|Table of Contents|

[1] Zhao Jie, Jin Baosheng, Xu Yin,. CFD simulation of ammonia-based CO2 absorption in a spray column [J]. Journal of Southeast University (English Edition), 2015, 31 (4): 479-488. [doi:10.3969/j.issn.1003-7985.2015.04.009]
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CFD simulation of ammonia-based CO2 absorption in a spray column()
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Journal of Southeast University (English Edition)[ISSN:1003-7985/CN:32-1325/N]

Volumn:
31
Issue:
2015 4
Page:
479-488
Research Field:
Energy and Power Engineering
Publishing date:
2015-12-30

Info

Title:
CFD simulation of ammonia-based CO2 absorption in a spray column
Author(s):
Zhao Jie Jin Baosheng Xu Yin
Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, China
Keywords:
CO2 absorption spray column computational fluid dynamics(CFD) aqueous ammonia
PACS:
TK09
DOI:
10.3969/j.issn.1003-7985.2015.04.009
Abstract:
A comprehensive computational fluid dynamics(CFD)model is developed based on the gas-liquid two-phase hydrodynamics, gas-liquid mass-transfer theory and chemical reaction kinetics, and the ammonia-based CO2 absorption in a spray column is numerically studied. The Euler-Lagrange model is applied to describe the behavior of gas-liquid two-phase flow and heat transfer. The dual-film theory and related correlations are adopted to model the gas-liquid mass transfer and chemical absorption process. The volatilization model of multi-component droplet is utilized to account for ammonia slippage. The effect of operation parameters on CO2 removal efficiency is numerically studied. The results show a good agreement with the previous experimental data, proving the validity of the proposed model. The profile studies of gas-phase velocity and CO2 concentration suggest that the flow field has a significant impact on the CO2 concentration field. Also, the local CO2 absorption rate is influenced by both local turbulence and the local liquid-gas ratio. Furthermore, the velocity field of gas phase is optimized by the method of adjusting the orifice plate, and the results show that the CO2 removal efficiency is improved by approximately 4%.

References:

