热泵精馏隔壁塔分离宽沸程物系的模拟

doi:10.11949/j.issn.0438-1157.20161638

化工学报 ›› 2017, Vol. 68 ›› Issue (5): 1906-1912.DOI: 10.11949/j.issn.0438-1157.20161638

热泵精馏隔壁塔分离宽沸程物系的模拟

李沐荣¹, 许良华¹, 辛春伟¹, 袁希钢²

1 天津理工大学化学化工学院, 天津 300384;
2 天津大学化工学院化学工程联合国家重点实验室, 天津 300072

收稿日期:2016-11-18 修回日期:2017-01-10 出版日期:2017-05-05 发布日期:2017-05-05
通讯作者: 许良华
基金资助:
国家自然科学基金项目（21406170）；化学工程联合国家重点实验室开放课题项目（SKL-ChE-15B04）；天津市教委基金项目（20140509）。

Simulation of vapor recompression assisted dividing wall column for wide boiling mixture separation

LI Murong¹, XU Lianghua¹, XIN Chunwei¹, YUAN Xigang²

1 School of Chemistry and Chemical Engineering, Tianjin University of Technology, Tianjin 300384, China;
2 State Key Laboratory of Chemical Engineering, School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China

Received:2016-11-18 Revised:2017-01-10 Online:2017-05-05 Published:2017-05-05
Supported by:
supported by the National Natural Science Foundation of China (21406170), the State Key Laboratory of Chemical Engineering (SKL-ChE-15B04), and the Tianjin Municipal Education Commission (20140509).

摘要/Abstract

摘要：

将中间换热和热泵精馏两种精馏节能技术应用到隔壁塔中，提出了带中间换热器的热泵精馏隔壁塔流程，以解决隔壁塔在分离宽沸程物系时出现的塔顶与塔底温差过高而不宜应用热泵精馏的问题。利用精馏塔总复合曲线图，可确定中间产品塔板采出流股的相态，从而得到不同类型的热泵精馏隔壁塔流程。宽沸程物系分离实例的模拟计算结果表明，该类流程在主塔气液相流量较大的情况下具有较高的节能效率。

关键词: 隔壁塔, 热泵精馏, 分离, 模拟, 优化

Abstract:

Big temperature difference between the overhead and bottom of the dividing wall column (DWC) limited the application of vapor recompression technology into DWC for separating wide boiling mixture, so the DWC with vapor recompression at side product stage scheme is investigated in this paper. With the aid of CGCC profiles, the phase of stream withdrawn from side product stage can be determined, and the corresponding VRC assisted DWC schemes can be achieved. Simulation results for wide boiling mixture separation show that the proposed schemes have high energy efficiency under large vapor and liquid flow rate in the main column.

Key words: dividing wall column, vapor recompression, separation, simulation, optimization

中图分类号:

TQ028

李沐荣, 许良华, 辛春伟, 袁希钢. 热泵精馏隔壁塔分离宽沸程物系的模拟[J]. 化工学报, 2017, 68(5): 1906-1912.

LI Murong, XU Lianghua, XIN Chunwei, YUAN Xigang. Simulation of vapor recompression assisted dividing wall column for wide boiling mixture separation[J]. CIESC Journal, 2017, 68(5): 1906-1912.

