Optimization of Batch Heteroazeotropic Distillation Operational Strategies with Entrainer Recycle

被引:5
|
作者
Hegely, Laszlo [1 ]
Lang, Peter [1 ]
机构
[1] Budapest Univ Technol & Econ, Dept Bldg Serv & Proc Engn, Muegyetem Rkp 3-9, H-1111 Budapest, Hungary
来源
28TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING | 2018年 / 43卷
关键词
batch heteroazeotropic distillation; optimization; entrainer recycle; ISOPROPYL-ALCOHOL; TOLUENE; SYSTEM; WATER;
D O I
10.1016/B978-0-444-64235-6.50262-X
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The batch heteroazeotropic distillation (BHAD) separation of a minimum boiling azeotropic mixture (isopropyl alcohol(A) - water(B)) with toluene as entrainer(E) is simulated and optimized with GA. The production cycle consists of processing three consecutive batches. Both BHAD operational modes (sequential (Mode I) and simultaneous (Mode II) distillation + decantation) are studied. The E-rich phase and (eventually) the off-cut can be recycled to the next batch to reduce the loss of both isopropyl alcohol and the entrainer. The optimization variables are the amount of E added to the charge and the reflux ratios of the steps. The effect of the recycling is discussed and the optimization results are compared with those of the non-optimized processes.
引用
收藏
页码:1505 / 1511
页数:7
相关论文
共 50 条
  • [21] Control comparison of conventional and thermally coupled ternary extractive distillation processes with recycle splitting using a mixed entrainer as separating agent
    Zhang, Qingjun
    Zeng, Aiwu
    Yuan, Xigang
    Ma, Youguang
    SEPARATION AND PURIFICATION TECHNOLOGY, 2019, 224 : 70 - 84
  • [22] Conceptual Design of Distillation Processes for Mixtures with Distillation Boundaries. II. Optimization of Recycle Policies
    Brueggermann, Stefan
    Marquardt, Wolfgang
    AICHE JOURNAL, 2011, 57 (06) : 1540 - 1556
  • [23] The Effect of Charge Composition on the Optimal Operational Parameters of a Batch Extractive Distillation Process
    Hegely, Laszlo
    Lang, Peter
    12TH INTERNATIONAL SYMPOSIUM ON PROCESS SYSTEMS ENGINEERING (PSE) AND 25TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING (ESCAPE), PT B, 2015, 37 : 1409 - 1414
  • [24] Thermodynamic Efficiency and Cost-Effective Optimization of Heterogeneous Batch Distillation
    Rodriguez-Donis, Ivonne
    Hernandez-Gonzalez, Noslen
    Gerbaud, Vincent
    Joulia, Xavier
    22 EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, 2012, 30 : 362 - 366
  • [25] Design and optimization of batch reactive distillation processes with off-cut
    Kao, Yu-Lung
    Ward, Jeffrey D.
    JOURNAL OF THE TAIWAN INSTITUTE OF CHEMICAL ENGINEERS, 2014, 45 (02) : 411 - 420
  • [26] Optimization of a batch extractive distillation process with recycling off-cuts
    Hegely, Laszlo
    Lang, Peter
    JOURNAL OF CLEANER PRODUCTION, 2016, 136 : 99 - 110
  • [27] Methyl lactate synthesis using batch reactive distillation: Operational challenges and strategy for enhanced performance
    Agar, Dhia Y.
    Rahmanian, Nejat
    Mujtaba, Iqbal M.
    SEPARATION AND PURIFICATION TECHNOLOGY, 2016, 158 : 193 - 203
  • [28] Integrated design and optimization of reactor-distillation sequence-recycle-heat exchanger network
    Yin, Changfang
    Sun, Huifeng
    Lv, Donghui
    Liu, Guilian
    ENERGY, 2022, 238
  • [29] Optimization of multiple-fraction batch distillation with detailed dynamic process model
    Li, P
    Wozny, G
    Reuter, E
    DISTILLATION AND ABSORPTION '97, VOLS 1 AND 2, 1997, (142): : 289 - 300
  • [30] Optimization of the Variable Reflux Ratio in a Batch Distillation Column through a Heuristic Method
    Manca, Davide
    CHEMICAL PRODUCT AND PROCESS MODELING, 2007, 2 (01):