Design and control of cyclohexanol reactive-distillation process with alternative decanter configurations

Hao Yeh Lee; Yuan Lin Lin; Hsiao Ping Huang; Cheng Liang Chen; I. Lung Chien

Design and control of cyclohexanol reactive-distillation process with alternative decanter configurations

Hao Yeh Lee
, Yuan Lin Lin
, Hsiao Ping Huang
, Cheng Liang Chen
, I. Lung Chien^*

^*Corresponding author for this work

National Taiwan University

Research output: Contribution to conference › Conference Paper › peer-review

Abstract

Cyclohexanol is widely used in industry as a precursor for the synthesis of intermediates of Nylon. In this paper, design and control of reactive-distillation process for the production of cyclohexanol have been studied. The total annual costs of two alternative decanter configurations are comparable. However, one configuration gives much better operability than the others in the face of feed disturbances. To achieve wider operability, proper selection of the overall control strategy is critically important. Rigorous dynamic simulations will be used to illustrate the findings.

Original language	English
Pages	78-83
Number of pages	6
State	Published - 2011
Externally published	Yes
Event	2011 International Symposium on Advanced Control of Industrial Processes, ADCONIP 2011 - Hangzhou, Zhejiang, China Duration: 23 05 2011 → 26 05 2011

Conference

Conference	2011 International Symposium on Advanced Control of Industrial Processes, ADCONIP 2011
Country/Territory	China
City	Hangzhou, Zhejiang
Period	23/05/11 → 26/05/11

Cite this

@conference{ccd68f7fcc9341f49567a8a6c345d122,

title = "Design and control of cyclohexanol reactive-distillation process with alternative decanter configurations",

abstract = "Cyclohexanol is widely used in industry as a precursor for the synthesis of intermediates of Nylon. In this paper, design and control of reactive-distillation process for the production of cyclohexanol have been studied. The total annual costs of two alternative decanter configurations are comparable. However, one configuration gives much better operability than the others in the face of feed disturbances. To achieve wider operability, proper selection of the overall control strategy is critically important. Rigorous dynamic simulations will be used to illustrate the findings.",

author = "Lee, \{Hao Yeh\} and Lin, \{Yuan Lin\} and Huang, \{Hsiao Ping\} and Chen, \{Cheng Liang\} and Chien, \{I. Lung\}",

year = "2011",

language = "英语",

pages = "78--83",

note = "2011 International Symposium on Advanced Control of Industrial Processes, ADCONIP 2011 ; Conference date: 23-05-2011 Through 26-05-2011",

}

Design and control of cyclohexanol reactive-distillation process with alternative decanter configurations. / Lee, Hao Yeh; Lin, Yuan Lin; Huang, Hsiao Ping et al.
2011. 78-83 Paper presented at 2011 International Symposium on Advanced Control of Industrial Processes, ADCONIP 2011, Hangzhou, Zhejiang, China.

Research output: Contribution to conference › Conference Paper › peer-review

TY - CONF

T1 - Design and control of cyclohexanol reactive-distillation process with alternative decanter configurations

AU - Lee, Hao Yeh

AU - Lin, Yuan Lin

AU - Huang, Hsiao Ping

AU - Chen, Cheng Liang

AU - Chien, I. Lung

PY - 2011

Y1 - 2011

N2 - Cyclohexanol is widely used in industry as a precursor for the synthesis of intermediates of Nylon. In this paper, design and control of reactive-distillation process for the production of cyclohexanol have been studied. The total annual costs of two alternative decanter configurations are comparable. However, one configuration gives much better operability than the others in the face of feed disturbances. To achieve wider operability, proper selection of the overall control strategy is critically important. Rigorous dynamic simulations will be used to illustrate the findings.

AB - Cyclohexanol is widely used in industry as a precursor for the synthesis of intermediates of Nylon. In this paper, design and control of reactive-distillation process for the production of cyclohexanol have been studied. The total annual costs of two alternative decanter configurations are comparable. However, one configuration gives much better operability than the others in the face of feed disturbances. To achieve wider operability, proper selection of the overall control strategy is critically important. Rigorous dynamic simulations will be used to illustrate the findings.

UR - https://www.scopus.com/pages/publications/79960661762

M3 - 论文

AN - SCOPUS:79960661762

SP - 78

EP - 83

T2 - 2011 International Symposium on Advanced Control of Industrial Processes, ADCONIP 2011

Y2 - 23 May 2011 through 26 May 2011

ER -

Design and control of cyclohexanol reactive-distillation process with alternative decanter configurations

Abstract

Conference

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