参考文献 24

[1]	Dejanovic I, Matijasevic L, Olujic Z. Dividing wall column—a breakthrough towards sustainable distilling[J]. Chem. Eng. Pro., 2010, 49(6): 559-580.
[2]	Asprion N, Kaibel G. Dividing wall columns: fundamentals and recent advances[J]. Chem. Eng. Pro., 2010, 49(2): 139-146.
[3]	Yildirim O, Kiss A A, Kenig E Y. Dividing wall columns in chemical process industry: a review on current activities[J]. Sep. Purif. Technol., 2011, 80(3): 403-417.
[4]	龚超, 余爱平, 罗祎青, 等. 完全能量耦合精馏塔的设计、模拟与优化[J]. 化工学报, 2012, 63(1): 177-184. GONG C, YU A P, LUO Y Q, et al. The design, simulation and optimization of fully thermally coupled distillation column[J]. CIESC Journal, 2012, 63(1): 177-184.
[5]	Halvorsen I J, Skogestad S. Minimum energy consumption in multicomponent distillation (Ⅱ): Three-product Petlyuk arrangements[J]. Ind. Eng. Chem. Res., 2003, 42: 605-615.
[6]	Ferre J A, Castells F, Flores J. Optimization of a distillation column with a direct vapor recompression heat pump[J]. Ind. Eng. Chem. Process Des. Dev., 1985, 24(1): 128-132.
[7]	Felbab N, Patel B, El-Halwagi M M, et al. Vapor recompression for efficient distillation (Ⅰ): A new synthesis perspective on standard configurations[J]. AIChE J., 2013, 59(8): 2977-2992.
[8]	Chew J M, Reddy C C S, Rangaiah G P. Improving energy efficiency of dividing-wall columns using heat pumps, Organic Rankine Cycle and Kalina Cycle[J]. Chem. Eng. Process, 2014, 76: 45-59.
[9]	Long N V D, Minh L Q, Nhien L C, et al. Novel self-heat recuperative dividing wall column to maximize energy efficiency and column throughput in retrofitting and debottlenecking of a side stream column[J]. Appl. Energy, 2015, 159: 28-38.
[10]	Kumar V, Kiran B, Jana K A, et al. A novel multistage vapor recompression reactive distillation system with intermediate reboilers[J]. AIChE J., 2013, 59(3): 761-771.
[11]	Yu J P, Wang S J, Huang K J, et al. Improving the performance of extractive dividing-wall columns with intermediate heating[J]. Ind. Eng. Chem. Res., 2015, 54(10): 2709-2723.
[12]	Navarro-Amoros M A, Ruiz-Femenia R, Caballero J A. A new technique for recovering energy in thermally coupled distillation using vapor recompression cycles[J]. AIChE J., 2013, 59(10): 3767-3781.
[13]	Dhole V R, Linnhoff B. Distillation column targets[J]. Comput. Chem. Eng., 1993, 17: 549-560.
[14]	Chen D W, Yuan X G, XU L H, et al. Comparison between different configurations of internally and externally heat-integrated distillation by numerical simulation[J]. Ind. Eng. Chem. Res., 2013, 52(16): 5781-5790.
[15]	RAMIREZ-CORONA N, Jimenez-Gutierrez A, Castro- Aguero A, et al. Optimum design of Petlyuk and divided-wall distillation systems using a shortcut model[J]. Chem. Eng. Res. Des., 2010, 88(10): 1405-1418.
[16]	GE X L, YUAN X G, AO C, et al. Simulation based approach to optimal design of dividing wall column using random search method[J]. Comput. Chem. Eng., 2014, 68: 38-46.
[17]	GE X L, AO C, YUAN X G, et al. Investigation of the effect of the vapor split ratio decision in design on operability for DWC by numerical simulation[J]. Ind. Eng. Chem. Res., 2014, 53(34): 13383-13390.
[18]	牟祖霖, 盖晓龙, 袁希钢, 等. 三组分精馏隔板塔的操作柔性模拟与分析[J]. 化工学报, 2016, 67(2): 573-579. MU Z L, GE X L, YUAN X G, et al. Simulation and analysis of operation flexibility of divided wall column for ternary distillation[J]. CIESC Journal, 2016, 67(2): 573-579.
[19]	JANA A K, MANE A. Heat pump assisted reactive distillation: wide boiling mixture[J]. AIChE J., 2011, 57(11): 3233-3237.
[20]	TURTON R, BAILIE R C, WHITING W B, et al. Analysis, Synthesis and Design of Chemical Processes[M]. 4th ed. Upper Saddle River, NJ: Prentice Hall, 2012.
[21]	Douglas J M. Conceptual Design of Chemical Processes[M]. New York: McGraw-Hill, 1988.
[22]	Olujic Z, Sun L, deRijke A, et al. Conceptual design of an internally heat integrated propylene-propane splitter[J]. Energy, 2006, 31(15): 3083-3096.
[23]	Luo H, Bildea C S, Kiss A A. Novel heat-pump-assisted extractive distillation for bioethanol purification[J]. Ind. Eng. Chem. Res., 2015, 54(7): 2208-2213
[24]	AN D C, CAI W F, XIA M, et al. Design and control of reactive dividing-wall column for the production of methyl acetate[J]. Chem. Eng. Pro., 2015, 92: 45-60.

