Dual fluidized bed based technologies for carbon dioxide reduction — example hot metal production
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In: Biomass conversion and biorefinery, 03.10.2020.
Research output: Contribution to journal › Article › Research › peer-review
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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 -