Design and optimization of the separation process of acrylic acid and corresponding esters from aqueous solution of formaldehyde-a systematic procedure

被引:1
作者
Li, Jie [1 ,2 ]
Yang, Dan [2 ]
Peng, Zhijian [1 ]
Li, Chunshan [2 ]
Nie, Yi [3 ]
机构
[1] China Univ Geosci, Sch Engn & Technol, 29 Xueyuan Rd, Beijing 100083, Peoples R China
[2] Chinese Acad Sci, Inst Proc Engn, Key Lab Multiphase Complex Syst, Beijing Key Lab Ion Liquids Clean Proc,Key Lab Gr, Beijing 100190, Peoples R China
[3] Zhengzhou Inst Emerging Technol Ind, Zhengzhou 450000, Henan, Peoples R China
关键词
acrylic acid (esters); formaldehyde; separation; systematic procedure; VAPOR-LIQUID-EQUILIBRIUM; METHYL ACETATE; CHEMICAL-EQUILIBRIA; PHASE-EQUILIBRIA; ACETIC-ACID; WATER; MIXTURES; METHANOL; DISTILLATION; PERFORMANCE;
D O I
10.1002/cjce.22967
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The design and optimization of the separation process of acrylic acid and corresponding esters in formaldehyde aqueous solution was systematically researched in this work. Thermodynamics was provided for formaldehyde, acrylic acid, and corresponding esters system according to the particularly. On basis of the thermodynamics, optional separation sequence and separation technology were designed, which reduced separation complexity and search scope. In addition, system integration including process optimization and energy integration were optimized in detail in the procedure. The proposed systematic procedure was applied to acrylic acid and corresponding esters production using methyl acetate and formaldehyde as raw materials. The systematic procedure provided a significant guidance for the separation of the formaldehyde, acrylic acid, and corresponding esters.
引用
收藏
页码:749 / 755
页数:7
相关论文
共 32 条
[1]   New method for acrylic acid recovery from industrial waste water via esterification with 2-ethyl hexanol [J].
Ahmad, M. A. A. ;
Kamaruzzaman, M. R. ;
Chin, S. Y. .
PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 2014, 92 (06) :522-531
[2]   Vapor-liquid and chemical equilibria of formaldehyde-water mixtures [J].
Albert, M ;
García, BC ;
Kreiter, C ;
Maurer, G .
AICHE JOURNAL, 1999, 45 (09) :2024-2033
[3]   Vapor-liquid equilibrium of formaldehyde mixtures: New data and model revision [J].
Albert, M ;
Hahnenstein, I ;
Hasse, H ;
Maurer, G .
AICHE JOURNAL, 1996, 42 (06) :1741-1752
[4]   Vapor-liquid equilibrium of aqueous solutions of formaldehyde and methanol [J].
Albert, M ;
García, BC ;
Kuhnert, C ;
Peschla, R ;
Maurer, G .
AICHE JOURNAL, 2000, 46 (08) :1676-1687
[5]  
[Anonymous], 2000, INT J THERMODYN
[6]  
Bernatov S., 2006, Fluid Phase Equilib, V247, P96
[7]   Linking pinch analysis and bridge analysis to save energy by heat-exchanger network retrofit [J].
Bonhivers, Jean-Christophe ;
Moussavi, Alireza ;
Alva-Argaez, Alberto ;
Stuart, Paul R. .
APPLIED THERMAL ENGINEERING, 2016, 106 :443-472
[8]   Vapor-Liquid Equilibrium and Liquid-Liquid Equilibrium of Methyl Acetate plus Methanol+1-Ethyl-3-methylimidazolium Acetate [J].
Cai, Jialin ;
Cui, Xianbao ;
Zhang, Ying ;
Li, Rui ;
Feng, Tianyang .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2011, 56 (02) :282-287
[9]   Investigation on Isobaric Vapor-Liquid Equilibrium for Water plus Acetic Acid plus sec-Butyl Acetate [J].
Chai, Qing ;
Wan, Hui ;
Wang, Lei ;
Guan, Guofeng .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2014, 59 (06) :1998-2003
[10]   Phase equilibria of aqueous solutions of formaldehyde and methanol: Improved approach using UNIQUAC coupled to chemical equilibria [J].
Detcheberry, M. ;
Destrac, P. ;
Meyer, X. -M. ;
Condoret, J. -S. .
FLUID PHASE EQUILIBRIA, 2015, 392 :84-94