热泵精馏隔壁塔分离宽沸程物系的模拟

Simulation of vapor recompression assisted dividing wall column for wide boiling mixture separation

PDF (PC)

可视化

被引次数

摘要/Abstract

引用本文

使用本文

参考文献 24

相关文章 15

编辑推荐

Metrics

本文评价

[1]	杨欣, 王文, 徐凯, 马凡华. 高压氢气加注过程中温度特征仿真分析[J]. 化工学报, 2023, 74(S1): 280-286.
[2]	宋嘉豪, 王文. 斯特林发动机与高温热管耦合运行特性研究[J]. 化工学报, 2023, 74(S1): 287-294.
[3]	张思雨, 殷勇高, 贾鹏琦, 叶威. 双U型地埋管群跨季节蓄热特性研究[J]. 化工学报, 2023, 74(S1): 295-301.
[4]	叶展羽, 山訸, 徐震原. 用于太阳能蒸发的折纸式蒸发器性能仿真[J]. 化工学报, 2023, 74(S1): 132-140.
[5]	张龙, 宋孟杰, 邵苛苛, 张旋, 沈俊, 高润淼, 甄泽康, 江正勇. 管翅式换热器迎风侧翅片末端霜层生长模拟研究[J]. 化工学报, 2023, 74(S1): 179-182.
[6]	张义飞, 刘舫辰, 张双星, 杜文静. 超临界二氧化碳用印刷电路板式换热器性能分析[J]. 化工学报, 2023, 74(S1): 183-190.
[7]	王志国, 薛孟, 董芋双, 张田震, 秦晓凯, 韩强. 基于裂隙粗糙性表征方法的地热岩体热流耦合数值模拟与分析[J]. 化工学报, 2023, 74(S1): 223-234.
[8]	赵亚欣, 张雪芹, 王荣柱, 孙国, 姚善泾, 林东强. 流穿模式离子交换层析去除单抗聚集体[J]. 化工学报, 2023, 74(9): 3879-3887.
[9]	陈哲文, 魏俊杰, 张玉明. 超临界水煤气化耦合SOFC发电系统集成及其能量转化机制[J]. 化工学报, 2023, 74(9): 3888-3902.
[10]	宋明昊, 赵霏, 刘淑晴, 李国选, 杨声, 雷志刚. 离子液体脱除模拟油中挥发酚的多尺度模拟与研究[J]. 化工学报, 2023, 74(9): 3654-3664.
[11]	胡建波, 刘洪超, 胡齐, 黄美英, 宋先雨, 赵双良. 有机笼跨细胞膜易位行为的分子动力学模拟研究[J]. 化工学报, 2023, 74(9): 3756-3765.
[12]	赵佳佳, 田世祥, 李鹏, 谢洪高. SiO₂-H₂O纳米流体强化煤尘润湿性的微观机理研究[J]. 化工学报, 2023, 74(9): 3931-3945.
[13]	齐聪, 丁子, 余杰, 汤茂清, 梁林. 基于选择吸收纳米薄膜的太阳能温差发电特性研究[J]. 化工学报, 2023, 74(9): 3921-3930.
[14]	何松, 刘乔迈, 谢广烁, 王斯民, 肖娟. 高浓度水煤浆管道气膜减阻两相流模拟及代理辅助优化[J]. 化工学报, 2023, 74(9): 3766-3774.
[15]	刘远超, 关斌, 钟建斌, 徐一帆, 蒋旭浩, 李耑. 单层XSe₂（X=Zr/Hf）的热电输运特性研究[J]. 化工学报, 2023, 74(9): 3968-3978.