Homogeneous and Heterogeneous Catalyzed Esterification of Acrylic Acid with Ethanol: Reaction Kinetics and Modeling

被引:41
作者
Jyoti, Ghoshna [1 ]
Keshav, Amit [1 ]
Anandkumar, J. [1 ]
Bhoi, Stutee [2 ]
机构
[1] Natl Inst Technol Raipur, Dept Chem Engn, Raipur, Madhya Pradesh, India
[2] Indian Inst Technol Kharagpur, Dept Chem Engn, Kharagpur, W Bengal, India
关键词
LIQUID-PHASE ESTERIFICATION; ION-EXCHANGE-RESINS; CARBON-CHAIN LENGTH; ACETIC-ACID; PROPIONIC-ACID; PERVAPORATION MEMBRANE; N-BUTANOL; ALCOHOL; METHANOL; DISTILLATION;
D O I
10.1002/kin.21167
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Kinetics of esterification of acrylic acid with ethanol in the presence of homogeneous (H2SO4, HCl, p-TSA, HI) catalysts as well as heterogeneous catalysts (Dowex 50WX, Amberlyst 15) was studied. The effects and performance of these catalysts on the conversion of acrylic acid were evaluated. In the kinetics of homogeneous catalyzed reaction, both concentration and activity-based model were employed. Activity coefficients were predicted by the Universal Functional group Contribution (UNIFAC) method to consider nonideal behavior of the liquid phase. The heterogeneous catalyzed reaction mechanisms were developed using Eley-Rideal theory. The model results were compared with the experimental results and were in good agreement. The temperature dependency of the constants, reaction enthalpy, and entropy, and activation energy were determined. The conversion of acrylic acid was obtained as 63.2%, 61.02%, 53.3%, 21.4%, 34.96%, and 14.84% for H2SO4, p-TSA, HCl, HI, Dowex 50WX, and Amberlyst 15, respectively, under process temperature of 70 degrees C, reactant molar ratio of 1:1, and catalyst concentration of 2% (v/v) for homogeneous and 2.17 g for heterogeneous catalyst. These outcomes provide an approach to understand the significant effect of each catalyst on the esterification kinetics of acrylic acid and ethanol.
引用
收藏
页码:370 / 380
页数:11
相关论文
共 37 条
  • [1] Kinetics of esterification of palmitic acid with isopropanol using p-toluene sulfonic acid and zinc ethanoate supported over silica gel as catalysts
    Aafaqi, R
    Mohamed, AR
    Bhatia, S
    [J]. JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2004, 79 (10) : 1127 - 1134
  • [2] Synthesis of esters: Development of the rate expression for the Dowex 50 Wx8-400 catalyzed esterification of propionic acid with 1-propanol
    Ali, Sami H.
    Tarakmah, Alia
    Merchant, Sabiha Q.
    Al-Sahhaf, Taher
    [J]. CHEMICAL ENGINEERING SCIENCE, 2007, 62 (12) : 3197 - 3217
  • [3] Kinetics study of esterification of acetic acid with isobutanol in the presence of amberlite catalyst
    Altiokka, MR
    Çitak, A
    [J]. APPLIED CATALYSIS A-GENERAL, 2003, 239 (1-2) : 141 - 148
  • [4] Bart HJ, 1996, INT J CHEM KINET, V28, P649
  • [5] Bhatia S., 1973, ION EXCH MEMBR, V1, P127
  • [6] Process optimization and kinetic modeling for esterification of propionic acid with benzyl alcohol on ion-exchange resin catalyst
    Chandane, Vishal Suresh
    Rathod, Ajit Pralhad
    Wasewar, Kailas Lachchhuram
    Sonawane, Shriram Shaligram
    [J]. KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2017, 34 (04) : 987 - 996
  • [7] Liquid phase esterification of acrylic acid with 1-butanol catalyzed by solid acid catalysts
    Chen, X
    Xu, Z
    Okuhara, T
    [J]. APPLIED CATALYSIS A-GENERAL, 1999, 180 (1-2) : 261 - 269
  • [8] Experimental study of feasibility in kinetically-controlled reactive distillation
    Chiplunkar, M
    Hong, M
    Malone, MF
    Doherty, MF
    [J]. AICHE JOURNAL, 2005, 51 (02) : 464 - 479
  • [9] Reaction kinetics of the esterification of myristic acid with isopropanol and n-propanol using p-toluene sulphonic acid as catalyst
    de Jong, M. C.
    Feijt, R.
    Zondervan, E.
    Nijhuis, T. A.
    de Haan, A. B.
    [J]. APPLIED CATALYSIS A-GENERAL, 2009, 365 (01) : 141 - 147
  • [10] FOMIN VA, 1991, J APPL CHEM-USSR+, V64, P1811