气固循环流化床全回路数值模拟研究进展

doi:10.16085/j.issn.1000-6613.2018-1157

摘要/Abstract

摘要：

气固循环流化床具有良好的混合、传热、传质、反应特性，同时还具有处理量大、可连续生产等优点，在众多领域均有广泛应用。气固循环流化床是一个由多个单元连接组合形成的循环回路，各单元间相互耦合、相互影响。对整个循环流化床系统进行全回路数值模拟，不仅能够获得更全面和详实的结果，而且在揭示系统流动规律和探究各单元内、单元间、单元与系统间的相互作用上具有独特优势。近十年来，以气固循环流化床全系统为模拟对象的全回路数值模拟研究逐渐兴起。本文对气固循环流化床全回路数值模拟方法的研究进展进行综述，对该方法的应用情况进行详细介绍，并对方法中采用的模型及相应特点进行逐一分析。循环流化床全回路系统同时存在多种流态，有待于建立适用于全回路系统的多流态物理模型（气固曳力模型与固相应力模型）。随着计算能力的提高以及物理建模的不断发展，全回路模拟方法将不断完善并发挥出更大的作用。

关键词: 气固循环流化床, 全回路, 数值模拟, 两相流

Abstract:

Gas-solid circulating fluidized bed (CFB) has been widely used in many fields due to its good mixing, heat transfer, mass transfer and reaction characteristics as well as advantages of large processing capacity and continuous production. CFB is a circulating loop composed of several units, and all the units are coupled and interacted with each other. Therefore, the full-loop simulation, in which the whole CFB system is chosen as the simulation object, is more conducive to obtain accurate and comprehensive results and has advantages in revealing the flow dynamics in the CFB system and in studying the interactions inside the unit between the unit and between the unit and the system. This kind of full-loop simulation has been emerged as a promising research method in the recent decade for the CFB system. The present work will conduct review on the research progress of full-loop simulation, and have in-depth introduction on the application of such simulation method and its relating model and model characteristics. For the CFB, a system with multi flow patterns, it is necessary to establish the multi flow physical model (e.g. interphase drag model, model for the solid pressure) for the full-loop simulation of the CFB system. With the improvement of computing capacity and the development of physical modeling, the full loop simulation method will play an increasingly important role.

Key words: gas-solid circulating fluidized bed, full-loop, numerical simulation, two-phase flow

中图分类号:

TQ021.1

王敏, 吴迎亚, 石孝刚, 蓝兴英, 高金森. 气固循环流化床全回路数值模拟研究进展[J]. 化工进展, 2019, 38(01): 111-121.

Min WANG, Yingya WU, Xiaogang SHI, Xingying LAN, Jinsen GAO. Review of full-loop simulation of gas-solid circulating fluidized bed[J]. Chemical Industry and Engineering Progress, 2019, 38(01): 111-121.

图/表 9

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作者	年份	模拟对象	颗粒类型	多相流模型	曳力模型	固相应力模型
Zhang等^[12]	2008	半工业级CFB装置	A	TFM	EMMS	KTGF
Liu等^[13]	2010	50MWe CFB锅炉	B	TFM	Gidaspow	KTGF 摩擦应力
Zhang等^[14]	2010	150MWe CFB锅炉	B	TFM	EMMS	KTGF
张楠等^[15]	2010	半工业级CFB装置	A	TFM	EMMS	KTGF
Wang等^[16]	2011	化学链燃烧（CLC）装置	B	TFM	Gidaspow	KTGF
Wang等^[17]	2011	高密度循环流化床（HDCFB）装置	B	TFM	Revised EMMS	KTGF
Nguyen等^[18]	2012	CFB 气化炉	B	TFM	Gidaspow	KTGF
Dietiker等^[19]	2013	CFB装置	B	TFM	Gidaspow	—
Lu等^[20]	2013	工业级CFB锅炉	B	MFM	EMMS Gidaspow	KTGF
Nikolopoulos等^[21]	2013	CFB 碳酸化器	B	TFM	EMMS Gidaspow	KTGF 摩擦应力
霍荥等^[22]	2013	中试CFB装置	A	TFM	EMMS	—
王雪瑶等^[23]	2013	CFB装置	B	TFM	EMMS	KTGF
Li等^[24]	2014	NETL中试CFB装置	B	TFM	Gidaspow	KTGF
Geng等^[25]	2015	CLC装置	B	TFM	Syamlal–O’Brien	KTGF
Liu等^[26]	2015	CFB装置	A	TFM	EMMS /Matrix	KTGF
Guan等^[27]	2014	CLC装置	B	TFM	Gidaspow	KTGF
Su等^[28]	2015	CLC装置	B	TFM	Gidaspow	KTGF
Guan等^[29]	2016	CLC装置	B	TFM	Gidaspow	KTGF

