进料组成对中部蒸汽压缩两段式精馏塔节能与经济效益的影响

doi:10.16085/j.issn.1000-6613.2020-0765

化工进展 ›› 2020, Vol. 39 ›› Issue (12): 5042-5048.DOI: 10.16085/j.issn.1000-6613.2020-0765

• 专栏：煤基甲醇制燃料和化学品新技术 • 上一篇下一篇

进料组成对中部蒸汽压缩两段式精馏塔节能与经济效益的影响

陈颢(), 从海峰(), 何林, 李洪, 高鑫, 李鑫钢

天津大学化工学院，精馏技术国家工程研究中心，天津化学化工协同创新中心，天津 300350

出版日期:2020-12-05 发布日期:2020-12-02
通讯作者: 从海峰
作者简介:陈颢（1992—），男，博士研究生，研究方向为能量集成。E-mail：cherly@tju.edu.cn。
基金资助:
国家重点研发计划(2018YFB0604903)

Influence of feed compositions on energy-saving and economic benefit of the novel middle vapor recompression distillation column

Hao CHEN(), Haifeng CONG(), Lin HE, Hong LI, Xin GAO, Xingang LI

School of Chemical Engineering and Technology, Tianjin University, National Engineering Research Centre of Distillation Technology, Collaborative Innovation Center of Chemical Science and Engineering (Tianjin), Tianjin 300072, China

Online:2020-12-05 Published:2020-12-02
Contact: Haifeng CONG

摘要/Abstract

摘要：

提出一种中部蒸汽压缩两段式新型精馏塔，并以丙烯和丙烷分离过程为例，对中部蒸汽压缩两段式精馏塔与常规精馏塔的性能进行比较。通过使用Aspen Plus模拟软件对流程建模及优化，探讨了丙烯和丙烷在不同配比进料条件情况下对中部蒸汽压缩两段式精馏塔的节能效果、全局有效能损失和经济效益的影响。结果发现，中部蒸汽压缩两段式精馏塔相比于常规精馏塔有着良好的节能效果，在丙烯和丙烷比例为3∶1时节能效果最为显著。中部蒸汽压缩两段式精馏塔比常规精馏塔全局有效能损失明显减少，并且受进料组成配比的影响不大。在经济投资方面，中部蒸汽压缩两段式精馏塔有着良好的经济效益，最后的年总投资节省率受进料组成配比的影响不大。说明该中部蒸汽压缩两段式精馏塔在进料组成配比上具有良好的适应性。

关键词: 进料组成, 精馏, 中部蒸汽压缩, 节能, 经济效益

Abstract:

In this study, a novel middle vapor recompression distillation column (MVRC) was proposed and compared with the conventional distillation column (CD). Meanwhile, their performance was investigated by the separation of the propylene and propane. Process modeling and optimization were realized by using the Aspen Plus simulation software, and the energy-saving, overall exergy loss, and economic benefits were discussed according to different ratios of propylene to propane. The results show that the MVRC has good energy-saving effect compared with CD, especially, it is the most significant when the ratio of propylene to propane is 3∶1. The MVRC has a significant overall exergy loss reduction compared with CD, and almost unaffected by the different ratios of propylene to propane in the feed. In terms of economic investment, the large economic benefit is obtained in the MVRC and the total annual investment saving rate is affected little by the feed composition ratio. It shows that the middle vapor recompression distillation column has good adaptability in feed composition ratio.

Key words: feed composition, distillation, middle vapor recompression, energy-saving, economic benefit

中图分类号:

TQ028

陈颢, 从海峰, 何林, 李洪, 高鑫, 李鑫钢. 进料组成对中部蒸汽压缩两段式精馏塔节能与经济效益的影响[J]. 化工进展, 2020, 39(12): 5042-5048.

Hao CHEN, Haifeng CONG, Lin HE, Hong LI, Xin GAO, Xingang LI. Influence of feed compositions on energy-saving and economic benefit of the novel middle vapor recompression distillation column[J]. Chemical Industry and Engineering Progress, 2020, 39(12): 5042-5048.

