Improvements in configuration of a middle vessel batch distillation by means of rigorous dynamic modelling and simulation

被引:0
|
作者
Gruetzmann, S. [1 ]
Fieg, G. [1 ]
机构
[1] Tech Univ Hamburg, Schwarzenbergstr 95C, D-21073 Hamburg, Germany
关键词
dynamic modelling; batch distillation; configuration; design; ambient conditions; startup;
D O I
暂无
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
The objective of this contribution is to compare various column configurations for the practical realisation of a middle vessel batch distillation column (MVBD). By means of extensive simulations, the entire process, beginning from a column at ambient conditions, has been analysed for the first time. Three column configurations have been investigated. Physical phenomena, such as condensation at the column wall and internals, have been considered. The results exhibit that a liquid bypass of the middle vessel during startup can decrease the process time by 20%. Industrial engineers are now capable of considering these new facts during the design and redesign phase of a new and existing columns, respectively.
引用
收藏
页码:106 / +
页数:2
相关论文
共 50 条
  • [21] DYNAMIC SIMULATION OF A BATCH EXTRACTIVE DISTILLATION PROCESS
    YATIM, H
    MOSZKOWICZ, P
    OTTERBEIN, M
    LANG, P
    COMPUTERS & CHEMICAL ENGINEERING, 1993, 17 : S57 - S62
  • [22] Neural-network approach to dynamic optimization of batch distillation - Application to a middle-vessel column
    Greaves, MA
    Mujtaba, IM
    Barolo, M
    Trotta, A
    Hussain, MA
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2003, 81 (A3): : 393 - 401
  • [23] Control and dynamic optimization of middle vessel batch distillation column for the separation of ethanol/propanol/butanol mixture
    Krishna, Pranav
    Desikan, Bharath
    Rao, Chinta Sankar
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2021, 176 : 267 - 278
  • [24] Dual composition control in a middle-vessel batch distillation column
    Monroy-Loperena, R
    Alvarez-Ramirez, J
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2001, 40 (20) : 4377 - 4390
  • [25] On the integration of reaction and separation in a batch extractive distillation column with a middle vessel
    Espinosa, J
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (15) : 3657 - 3668
  • [26] Some issues in the design and operation of a batch distillation column with a middle vessel
    Barolo, M
    Guarise, GB
    Ribon, N
    Rienzi, S
    Trotta, A
    Macchietto, S
    COMPUTERS & CHEMICAL ENGINEERING, 1996, 20 : S37 - S42
  • [27] Integration of reaction and separation in a batch extractive distillation column with a middle vessel
    Espinosa, J
    EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING - 12, 2002, 10 : 187 - 192
  • [28] An efficient algorithm for rigorous dynamic simulation of reactive distillation columns
    Rahul, Mayur
    Kumar, M. V. Pavan
    Dwivedi, Deeptanshu
    Kaistha, Nitin
    COMPUTERS & CHEMICAL ENGINEERING, 2009, 33 (08) : 1336 - 1343
  • [29] Rigorous Dynamic Modelling and Identification of Distillation Column using Aspen Plus
    Taqvi, Syed A.
    Tufa, Lemma Dendana
    Zabiri, Haslinda
    Mahadzir, Shuhaimi
    Maulud, Abdulhalim Shah
    Uddin, Fahim
    2017 IEEE 8TH CONTROL AND SYSTEM GRADUATE RESEARCH COLLOQUIUM (ICSGRC), 2017, : 262 - 267
  • [30] Rigorous modeling, simulation and optimization of a conventional and nonconventional batch reactive distillation column: A comparative study of dynamic optimization approaches
    Soraya Lopez-Saucedo, Edna
    Grossmann, Ignacio E.
    Gabriel Segovia-Hernandez, Juan
    Hernandez, Salvador
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2016, 111 : 83 - 99