• 全部
主办单位:煤炭科学研究总院有限公司、中国煤炭学会学术期刊工作委员会
基于AspenPlus的废锅流程粉煤气化炉稳态流程模拟
  • Title

    Steady state simulation of coal gasification with radiant syngas cooler based on Aspen Plus

  • 作者

    朱莎弘杨欣华张双铭张扬张缦张建胜杨海瑞

  • Author

    ZHU Shahong;YANG Xinhua;ZHANG Shuangming;ZHANG Yang;ZHANG Man;ZHANG Jiansheng;YANG Hairui

  • 单位

    清华大学热科学与动力工程教育部重点实验室

  • Organization
    Key Laboratory for Thermal Science and Power Engineering of Ministry of Education,Tsinghua University
  • 摘要

    粉煤气流床具有氧耗低、煤耗低、碳转换率高等优点,在工业中应用广泛。废锅流程可有效回收粉煤气化炉产生的粗合成气余热,从长远角度看更为经济环保。基于Aspen Plus 建立了废锅流程粉煤气化炉稳态流程模型。在建模过程中,由于粗合成气进入辐射废锅时温度较高,需将辐射废锅内进一步的气化反应考虑在内。依据工程经验数据,将散热损失和碳转化率考虑在模型内,并与工业现场数据对比验证了模型的准确性。基于搭建的模型,研究了氧煤比、蒸汽煤比、碳转换率对气化参数的影响。研究结果表明,合成气有效成分随氧煤比的增加先急速增加后缓慢减少,在氧煤比为0.5 时达到峰值。氧煤比低于0.5 时,气化温度随着氧煤比的增加缓慢增长;氧煤比在0.5~0.9 时,气化温度随氧煤比的增加剧烈增长;氧煤比高于1 时,气化温度几乎不随氧煤比的增加而变化。考虑到气化温度不能低于煤种的熔融温度以利于炉内排渣,运行时应控制氧煤比高于0.6。合成气中有效成分(CO+H2)含量随蒸汽煤比的增加几乎呈线性降低,随碳转化率的增加而增加;气化温度随蒸汽比和碳转化率的增加而降低。

  • Abstract
    Pulverized coal airflow bed has the advantages of low oxygen consumption, low coal consumptionand high carbon conversion rate,and is widely used in industry. Radiant syngas cooler can effectively recover thewaste heat of syngas produced by pulverized coal gasifier,which is more economical and environmental friendly in thelong run. A steady state model of coal gasifier with radiant syngas cooler (RSC) was constructed using AspenPlus. Since the temperature of RSC is quite high,the further gasification reaction was considered in this model. Moreo⁃ver,the heat loss and unburned carbon was considered according to the industrial experience data and the simulation isvalidated as reliable by industrial operation results. Based on the model,the influences of core operation parameterslike oxygen⁃coal ratio,steam⁃coal ratio and carbon conversion rate were analyzed to provide a theoretical guidance. Thestudy results show that the effective composition of syngas increases rapidly at first and then decreases graduallywith the increase of oxygen⁃coal ratio,and reaches the peak value when the oxygen⁃coal ratio is 0.5. When the oxy⁃gen⁃coal ratio is lower than 0.5,the gasification temperature increases slightly with the oxygen⁃coal ratio and when theoxygen⁃coal ratio is between 0. 5 and 1, the gasification temperature increases rapidly with the oxygen⁃coalratio. When the oxygen⁃coal ratio is higher than 1, the gasification temperature almost remains unchanged.Since the gasification temperature should be higher than ash fusion point to facilitate discharging slag in furnace,theoxygen⁃coal ratio is suggested to be higher than 0.6. The effective composition of the syngas (CO+H2) almost decrea⁃ses linearly with the increase of steam-coal ratio. The effective composition of the syngas (CO+H2) almost increaseslinearly with the increase of carbon conversion rate. The gasification temperature decreases linearly with the increase ofsteam⁃coal ratio and carbon conversion rate.
  • 关键词

    :Aspen Plus辐射废锅稳态流程过程系统合成气煤气化

  • KeyWords

    Aspen Plus; radiant syngas cooler; steady state;process systems; syngas; coal gasification

  • 相关文章
  • 图表
    •  
    •  
    • 碳转化率对于气化温度的影响

    图(8) / 表(0)

相关问题

主办单位:煤炭科学研究总院有限公司 中国煤炭学会学术期刊工作委员会

©版权所有2015 煤炭科学研究总院有限公司 地址:北京市朝阳区和平里青年沟东路煤炭大厦 邮编:100013
京ICP备05086979号-16  技术支持:云智互联