Distillation Sequence Efficiency (DSE) Applied to Trains of Columns with Recycle Streams

被引:2
|
作者
Bonet, Jordi [1 ]
Parra-Paz, Alex [1 ]
Bonet-Ruiz, Alexandra E. [1 ]
Plesu, Valentin [2 ]
Iancu, Petrica [2 ]
Llorens, Joan [1 ]
机构
[1] Univ Barcelona, Dept Chem Engn & Analyt Chem, Fac Chem, 1 Marti & Franques St, ES-08028 Barcelona, Spain
[2] Univ Politehn Bucuresti, Dept Chem & Biochem Engn, Ctr Technol Transfer Proc Ind, 1 Polizu St Bldg A,Room A056, RO-011061 Bucharest, Romania
关键词
infinite/infinite analysis; Gibbs diagram;
D O I
10.1016/B978-0-444-63965-3.50127-6
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Process modelling is usually simplified during chemical process analysis because it is less computing demanding and does not require so many parameters which are unknown at early stages of design. Fixing certain parameters to infinite allows to explore the process at its boundaries and the maximum attainable as indicator of the process potential. The infinity/infinity analysis assuming infinite reflux and infinite number of stages for the distillation columns trains is very useful for feasibility analysis. There are many methods in literature for distillation sequencing selection once the crude feed composition is defined. Most of them are very computing demanding and not applied to map all the feed compositions. A simple parameter called DSE (Distillation Sequence Efficiency) to rank the distillation sequences has been validated by comparing its results with the available computing demanding methods. Due to its simplicity and that requires only infinity/infinity analysis data and boiling temperatures, it has been applied to multicomponent mixtures with large amount of components. The goal of the present study is to show the potential of DSE method to solve trains of columns with recycle streams, being able to map all the feasible crude feed compositions.
引用
收藏
页码:751 / 756
页数:6
相关论文
共 50 条
  • [41] Improving efficiency of distillation with new thermally-coupled configurations of columns
    Agrawal, R
    Fidkowski, ZT
    [J]. FIFTH INTERNATIONAL CONFERENCE ON FOUNDATIONS OF COMPUTER-AIDED PROCESS DESIGN, 2000, 96 (323): : 381 - 384
  • [42] FRACTIONATING EFFICIENCY OF VARIOUS PACKINGS - IN DISTILLATION COLUMNS OPERATING AT REDUCED PRESSURE
    MYLES, M
    FELDMAN, J
    WENDER, I
    ORCHIN, M
    [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1951, 43 (06): : 1452 - 1456
  • [43] Improving energy efficiency of distillation using heat pump assisted columns
    Reddy, C. C. S.
    Fang, Y.
    Rangaiah, G. P.
    [J]. ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, 2014, 9 (06) : 905 - 928
  • [44] Integrated design and optimization of reactor-distillation sequence-recycle-heat exchanger network
    Yin, Changfang
    Sun, Huifeng
    Lv, Donghui
    Liu, Guilian
    [J]. ENERGY, 2022, 238
  • [45] DISCRETE-EVENT SIMULATION OF A SEQUENCE OF MULTICOMPONENT BATCH DISTILLATION-COLUMNS
    BARNETTE, DT
    SOMMERFELD, JT
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 1987, 11 (04) : 395 - 398
  • [46] Approximate Dynamic Programming Based Optimal Control Applied to an Integrated Plant with a Reactor and a Distillation Column with Recycle
    Tosukhowong, Thidarat
    Lee, Jay H.
    [J]. AICHE JOURNAL, 2009, 55 (04) : 919 - 930
  • [47] A new efficiency relaxation model for rigorous stage number optimization of distillation columns
    Jia, Shengkun
    Qian, Xing
    Liu, Xingwei
    Luo, Yiqing
    Yuan, Xigang
    [J]. CHEMICAL ENGINEERING SCIENCE, 2022, 260
  • [48] Calculation of the Efficiency of Contact Stages of Distillation Columns with Cocurrent Swirl Contact Devices
    A. A. Shagivaleev
    A. A. Ovchinnikov
    N. A. Nikolaev
    [J]. Theoretical Foundations of Chemical Engineering, 2005, 39 : 590 - 593
  • [49] Calculation of the efficiency of contact stages of distillation columns with cocurrent swirl contact devices
    Shagivaleev, AA
    Ovchinnikov, AA
    Nikolaev, NA
    [J]. THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING, 2005, 39 (06) : 590 - 593
  • [50] Hydrodynamic and mass transfer efficiency of ceramic foam packing applied to distillation
    Leveque, Julien
    Rouzineau, David
    Prevost, Michel
    Meyer, Michel
    [J]. CHEMICAL ENGINEERING SCIENCE, 2009, 64 (11) : 2607 - 2616