入口结构对18 m气固循环流化床提升管内颗粒流动特性的影响

doi:10.11949/j.issn.0438-1157.20180016

化工学报 ›› 2018, Vol. 69 ›› Issue (5): 1931-1937.DOI: 10.11949/j.issn.0438-1157.20180016

入口结构对18 m气固循环流化床提升管内颗粒流动特性的影响

毛晓阳, 王成秀, 蓝兴英, 高金森

中国石油大学(北京)重质油国家重点实验室, 北京 102249

收稿日期:2018-01-08 修回日期:2018-01-16 出版日期:2018-05-05 发布日期:2018-05-05
通讯作者: 王成秀
基金资助:
国家自然科学基金重点项目（91534204）；国家自然科学基金青年基金项目（21506253）；中国石油大学（北京）科研基金项目（2462014YJRC018）。

Effects of inlet distributor on particle flow characteristics in 18 m circulating fluidized bed riser

MAO Xiaoyang, WANG Chengxiu, LAN Xingying, GAO Jinsen

State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China

Received:2018-01-08 Revised:2018-01-16 Online:2018-05-05 Published:2018-05-05
Supported by:
supported by the National Natural Science Foundation of China(91534204), the National Natural Science Foundation of China(21506253), the Science Foundation of China University of Petroleum(Beijing)(2462014YJRC018).

摘要/Abstract

摘要：

在高18 m、内径80 mm的循环流化床提升管内分别考察了三种入口结构对颗粒流动特性的影响。实验结果表明：入口结构主要影响提升管底部区域的颗粒流动特性，不同入口结构对颗粒流动影响不同。相同操作条件下，当采用多管式入口结构时，径向上提升管底部区域的颗粒浓度分布相对均匀，轴向上颗粒能够迅速达到充分发展状态，充分发展高度在9 m左右；当采用多孔板入口结构时，径向上提升管底部颗粒浓度差别较大，轴向上颗粒发展较慢，需要更高高度才能达到充分发展，充分发展高度约为11 m；当采用单管式入口结构时，径向上颗粒浓度分布和轴向上颗粒充分发展速度均处于前两者之间，底部颗粒浓度径向分布仍为中间稀、边壁浓的不均匀分布，颗粒浓度轴向充分发展高度约为10 m。

关键词: 循环流化床, 提升管, 两相流, 入口结构

Abstract:

Three kinds of riser inlet distributors were designed to investigate their effects on particle flow characteristics in a CFB riser with 18 m in height and 80 mm in diameter. The results show that inlet distributors have significant impact on particle hydrodynamics at the bottom region of the riser and different inlet distributors have different effects as indicated by characteristic length of the developing section. At the same operating condition, multiple tube inlet had uniform radial distribution of solid holdup and particle movement reached fully-developed state at about 9 m in axial direction, whereas perforated plate inlet had large concentration difference at bottom and particle movement developed slowly in axial direction requiring about 11 m in length to reach fully-developed state. On the other hand, single tube inlet had radial solid holdup and axial development region somewhere between those of the other two inlets. The single tube inlet had non-uniform radial solid holdup distribution of dilute center and dense side at the bottom of the riser and required 10 m axial length to reach fully-development state.

Key words: circulating fluidized bed, riser, two-phase flow, inlet distributor

中图分类号:

TQ021.1

毛晓阳, 王成秀, 蓝兴英, 高金森. 入口结构对18 m气固循环流化床提升管内颗粒流动特性的影响[J]. 化工学报, 2018, 69(5): 1931-1937.

MAO Xiaoyang, WANG Chengxiu, LAN Xingying, GAO Jinsen. Effects of inlet distributor on particle flow characteristics in 18 m circulating fluidized bed riser[J]. CIESC Journal, 2018, 69(5): 1931-1937.

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入口结构对18 m气固循环流化床提升管内颗粒流动特性的影响

Effects of inlet distributor on particle flow characteristics in 18 m circulating fluidized bed riser

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