Modeling and process design of an internally heat-integrated distillation column

Keigo Matsuda; Koichi Iwakabe; Masaru Nakaiwa; Toshinari Nakanishi; Takao Ohmori; Akira Endo; Takuji Yamamoto; Sho Kataoka

Modeling and process design of an internally heat-integrated distillation column

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

^*この研究の対応する著者

研究成果: Conference contribution

抄録

A modeling and process design of the HIDiC was developed. The model of HIDiC with structured packing was developed by rate-based model using Maxwell-Stefan equations. The HIDiC models were developed by the process simulator "gPROMS". A benzene-toluene system was considered. Predicted simulation results showed a good agreement with observed data. The bench HIDiC showed about 40% reduction of energy consumption than the conventional distillation column. The effect of process design in the HIDiC is also presented. This is an abstract of a paper presented at the 2006 AIChE National Meeting (San Francisco, CA 11/12-17/2006).

本文言語	English
ホスト出版物のタイトル	2006 AIChE Annual Meeting
出版ステータス	Published - 2006
外部発表	はい
イベント	2006 AIChE Annual Meeting - San Francisco, CA, United States 継続期間: 2006 11月 12 → 2006 11月 17

出版物シリーズ

名前	AIChE Annual Meeting, Conference Proceedings

Conference

Conference	2006 AIChE Annual Meeting
国/地域	United States
City	San Francisco, CA
Period	06/11/12 → 06/11/17

ASJC Scopus subject areas

バイオテクノロジー
化学工学（全般）
バイオエンジニアリング
安全性、リスク、信頼性、品質管理

UN SDG

この成果は、次の持続可能な開発目標に貢献しています

他のファイルとリンク

引用スタイル

@inproceedings{57f5ea38604c429b88d710d5ec710cf4,

title = "Modeling and process design of an internally heat-integrated distillation column",

abstract = "A modeling and process design of the HIDiC was developed. The model of HIDiC with structured packing was developed by rate-based model using Maxwell-Stefan equations. The HIDiC models were developed by the process simulator {"}gPROMS{"}. A benzene-toluene system was considered. Predicted simulation results showed a good agreement with observed data. The bench HIDiC showed about 40% reduction of energy consumption than the conventional distillation column. The effect of process design in the HIDiC is also presented. This is an abstract of a paper presented at the 2006 AIChE National Meeting (San Francisco, CA 11/12-17/2006).",

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

year = "2006",

language = "English",

isbn = "081691012X",

series = "AIChE Annual Meeting, Conference Proceedings",

booktitle = "2006 AIChE Annual Meeting",

note = "2006 AIChE Annual Meeting ; Conference date: 12-11-2006 Through 17-11-2006",

}

TY - GEN

T1 - Modeling and process design of an internally heat-integrated distillation column

AU - Matsuda, Keigo

AU - Iwakabe, Koichi

AU - Nakaiwa, Masaru

AU - Nakanishi, Toshinari

AU - Ohmori, Takao

AU - Endo, Akira

AU - Yamamoto, Takuji

AU - Kataoka, Sho

PY - 2006

Y1 - 2006

N2 - A modeling and process design of the HIDiC was developed. The model of HIDiC with structured packing was developed by rate-based model using Maxwell-Stefan equations. The HIDiC models were developed by the process simulator "gPROMS". A benzene-toluene system was considered. Predicted simulation results showed a good agreement with observed data. The bench HIDiC showed about 40% reduction of energy consumption than the conventional distillation column. The effect of process design in the HIDiC is also presented. This is an abstract of a paper presented at the 2006 AIChE National Meeting (San Francisco, CA 11/12-17/2006).

AB - A modeling and process design of the HIDiC was developed. The model of HIDiC with structured packing was developed by rate-based model using Maxwell-Stefan equations. The HIDiC models were developed by the process simulator "gPROMS". A benzene-toluene system was considered. Predicted simulation results showed a good agreement with observed data. The bench HIDiC showed about 40% reduction of energy consumption than the conventional distillation column. The effect of process design in the HIDiC is also presented. This is an abstract of a paper presented at the 2006 AIChE National Meeting (San Francisco, CA 11/12-17/2006).

UR - http://www.scopus.com/inward/record.url?scp=58049115649&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=58049115649&partnerID=8YFLogxK

M3 - Conference contribution

AN - SCOPUS:58049115649

SN - 081691012X

SN - 9780816910120

T3 - AIChE Annual Meeting, Conference Proceedings

BT - 2006 AIChE Annual Meeting

T2 - 2006 AIChE Annual Meeting

Y2 - 12 November 2006 through 17 November 2006

ER -

Modeling and process design of an internally heat-integrated distillation column

抄録

出版物シリーズ

Conference

ASJC Scopus subject areas

UN SDG

他のファイルとリンク

フィンガープリント

引用スタイル