参考文献

1	NIGAM P S, SINGH A. Production of liquid biofuels from renewable resources[J]. Progress in Energy and Combustion Science, 2011, 37(1): 52-68.
2	HOLTBRUEGGE J, WIERSCHEM M, LUTZE P. Synthesis of dimethyl carbonate and propylene glycol in a membrane-assisted reactive distillation process: pilot-scale experiments, modeling and process analysis[J]. Chemical Engineering and Processing: Process Intensification, 2014, 84: 54-70.
3	YANG A, SUN S, ESLAMIMANESH A, et al. Energy-saving investigation for diethyl carbonate synthesis through the reactive dividing wall column combining the vapor recompression heat pump or different pressure thermally coupled technique[J]. Energy, 2019, 172: 320-332.
4	YANG A, JIN S, SHEN W, et al. Investigation of energy-saving azeotropic dividing wall column to achieve cleaner production via heat exchanger network and heat pump technique[J]. Journal of Cleaner Production, 2019, 234: 410-422.
5	SUN S, YANG A, CHIEN I L, et al. Intensification and performance assessment for synthesis of 2-methoxy-2-methyl-heptane through the combined use of different pressure thermally coupled reactive distillation and heat integration technique[J]. Chemical Engineering and Processing: Process Intensification, 2019, 142: 107561.
6	YANG A, SU Y, SHEN W, et al. Multi-objective optimization of organic Rankine cycle system for the waste heat recovery in the heat pump assisted reactive dividing wall column[J]. Energy Conversion and Management, 2019, 199: 112041.
7	SHI T, CHUN W, YANG A, et al. Optimization and control of energy saving side-stream extractive distillation with heat integration for separating ethyl acetate-ethanol azeotrope[J].Chemical Engineering Science, 2020, 215: 115373.
8	SHI T, CHUN W, YANG A, et al. The process control of the triple-column pressure-swing extractive distillation with partial heat integration[J]. Separation and Purification Technology, 2020, 238: 116416.
9	CHEN H, LI X, HE L, et al. Energy, exergy, economic, and environmental analysis for methyl acetate hydrolysis process with heat integrated technology used[J]. Energy Conversion and Management, 2020, 216: 112919.
10	WAHEED M A, ONI A O, ADEJUYIGBE S B, et al. Performance enhancement of vapor recompression heat pump[J]. Applied Energy, 2014, 114: 69-79.
11	方静, 刁梦宇, 李春利, 等. 内部热耦合塔的热力学分析和节能研究[J].化工进展, 2019, 38(2): 834-841.
11	FANG Jing, DIAO Mengyu, LI Chunli, et al. Study on thermodynamic analysis and energy saving of heat integrated distillation column[J]. Chemical Industry and Engineering Progress, 2019, 38(2): 834-841.
12	SHAHANDEH H, IVAKPOUR J, KASIRI N. Internal and external HIDiCs (heat-integrated distillation columns) optimization by genetic algorithm[J]. Energy, 2014, 64：875-886.
13	PAPASTATHOPOULOU H S, LUYBEN W L. Control of a binary sidestream distillation column[J]. Industrial & Engineering Chemistry Research, 1991, 30(4): 705-713.
14	HARWARDT A, MARQUARDT W. Heat-integrated distillation columns: vapor recompression or internal heat integration?[J]. AIChE Journal, 2012, 58(12): 3740-3750.
15	? OLUJI?, SUN L, DE RIJKE A, et al. Conceptual design of an internally heat integrated propylene-propane splitter[J]. Energy, 2006, 31(15): 3083-3096.
16	SCHMAL J P, KOOI H J VAN DER, DE RIJKE A, et al. Internal versus external heat integration: operational and economic analysis[J]. Chemical Engineering Research and Design, 2006, 84(5): 374-380.
17	SUPHANIT B. Optimal heat distribution in the internally heat-integrated distillation column (HIDiC)[J]. Energy, 2011, 36(7): 4171-4181.
18	T-J HO, HUANG C-T, L-S LEE, et al. Extended Ponchon-Savarit method for graphically analyzing and designing internally heat-integrated distillation columns[J]. Industrial & Engineering Chemistry Research, 2010, 49(1): 350-358.
19	KIRAN B, JANA A K, SAMANTA A N. A novel intensified heat integration in multicomponent distillation[J]. Energy, 2012, 41(1): 443-453.
20	BISGAARD T, HUUSOM J K, ABILDSKOV J. Modeling and analysis of conventional and heat-integrated distillation columns[J]. AIChE Journal, 2015, 61(12): 4251-4263.
21	李萱, 李洪, 高鑫, 等. 热耦合精馏工艺的模拟[J]. 化工进展, 2016, 35(1): 48-56.
21	LI Xuan, LI Hong, GAO Xin, et al. Simulation on heat integrated distillation technology[J]. Chemical Industry and Engineering Progress, 2016, 35(1):48-56.
22	DOUGLAS J M. Conceptual design of chemical processes[M]. New York: McGraw-Hill New York, 1988.

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进料组成对中部蒸汽压缩两段式精馏塔节能与经济效益的影响

Influence of feed compositions on energy-saving and economic benefit of the novel middle vapor recompression distillation column

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