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煤间接液化中费托合成单元装置的(火用)分析

吴建民 孙启文 岳建平 庞利峰

化学工程2012,Vol.40Issue(12):53-56,78,5.
化学工程2012,Vol.40Issue(12):53-56,78,5.DOI:10.3969/j.issn.1005-9954.2012.12.013

煤间接液化中费托合成单元装置的(火用)分析

Exergy analysis of Fischer-Tropsch synthesis unit apparatus during coal indirect liquefaction

吴建民 1孙启文 1岳建平 1庞利峰1

作者信息

  • 1. 上海兖矿能源科技研发有限公司煤液化及煤化工国家重点实验室,上海201203
  • 折叠

摘要

Abstract

Based on the PRO/ II simulation and optimization results of low temperature Fischer-Tropsch synthesis (FTS) system, the exergy thermodynamic analysis was applied to calculate the exergy distribution of Fischer-Tropsch synthesis system. The exergy efficiency and exergy losses of this system were also analyzed. The results show that FTS reaction process is the largest exergy loss process. The equipment with the maximum exergy loss is FTS reactor,with exergy efficiency 86. 80% , sharing 85. 15% of total exergy loss;the condensate backflow pump has the lowest exergy efficiency,which is only 6. 71% ;the exergy efficiencies of wax collection tank,wax pump and wax intermediate tank are the highest, which have no exergy loss nearly. By using exergy analysis method, it can be more accurate and convenient to uncover the process and devices with the maximal exergy loss, which can set up the target and provide suggestions for equipment improving and energy saving.

关键词

热力学分析/费托合成/(火用)效率/(火用)损失

Key words

thermodynamic analysis/ Fischer-Tropsch synthesis/ exergy efficiency/ exergy loss

分类

化学化工

引用本文复制引用

吴建民,孙启文,岳建平,庞利峰..煤间接液化中费托合成单元装置的(火用)分析[J].化学工程,2012,40(12):53-56,78,5.

基金项目

国家重点基础研究发展计划(973计划)(2010CB736203) (973计划)

化学工程

OA北大核心CSCDCSTPCD

1005-9954

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