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Kinetics of Aqueous Phase Dehydration of Xylose into Furfural Catalyzed by ZSM-5 Zeolite

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Kinetics of Aqueous Phase Dehydration of Xylose into Furfural Catalyzed by ZSM-5 Zeolite. / O'Neill, Rebecca; Ahmad, Mohammad Najeeb; Vanoye, Laurent et al.
In: Industrial and Engineering Chemistry Research, Vol. 48, No. 9, 06.05.2009, p. 4300-4306.

Research output: Contribution to Journal/MagazineJournal articlepeer-review

Harvard

O'Neill, R, Ahmad, MN, Vanoye, L & Aiouache, F 2009, 'Kinetics of Aqueous Phase Dehydration of Xylose into Furfural Catalyzed by ZSM-5 Zeolite', Industrial and Engineering Chemistry Research, vol. 48, no. 9, pp. 4300-4306. https://doi.org/10.1021/ie801599k

APA

O'Neill, R., Ahmad, M. N., Vanoye, L., & Aiouache, F. (2009). Kinetics of Aqueous Phase Dehydration of Xylose into Furfural Catalyzed by ZSM-5 Zeolite. Industrial and Engineering Chemistry Research, 48(9), 4300-4306. https://doi.org/10.1021/ie801599k

Vancouver

O'Neill R, Ahmad MN, Vanoye L, Aiouache F. Kinetics of Aqueous Phase Dehydration of Xylose into Furfural Catalyzed by ZSM-5 Zeolite. Industrial and Engineering Chemistry Research. 2009 May 6;48(9):4300-4306. doi: 10.1021/ie801599k

Author

O'Neill, Rebecca ; Ahmad, Mohammad Najeeb ; Vanoye, Laurent et al. / Kinetics of Aqueous Phase Dehydration of Xylose into Furfural Catalyzed by ZSM-5 Zeolite. In: Industrial and Engineering Chemistry Research. 2009 ; Vol. 48, No. 9. pp. 4300-4306.

Bibtex

@article{975f3309c88849478c52d45bdc0b79dd,
title = "Kinetics of Aqueous Phase Dehydration of Xylose into Furfural Catalyzed by ZSM-5 Zeolite",
abstract = "ZSM-5 zeolite in H+ form with an average pore size of 1.2 nm was used for aqueous phase dehydration of xylose to furfural at low temperatures;, that is, from 413 to 493 K. The selectivity in furfural increased with the temperature to a value of 473 K. Beyond this temperature, condensation reactions were significant and facilitated by the intrinsic structure of ZSM-5. A reaction mechanism that included isomerization of xylose to lyxose, dehydration of lyxose and xylose to furfural, fragmentation of furfural to organic acids, oligomerization of furfural to bi- and tridimensional furilic species, and complete dehydration of organic acids to carbonaceous deposits was developed, and the associated kinetic parameters were estimated. The rate of furfural production was found to be more sensitive to temperature than the rates of side reactions, with an estimated activation energy of 32.1 kcal/mol. This value correlated well with data in the literature obtained by homogeneous catalytic dehydration.",
author = "Rebecca O'Neill and Ahmad, {Mohammad Najeeb} and Laurent Vanoye and Farid Aiouache",
year = "2009",
month = may,
day = "6",
doi = "10.1021/ie801599k",
language = "English",
volume = "48",
pages = "4300--4306",
journal = "Industrial and Engineering Chemistry Research",
issn = "0888-5885",
publisher = "American Chemical Society",
number = "9",

}

RIS

TY - JOUR

T1 - Kinetics of Aqueous Phase Dehydration of Xylose into Furfural Catalyzed by ZSM-5 Zeolite

AU - O'Neill, Rebecca

AU - Ahmad, Mohammad Najeeb

AU - Vanoye, Laurent

AU - Aiouache, Farid

PY - 2009/5/6

Y1 - 2009/5/6

N2 - ZSM-5 zeolite in H+ form with an average pore size of 1.2 nm was used for aqueous phase dehydration of xylose to furfural at low temperatures;, that is, from 413 to 493 K. The selectivity in furfural increased with the temperature to a value of 473 K. Beyond this temperature, condensation reactions were significant and facilitated by the intrinsic structure of ZSM-5. A reaction mechanism that included isomerization of xylose to lyxose, dehydration of lyxose and xylose to furfural, fragmentation of furfural to organic acids, oligomerization of furfural to bi- and tridimensional furilic species, and complete dehydration of organic acids to carbonaceous deposits was developed, and the associated kinetic parameters were estimated. The rate of furfural production was found to be more sensitive to temperature than the rates of side reactions, with an estimated activation energy of 32.1 kcal/mol. This value correlated well with data in the literature obtained by homogeneous catalytic dehydration.

AB - ZSM-5 zeolite in H+ form with an average pore size of 1.2 nm was used for aqueous phase dehydration of xylose to furfural at low temperatures;, that is, from 413 to 493 K. The selectivity in furfural increased with the temperature to a value of 473 K. Beyond this temperature, condensation reactions were significant and facilitated by the intrinsic structure of ZSM-5. A reaction mechanism that included isomerization of xylose to lyxose, dehydration of lyxose and xylose to furfural, fragmentation of furfural to organic acids, oligomerization of furfural to bi- and tridimensional furilic species, and complete dehydration of organic acids to carbonaceous deposits was developed, and the associated kinetic parameters were estimated. The rate of furfural production was found to be more sensitive to temperature than the rates of side reactions, with an estimated activation energy of 32.1 kcal/mol. This value correlated well with data in the literature obtained by homogeneous catalytic dehydration.

U2 - 10.1021/ie801599k

DO - 10.1021/ie801599k

M3 - Journal article

VL - 48

SP - 4300

EP - 4306

JO - Industrial and Engineering Chemistry Research

JF - Industrial and Engineering Chemistry Research

SN - 0888-5885

IS - 9

ER -