化工学报 ›› 2023, Vol. 74 ›› Issue (7): 2988-2998.DOI: 10.11949/0438-1157.20230240

• 过程系统工程 • 上一篇    下一篇

基于自热再生的隔壁塔深冷空分工艺设计及优化

文兆伦1(), 李沛睿1, 张忠林1(), 杜晓1, 侯起旺1,2, 刘叶刚1,3, 郝晓刚1(), 官国清4   

  1. 1.太原理工大学化学工程与技术学院,山西 太原 030024
    2.中化二建集团有限公司,山西 太原 030021
    3.上海电气集团国控环球工程有限公司,山西 太原 030001
    4.日本弘前大学地域战略研究所,日本 青森 030-0813
  • 收稿日期:2023-03-15 修回日期:2023-06-16 出版日期:2023-07-05 发布日期:2023-08-31
  • 通讯作者: 张忠林,郝晓刚
  • 作者简介:文兆伦(1997—),男,硕士研究生,2269135417@qq.com
  • 基金资助:
    国家自然科学基金项目(U1710101)

Design and optimization of cryogenic air separation process with dividing wall column based on self-heat regeneration

Zhaolun WEN1(), Peirui LI1, Zhonglin ZHANG1(), Xiao DU1, Qiwang HOU1,2, Yegang LIU1,3, Xiaogang HAO1(), Guoqing GUAN4   

  1. 1.College of Chemical Engineering and Technology, Taiyuan University of Technology, Taiyuan 030024, Shanxi, China
    2.China Chemical Engineering Second Construction Corporation, Taiyuan 030021, Shanxi, China
    3.Shanghai Electric Guokong Global Engineering Corporation, Taiyuan 030001, Shanxi, China
    4.Institute of Regional Innovation, Hirosaki University, Aomori 030-0813, Japan
  • Received:2023-03-15 Revised:2023-06-16 Online:2023-07-05 Published:2023-08-31
  • Contact: Zhonglin ZHANG, Xiaogang HAO

摘要:

工业气体应用广泛,当前常用深冷精馏法获取,工艺能耗巨大,其中压缩和精馏部分的耗能占比最大。基于自热再生和隔壁塔技术,提出了一种隔壁塔深冷空分方案,用单塔精馏空分过程代替双塔精馏空分过程,利用自热再生优化过程换热。利用夹点原理对优化前后的工艺进行能量分析,并从总能量消耗(TEC)、二氧化碳排放量([CO2]em)、年度总费用(TAC)三个角度分别进行评价。结果表明,基于自热再生的隔壁塔深冷空分工艺较常规空分工艺,制氧消耗降低了26.19%,二氧化碳排放减少了25.18%,年度总费用降低了31.93%。利用自热再生技术和隔壁塔技术优化后的空分工艺,在节能、经济以及环保方面表现出更强的优越性。

关键词: 自热再生, 隔壁塔, 空气分离, 计算机模拟, 优化设计, 系统节能

Abstract:

Industrial gases commonly obtained by cryogenic distillation are widely used currently. The energy consumption of the process is always huge, and the energy consumption of compression and rectification accounts for the largest proportion. A cryogenic air separation process with a dividing wall column was proposed based on the self-heat regeneration, in which the double-tower distillation air separation process was replaced by a single-tower distillation process applying the self-heat regeneration technology to complete the process of heat exchange. The energy of the process was analyzed by the pinch principle, and the total energy consumption (TEC), carbon dioxide emissions ([CO2]em), and total annual cost (TAC) were evaluated, respectively. The results showed the cryogenic air separation process based on the self-heating regeneration in the dividing wall column reduced energy consumption for oxygen production by 26.19%, CO2 emission by 25.18%, and the TAC by 31.93%. The optimized air separation process using self-heat regeneration technology and dividing wall column technology has shown stronger advantages in energy saving, economy, and environmental protection.

Key words: self-heat regeneration, dividing wall column, air separation, computer simulation, optimal design, systemic energy saving

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