Feasibility and synthesis of hybrid reactive distillation systems

被引:14
|
作者
Chadda, N
Malone, MF [1 ]
Doherty, MF
机构
[1] Univ Massachusetts, Dept Chem Engn, Amherst, MA 01003 USA
[2] Univ Calif Santa Barbara, Dept Chem Engn, Santa Barbara, CA 93106 USA
关键词
D O I
10.1002/aic.690481206
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A systematic method to synthesize hybrid reactive distillation configurations described here uses three building blocks. These building blocks are a cocurrent rectifying cascade, a cocurrent stripping cascade, and a countercurrent cascade. A feasibility diagram and a product purity diagram provide a global view of the "direct" and "indirect" sharp split products that can be obtained as a function of the reaction rate from single-feed and double-feed hybrid columns, respectively. These diagrams are used as a basis for quickly and systematically generating feasible column configurations (if any) that produce the desired product. Three esterification examples are used to illustrate the method. In spite of the fact that the examples form a homologous series, the feasible designs are quite different. The results compare well with column simulations.
引用
收藏
页码:2754 / 2768
页数:15
相关论文
共 50 条
  • [1] Feasibility of reactive distillation for methanol synthesis
    Ghosh, Shashwata
    Seethamraju, Srinivas
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2019, 145
  • [2] Feasibility studies on quaternary reactive distillation systems
    Lee, JW
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (18) : 4632 - 4642
  • [3] Feasibility study of batch reactive distillation in hybrid columns
    Steger, Csaba
    Rev, Endre
    Fonyo, Zsolt
    Meyer, Michel
    Lelkes, Zoltan
    16TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING AND 9TH INTERNATIONAL SYMPOSIUM ON PROCESS SYSTEMS ENGINEERING, 2006, 21 : 1063 - 1068
  • [4] Feasibility of reactive distillation for Fischer-Tropsch synthesis
    Srinivas, S.
    Malik, Ranjan K.
    Mahajani, Sanjay M.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (03) : 889 - 899
  • [5] A Generic Feasibility Study of Batch Reactive Distillation in Hybrid Configurations
    Steger, C.
    Lukacs, T.
    Rev, E.
    Meyer, M.
    Lelkes, Z.
    AICHE JOURNAL, 2009, 55 (05) : 1185 - 1199
  • [6] Generalized feasibility evaluation of equilibrated quaternary reactive distillation systems
    Chin, J
    Kattukaran, HJ
    Lee, JW
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (22) : 7092 - 7102
  • [7] Optimal design and operation of reactive distillation systems and reactive dividing wall systems with pressure swing distillation and hybrid distillation-pervaporation
    Duanmu, Fanyi
    Chia, Dian Ning
    Tsatse, Aikaterini
    Sorensen, Eva
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2024, 201
  • [8] Feasibility of Reactive Distillation for Ternary Systems with Azeotropic Mixtures: Decomposition Reaction
    Chen, Chin-Shih
    Ward, Jeffrey D.
    Yu, Cheng-Ching
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (03) : 1305 - 1320
  • [9] MINLP Synthesis of Reactive Distillation Using a Disjunctive, Hybrid Model
    Ropotar, Marcel
    Pintaric, Zorka Novak
    Reneaume, Jean-Michel
    Kravanja, Zdravko
    10TH INTERNATIONAL SYMPOSIUM ON PROCESS SYSTEMS ENGINEERING, 2009, 27 : 543 - 548
  • [10] Feasibility of Reactive Distillation for Fischer-Tropsch Synthesis. 3.
    Srinivas, Seethamraju
    Malik, Ranjan K.
    Mahajani, Sanjay M.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (10) : 4719 - 4730