HTW加压流化床煤气化模拟

赵创; 汪大千; 杨海平; 王贤华; 张世红; 陈汉平

doi:10.12096/j.2096-4528.pgt.2018.064

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HTW加压流化床煤气化模拟

火电及环境保护 | 更新时间：2025-06-06

- HTW加压流化床煤气化模拟
- Simulated of HTW Pressurized Fluidized Bed Gasifier
- 发电技术 2018年39卷第5期页码：419-424
- 作者机构：
  
  煤燃烧国家重点实验室(华中科技大学), 湖北省武汉市 430074
- 作者简介：
  
  [ "赵创(1997), 男, 硕士研究生, 主要研究方向为高温高压煤气化技术、Aspen Plus模拟等, zhao_chuang@hust.edu.cn" ]
- 基金信息：
  
  国家重点研发计划项目(2017YFB0602701-02)
- DOI：10.12096/j.2096-4528.pgt.2018.064
  中图分类号：
- 收稿：2018-08-15，
  
  纸质出版：2018-10-30
- 稿件说明：
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赵创, 汪大千, 杨海平, 等. HTW加压流化床煤气化模拟[J]. 发电技术, 2018,39(5):419-424.

Chuang ZHAO, Daqian WANG, Haiping YANG, et al. Simulated of HTW Pressurized Fluidized Bed Gasifier[J]. Power Generation Technology, 2018, 39(5): 419-424.
赵创, 汪大千, 杨海平, 等. HTW加压流化床煤气化模拟[J]. 发电技术, 2018,39(5):419-424. DOI： 10.12096/j.2096-4528.pgt.2018.064.

Chuang ZHAO, Daqian WANG, Haiping YANG, et al. Simulated of HTW Pressurized Fluidized Bed Gasifier[J]. Power Generation Technology, 2018, 39(5): 419-424. DOI： 10.12096/j.2096-4528.pgt.2018.064.

摘要

为深入了解高温温克勒（high-temperature Winkler，HTW）加压流化床煤气化过程，采用Aspen Plus构建相应模型，以氧煤比和蒸汽煤比为变量，对HTW加压流化床气化炉的气化气成分、热值、气体产率和冷煤气效率进行了模拟。模拟结果表明，随着氧煤比的增加，出口温度升高，CO含量增加，H

含量先增加然后略有减小，CO

和CH

的含量降低，气体产率增加，气体热值下降，冷煤气效率下降。HTW加压流化床气化炉的常见运行温度为1 050℃，在此工况下的氧煤比大约为0.71，而水蒸气煤比对HTW加压流化床气化炉的运行性能影响较小。模拟结果对HTW加压流化床煤气化技术的深入研究与实际设计具有指导意义。

Abstract

To have a better understanding about coal gasification process in HTW pressurized fluidized bed

the model was developed using process simulation software Aspen Plus. Gas composition

low heating value(LHV)

gas yield and cold gas efficiency were simulated with the change in the oxygen/coal ratio and steam/coal ratio. The results show that with the oxygen/coal ratio increaseing

outlet temperature decreases

the yield of CO increases

first increases and then decreases slightly

CO and CH

decreases

gas yield increases

LHV decreases

cold gas efficiency decreases. The usual operating temperature of high-temperature Winkler(HTW) pressurized fluidized bed gasifier is about 1050℃

and the corresponding oxygen/coal ratio is 0.71. The steam/coal ratio less affects the operating performance of HTW pressurized fluidized bed gasifier. The result of the simulation was meaningful for the followi

ng research about coal gasification process in HTW pressurized fluidized bed and the design of the gasifier.

关键词

Keywords

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基于Aspen Plus的气流床煤气化炉建模及其变工况特性研究