1. Catalytic gasification of biomass (Miscanthus) enhanced by CO2 sorption
- Author
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Muriel Matt, Yann Rogaume, Claire Courson, Pierre Girods, I. Zamboni, Alain Kiennemann, Matthieu Debal, Institut de chimie et procédés pour l'énergie, l'environnement et la santé (ICPEES), Université de Strasbourg (UNISTRA)-Institut de Chimie du CNRS (INC)-Centre National de la Recherche Scientifique (CNRS)-Matériaux et nanosciences d'Alsace (FMNGE), Institut de Chimie du CNRS (INC)-Université de Strasbourg (UNISTRA)-Université de Haute-Alsace (UHA) Mulhouse - Colmar (Université de Haute-Alsace (UHA))-Institut National de la Santé et de la Recherche Médicale (INSERM)-Centre National de la Recherche Scientifique (CNRS)-Université de Strasbourg (UNISTRA)-Université de Haute-Alsace (UHA) Mulhouse - Colmar (Université de Haute-Alsace (UHA))-Institut National de la Santé et de la Recherche Médicale (INSERM)-Centre National de la Recherche Scientifique (CNRS), Laboratoire d'Etude et de Recherche sur le Matériau Bois (LERMAB), Université de Lorraine (UL), and Laboratoire de Chimie et Physique - Approche Multi-échelle des Milieux Complexes (LCP-A2MC)
- Subjects
Sorbent ,Materials science ,Hydrogen ,020209 energy ,Health, Toxicology and Mutagenesis ,Inorganic chemistry ,chemistry.chemical_element ,02 engineering and technology ,Bi-functional materials ,Steam gasification ,7. Clean energy ,Miscanthus x giganteus ,Steam reforming ,Adsorption ,0202 electrical engineering, electronic engineering, information engineering ,Environmental Chemistry ,Biomass ,Hydrogen production ,Tar ,Sorption ,General Medicine ,021001 nanoscience & nanotechnology ,Pollution ,chemistry ,13. Climate action ,Fluidized bed ,[PHYS.COND.CM-MS]Physics [physics]/Condensed Matter [cond-mat]/Materials Science [cond-mat.mtrl-sci] ,0210 nano-technology ,CO2 sorption - Abstract
International audience; The main objective of this work concerns the coupling of biomass gasification reaction and CO2 sorption. The study shows the feasibility to promote biomass steam gasification in a dense fluidized bed reactor with CO2 sorption to enhance tar removal and hydrogen production. It also proves the efficiency of CaO-Ca12Al14O33/olivine bi-functional materials to reduce heavy tar production. Experiments have been carried out in a fluidized bed gasifier using steam as the fluidizing medium to improve hydrogen production. Bed materials consisting of CaO-based oxide for CO2 sorption (CaO-Ca12Al14O33) deposited on olivine for tar reduction were synthesized, their structural and textural properties were characterized by Brunauer-Emmett-Teller (BET), X-ray diffraction (XRD), and temperature-programmed reduction (TPR) methods, and the determination of their sorption capacity and stability analyzed by thermogravimetric analysis (TGA). It appears that this CaO-Ca12Al14O33/olivine sorbent/catalyst presents a good CO2 sorption stability (for seven cycles of carbonation/decarbonation). Compared to olivine and Fe/olivine in a fixed bed reactor for steam reforming of toluene chosen as tar model compound, it shows a better hydrogen production rate and a lower CO2 selectivity due to its sorption on the CaO phase. In the biomass steam gasification, the use of CaO-Ca12Al14O33/olivine as bed material at 700 A degrees C leads to a higher H-2 production than olivine at 800 A degrees C thanks to CO2 sorption. Similar tar concentration and lighter tar production (analyzed by HPLC/UV) are observed. At 700 A degrees C, sorbent addition allows to halve tar content and to eliminate the heaviest tars.
- Published
- 2016
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