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Fe-doped olivine and char for in-bed elimination of gasification tars in an air-blown fluidised bed reactor coupled with oxidative hot gas filtration

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Carbon Resources Conversion 2022年第4期5卷 271-288页

作者： Miguel Ruiz Adam Schnitzer claire courson Guillain Mauviel LRGP CNRSUniversity of LorraineENSIC1 Rue GrandvilleNancyFrance University of Lorraine LERMaBENSTIB27 Rue Philippe S´eguinPO Box 1041F-88051 EpinalFrance Institut of Chemistry and Processes for Energy Environment and HealthICPEES–UMR 7515University of Strasbourg25 Rue Becquerel67087 StrasbourgFrance

Gasification experiments were carried out in a pilot scale fluid bed reactor operated under allothermal mode and low fluidisation regime with iron-doped olivine and char as catalyst for in-situ tar *** catalyst combination resulted in a reduction of 50%in the overall tar yield with respect to the reference ***,the integration of an oxidative Hot Gas Filtration unit downstream the gasification reactor led to a further reduction in overall tar yield and relatively clean gas was obtained(approx.1 g/Nm3,benzene-free).The tar dew point of the resulting producer gas was estimated to 80℃,only 40℃ above the threshold value recommended for its valorisation in standard internal combustion ***,catalyst elutriation and char hold-up took place to a large extent inside the *** analysis of catalyst samples at different Time-On-Stream(TOS)revealed:(i)a considerable loss of iron oxides during the first hour of test because of the interparticle mechanical attrition(mostly surface abrasion)and partial reduction of hematite to magnetite and wustite but,stable composition at higher TOS,(ii)the loss of the iron oxide coverage of Fe/olivine particles and the formation of agglomerates with increasing TOS and,(iii)the amount of carbon deposited in the surface of the Fe/olivine particles increased with TOS,but in any case,these carbon deposits can be completely oxidized above 650℃.

关键词： Gasification Tar Oxidative hot gas filtration Char Iron-doped olivine

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Catalytic steam methane reforming enhanced by CO_2 capture on CaO based bi-functional compounds

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Journal of Energy Chemistry 2017年第5期26卷 1014-1025页

作者： Francesca Micheli Manuela Sciarra claire courson Katia Gallucci Institut de Chimie et Procédés pour l'énergie l'Environnement et la Santé UMR CNRS 7515 ECPM University of Strasbourg Department of Industrial Engineering University of L'Aquila

Sorption enhanced steam methane reforming（SE-SMR） was performed to maximize hydrogen production and contemporary remove COfrom the product stream using bi-functional sorbent-catalyst *** were tested at two different scales: micro and laboratory. The CaO amount varied in the CaO-CaAlOsorbent system synthesized by wet mixing(CaO content of 100 wt%, 56 wt%, 30 wt%, or 0 wt% and balance of CaAlO) which were upgraded to bi-functional compounds by impregnation of 3 wt% of Ni. Nitrogen adsorption（BET/BJH）, X-Ray Diffraction（XRD）, Temperature-Programmed Reduction（TPR） and Scanning and Transmission Electronic Microscopy（SEM and TEM, respectively） analyses were performed to characterize structural and textural properties and reducibility of the bi-functional materials and evaluate their catalytic behavior. A fixed sorbent composition CaO-CaAlO(56 wt% of CaO and CaAlObalance), was chosen to study the effect of different weight hourly space times（WHST） and CHstream compositions in SE-SMR activity. Impregnated mayenite at both micro and laboratory scales showed stable Hcontent of almost 74%, with CHconversion of 72% similarly to the values reported by the sample containing 30 wt% of CaO in the *** with 30 wt% of CaO showed promisingly behavior, enhancing Hcontent up to almost 94.5%.When the sorption enhanced reaction is performed roughly 89% of CHconversion is achieved, and after the pre-breakthrough, the catalyst worked at the thermodynamic level. During cycling sorption/regeneration experiments, even if COremoval efficiency slightly decreases, CHconversion and Hyield remain stable.

关键词： Sorption enhanced steam methane reforming By-functional sorbent-catalyst compounds Calcium oxide Nickel catalyst Mayenite

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