Design and optimization for the separation of xylene isomers with a novel double extractants-based extractive distillation

被引:4
作者
Zhang, Fangkun [1 ]
Wang, Yunlong [1 ]
Shan, Baoming [1 ]
Cui, Peizhe [2 ]
Wang, Yinglong [2 ]
Zhu, Zhaoyou [2 ]
Xu, Qilei [1 ]
机构
[1] Qingdao Univ Sci & Technol, Coll Automat & Elect Engn, Qingdao 266061, Peoples R China
[2] Qingdao Univ Sci & Technol, Coll Chem Engn, Qingdao 266042, Peoples R China
关键词
Xylene separation; Extractive distillation; Process Design; Process optimization; TAC; P-XYLENE; REACTIVE DISTILLATION; SIMULATION; MIXTURE;
D O I
10.1016/j.jiec.2024.05.027
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Xylene is a crucial chemical raw material, serving as a synthetic monomer and solvent extensively employed in coating, medicine, rubber and other industries. It contains of three isomers: o-xylene (OX), m-xylene (MX), and pxylene (PX), their separation is considered a worldwide challenge due to their extremely close boiling points. A novel extractive distillation based on double extractants is first proposed to separate these isomers in this paper, while it was considered impractical to separate these isomers by distillation technology alone in the past. Through the analysis of residual curve and extractant screening, two potential solvents, i.e., N-Methylpyrrolidone (NMP) and Tetramethylene sulfone (Sul) were used as extractants, and then the separation sequences were designed and optimized. The extractive distillation processes were optimized by sequential iterative method according to the minimum total annual cost (TAC), and the best separation sequence and process parameters were determined. For comparison, it was found that the optimized double extractant-based extractive distillation (DEED) process has the best economic performance with TAC of 5.72x10(6)$, and the energy consumption was greatly reduced by 41.2% compared to the single extractant-based extractive distillation (SEED). This article provides a new perspective on energy-efficient distillation technology for industrial xylene separation and purification production.
引用
收藏
页码:502 / 513
页数:12
相关论文
共 34 条
  • [1] Al-Nakash N.B., 2009, Eng. Technol. J., V27
  • [2] Hybrid Distillation/Melt Crystallization Process Using Thermally Coupled Arrangements: Optimization with evolutive algorithms
    Bravo-Bravo, Cristofer
    Gabriel Segovia-Hernandez, Juan
    Hernandez, Salvador
    Israel Gomez-Castro, Fernando
    Gutierrez-Antonio, Claudia
    Briones-Ramirez, Abel
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2013, 67 : 25 - 38
  • [3] Vapour-liquid equilibrium for xylenes plus tetrapropylene glycol binary systems: Experimental data and regression
    Fendu, Elena M.
    [J]. JOURNAL OF CHEMICAL THERMODYNAMICS, 2023, 178
  • [4] Optimization of the Design and Operation of Extractive Distillation Processes
    Figueiredo, M. F.
    Brito, K. D.
    Ramos, W. B.
    Vasconcelos, L. G. S.
    Brito, R. P.
    [J]. SEPARATION SCIENCE AND TECHNOLOGY, 2015, 50 (14) : 2238 - 2247
  • [5] Simulated moving bed reactor for p-xylene production: Dual-bed column
    Goncalves, Jonathan C.
    Rodrigues, Alirio E.
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2016, 104 : 75 - 83
  • [6] A nanoscopic approach on benzene-toluene-xylenes extraction by sulfolane
    Gutierrez, Alberto
    Atilhan, Mert
    Aparicio, Santiago
    [J]. JOURNAL OF MOLECULAR LIQUIDS, 2018, 249 : 1039 - 1046
  • [7] Li L., 2022, Science, V377, P335
  • [8] Simulation of sulfolane extraction distillation process
    Liu, Dexin
    [J]. CHEMICAL, MATERIAL AND METALLURGICAL ENGINEERING III, PTS 1-3, 2014, 881-883 : 324 - 328
  • [9] Lusi M, 2012, Angew. Chem. Int. Ed., V51, P3928
  • [10] Luyben W.L, 2013, Distillation design and control using Aspen simulation