Simulation of ternary distillation in a heat integrated distillation column (HIDiC) with a rate-based model

Keigo Matsuda; Toshinari Nakanishi; Koichi Iwakabe; Kejin Huang; Takuji Yamamoto; Akira Endo; Takao Ohmori; Masaru Nakaiwa

Simulation of ternary distillation in a heat integrated distillation column (HIDiC) with a rate-based model

Keigo Matsuda^*, Toshinari Nakanishi, Koichi Iwakabe, Kejin Huang, Takuji Yamamoto, Akira Endo, Takao Ohmori, Masaru Nakaiwa

^*Corresponding author for this work

Research output: Chapter in Book/Report/Conference proceeding › Conference contribution

1 Citation (Scopus)

Abstract

A simulation technique has been developed to calculate HIDiC models. A process simulator "gPROMS" for prediction of separation performance of the HIDiC with structured packing is developed by rate-based model using Maxwell-Stefan equations. Comparison of observed data from bench-scale (benzene-toluene system) separation concentric HIDiC plant, in which consisted of about 29 m in height and 254 mm in diameter. Predicted simulation results such as concentration, temperature and flow rate of top and bottom in the rectifying section and stripping section show good agreement with observed data. The effect of mass transfer and heat transfer in the HIDiC is also discussed. Moreover, a simulator using this model is developed to multicomponent HIDiC with concentric and compact heat exchanger systems.

Original language	English
Title of host publication	2006 AIChE Spring National Meeting
Publication status	Published - 2006
Externally published	Yes
Event	2006 AIChE Spring National Meeting - Orlando, FL, United States Duration: 2006 Apr 23 → 2006 Apr 27

Publication series

Name	AIChE Annual Meeting, Conference Proceedings

Conference

Conference	2006 AIChE Spring National Meeting
Country/Territory	United States
City	Orlando, FL
Period	06/4/23 → 06/4/27

ASJC Scopus subject areas

Chemical Engineering(all)
Chemistry(all)

Cite this

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title = "Simulation of ternary distillation in a heat integrated distillation column (HIDiC) with a rate-based model",

abstract = "A simulation technique has been developed to calculate HIDiC models. A process simulator {"}gPROMS{"} for prediction of separation performance of the HIDiC with structured packing is developed by rate-based model using Maxwell-Stefan equations. Comparison of observed data from bench-scale (benzene-toluene system) separation concentric HIDiC plant, in which consisted of about 29 m in height and 254 mm in diameter. Predicted simulation results such as concentration, temperature and flow rate of top and bottom in the rectifying section and stripping section show good agreement with observed data. The effect of mass transfer and heat transfer in the HIDiC is also discussed. Moreover, a simulator using this model is developed to multicomponent HIDiC with concentric and compact heat exchanger systems.",

author = "Keigo Matsuda and Toshinari Nakanishi and Koichi Iwakabe and Kejin Huang and Takuji Yamamoto and Akira Endo and Takao Ohmori and Masaru Nakaiwa",

year = "2006",

language = "English",

isbn = "0816910057",

series = "AIChE Annual Meeting, Conference Proceedings",

booktitle = "2006 AIChE Spring National Meeting",

note = "2006 AIChE Spring National Meeting ; Conference date: 23-04-2006 Through 27-04-2006",

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TY - GEN

T1 - Simulation of ternary distillation in a heat integrated distillation column (HIDiC) with a rate-based model

AU - Matsuda, Keigo

AU - Nakanishi, Toshinari

AU - Iwakabe, Koichi

AU - Huang, Kejin

AU - Yamamoto, Takuji

AU - Endo, Akira

AU - Ohmori, Takao

AU - Nakaiwa, Masaru

PY - 2006

Y1 - 2006

N2 - A simulation technique has been developed to calculate HIDiC models. A process simulator "gPROMS" for prediction of separation performance of the HIDiC with structured packing is developed by rate-based model using Maxwell-Stefan equations. Comparison of observed data from bench-scale (benzene-toluene system) separation concentric HIDiC plant, in which consisted of about 29 m in height and 254 mm in diameter. Predicted simulation results such as concentration, temperature and flow rate of top and bottom in the rectifying section and stripping section show good agreement with observed data. The effect of mass transfer and heat transfer in the HIDiC is also discussed. Moreover, a simulator using this model is developed to multicomponent HIDiC with concentric and compact heat exchanger systems.

AB - A simulation technique has been developed to calculate HIDiC models. A process simulator "gPROMS" for prediction of separation performance of the HIDiC with structured packing is developed by rate-based model using Maxwell-Stefan equations. Comparison of observed data from bench-scale (benzene-toluene system) separation concentric HIDiC plant, in which consisted of about 29 m in height and 254 mm in diameter. Predicted simulation results such as concentration, temperature and flow rate of top and bottom in the rectifying section and stripping section show good agreement with observed data. The effect of mass transfer and heat transfer in the HIDiC is also discussed. Moreover, a simulator using this model is developed to multicomponent HIDiC with concentric and compact heat exchanger systems.

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M3 - Conference contribution

AN - SCOPUS:77953026951

SN - 0816910057

SN - 9780816910052

T3 - AIChE Annual Meeting, Conference Proceedings

BT - 2006 AIChE Spring National Meeting

T2 - 2006 AIChE Spring National Meeting

Y2 - 23 April 2006 through 27 April 2006

ER -

Simulation of ternary distillation in a heat integrated distillation column (HIDiC) with a rate-based model

Abstract

Publication series

Conference

ASJC Scopus subject areas

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