Characteristics of CO2 absorption by N,N-dimethylethanolamine (DMEA) in hollow fiber membrane contactor

被引:0
|
作者
Wu J. [1 ]
Pan Z. [1 ]
Shang L. [2 ]
Sun X. [2 ]
Sun C. [3 ]
Sun X. [2 ]
机构
[1] College of Petroleum Engineering, Liaoning Petrochemical University, Fushun
[2] School of Environmental & Safety Engineering, Liaoning Petrochemical University, Fushun
[3] China Petroleum Pipeline Engineering Co., Ltd., Langfang
[4] Fushun Special Equipment Supervision and Inspection Institute, Fushun
关键词
CO[!sub]2[!/sub] capture; DMEA; Mass transfer; Membrane contactor; Numerical simulation;
D O I
10.16085/j.issn.1000-6613.2021-0757
中图分类号
学科分类号
摘要
N,N-dimethylethanolamine (DMEA) is a promising absorbent because of its fast reaction rate and high CO2 trapping ability. In this study, DMEA, as a new type of absorbent, was used in hollow fiber membrane contactors to separate CO2 from CO2/CH4 gas mixtures. A two-dimensional steady-state mathematical model was established to simulate the effects of MEA (monoethanolamine), DEA (diethanolamine), MDEA (N-methyldiethanolamine) and DMEA on the absorption properties of CO2 under different operating conditions. The results showed that the decarbonization performance was MEA>DMEA>DEA>MDEA, the effect of gas phase parameters on decarbonization rate was more significant than liquid phase parameters, the decarbonization rate decreased with the increase of gas flow rate and CO2 concentration, the decarbonization rate increased with the increase of liquid velocity and absorbent concentration, and the removal efficiency of CO2 can be improved by properly increasing absorbent flow rate and absorbent concentration. In addition, the CO2 absorption flux will increase with the increase of gas velocity and decrease with the increase of CO2 load in the liquid phase. Finally, through the joint action of two influencing factors, the best operating conditions of membrane contactor for acid gas separation were determined. Therefore, membrane absorption had good potential in natural gas decarbonization. © 2022, Chemical Industry Press Co., Ltd. All right reserved.
引用
下载
收藏
页码:2132 / 2139
页数:7
相关论文
共 33 条
  • [21] LU Shijian, LI Qingfang, ZHANG Jian, Overview of CO<sub>2</sub> absorption with organic amines solution and reaction theory, Science and Technology Innovation Herald, 6, 13, pp. 4-5, (2009)
  • [22] MANEEINTR K, LUEMUNKONG T, CHARINPANITKUL T., Vapor-liquid equilibrium of carbon dioxide in a 5m aqueous solution of 2-(dimethylamino) ethanol, Computers and Advanced Technology in Education/820: Modelling, Simulation and Identification/821: Environmental Management and Engineering, pp. 148-151, (2014)
  • [23] ZHANG N, PAN Z, ZHANG L, Et al., Decarburization characteristics of coalbed methane by membrane separation technology, Fuel, 242, pp. 470-478, (2019)
  • [24] SUN Chenggui, CAO Yiming, Xingming JIE, Et al., Mass transfer mechanism of CO<sub>2</sub> absorption through a non-porous hollow fiber contactor, Journal of Chemical Engineering of Chinese Universities, 21, 4, pp. 556-562, (2007)
  • [25] NWAOHA C, TONTIWACHWUTHIKUL P, BENAMOR A., CO<sub>2</sub> capture from water-gas shift process plant: comparative bench-scale pilot plant investigation of MDEA-PZ blend vs novel MDEA activated by 1,5-diamino-2-methylpentane, International Journal of Greenhouse Gas Control, 82, pp. 218-228, (2019)
  • [26] FAIZ R, AL-MARZOUQI M., Mathematical modeling for the simultaneous absorption of CO<sub>2</sub> and H<sub>2</sub>S using MEA in hollow fiber membrane contactors, Journal of Membrane Science, 342, 1, pp. 269-278, (2009)
  • [27] YAN Y F, ZHANG Z E, ZHANG L, Et al., Dynamic modeling of biogas upgrading in hollow fiber membrane contactors, Energy & Fuels, 28, 9, pp. 5745-5755, (2014)
  • [28] CAO F, GAO H X, LI H P, Et al., Experimental and theoretical studies on mass transfer performance for CO<sub>2</sub> absorption into aqueous N,N-dimethylethanolamine solution in the polytetrafluoroethylene hollow-fiber membrane contactor, Industrial & Engineering Chemistry Research, 57, 49, pp. 16862-16874, (2018)
  • [29] CAO F, GAO H X, LING H, Et al., Theoretical modeling of the mass transfer performance of CO<sub>2</sub> absorption into DEAB solution in hollow fiber membrane contactor, Journal of Membrane Science, 593, (2020)
  • [30] ZHANG Z E, YAN Y F, ZHANG L, Et al., Theoretical study on CO<sub>2</sub> absorption from biogas by membrane contactors: effect of operating parameters, Industrial & Engineering Chemistry Research, 53, 36, pp. 14075-14083, (2014)