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Rate acceleration of 2-methyl-1-butanol dehydration in a reactive distillation column

Research output: Contribution to journalJournal articlepeer-review

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Standard

Rate acceleration of 2-methyl-1-butanol dehydration in a reactive distillation column. / Aiouache, Farid ; Goto, Shigeo.

In: Journal of Chemical Engineering of Japan, Vol. 35, No. 5, 05.2002, p. 443-449.

Research output: Contribution to journalJournal articlepeer-review

Harvard

Aiouache, F & Goto, S 2002, 'Rate acceleration of 2-methyl-1-butanol dehydration in a reactive distillation column', Journal of Chemical Engineering of Japan, vol. 35, no. 5, pp. 443-449.

APA

Aiouache, F., & Goto, S. (2002). Rate acceleration of 2-methyl-1-butanol dehydration in a reactive distillation column. Journal of Chemical Engineering of Japan, 35(5), 443-449.

Vancouver

Aiouache F, Goto S. Rate acceleration of 2-methyl-1-butanol dehydration in a reactive distillation column. Journal of Chemical Engineering of Japan. 2002 May;35(5):443-449.

Author

Aiouache, Farid ; Goto, Shigeo. / Rate acceleration of 2-methyl-1-butanol dehydration in a reactive distillation column. In: Journal of Chemical Engineering of Japan. 2002 ; Vol. 35, No. 5. pp. 443-449.

Bibtex

@article{fe2f93bd67c742bd80718060f18c611b,
title = "Rate acceleration of 2-methyl-1-butanol dehydration in a reactive distillation column",
abstract = "Reactive distillation was used as a method to accelerate the reaction rate of 2-methyl-1-butanol (2M1BOH) dehydration. Since it is strongly inhibited by water, the trade-off between reaction rate and liquid-vapour mass transfer was investigated under experimental input variables, such as reboiler heat duty, the mass of the catalyst and reflux ratio. The reaction rate variations inside the column were simulated by using the equilibrium model of the ASPEN PLUS simulator. The effectiveness of reactive distillation was justified by the comparison of its performance with corresponding conventional reactors. A saving of 80% in reboiler heat duty was found when a decanter was added to the column. An industrial scale simulation was done to optimise the proposed process.",
author = "Farid Aiouache and Shigeo Goto",
year = "2002",
month = may,
language = "English",
volume = "35",
pages = "443--449",
journal = "Journal of Chemical Engineering of Japan",
issn = "0021-9592",
publisher = "Society of Chemical Engineers, Japan",
number = "5",

}

RIS

TY - JOUR

T1 - Rate acceleration of 2-methyl-1-butanol dehydration in a reactive distillation column

AU - Aiouache, Farid

AU - Goto, Shigeo

PY - 2002/5

Y1 - 2002/5

N2 - Reactive distillation was used as a method to accelerate the reaction rate of 2-methyl-1-butanol (2M1BOH) dehydration. Since it is strongly inhibited by water, the trade-off between reaction rate and liquid-vapour mass transfer was investigated under experimental input variables, such as reboiler heat duty, the mass of the catalyst and reflux ratio. The reaction rate variations inside the column were simulated by using the equilibrium model of the ASPEN PLUS simulator. The effectiveness of reactive distillation was justified by the comparison of its performance with corresponding conventional reactors. A saving of 80% in reboiler heat duty was found when a decanter was added to the column. An industrial scale simulation was done to optimise the proposed process.

AB - Reactive distillation was used as a method to accelerate the reaction rate of 2-methyl-1-butanol (2M1BOH) dehydration. Since it is strongly inhibited by water, the trade-off between reaction rate and liquid-vapour mass transfer was investigated under experimental input variables, such as reboiler heat duty, the mass of the catalyst and reflux ratio. The reaction rate variations inside the column were simulated by using the equilibrium model of the ASPEN PLUS simulator. The effectiveness of reactive distillation was justified by the comparison of its performance with corresponding conventional reactors. A saving of 80% in reboiler heat duty was found when a decanter was added to the column. An industrial scale simulation was done to optimise the proposed process.

M3 - Journal article

VL - 35

SP - 443

EP - 449

JO - Journal of Chemical Engineering of Japan

JF - Journal of Chemical Engineering of Japan

SN - 0021-9592

IS - 5

ER -