Dual fluidized bed based technologies for carbon dioxide reduction — example hot metal production

Research output: Contribution to journalArticleResearchpeer-review

Standard

Dual fluidized bed based technologies for carbon dioxide reduction — example hot metal production. / Müller, Stefan; Theiss, Lara; Fleiß, Benjamin et al.
In: Biomass conversion and biorefinery, 03.10.2020.

Research output: Contribution to journalArticleResearchpeer-review

APA

Vancouver

Müller S, Theiss L, Fleiß B, Hammerschmid M, Fuchs J, Penthor S et al. Dual fluidized bed based technologies for carbon dioxide reduction — example hot metal production. Biomass conversion and biorefinery. 2020 Oct 3. doi: https://doi.org/10.1007/s13399-020-01021-4

Bibtex - Download

@article{7d1080e9468b4be6a0eadcdaa3b2a868,
title = "Dual fluidized bed based technologies for carbon dioxide reduction — example hot metal production",
abstract = "The present work describes the results achieved during a study aiming at the full replacement of the natural gas demand of an integrated hot metal production. This work implements a novel approach using a biomass gasification plant combined with an electrolysis unit to substitute the present natural gas demand of an integrated hot metal production. Therefore, a simulation platform, including mathematical models for all relevant process units, enabling the calculation of all relevant mass and energy balances was created. As a result, the calculations show that a natural gas demand of about 385 MW can be replaced and an additional 100 MW hydrogen-rich reducing gas can be produced by the use of 132 MW of biomass together with 571 MW electricity produced from renewable energy. The results achieved indicate that a full replacement of the natural gas demand would be possible from a technological point of view. At the same time, the technological readiness level of available electrolysis units shows that a production at such a large scale has not been demonstrated yet.",
keywords = "Carbon dioxide reduction . Oxyfuel combustion . Sorption enhanced reforming . Biomass gasification",
author = "Stefan M{\"u}ller and Lara Theiss and Benjamin Flei{\ss} and Martin Hammerschmid and Josef Fuchs and Stefan Penthor and Daniel Rosenfeld and Markus Lehner and Hermann Hofbauer",
year = "2020",
month = oct,
day = "3",
doi = "https://doi.org/10.1007/s13399-020-01021-4",
language = "English",
journal = "Biomass conversion and biorefinery",
issn = "2190-6815",
publisher = "Springer Berlin",

}

RIS (suitable for import to EndNote) - Download

TY - JOUR

T1 - Dual fluidized bed based technologies for carbon dioxide reduction — example hot metal production

AU - Müller, Stefan

AU - Theiss, Lara

AU - Fleiß, Benjamin

AU - Hammerschmid, Martin

AU - Fuchs, Josef

AU - Penthor, Stefan

AU - Rosenfeld, Daniel

AU - Lehner, Markus

AU - Hofbauer, Hermann

PY - 2020/10/3

Y1 - 2020/10/3

N2 - The present work describes the results achieved during a study aiming at the full replacement of the natural gas demand of an integrated hot metal production. This work implements a novel approach using a biomass gasification plant combined with an electrolysis unit to substitute the present natural gas demand of an integrated hot metal production. Therefore, a simulation platform, including mathematical models for all relevant process units, enabling the calculation of all relevant mass and energy balances was created. As a result, the calculations show that a natural gas demand of about 385 MW can be replaced and an additional 100 MW hydrogen-rich reducing gas can be produced by the use of 132 MW of biomass together with 571 MW electricity produced from renewable energy. The results achieved indicate that a full replacement of the natural gas demand would be possible from a technological point of view. At the same time, the technological readiness level of available electrolysis units shows that a production at such a large scale has not been demonstrated yet.

AB - The present work describes the results achieved during a study aiming at the full replacement of the natural gas demand of an integrated hot metal production. This work implements a novel approach using a biomass gasification plant combined with an electrolysis unit to substitute the present natural gas demand of an integrated hot metal production. Therefore, a simulation platform, including mathematical models for all relevant process units, enabling the calculation of all relevant mass and energy balances was created. As a result, the calculations show that a natural gas demand of about 385 MW can be replaced and an additional 100 MW hydrogen-rich reducing gas can be produced by the use of 132 MW of biomass together with 571 MW electricity produced from renewable energy. The results achieved indicate that a full replacement of the natural gas demand would be possible from a technological point of view. At the same time, the technological readiness level of available electrolysis units shows that a production at such a large scale has not been demonstrated yet.

KW - Carbon dioxide reduction . Oxyfuel combustion . Sorption enhanced reforming . Biomass gasification

UR - http://www.scopus.com/inward/record.url?scp=85092040427&partnerID=8YFLogxK

U2 - https://doi.org/10.1007/s13399-020-01021-4

DO - https://doi.org/10.1007/s13399-020-01021-4

M3 - Article

JO - Biomass conversion and biorefinery

JF - Biomass conversion and biorefinery

SN - 2190-6815

ER -