A review of advances in production and separation of xylene isomers

被引:64
作者
Shi, Qian [1 ]
Gonsalves, Jonathan C. [2 ]
Ferreira, Alexandre F. P. [2 ]
Rodrigues, Alirio E. [2 ]
机构
[1] Sinopec Beijing Res Inst Chem Ind, 14,North 3rd Ring East Rd, Beijing, Peoples R China
[2] Univ Porto, Lab Separat & React Engn, Lab Catalysis & Mat LSRE LCM, Dept Chem Engn, Dr Roberto Frias S-N, P-4200465 Porto, Portugal
关键词
Xylene; Production; Separation; Simulated Moving Bed; Process intensification; Energy integration; SIMULATED MOVING-BED; DISTILLATION-COLUMNS SEQUENCE; VAPOR-PHASE ADSORPTION; P-XYLENE; LIQUID-PHASE; MEMBRANE REACTOR; ZEOLITE MEMBRANE; MINIMUM ENERGY; MFI MEMBRANES; ISOMERIZATION;
D O I
10.1016/j.cep.2021.108603
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The global p-xylene market has demonstrated positive growth thanks to increasing demand for polyester fibers in the textile industry. Additionally, the chemical process becomes a target for energy efficiency; thus, process improvement and intensification have increasingly gained the attention of the scientific community. This article summarizes the advances in the production and separation of xylene isomers. An overview of the aromatics complex is displayed followed by a detailed description of the p-xylene production and separation processes. It summarizes the improvement of the catalysts, adsorbents, advanced materials; processes that strengthen the performance of the existing units, membrane-based processes, and alternative sources in past years. Special attention is given to the Simulated Moving Bed technology for separation; the flushing strategies and model development studies are also addressed. Attention has also been given to the process intensification and the unit combination with other aromatic technologies. A brief review of the latest results of Simulated Moving Bed Reactor and heat integration is also included. In summary, process intensification and integration are promising to save energy and costs, and it also allows flexibility within the feeds and intermediate products, maximizing the advantages of each process.
引用
收藏
页数:16
相关论文
共 154 条
[1]   Liquid-Phase Multicomponent Adsorption and Separation of Xylene Mixtures by Flexible MIL-53 Adsorbents [J].
Agrawal, Mayank ;
Bhattacharyya, Souryadeep ;
Huang, Yi ;
Jayachandrababu, Krishna C. ;
Murdock, Christopher R. ;
Bentley, Jason A. ;
Rivas-Cardona, Alejandra ;
Mertens, Machteld M. ;
Walton, Krista S. ;
Sholl, David S. ;
Nair, Sankar .
JOURNAL OF PHYSICAL CHEMISTRY C, 2018, 122 (01) :386-397
[2]   Recent Advances in Reactions of Alkylbenzenes Over Novel Zeolites: The Effects of Zeolite Structure and Morphology [J].
Al-Khattaf, Sulaiman ;
Ali, Syed A. ;
Aitani, Abdullah M. ;
Zilkova, Nadezda ;
Kubicka, David ;
Cejka, Jiri .
CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 2014, 56 (04) :333-402
[3]   Selective adsorption and separation of xylene isomers and ethylbenzene with the microporous vanadium(IV) terephthalate MIL-47 [J].
Alaerts, Luc ;
Kirschhock, Christine E. A. ;
Maes, Michael ;
van der Veen, Monique A. ;
Finsy, Vincent ;
Depla, Anouschka ;
Martens, Johan A. ;
Baron, Gino V. ;
Jacobs, Pierre A. ;
Denayer, Joeri E. M. ;
De Vos, Dirk E. .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2007, 46 (23) :4293-4297
[4]  
Alario F., 2002, BOOSTYOU XYLENE LOOP
[5]  
Amelse J., 2018, Patent No. [US 9902666B2, 9902666]
[6]  
Amelse J., 2004, 2004 AICHE SPRING NA, P2278
[7]  
Amelse J.A., 2008, Patent No. [US 7405340B2, 7405340]
[8]  
Antos G., 2004, CATALYTIC NAPHTHA RE, DOI DOI 10.1016/j.cep.2008.06.012
[9]   Modeling adsorption equilibria of xylene isomers in a microporous metal-organic framework [J].
Barcia, Patrick S. ;
Nicolau, Marco P. M. ;
Gallegos, Jose M. ;
Chen, Banglin ;
Rodrigues, Alirio E. ;
Silva, Jose A. C. .
MICROPOROUS AND MESOPOROUS MATERIALS, 2012, 155 :220-226
[10]  
Bentley J., 2019, Patent No. [US 10392324B2, 10392324]