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

Abstract

A simulation technique was developed to calculate HIDiC models. A process simulator "gPROMS" for prediction of separation performance of the HIDiC with structured packing was developed by rate-based model using Maxwell-Stefan equations. Predicted simulation results such as concentration, temperature, and flow rate of top and bottom in the rectifying section and stripping section showed good agreement with observed data. The effect of mass transfer and heat transfer in the HIDiC is also discussed. A simulator using this model was developed to multicomponent HIDiC with concentric and compact heat exchanger systems. This is an abstract of paper presented at the AIChE Spring National Meeting (Orlando, FL 4/24-26/2006).

Original language	English
Title of host publication	2006 AIChE Spring Annual 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	2006 AIChE Spring Annual Meeting

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

Biotechnology
Chemical Engineering(all)
Bioengineering
Safety, Risk, Reliability and Quality

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 was developed to calculate HIDiC models. A process simulator {"}gPROMS{"} for prediction of separation performance of the HIDiC with structured packing was developed by rate-based model using Maxwell-Stefan equations. Predicted simulation results such as concentration, temperature, and flow rate of top and bottom in the rectifying section and stripping section showed good agreement with observed data. The effect of mass transfer and heat transfer in the HIDiC is also discussed. A simulator using this model was developed to multicomponent HIDiC with concentric and compact heat exchanger systems. This is an abstract of paper presented at the AIChE Spring National Meeting (Orlando, FL 4/24-26/2006).",

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 = "2006 AIChE Spring Annual Meeting",

booktitle = "2006 AIChE Spring Annual Meeting",

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

}

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 was developed to calculate HIDiC models. A process simulator "gPROMS" for prediction of separation performance of the HIDiC with structured packing was developed by rate-based model using Maxwell-Stefan equations. Predicted simulation results such as concentration, temperature, and flow rate of top and bottom in the rectifying section and stripping section showed good agreement with observed data. The effect of mass transfer and heat transfer in the HIDiC is also discussed. A simulator using this model was developed to multicomponent HIDiC with concentric and compact heat exchanger systems. This is an abstract of paper presented at the AIChE Spring National Meeting (Orlando, FL 4/24-26/2006).

AB - A simulation technique was developed to calculate HIDiC models. A process simulator "gPROMS" for prediction of separation performance of the HIDiC with structured packing was developed by rate-based model using Maxwell-Stefan equations. Predicted simulation results such as concentration, temperature, and flow rate of top and bottom in the rectifying section and stripping section showed good agreement with observed data. The effect of mass transfer and heat transfer in the HIDiC is also discussed. A simulator using this model was developed to multicomponent HIDiC with concentric and compact heat exchanger systems. This is an abstract of paper presented at the AIChE Spring National Meeting (Orlando, FL 4/24-26/2006).

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M3 - Conference contribution

AN - SCOPUS:56549084599

SN - 0816910057

SN - 9780816910052

T3 - 2006 AIChE Spring Annual Meeting

BT - 2006 AIChE Spring Annual 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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