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过程工程学报 ›› 2024, Vol. 24 ›› Issue (3): 315-325.DOI: 10.12034/j.issn.1009-606X.223196

• 研究论文 • 上一篇    下一篇

气化炉激冷室中多相流动过程模拟与结构优化

袁炳*, 郭进军, 李晓飞, 梁军辉, 李振祥, 龙晓东, 姜从斌   

  1. 航天长征化学工程股份有限公司,北京 100010
  • 收稿日期:2023-07-14 修回日期:2023-09-18 出版日期:2024-03-28 发布日期:2024-03-27
  • 通讯作者: 袁炳 bingyuanchina@163.com

Numerical simulation of multiphase flow process and structural improvement measures in the quench chamber of a gasifier

Bing YUAN*,  Jinjun GUO,  Xiaofei LI,  Junhui LIANG,  Zhenxiang Li,  Xiaodong LONG,   Congbin JIANG   

  1. Changzheng Engineering Co., Ltd., Beijing 100010, China
  • Received:2023-07-14 Revised:2023-09-18 Online:2024-03-28 Published:2024-03-27

摘要: 气流床煤气化技术是煤炭清洁利用的重要手段之一,气化炉作为气流床煤气化的核心设备,通常分为燃烧室和激冷室两部分。其中,下降管-上升管结构的激冷室在煤气化装置中广泛应用。本工作采用数值模拟的方法对激冷室中的气液两相流动进行研究,分析了激冷室中出现合成气从黑水管串气问题的原因,并针对串气问题提出了三种激冷室结构改进方案:延长黑水出水口(结构A);向下延长上升管(结构B);靠近黑水出口管方向,在上升管上增加挡板(结构C)。模拟结果表明三种改进方案均能够避免串气问题。此外,还对不同结构激冷室黑水池中液固两相流进行了数值模拟,研究激冷室结构对不同粒径灰渣颗粒带出率的影响,结果表明,结构C的激冷室灰渣带出率最小,其次为结构A,这两种结构方案适用于对滤饼无回收利用的情况;相比原始结构,结构B对粒径≤20 μm的颗粒带出率较高,大颗粒带出率降低,更适合对滤饼中残碳回收利用的情况。

关键词: 激冷室, 多相流, 串气, 结构优化, 颗粒带出率

Abstract: The entrained flow coal gasification technology is one of the important means for the clean utilization of coal. In the syngas cooling device, the quench chamber with riser-downcomer structure is widely used in the coal gasification device. There is a situation where synthetic gas escapes from the black water outlet in the quench chamber of this type of quench chamber, resulting in a waste of resources. In this work, the gas-liquid two phase flow in the quench chamber is stuided with the numerical simulation method. The causes of syngas escape problem from the black water outlet in the quench chamber are analyzed, and three improved structures for the quench chamber are proposed as follow: extending the black water outlet pipe (structure A), extending the riser pipe downwards (structure B), adding a baffle on the rising pipe near the black water outlet (structure C). The simulation results indicate that all three improvement schemes can avoid the problem of syngas escape. In addition, the liquid-solid two phase flow in the black pool with four structures (structures A, B, C, and the original structure) are simulated, and the carry-out rate of ash particles with different particle sizes under the same conditions are compared in different structures. The results show that the carry-out rate of ash particle in the improved structure C is the smallest, followed by the structure A. These two structural schemes are suitable for the situation where the residual carbon in the filter cake is not recycled, and the low carry-out rate of ash by black water is beneficial for improving the water quality of the water circulation system. Compared with the original structure, the structure B has a higher carry-out rate for particles size smaller than 20 μm, but a low carry-out rate for large particles, which is suitable for recycling the residual carbon in the filter cake.

Key words: quench chamber, multi-phase flow, gas escape, structure improvement, particle carry-out rate