化工学报 ›› 2022, Vol. 73 ›› Issue (5): 2073-2082.doi: 10.11949/0438-1157.20211568

• 过程系统工程 • 上一篇    下一篇

一种煤基多联产碳循环系统的设计及评价

侯起旺1(),文兆伦1,张忠林1(),刘叶刚1,2,杨景轩1,陈东良1,2,郝晓刚1(),官国清3   

  1. 1.太原理工大学化学化工学院，山西 太原 030024
    2.上海电气集团国控环球工程有限公司，山西 太原 030001
    3.日本弘前大学地域战略研究所，青森 030-0813，日本
  • 收稿日期:2021-11-03 修回日期:2022-02-09 出版日期:2022-05-05 发布日期:2022-05-24
  • 通讯作者: 张忠林,郝晓刚 E-mail:1062581355@qq.com;zlzhang@tyut.edu.cn;xghao@tyut.edu.cn
  • 作者简介:侯起旺（1995—），男，硕士研究生，1062581355@qq.com
  • 基金资助:
    国家自然科学基金项目(U1710101)

Design and evaluation of a coal-based polygeneration system with carbon cycle

Qiwang HOU1(),Zhaolun WEN1,Zhonglin ZHANG1(),Yegang LIU1,2,Jingxuan YANG1,Dongliang CHEN1,2,Xiaogang HAO1(),Guoqing GUAN3   

  1. 1.College of Chemistry and Chemical Engineering, Taiyuan University of Technology, Taiyuan 030024, Shanxi, China
    2.Shanghai Electric Guokong Global Engineering Corporation, Taiyuan 030001, Shanxi, China
    3.Institute of Regional Innovation, Hirosaki University, Aomori 030-0813, Japan
  • Received:2021-11-03 Revised:2022-02-09 Published:2022-05-05 Online:2022-05-24
  • Contact: Zhonglin ZHANG,Xiaogang HAO E-mail:1062581355@qq.com;zlzhang@tyut.edu.cn;xghao@tyut.edu.cn

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摘要：

将高密度三塔式循环流化床(TBCFB)应用于串并联综合型多联产系统，提出一种基于碳循环的流程与参数共优化的煤基多联产系统，促进低阶煤资源的高质高效转化。碳循环体现在两方面，一是系统以热解煤气循环作为热解气氛，提高了焦油产率，实现低阶煤高质化转化；二是在TBCFB使用富氧燃烧，提高了烟气中二氧化碳浓度，将烟气替代氮气直接用于燃气轮机发电工质，减少了氮气消耗。利用Aspen Plus对全系统进行模拟，对多联产系统进行物料、能量和?衡算，研究未反应合成气循环比和烟气注入量对过程的影响；以能量利用效率为优化目标，对煤基多联产碳循环系统的操作条件寻优。结果表明，动力单元注入气体使用烟气时，煤基多联产碳循环系统的能量利用效率达49.7%，高于用氮气作为热解气氛的传统煤基多联产系统，相比传统的单产系统，煤基多联产系统的能量可节约13%，对于年处理30万吨煤的系统，折合减少二氧化碳排放量为14.9万吨/年。

关键词: 碳循环, 煤基多联产, 能量分析, 计算机模拟, 集成, 优化设计

Abstract:

By applying the high-density triple bed circulating fluidized bed (TBCFB) to a series-parallel integrated polygeneration system, a coal-based polygeneration system based on carbon cycle process and parameters co-optimization is proposed, which can promote the high-quality and high-efficiency conversion of low-rank coal resources. The carbon cycle is embodied in two aspects. First, this system uses a pyrolysis gas cycle as the pyrolysis atmosphere, which can increase the tar yield and realize the high-quality conversion of low-rank coal.The second is the use of oxygen-enriched combustion in TBCFB, which can increase the concentration of carbon dioxide in the flue gas. While, using the flue gas instead of nitrogen directly as a working fluid for gas turbine power generation also reduces nitrogen consumption. The Aspen Plus is used here to investigate the influence of unreacted syngas circulation ratio and flue gas injection rate on the process via performing material, energy and exergy balance calculations for polygeneration systems. In addition, with energy efficiency as the optimization goal, suitable operating conditions are further found for the coal-based polygeneration system with carbon cycle. The results show that when the flue gas is used for gas injection in the power unit, the energy utilization efficiency of the coal-based polygeneration system with carbon cycle reaches 49.7%, which is higher than that of the traditional system using nitrogen as the pyrolysis atmosphere. Compared with the traditional unit production system, the coal-based polygeneration system can save 13% of energy, which is equivalent to reducing carbon dioxide emissions by 14.9×104 tons per year for a system with an annual capacity of 30×104 tons of coal.

Key words: carbon cycle, coal-based polygeneration system, energy analysis, computer simulation, integration, optimization design

中图分类号: 

  • TQ 015.2

图1

煤基多联产碳循环系统过程图"

表1

NMH工业分析和元素分析［16］"

Proximate analysis/ %(mass，d)Ultimate analysis/ %(mass，daf)LHV/(MJ/kg)
FCAVCHNSO①
47.215.846.9974.355.130.720.3119.4923.45

图2

煤基多联产碳循环系统工艺流程"

表2

燃气轮机、蒸汽轮机参数"

参数值
压气机绝热压缩效率/%91
透平绝热膨胀效率/%86
氧气温度/℃15
氧气压缩比/%29.6
汽轮机高压缸效率/%87
汽轮机中压缸效率/%90
汽轮机低压缸效率/%88
机械电机效率/%98

图3

碳循环多联产循环比对系统能量利用率的影响A—发电量与循环压缩机功耗、精馏能耗之差;B—系统能量利用率;C—甲醇能量"

图4

碳循环多联产烟气回注量对动力单元的影响A—NO x 排放量;B—动力单元输出电量;C—燃烧室出口温度"

图5

煤基多联产碳循环系统物料衡算（kg/h）"

表3

多联产碳循环系统主要物流模拟数据"

物流摩尔分数/%摩尔流量/ (kmol/h)质量流量/(t/h)温度/℃压力/MPa
H2+CH4COCO2N2O2H2OCH3OH
1————————37.52000.1
259.127.75.4——7.7—1398.118.3406.5
367.930.02.1————1204.613.235.95.57
4—————10.886.6462.014.365.33.5
5——93.61.25.1——885.838.3843.80.1
63.63.46.8——85.3—599.912.0593.75.0
7——54.60.63.041.8—1347.244.1227.80.1

图6

煤基多联产碳循环系统能量衡算（MW）"

图7

煤基多联产碳循环系统?衡算（MW）"

表4

两种多联产系统性能对比分析"

系统系统输入 总能量/MW系统输出 总功率/ MW系统输出 净功率/MW产生甲醇 能量/MW产生焦油 能量/MW系统能量 利用率/%?效率/%
传统煤基多联产244.2724.3218.4466.5332.1547.939
煤基多联产碳循环244.2726.3320.4563.3237.5749.740

表5

联产系统与单产系统性能"

项目输入输出系统输出能量/MW相对能量节约率/%
煤/(t/h)甲醇/(t/h)焦油/(t/h)
煤基多联产碳循环系统37.511.464.126.3313
煤气化联合循环发电系统11.89——26.33—
煤制甲醇系统24.3711.46———
费托合成油系统6.83—4.1——
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