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| Fältnamn | Indikatorer | Metadata |
|---|---|---|
| 000 | 03797naa a2200445 4500 | |
| 001 | oai:DiVA.org:miun-23247 | |
| 003 | SwePub | |
| 008 | 141017s2015 | |||||||||||000 ||eng| | |
| 024 | 7 | a https://urn.kb.se/resolve?urn=urn:nbn:se:miun:diva-232472 URI |
| 024 | 7 | a https://doi.org/10.1007/s13399-014-0151-52 DOI |
| 040 | a (SwePub)miun | |
| 041 | a engb eng | |
| 042 | 9 SwePub | |
| 072 | 7 | a ref2 swepub-contenttype |
| 072 | 7 | a art2 swepub-publicationtype |
| 100 | 1 | a Göransson, Kristinau Mittuniversitetet,Avdelningen för kemiteknik,FSCN Bioenergy - gasification4 aut0 (Swepub:miun)krigor |
| 245 | 1 0 | a Internal tar/CH4 reforming in a biomass dual fluidised bed gasifier. |
| 264 | c 2014-10-02 | |
| 264 | 1 | b Springer Science and Business Media LLC,c 2015 |
| 338 | a electronic2 rdacarrier | |
| 500 | a Published online 2nd Oct 2014. | |
| 520 | a An internal reformer is developed for in situ catalyticreforming of tar and methane (CH4) in allothermal gasifiers.The study has been performed in the 150 kW dual fluidised bed (DFB) biomass gasifier at Mid Sweden University(MIUN). The MIUN gasifier is built for research onsynthetic fuel production. Reduction of tars and CH4 (exceptfor methanation application) in the syngas is a major challengefor commercialization of biomass fluidised-bed gasificationtechnology towards automotive fuel production. The MIUN gasifier has a unique design with an internal reformer, where intensive contact of gas and catalytic solids improves the reforming reactions. This paper presents an initial study on the internal reformer operated with and without Ni-catalytic pellets, by evaluation of the syngas composition and tar/CH4 content. A novel application of Ni-catalyst in DFB gasifiers is proposed and studied in this work. It can be concluded that the reformer with Ni-catalytic pellets clearly gives a higher H2 content together with lower CH4 and tar contents in the syngas than the reformer without Ni-catalytic pellets. The gravimetric tar content decreases down to 5 g/m3 and the CH4 content down below 6 % in the syngas. The tar content can be decreased further to lower levels, with increased gas contact to the specific surface area of the catalyst and increased catalyst surface-to-volume ratio. The new design in the MIUN gasifier increases the gasification efficiency, suppresses the tar generation and upgrades the syngas quality. | |
| 650 | 7 | a TEKNIK OCH TEKNOLOGIERx Kemiteknik0 (SwePub)2042 hsv//swe |
| 650 | 7 | a ENGINEERING AND TECHNOLOGYx Chemical Engineering0 (SwePub)2042 hsv//eng |
| 653 | a Biomass gasification | |
| 653 | a Syngas cleaning | |
| 653 | a Tar removal | |
| 653 | a Tar/CH4 reformning | |
| 653 | a Dual fluidised bed | |
| 653 | a Ni-catalyst | |
| 700 | 1 | a Söderlind, Ulfu Mittuniversitetet,Avdelningen för kemiteknik,FSCN Bioenergy - gasification4 aut0 (Swepub:miun)ulfsod |
| 700 | 1 | a Henschel, Tillu Mittuniversitetet,Avdelningen för kemiteknik,FSCN Bioenergy - gasification4 aut0 (Swepub:miun)tilhen |
| 700 | 1 | a Engstrand, Peru Mittuniversitetet,Avdelningen för kemiteknik,FSCN4 aut0 (Swepub:miun)pereng |
| 700 | 1 | a Zhang, Wennanu Mittuniversitetet,Avdelningen för kemiteknik,FSCN Bioenergy - gasification4 aut0 (Swepub:miun)wenzha |
| 710 | 2 | a Mittuniversitetetb Avdelningen för kemiteknik4 org |
| 773 | 0 | t Biomass Conversion and Biorefineryd : Springer Science and Business Media LLCg 5, s. 355-366q 5<355-366x 2190-6815x 2190-6823 |
| 856 | 4 | u https://miun.diva-portal.org/smash/get/diva2:756378/FULLTEXT02.pdfx primaryx Raw objecty fulltext:print |
| 856 | 4 | u http://miun.diva-portal.org/smash/get/diva2:756378/FULLTEXT02 |
| 856 | 4 8 | u https://urn.kb.se/resolve?urn=urn:nbn:se:miun:diva-23247 |
| 856 | 4 8 | u https://doi.org/10.1007/s13399-014-0151-5 |
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