作者	年份	模拟对象	颗粒类型	多相流模型	曳力模型	固相应力模型
Zhang等^[12]	2008	半工业级CFB装置	A	TFM	EMMS	KTGF
Liu等^[13]	2010	50MWe CFB锅炉	B	TFM	Gidaspow	KTGF 摩擦应力
Zhang等^[14]	2010	150MWe CFB锅炉	B	TFM	EMMS	KTGF
张楠等^[15]	2010	半工业级CFB装置	A	TFM	EMMS	KTGF
Wang等^[16]	2011	化学链燃烧（CLC）装置	B	TFM	Gidaspow	KTGF
Wang等^[17]	2011	高密度循环流化床（HDCFB）装置	B	TFM	Revised EMMS	KTGF
Nguyen等^[18]	2012	CFB 气化炉	B	TFM	Gidaspow	KTGF
Dietiker等^[19]	2013	CFB装置	B	TFM	Gidaspow	—
Lu等^[20]	2013	工业级CFB锅炉	B	MFM	EMMS Gidaspow	KTGF
Nikolopoulos等^[21]	2013	CFB 碳酸化器	B	TFM	EMMS Gidaspow	KTGF 摩擦应力
霍荥等^[22]	2013	中试CFB装置	A	TFM	EMMS	—
王雪瑶等^[23]	2013	CFB装置	B	TFM	EMMS	KTGF
Li等^[24]	2014	NETL中试CFB装置	B	TFM	Gidaspow	KTGF
Geng等^[25]	2015	CLC装置	B	TFM	Syamlal–O’Brien	KTGF
Liu等^[26]	2015	CFB装置	A	TFM	EMMS /Matrix	KTGF
Guan等^[27]	2014	CLC装置	B	TFM	Gidaspow	KTGF
Su等^[28]	2015	CLC装置	B	TFM	Gidaspow	KTGF
Guan等^[29]	2016	CLC装置	B	TFM	Gidaspow	KTGF

作者	年份	模拟对象	颗粒类型	颗粒数	多相流模型	曳力模型
Chu等^[30]	2008	CFB装置	D	2×10⁴	DEM	Di Felice
Luo等^[31]	2015	CFB装置	D	2×10⁵	DEM	Gidaspow
Luo等^[32]	2015	CFB装置	D	9.2×10⁴	DEM	Gidaspow
Xie等^[33]	2015	工业级CFB锅炉	—	—	DEM	—
Wang等^[34]	2017	CFB装置（6个旋分）	D	9×10⁵	DEM	Gidaspow
Wang等^[35]	2017	双侧返料循环流化床（DRCFB）装置	D	3×10⁵	DEM	Gidaspow
Wang等^[36]	2017	CFB装置	D	9×10³	DEM	Gidaspow
Xu等^[37]	2017	CFB装置	D	—	DEM	BVK, Gidaspow, Hill-Koch-Ladd, and Wen and Yu
Jiang等^[38]	2014	CFB装置（6个旋分）	B	—	CPFD	Wen-Yu/ Ergun
Parker^[39]	2014	CLC装置	B	—	CPFD	—
Wang等^[40]	2014	CFB装置	B	—	CPFD	Wen-Yu, Wen-Yu/Ergun, Ganser
Wang等^[41]	2014	CFB装置	B	—	CPFD	Wen-Yu/ Ergun
殷上轶等^[42]	2016	HDCFB装置	B	—	CPFD	Gidaspow
Tu等^[43]	2018	中试CFB装置	B	—	CPFD	EMMS

作者	年份	模拟对象	颗粒类型	颗粒数	多相流模型	曳力模型
Chu等^[30]	2008	CFB装置	D	2×10⁴	DEM	Di Felice
Luo等^[31]	2015	CFB装置	D	2×10⁵	DEM	Gidaspow
Luo等^[32]	2015	CFB装置	D	9.2×10⁴	DEM	Gidaspow
Xie等^[33]	2015	工业级CFB锅炉	—	—	DEM	—
Wang等^[34]	2017	CFB装置（6个旋分）	D	9×10⁵	DEM	Gidaspow
Wang等^[35]	2017	双侧返料循环流化床（DRCFB）装置	D	3×10⁵	DEM	Gidaspow
Wang等^[36]	2017	CFB装置	D	9×10³	DEM	Gidaspow
Xu等^[37]	2017	CFB装置	D	—	DEM	BVK, Gidaspow, Hill-Koch-Ladd, and Wen and Yu
Jiang等^[38]	2014	CFB装置（6个旋分）	B	—	CPFD	Wen-Yu/ Ergun
Parker^[39]	2014	CLC装置	B	—	CPFD	—
Wang等^[40]	2014	CFB装置	B	—	CPFD	Wen-Yu, Wen-Yu/Ergun, Ganser
Wang等^[41]	2014	CFB装置	B	—	CPFD	Wen-Yu/ Ergun
殷上轶等^[42]	2016	HDCFB装置	B	—	CPFD	Gidaspow
Tu等^[43]	2018	中试CFB装置	B	—	CPFD	EMMS

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