化工进展 ›› 2020, Vol. 39 ›› Issue (S2): 57-65.DOI: 10.16085/j.issn.1000-6613.2020-0720

• 化工过程与装备 • 上一篇    下一篇

异丁烯提纯装置换热网络的能效分析

邵缨迪1(), 胡建杭1,2(), 刘慧利2, 蔡正达3   

  1. 1.昆明理工大学冶金节能减排教育部工程研究中心,云南 昆明 650093
    2.冶金化工节能环保技术国家地方联合工程研究中心,云南 昆明 650093
    3.云南省科学技术院,云南 昆明 650228
  • 收稿日期:2020-04-30 出版日期:2020-11-20 发布日期:2020-11-17
  • 通讯作者: 胡建杭
  • 作者简介:邵缨迪(1996—),女,硕士研究生, 研究方向为能源化工。E-mail:754114817@qq.com
  • 基金资助:
    国家自然科学基金(51966007);NSFC-云南联合基金(U1602272);云南省科技领军人才项目(2015HA019);国家重点实验室自主课题(CNMRCUTS1706)

Energy efficiency analysis of heat exchange network of isobutylene purification unit

Yingdi SHAO1(), Jianhang HU1,2(), Huili LIU2, Zhengda CAI3   

  1. 1.Engineering Research Center of Metallurgical Energy Conservation and Emission Reduction, Ministry of Education, Kunming 650093, Yunnan, China
    2.National Joint Engineering Research Center of Energy Saving and Environmental Protection Technology in Metallurgical Industry, Kunming 650093, Yunnan, China
    3.Yunnan Institute of Science and Technology, Kunming 650228, Yunnan, China
  • Received:2020-04-30 Online:2020-11-20 Published:2020-11-17
  • Contact: Jianhang HU

摘要:

基于Aspen Plus对抽余C4提取高纯度异丁烯的工艺流程进行系统灵敏度分析,并以目前我国用户最重视的能源消耗问题与投资成本问题等为改造优化目标,基于Aspen Energy Analyzer对换热网络进行优化分析。对系统灵敏度进行分析得出:在精制塔理论塔板数为36、回流比为5的优化条件下,精制后异丁烯的质量纯度可达到99.95%,回收率可达到99.6% 。本文从夹点理论概念设计法着手,对异丁烯提纯装置换热并对其换热网络进行能效分析,结果表明,在反应温度为60℃,D006树脂做催化剂,结合Aspen Energy Analyzer优化后的能耗参数,计算得出工艺流程的热公用工程用量达到1944.17kW,相比原工艺过程的用能节约了12.9%;冷公用工程用量达到3877.78 kW,相比原工艺流程节约了23.4%,大幅度提升节能降耗效果并节省投资,因此本研究可以为能量的更优利用提供理论依据和可行方案。

关键词: 换热网络, Aspen Plus, Aspen Energy Analyzer, 夹点技术

Abstract:

Based on Aspen Plus, a systematic sensitivity analysis of the extraction process of high purity isobutene from extracted C4 is carried out, and the energy consumption and investment cost, which are the most important problems for Chinese consumers, are taken as the optimization targets, optimization analysis of heat exchanger network based on Aspen Energy Analyzer. The system sensitivity analysis shows that the purity of isobutene can reach 99.95% and the recovery can reach 99.6% under the optimum conditions of theoretical plate number 36 and reflux ratio 5. Based on the conceptual design method of pinch theory, analyzing the heat exchange of isobutene purification unit and its heat exchange network, the result demonstrates, at 60℃, and D006 resin as catalyst, and combines the Energy consumption parameters optimized by Aspen Energy Analyzer, the calculation results show that the energy consumption of the heat utility project reaches 1944.17kW, which saves 12.9% compared with the original process, and that of the cold utility project.

Key words: heat exchanger network, Aspen Plus, Aspen Energy Analyzer, pinch technology

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