王祖武,张承彪,李绍箕.三相流化床的流动特性预测[J].武汉水利电力大学学报,1997,30(2):89-93. 被引量:2
  • 4Gyu Lee,M.,et al.,Mineral carbonation of flue gas desulfurization gypsum for CO2 sequestration.Energy,2012.47(1):p.370-377.
  • 5Mathias P M,Ready S,O'Connell J P.Quantitative Evaluation of the Aqueous-Ammonia Process for CO2 Capture U-sing Fundamental Data and Thermodynamic Analysis[J].Energy Procedia,2009,1:1227-1234.
  • 6Zhu Jiahua(朱家骅),Xie Heping(谢和平),Xia Sulan(夏素兰),et al.One step clean process to convert flue gas CO2by phosphogypsum with low energy and water cost[P]:CN,201210223218.4.2014-10-15.
  • 7Mewes D.Mass Transfer with Chemical Reaction in Multiphase Systems,Vol.1:Two-phase Systems,Vol.2:Three-phase Systems.Herausgeg.von E.Alper.Martinus Nijhoff Publishers BV,Den Haag 1983.Vol.1:XI,679.
  • 8S.,zahlr.Abb.u.Tab.;Vol.2:X,399 S.,zahlr.Abb.u.Tab.,geb.,zus.$140,-.[J].Chemie Ingenieur Technik,1984,56(10):806-806.
  • 9陈毓琛,丁洁,沈自求.相际传质(三)填料塔相际面积的测定和传质模型的研究[J].化工学报,1984(4):294-302.
  • 10Tsai R E,Frank S A,Bruce E R,et al.A Dimensionless Model for Predicting the Mass-Transfer Area of Structured Packing[J].Aiche Journal,2011,57(5):1173-1184.

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