[1] Yeh A C, Bai H L. Comparison of ammonia and monoethanolamine solvents to reduce CO2 greenhouse gas emissions[J]. Science of the Total Environment, 1999, 228(2/3):121-133.
[2] Kuntz J, Aroonwilas A. Performance of spray column for CO2 capture application[J]. Industry & Engineering Chemistry Research, 2007, 47(1):145-153.
[3] Lim Y, Choi M, Han K, et al. Performance characteristics of CO2 capture using aqueous ammonia in a single-nozzle spray tower[J]. Industry & Engineering Chemistry Research, 2013, 52(43):15131-15137.
[4] Niu Zhenqi, Guo Yincheng, Lin Wenyi. Carbon dioxide removal efficiencies by fine sprays of MEA, NaOH and aqueous ammonia solutions[J]. Journal of Tsignhua University, 2010, 50(7):1130-1140.(in Chinese)
[5] Javed K H, Mahmud T, Purba E. The CO2 capture performance of a high-intensity vortex spray scrubber [J]. Chemical Engineering Journal, 2010, 162(2): 448-456.
[6] Zhang D S, Deen N G, Kuipers G A M. Euler-Euler modeling of flow, mass transfer, and chemical reaction in a bubble column[J]. Industry & Engineering Chemistry Research, 2009, 48(1): 47-57.
[7] Zhang D S. Eulerian modeling of reactive gas-liquid flow in a bubble column[D]. Enschede, The Netherlands: University of Twente, 2007.
[8] Yu Hai, Morgan S, Allport A, et al. Results from trialling aqueous NH3 based post-combustion capture in a pilot plant Munmorah power station:absorption[J]. Chemical Engineering Research and Design, 2011, 89(8): 1204-1215.
[9] Liu Guobiao. Computational transport and its application to mass transfer and reaction processes in packed-beds[D]. Tianjin: School of Chemical Engineering, University of Tianjin, 2006.(in Chinese)
[10] Lu Tongchang. Experimental research and CFD simulation of ammonia absorption of CO2 from flue gas [D]. Baoding: School of Energy, Power and Mechanical Engineering, North China Electrical Power University, 2013.(in Chinese)
[11] Zeng Qing. The experimental investigation on CO2 absorption by aqueous ammonia[D]. Beijing: School of Aerospace Engineering, TsingHua University, 2011.(in Chinese)
[12] Zhu Jie, Wu Zhenyuan, Ye S, et al. Drop size distribution and specific surface area in spray tower[J]. Journal of Chemical Industry and Engineering, 2014, 65(12):4710-4715.(in Chinese)
[13] Cai Bin, Li Lei, Wang Zhaolin. Numerical analysis of liquid droplet breakup in airflow[J]. Journal of Engineering Thermophysics, 2003, 24(4):613-616.(in Chinese)
[14] Du Zhanbo, Mao Jingru, Sun Bi. Measurements of droplet sizes at mid-hight of stationary turbine blades and analysis of the critical weber number[J]. Journal of Power Engineering, 2005, 25(5):643-684.(in Chinese)
[15] Li Tongming. Coalescence between small bubbles or droplets[J]. Journal of Chemical Industry and Engineering, 1994, 45(1):38-44.(in Chinese)
[16] Li Tongming, Zhao Liyan. The influence of interfacial rheological property on coalescence process of small droplet[J]. Acta Physico-Chimica Sinica, 1996, 12(8):708-714.(in Chinese)
[17] Yu Guocong, Yuan Xigang. Computational mass transfer introduction for chemical engineering process[M]. Tianjin: Tianjin University Press, 2011.(in Chinese)
[18] Fluent Inc.Fluent user’s guide[EB/OL].(2006-09)[2015-05-15]. http://wenku.baidu.com/link?url=MU4BlrL5d_b-uHKVD41mdubXvw94p9FQ22UXE_EQStKH5piDiYVwDgCPcT4Ib43S5D5rMRVAdy-XsC2V E9RYpidwEi_fd8jSzaoDya4eX9a.
[19] Zhong Yi, Gao Xiang, Wang Huiting, et al. The performance optimization of the wet flue gas desulfurization system based on CFD[J]. Proceedings of the CSEE, 2008, 28(32):18-23.(in Chinese)
[20] de Montigny D, Tontiwachwuthikul P, Chakma A. Comparing the absorption performance of packed columns and membrane contactors[J]. Industry & Engineering Chemistry Research, 2005, 44(15):5726-5732.
[21] Warych J, Szymanowski M.Model of the wet limestone flue gas desulfurization process for cost optimization[J].Industry & Engineering Chemistry Research, 2001, 40(12):2597-2605.
[22] Derks P W J, Versteeg G F. Kinetics of absorption of carbon dioxide in aqueous ammonia solutions[J]. Energy Procedia, 2009, 1(1):1139-1146.
[23] Liu Jinzhao, Wang Shujuan, Qi Guojie, et al. Kinetics and mass transfer of carbon dioxide absorption into aqueous ammonia[J]. Energy Procedia, 2011(4): 525-532.
[24] Liu Jinzhao, Wang Shujuan, Zhao Bo, et al. Absorption of carbon dioxide in aqueous ammonia[J]. Energy Procedia, 2009, 1(1):933-940.
[25] Bai H L, Yeh A C. Removal of CO2 greenhouse gas by ammonia scrubbing[J]. Industry & Engineering Chemistry Research, 1997, 36(6):2490-2493.
[26] Liu Nailing, Zhang Xu. Experimental study of atomization characteristic of pressure spiral nozzle[J]. Journal of Experiments for Fluid Mechanics, 2006, 20(3):8-12.(in Chinese)
[27] Chen Hongyu, Liu Guorong. The theoretical study of a novel water-spraying desulfurization by aqueous ammonia[J]. General Machinery, 2007(4):23-26.(in Chinese)
[28] Budzianowski W M. CO2 reactive absorption from flue gases into aqueous ammonia solutions: the NH3 slippage effects[J]. Environment Protection Engineering, 2011, 37(4):5-19.
[29] Li Liqing, Zhang Chun, Huang Guijie, et al. A multicomponent droplet model in simulating mass transfer of the ammonia-based spray process[J]. Proceedings of the CSEE, 2014, 34(32):5741-5749.(in Chinese)
[30] Liu Xi. Experimental research on effects of additives to the ammonia-based CO2 capture process[D]. Nanjing: School of Energy and Environment, Southeast University, 2014.(in Chinese)

Memo

Memo:
Biographies: Zhao Jie(1991—), female, graduate;Jin Baosheng(corresponding author), male, professor, bsjin@seu.edu.cn.
Foundation item: The National Natural Science Foundation of China(No.51276038).
Citation: Zhao Jie, Jin Baosheng, Xu Yin.CFD simulation of ammonia-based CO2 absorption in a spray column[J].Journal of Southeast University(English Edition), 2015, 31(4):479-488.[doi:10.3969/j.issn.1003-7985.2015.04.009]
Last Update: 2015-12-20