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基于流程模拟的脱矿胜利褐煤水蒸气气化研究

朱宏跃 路荣荣 班延鹏 周丹 刘一鸣

大连理工大学学报2024,Vol.64Issue(4):338-345,8.
大连理工大学学报2024,Vol.64Issue(4):338-345,8.DOI:10.7511/dllgxb202404002

基于流程模拟的脱矿胜利褐煤水蒸气气化研究

Study of steam gasification of demineralized Shengli lignite based on process simulation

朱宏跃 1路荣荣 2班延鹏 2周丹 1刘一鸣1

作者信息

  • 1. 太原科技大学催化转化能源耦合山西省重点实验室,山西太原 030024
  • 2. 大连理工大学化工学院,辽宁大连 116024
  • 折叠

摘要

Abstract

Aspen Plus V14 is used to establish a steady-state process model of a fixed-bed coal gasifier,and simulation research is conducted on the steam gasification process of demineralized Shengli lignite(SL)and its added sodium hydroxide sample(SL+-NaOH).The accuracy of the built model is verified based on experimental data,and it is testified that the syngas yield predicted by the model is in good agreement with the experimental values.Based on this model,the effects of steam-to-coal ratio and gasification temperature on the composition of syngas and the yield of effective gas(CO+H2)are studied.The results show that the mole fraction of effective gas in SL+gasification syngas first increases and then decreases with the increase of steam-to-coal ratio,reaching a maximum value of 75.7%at 0.74 of steam-to-coal ratio.The gasification temperature has a greater impact on the effective gas composition of the two coal samples.The production of H2 and CO2 in SL+-NaOH increases significantly,while the production of CO decreases significantly compared with that in SL+.

关键词

Aspen Plus/脱矿胜利褐煤/稳态模拟/水蒸气气化/有效气组成

Key words

Aspen Plus/demineralized Shengli lignite/steady-state simulation/steam gasification/effective gas composition

分类

化学化工

引用本文复制引用

朱宏跃,路荣荣,班延鹏,周丹,刘一鸣..基于流程模拟的脱矿胜利褐煤水蒸气气化研究[J].大连理工大学学报,2024,64(4):338-345,8.

基金项目

国家自然科学基金资助项目(22075197,22278290) (22075197,22278290)

来晋工作优秀博士奖励资金资助项目(20232066) (20232066)

太原科技大学校级博士科研启动金资助项目(20222082) (20222082)

太原科技大学校级大创项目(XJ2023053). (XJ2023053)

大连理工大学学报

OA北大核心CSTPCD

1000-8608

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