Exergy and energy analysis of a polygeneration scheme for hydrogen production using steam gasification of biomass; International Journal of Hydrogen Energy; Vol. 218

Λεπτομέρειες βιβλιογραφικής εγγραφής
Parent link:International Journal of Hydrogen Energy.— .— Amsterdam: Elsevier Science Publishing Company Inc.
Vol. 218.— 2026.— Article number 154035, 12 p.
Κύριος συγγραφέας: Shevyrev S. A. Sergey Aleksandrovich
Άλλοι συγγραφείς: Strizhak P. A. Pavel Alexandrovich
Περίληψη:Title screen
The principles of polygeneration for hydrogen production during steam gasification of biomass have been studied. A distinctive feature of the proposed scheme is its unconventional method for producing superheated steam, which is subsequently used in the gasification of plant-based materials. This method involves generating superheated steam of high temperature (up to 1000 °C) and low pressure (up to 30 bar) in a boiler and a turbine unit during biomass combustion. The polygeneration scheme was modeled using the Aspen Plus software package. The calculation results were validated against the authors experimental data on oxygen-free steam gasification of biomass, as well as against published data from other researchers. The calculation errors for the volume concentrations of CO and H2 in the producer gas do not exceed 20 %. For the studied temperature range of 700–960 °C and pressure range of 2–30 bar, the exergy and energy efficiencies of the polygeneration scheme were determined to be 34.9–38.8 % and 40.1–45.6 %, respectively. The energy and exergy efficiencies of biomass conversion to H2 for the studied modes are 15.9–24.4 % and 13.85–21.31 %, respectively. The study demonstrated that the best conditions for hydrogen production in the proposed scheme are achieved using superheated steam of 960 °C and 2 bar
Текстовый файл
AM_Agreement
Γλώσσα:Αγγλικά
Έκδοση: 2026
Θέματα:
Διαθέσιμο Online:https://doi.org/10.1016/j.ijhydene.2026.154035
Μορφή: Ηλεκτρονική πηγή Κεφάλαιο βιβλίου
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=685146

MARC

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330 |a The principles of polygeneration for hydrogen production during steam gasification of biomass have been studied. A distinctive feature of the proposed scheme is its unconventional method for producing superheated steam, which is subsequently used in the gasification of plant-based materials. This method involves generating superheated steam of high temperature (up to 1000 °C) and low pressure (up to 30 bar) in a boiler and a turbine unit during biomass combustion. The polygeneration scheme was modeled using the Aspen Plus software package. The calculation results were validated against the authors experimental data on oxygen-free steam gasification of biomass, as well as against published data from other researchers. The calculation errors for the volume concentrations of CO and H2 in the producer gas do not exceed 20 %. For the studied temperature range of 700–960 °C and pressure range of 2–30 bar, the exergy and energy efficiencies of the polygeneration scheme were determined to be 34.9–38.8 % and 40.1–45.6 %, respectively. The energy and exergy efficiencies of biomass conversion to H2 for the studied modes are 15.9–24.4 % and 13.85–21.31 %, respectively. The study demonstrated that the best conditions for hydrogen production in the proposed scheme are achieved using superheated steam of 960 °C and 2 bar 
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461 1 |t International Journal of Hydrogen Energy  |c Amsterdam  |n Elsevier Science Publishing Company Inc. 
463 1 |t Vol. 218  |v Article number 154035, 12 p.  |d 2026 
610 1 |a электронный ресурс 
610 1 |a труды учёных ТПУ 
610 1 |a Biomass 
610 1 |a Steam gasification 
610 1 |a Synthesis gas 
610 1 |a Fluidized bed gasifier 
610 1 |a Cold gas efficiency 
610 1 |a Exergy efficiency 
610 1 |a Polygeneration scheme 
610 1 |a Aspen plus model 
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701 1 |a Strizhak  |b P. A.  |c Specialist in the field of heat power energy  |c Doctor of Physical and Mathematical Sciences (DSc), Professor of Tomsk Polytechnic University (TPU)  |f 1985-  |g Pavel Alexandrovich  |9 15117 
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