Stabilization of biomass-derived pyrolysis oils
BACKGROUND: Biomass is the only renewable feedstock containing carbon, and therefore the only alternative to fossil-derived crude oil derivatives. However, the main problems concerning the application of biomass for biofuels and bio-based chemicals are related to transport and handling, the limited...
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Published in | Journal of chemical technology and biotechnology (1986) Vol. 85; no. 5; pp. 674 - 686 |
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Main Authors | , , , , |
Format | Journal Article |
Language | English |
Published |
Chichester, UK
John Wiley & Sons, Ltd
01.05.2010
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Subjects | |
Online Access | Get full text |
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Summary: | BACKGROUND: Biomass is the only renewable feedstock containing carbon, and therefore the only alternative to fossil-derived crude oil derivatives. However, the main problems concerning the application of biomass for biofuels and bio-based chemicals are related to transport and handling, the limited scale of the conversion process and the competition with the food industry. To overcome such problems, an integral processing route for the conversion of (non-feed) biomass (residues) to transportation fuels is proposed. It includes a pretreatment process by fast pyrolysis, followed by upgrading to produce a crude-oil-like product, and finally co-refining in traditional refineries.RESULTS: This paper contributes to the understanding of pyrolysis oil upgrading. The processes include a thermal treatment step and/or direct hydroprocessing. At temperatures up to 250 °C (in the presence of H₂ and catalyst) parallel reactions take place including re-polymerization (water production), decarboxylation (limited CO₂ production) and hydrotreating. Water is produced in small quantities (approx. 10% extra), likely caused by repolymerization. This repolymerization takes place faster (order of minutes) than the hydrotreating reactions (order of tens of minutes, hours).CONCLUSIONS: In hydroprocessing of bio-oils, a pathway is followed by which pyrolysis oils are further polymerized if H₂ and/or catalyst is absent, eventually to char components, or, with H₂/catalyst, to stabilized components that can be further upgraded. Results of the experiments suggest that specifically the cellulose-derived fraction of the oil needs to be transformed first, preferably into alcohols in a 'mild hydrogenation' step. This subsequently allows further dehydration and hydrogenation. Copyright |
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Bibliography: | http://dx.doi.org/10.1002/jctb.2354 ark:/67375/WNG-PQQ7VB6H-Z ArticleID:JCTB2354 SenterNovem istex:44344F1A561EABD57B896039807B98F00E23886C ObjectType-Article-1 SourceType-Scholarly Journals-1 ObjectType-Feature-2 content type line 23 |
ISSN: | 0268-2575 1097-4660 1097-4660 |
DOI: | 10.1002/jctb.2354 |