Techno-Economic Analysis for Production of L-Arabitol from L-Arabinose

Dmitry Yu Murzin; Emilien Daigue; Robert Slotte; Dmitry A. Sladkovskiy; Tapio Salmi

doi:10.1002/ceat.202000125

Techno-Economic Analysis for Production of L-Arabitol from L-Arabinose

Dmitry Yu Murzin^*
, Emilien Daigue
, Robert Slotte
, Dmitry A. Sladkovskiy
, Tapio Salmi

^*Tämän työn vastaava kirjoittaja

Tutkimustuotos: Lehtiartikkeli › Artikkeli › Tieteellinen › vertaisarvioitu

6 Sitaatiot (Scopus)

Abstrakti

The process design for synthesis of arabitol by hydrogenation of arabinose on a supported ruthenium catalyst is described. Aspen HYSYS software was used to design an arabitol production plant for subsequent generation of hydrogen through aqueous phase reforming (APR). The process design included hydrogen recycling requiring a flash drum and recompression. The total costs of arabitol were estimated to be substantially dependent on the feedstock costs and are closely related to arabinose feed cost. Feasible production of hydrogen using APR requires efficient extraction of hemicellulose from lignocellulosic biomass and subsequent hydrolysis.

Alkuperäiskieli	Englanti
Sivut	1260-1267
Sivumäärä	8
Julkaisu	Chemical Engineering and Technology
Vuosikerta	43
Numero	7
DOI - pysyväislinkit	https://doi.org/10.1002/ceat.202000125
Tila	Julkaistu - 1 heinäk. 2020
OKM-julkaisutyyppi	A1 Julkaistu artikkeli, soviteltu

Rahoitus

DAS acknowledges funding through the grant of the Government of the Russian Federation for support of scientific research conducted under the supervision of leading scientists at Russian institutions of higher education, research institutions of State Academies of Sciences, and State Research Center of the Russian Federation on March 19, 2014, No. 14.Z50.31.0013.

Pääsy asiakirjaan

10.1002/ceat.202000125Lisenssi: CC BY

Muut tiedostot ja linkit

Linkki julkaisuun Scopuksessa

Viittausmuodot

@article{5769fa711cf14e1f96abbaf95d28d11d,

title = "Techno-Economic Analysis for Production of L-Arabitol from L-Arabinose",

abstract = "The process design for synthesis of arabitol by hydrogenation of arabinose on a supported ruthenium catalyst is described. Aspen HYSYS software was used to design an arabitol production plant for subsequent generation of hydrogen through aqueous phase reforming (APR). The process design included hydrogen recycling requiring a flash drum and recompression. The total costs of arabitol were estimated to be substantially dependent on the feedstock costs and are closely related to arabinose feed cost. Feasible production of hydrogen using APR requires efficient extraction of hemicellulose from lignocellulosic biomass and subsequent hydrolysis.",

keywords = "Arabinose, Arabitol, Hydrogen production, Hydrogenation, Techno-economics",

author = "Murzin, \{Dmitry Yu\} and Emilien Daigue and Robert Slotte and Sladkovskiy, \{Dmitry A.\} and Tapio Salmi",

note = "Funding Information: DAS acknowledges funding through the grant of the Government of the Russian Federation for support of scientific research conducted under the supervision of leading scientists at Russian institutions of higher education, research institutions of State Academies of Sciences, and State Research Center of the Russian Federation on March 19, 2014, No. 14.Z50.31.0013. Publisher Copyright: {\textcopyright} 2020 The Authors. Published by WILEY-VCH Verlag GmbH \& Co. KGaA, Weinheim Copyright: Copyright 2020 Elsevier B.V., All rights reserved.",

year = "2020",

month = jul,

day = "1",

doi = "10.1002/ceat.202000125",

language = "English",

volume = "43",

pages = "1260--1267",

journal = "Chemical Engineering and Technology",

issn = "0930-7516",

publisher = "Wiley",

number = "7",

}

TY - JOUR

T1 - Techno-Economic Analysis for Production of L-Arabitol from L-Arabinose

AU - Murzin, Dmitry Yu

AU - Daigue, Emilien

AU - Slotte, Robert

AU - Sladkovskiy, Dmitry A.

AU - Salmi, Tapio

N1 - Funding Information: DAS acknowledges funding through the grant of the Government of the Russian Federation for support of scientific research conducted under the supervision of leading scientists at Russian institutions of higher education, research institutions of State Academies of Sciences, and State Research Center of the Russian Federation on March 19, 2014, No. 14.Z50.31.0013. Publisher Copyright: © 2020 The Authors. Published by WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim Copyright: Copyright 2020 Elsevier B.V., All rights reserved.

PY - 2020/7/1

Y1 - 2020/7/1

N2 - The process design for synthesis of arabitol by hydrogenation of arabinose on a supported ruthenium catalyst is described. Aspen HYSYS software was used to design an arabitol production plant for subsequent generation of hydrogen through aqueous phase reforming (APR). The process design included hydrogen recycling requiring a flash drum and recompression. The total costs of arabitol were estimated to be substantially dependent on the feedstock costs and are closely related to arabinose feed cost. Feasible production of hydrogen using APR requires efficient extraction of hemicellulose from lignocellulosic biomass and subsequent hydrolysis.

AB - The process design for synthesis of arabitol by hydrogenation of arabinose on a supported ruthenium catalyst is described. Aspen HYSYS software was used to design an arabitol production plant for subsequent generation of hydrogen through aqueous phase reforming (APR). The process design included hydrogen recycling requiring a flash drum and recompression. The total costs of arabitol were estimated to be substantially dependent on the feedstock costs and are closely related to arabinose feed cost. Feasible production of hydrogen using APR requires efficient extraction of hemicellulose from lignocellulosic biomass and subsequent hydrolysis.

KW - Arabinose

KW - Arabitol

KW - Hydrogen production

KW - Hydrogenation

KW - Techno-economics

UR - https://www.scopus.com/pages/publications/85084468842

U2 - 10.1002/ceat.202000125

DO - 10.1002/ceat.202000125

M3 - Article

AN - SCOPUS:85084468842

SN - 0930-7516

VL - 43

SP - 1260

EP - 1267

JO - Chemical Engineering and Technology

JF - Chemical Engineering and Technology

IS - 7

ER -