Integrated Operation and Design of a Simulated Moving Bed Reactor

Edwin Zondervan; Nikola Nikacevic; Harish Khajuria; Efstratios N. Pistikopoulos; André B. de Haan

doi:10.1016/B978-0-444-59519-5.50129-5

Integrated Operation and Design of a Simulated Moving Bed Reactor

Edwin Zondervan^*, Nikola Nikacevic, Harish Khajuria, Efstratios N. Pistikopoulos, André B. de Haan

^*Corresponding author for this work

Research output: Contribution to journal › Conference article › Academic › peer-review

2 Citations (Scopus)

Abstract

In this work we use a simulated moving bed reactor (SMBR) model that can be used to optimize operational and design parameters of the process. An SMB unit contains several columns with specific lengths that are connected sequentially. Feed and desorbent are supplied and extract and raffinate can be withdrawn from the system. The process of supply/withdrawal is cyclic, which makes optimization of operation and design a challenging task. We will discuss our model in this contribution and show the preliminary results that we obtain for an isomerization process of glucose into fructose. In addition we discuss how the model can be incorporated in a conceptual framework that can be used to integrate the operation and design of the SMBR.

Original language	English
Pages (from-to)	642-646
Number of pages	5
Journal	Computer Aided Chemical Engineering
Volume	30
DOIs	https://doi.org/10.1016/B978-0-444-59519-5.50129-5
Publication status	Published - 2012
Externally published	Yes
Event	22nd European Symposium on Computer Aided Process Engineering, ESCAPE 2012 - University College London, London, United Kingdom Duration: 17 Jun 2012 → 20 Jun 2012 Conference number: 22

Keywords

Dynamic optimization
Modeling
Process intensification
Simulated moving bed reactor

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10.1016/B978-0-444-59519-5.50129-5

Cite this

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title = "Integrated Operation and Design of a Simulated Moving Bed Reactor",

abstract = "In this work we use a simulated moving bed reactor (SMBR) model that can be used to optimize operational and design parameters of the process. An SMB unit contains several columns with specific lengths that are connected sequentially. Feed and desorbent are supplied and extract and raffinate can be withdrawn from the system. The process of supply/withdrawal is cyclic, which makes optimization of operation and design a challenging task. We will discuss our model in this contribution and show the preliminary results that we obtain for an isomerization process of glucose into fructose. In addition we discuss how the model can be incorporated in a conceptual framework that can be used to integrate the operation and design of the SMBR.",

keywords = "Dynamic optimization, Modeling, Process intensification, Simulated moving bed reactor",

author = "Edwin Zondervan and Nikola Nikacevic and Harish Khajuria and Pistikopoulos, {Efstratios N.} and {de Haan}, {Andr{\'e} B.}",

year = "2012",

doi = "10.1016/B978-0-444-59519-5.50129-5",

language = "English",

volume = "30",

pages = "642--646",

journal = "Computer Aided Chemical Engineering",

issn = "1570-7946",

publisher = "Elsevier B.V.",

note = "22nd European Symposium on Computer Aided Process Engineering, ESCAPE 2012, ESCAPE 2012 ; Conference date: 17-06-2012 Through 20-06-2012",

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TY - JOUR

T1 - Integrated Operation and Design of a Simulated Moving Bed Reactor

AU - Zondervan, Edwin

AU - Nikacevic, Nikola

AU - Khajuria, Harish

AU - Pistikopoulos, Efstratios N.

AU - de Haan, André B.

N1 - Conference code: 22

PY - 2012

Y1 - 2012

N2 - In this work we use a simulated moving bed reactor (SMBR) model that can be used to optimize operational and design parameters of the process. An SMB unit contains several columns with specific lengths that are connected sequentially. Feed and desorbent are supplied and extract and raffinate can be withdrawn from the system. The process of supply/withdrawal is cyclic, which makes optimization of operation and design a challenging task. We will discuss our model in this contribution and show the preliminary results that we obtain for an isomerization process of glucose into fructose. In addition we discuss how the model can be incorporated in a conceptual framework that can be used to integrate the operation and design of the SMBR.

AB - In this work we use a simulated moving bed reactor (SMBR) model that can be used to optimize operational and design parameters of the process. An SMB unit contains several columns with specific lengths that are connected sequentially. Feed and desorbent are supplied and extract and raffinate can be withdrawn from the system. The process of supply/withdrawal is cyclic, which makes optimization of operation and design a challenging task. We will discuss our model in this contribution and show the preliminary results that we obtain for an isomerization process of glucose into fructose. In addition we discuss how the model can be incorporated in a conceptual framework that can be used to integrate the operation and design of the SMBR.

KW - Dynamic optimization

KW - Modeling

KW - Process intensification

KW - Simulated moving bed reactor

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U2 - 10.1016/B978-0-444-59519-5.50129-5

DO - 10.1016/B978-0-444-59519-5.50129-5

M3 - Conference article

AN - SCOPUS:84862838623

SN - 1570-7946

VL - 30

SP - 642

EP - 646

JO - Computer Aided Chemical Engineering

JF - Computer Aided Chemical Engineering

T2 - 22nd European Symposium on Computer Aided Process Engineering, ESCAPE 2012

Y2 - 17 June 2012 through 20 June 2012

ER -

Integrated Operation and Design of a Simulated Moving Bed Reactor

Abstract

Keywords

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