Dynamic behavior of the intensified alternative configurations for quaternary distillation

被引:6
作者
Ramirez-Marquez, Cesar [1 ]
Cabrera-Ruiz, Julian [1 ]
Segovia-Hernandez, Juan Gabriel [1 ]
Hernandez, Salvador [1 ]
Errico, Massimiliano [2 ]
Rong, Ben-Guang [2 ]
机构
[1] Univ Guanajuato, Dept Ingn Quim, Div Ciencias Nat & Exactas, Campus Guanajuato,Noria Alta S-N, Guanajuato 20256, Mexico
[2] Univ Southern Denmark, Dept Chem Engn Biotechnol & Environm Technol, Campusvej 55, DK-5230 Odense M, Denmark
关键词
Quaternary distillation; Process intensification; Dynamic behavior; Closed-loop operation; EXTRACTIVE DISTILLATION; OPTIMAL-DESIGN; COLUMNS; OPTIMIZATION; SEPARATION; SYSTEMS; SEQUENCES; ENERGY;
D O I
10.1016/j.cep.2016.07.016
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Process intensification emerges as an important tool in the synthesis of multicomponent distillation configurations aimed at the reduction of the energy use and capital costs. Operational and fixed costs savings coupled with simplicity and controllability design configurations appear as an essential characteristic for industrial acceptance of intensified configurations. Following the aforementioned principles, two intensified configurations for the separation of quaternary mixture, were considered. These configurations were recognized as a valid alternative to overcome the complexity of the quaternary Petlyuk scheme. The study of the dynamics and control properties represent an important research issue in the analysis of new configurations to prove their effective applicability. The theoretical control properties of the alternative intensified configurations were obtained using the singular value decomposition technique in all frequency domain. In order to complete the control study, the distillation schemes were subjected to closed-loop dynamic simulations. The results show that there are cases in which the intensified sequences do not only provide energy savings, but also may offer dynamic advantages in comparison to the conventional four-component scheme. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:151 / 163
页数:13
相关论文
共 35 条
  • [1] Synthesis of multicomponent distillation column configurations
    Agrawal, R
    [J]. AICHE JOURNAL, 2003, 49 (02) : 379 - 401
  • [2] Design and optimization of fully thermally coupled distillation columns part 1: Preliminary design and optimization methodology
    Amminudin, KA
    Smith, R
    Thong, DYC
    Towler, GP
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2001, 79 (A7) : 701 - 715
  • [3] [Anonymous], 2001, AICHE ANN M
  • [4] Reducing energy consumption and CO2 emissions in extractive distillation: Part II. Dynamic behavior
    de Jesus Ibarra-Sanchez, Jose
    Gabriel Segovia-Hernandez, Juan
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2010, 88 (2A) : 135 - 145
  • [5] Designing four-product dividing wall columns for separation of a multicomponent aromatics mixture
    Dejanovic, I.
    Matijasevic, Lj.
    Halvorsen, I. J.
    Skogestad, S.
    Jansen, H.
    Kaibel, B.
    Olujic, Z.
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2011, 89 (8A) : 1155 - 1167
  • [6] Hydraulic design, technical challenges and comparison of alternative configurations of a four-product dividing wall column
    Dejanovic, Igor
    Halvorsen, Ivar J.
    Skogestad, Sigurd
    Jansen, Helmut
    Olujic, Zarko
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2014, 84 : 71 - 81
  • [7] Optimal design of thermally coupled distillation columns
    Dünnebier, G
    Pantelides, CC
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (01) : 162 - 176
  • [8] Alternative Petlyuk Distillation Configurations for the Separation of Four-Component Mixtures
    Errico, Massimiliano
    Pirellas, Pietro
    Rong, Ben-Guang
    Gabriel Segovia-Hernandez, Juan
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2015, 54 (17) : 4788 - 4794
  • [9] A combined method for the design and optimization of intensified distillation systems
    Errico, Massimiliano
    Pirellas, Pietro
    Torres-Ortega, Carlo Edgar
    Rong, Ben-Guang
    Gabriel Segovia-Hernandez, Juan
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2014, 85 : 69 - 76
  • [10] The importance of the sequential synthesis methodology in the optimal distillation sequences design
    Errico, Massimiliano
    Rong, Ben-Guang
    Edgar Torres-Ortega, Carlo
    Gabriel Segovia-Hernandez, Juan
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2014, 62 : 1 - 9