Supercritical water conversion of glycerol : comparative parametric study between batch and continuous process
hal.structure.identifier | Centre de recherche d'Albi en génie des procédés des solides divisés, de l'énergie et de l'environnement [RAPSODEE] | |
dc.contributor.author | WU, Qian | |
dc.contributor.author | BULZA, Silviu | |
dc.contributor.author | CORCOVEANU, C. | |
hal.structure.identifier | Centre de recherche d'Albi en génie des procédés des solides divisés, de l'énergie et de l'environnement [RAPSODEE] | |
dc.contributor.author | WEISS-HORTALA, Elsa | |
hal.structure.identifier | Centre de recherche d'Albi en génie des procédés des solides divisés, de l'énergie et de l'environnement [RAPSODEE] | |
dc.contributor.author | BARNA, Radu | |
hal.structure.identifier | Institut de Chimie de la Matière Condensée de Bordeaux [ICMCB] | |
dc.contributor.author | LOPPINET SERANI, Anne | |
hal.structure.identifier | Institut de Chimie de la Matière Condensée de Bordeaux [ICMCB] | |
dc.contributor.author | AYMONIER, Cyril | |
dc.date.issued | 2011 | |
dc.date.conference | 2011-10-09 | |
dc.description.abstractEn | • Glycerol, a main by-product of the biodiesel production, has a high valorization potential. This paper proposes a comparison of hydrogen production from glycerol using batch (5 mL and 500 mL) and continuous (100 mL) processes. The influence of different operating parameters has been studied: temperature (450°C-600°C), pressure (20-28MPa), glycerol concentration (5-20wt%), catalyst concentration (K 2 CO 3 or NaOH, 0-5 wt%), reaction time (5-120 min, batch), residence time (12 min, continuous process), stirring rate (500-1500 rpm, batch of 500ml), and heating rate (50% and 100% of heating power). • Quantitative glycerol conversion has been observed: until 99% of TOC removal by SCWG. While the amount of solid formed is insignificant, the produced gas volume reached 43 L gas/L solution (5 wt% glycerol) with a molar composition up to 60% H 2 and 30% CO 2 (atmospheric pressure). Various proportions of CH 4 , C 2 H 6 and C 2 H 4 have been observed. Catalyst contribution to the gasification yield of glycerol is relevant. • SCW conversion of glycerol, quantitative by-product in biodiesel industry, into hydrogen is a sustainable process. The yield obtained in the continuous laboratory reactor (3 mol H 2 /L of reactor/h) under homogeneous catalysis (K salts, low concentrations) recommends the process for further research and pilot development. | |
dc.language.iso | en | |
dc.publisher | INTERNATIONAL SOCIETY FOR THE ADVANCEMENT OF SUPERCRITICAL FLUIDS | |
dc.source.title | 13th European meeting on supercritical fluids | |
dc.subject.en | Glycerol | |
dc.subject.en | K 2 CO 3 | |
dc.subject.en | NaOH | |
dc.subject.en | Hydrogen | |
dc.subject.en | Supercritical water | |
dc.subject.en | Batch | |
dc.subject.en | Continuous reactor | |
dc.title.en | Supercritical water conversion of glycerol : comparative parametric study between batch and continuous process | |
dc.type | Communication dans un congrès | |
dc.subject.hal | Sciences de l'ingénieur [physics] | |
bordeaux.page | 12 p. | |
bordeaux.country | NL | |
bordeaux.title.proceeding | 13th European meeting on supercritical fluids | |
bordeaux.conference.city | The Hague | |
bordeaux.peerReviewed | oui | |
hal.identifier | hal-01753250 | |
hal.version | 1 | |
hal.invited | non | |
hal.proceedings | oui | |
hal.conference.end | 2011-10-12 | |
hal.popular | non | |
hal.audience | Internationale | |
hal.origin.link | https://hal.archives-ouvertes.fr//hal-01753250v1 | |
bordeaux.COinS | ctx_ver=Z39.88-2004&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.btitle=13th%20European%20meeting%20on%20supercritical%20fluids&rft.date=2011&rft.spage=12%20p.&rft.epage=12%20p.&rft.au=WU,%20Qian&BULZA,%20Silviu&CORCOVEANU,%20C.&WEISS-HORTALA,%20Elsa&BARNA,%20Radu&rft.genre=unknown |
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