|Table of Contents|

[1] Shao Yali, Wang Xudong, Jin Baosheng, et al. Numerical simulation of solid circulation mechanismand gas flow paths in a chemical looping combustion system [J]. Journal of Southeast University (English Edition), 2021, 37 (3): 272-275. [doi:10.3969/j.issn.1003-7985.2021.03.006]
Copy

Numerical simulation of solid circulation mechanismand gas flow paths in a chemical looping combustion system()
Share:

Journal of Southeast University (English Edition)[ISSN:1003-7985/CN:32-1325/N]

Volumn:
37
Issue:
2021 3
Page:
272-275
Research Field:
Energy and Power Engineering
Publishing date:
2021-09-20

Info

Title:
Numerical simulation of solid circulation mechanismand gas flow paths in a chemical looping combustion system
Author(s):
Shao Yali1 2 Wang Xudong2 Jin Baosheng2
1School of Energy and Mechanical Engineering, Nanjing Normal University, Nanjing 210023, China
2School of Energy and Environment, Southeast University, Nanjing 210096, China
Keywords:
chemical looping combustion two-stage air reactor solid circulation gas leakage
PACS:
TK16
DOI:
10.3969/j.issn.1003-7985.2021.03.006
Abstract:
To study the gas-solid flow characteristics in a chemical looping combustion system integrated with a moving bed air reactor, a 3D full-loop numerical model was established using the Eulerian-Eulerian approach integrated with the kinetic theory of granular flow. The solid circulation mechanism and gas leakage performance were studied in detail. The simulation results showed that in the start-up process, the solid circulation rate first increased to approximately 5 kg/s and then dropped to approximately 1.2 kg/s; this observation was related to the dynamic control of the pressure distribution. In this system, the gas leakage between the inertial separator, upper air reactor, and lower air reactor was restrained by adjusting the pressure difference, thus obtaining optimal gas flow paths. When the pressures at the outlets of the inertial separator, upper air reactor, and lower air were 7.4, 11.0, and 14.6 kPa, respectively, the gas leakage ratio was less than 1% in the system.

References:

[1] Wang X D, Shao Y L, Jin B S. Spatiotemporal statistical characteristics of multiphase flow behaviors in fuel reactor for separated-gasification chemical looping combustion of solid fuel[J]. Chemical Engineering Journal, 2021, 412: 128575. DOI: 10.1016/j.cej.2021.128575.
[2] Francisco J V, Carmen R F, I�F1;aki A, et al. Assessment of low-cost oxygen carrier in South-western Colombia, and its use in the in-situ gasification chemical looping combustion technology[J]. Fuel, 2018, 218: 417-424. DOI: 10.1016/j.fuel.2017.11.078.
[3] Li S Y, Shen Y S. Numerical study of gas-solid flow behaviors in the air reactor of coal-direct chemical looping combustion with Geldart D particles[J]. Powder Technology, 2020, 361: 74-86. DOI: 10.1016/j.powtec.2019.10.045.
[4] Shao Y L, Zhang Y, Wang X J, et al. Three-dimensional full loop modeling and optimization of an in situ gasification chemical looping combustion system[J]. Energy and Fuels, 2017, 31(12): 13859-13870. DOI: 10.1021/acs.energyfuels.7b02119.
[5] Zhou L, Han C, Bai L, et al. Numerical and experimental study of multiphase transient core-annular flow patterns in a spouted bed[J]. Journal of Energy Resources Technology, 2020, 142(9): 1-13. DOI: 10.1115/1.4047305.
[6] Hamidouche Z, Masi E, Fede P, et al. Unsteady three-dimensional theoretical model and numerical simulation of a 120 kW chemical looping combustion pilot plant. Chemical Engineering Science, 2019, 193: 102-119. DOI: 10.1016/j.ces.2018.08.032.
[7] Banerjee S, Ramesh K A. Computational fluid dynamics simulations of a binary particle bed in a riser-based carbon stripper for chemical looping combustion[J]. Powder Technology. 2018, 325: 361-367. DOI: 10.1016/j.powtec.2017.11.032.
[8] Mahalatkar K, Kuhlman J, Huckaby E D, et al. CFD simulation of a chemical-looping fuel reactor utilizing solid fuel[J]. Chemical Engineering Science, 2011, 66(16): 3617-3627. DOI: 10.1016/j.ces.2011.04.025.
[9] Yin W J, Wang S, Zhang K. Numerical investigation of in situ gasification chemical looping combustion of biomass in a fluidized bed reactor[J].Renewable Energy, 2020, 151: 216-225. DOI: 10.1016/j.renene.2019.11.016.
[10] Ding J M, Gidaspow D. A bubbling fluidization model using kinetic theory of granular flow[J]. AIChE Journal, 1990, 36(4): 523-538. DOI: 10.1002/aic.690360404.
[11] Menon G K, Patnaikuni V S. CFD simulation of fuel reactor for chemical looping combustion of Indian coal[J]. Fuel, 2017, 203: 90-101. DOI: 10.1016/j.fuel.2017.04.084.

Memo

Memo:
Biographies: Shao Yali(1993—), female, Ph.D. candidate, lecturer; Jin Baosheng(corresponding author), male, professor, bsjin@seu.edu.cn.
Foundation items: The National Natural Science Foundation of China(No. 51976034), China Postdoctoral Science Foundation(No. 2020M681455), the National Key R&D Program of China(No. 2018YFC1901200), Jiangsu Planned Projects for Postdoctoral Research Funds, the Fundamental Research Funds for the Central Universities.
Citation: Shao Yali, Wang Xudong, Jin Baosheng.Numerical simulation of solid circulation mechanism and gas flow paths in a chemical looping combustion system[J].Journal of Southeast University(English Edition), 2021, 37(3):272-275.DOI:10.3969/j.issn.1003-7985.2021.03.006.
Last Update: 2021-09-20