Influence of different bed material mixtures on dual fluidized bed steam gasification

Within this paper, investigations to convert softwood with four different types of bed materials in the 100 kWth dual fluidized bed steam gasification pilot plant at TU Wien are presented and discussed. The results of ten different experiments were compared. Quartz, olivine and feldspar were mixed w...

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Veröffentlicht in:Energy (Oxford) 2018-08, Vol.157, p.957-968
Hauptverfasser: Mauerhofer, A.M., Benedikt, F., Schmid, J.C., Fuchs, J., Müller, S., Hofbauer, H.
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container_start_page 957
container_title Energy (Oxford)
container_volume 157
creator Mauerhofer, A.M.
Benedikt, F.
Schmid, J.C.
Fuchs, J.
Müller, S.
Hofbauer, H.
description Within this paper, investigations to convert softwood with four different types of bed materials in the 100 kWth dual fluidized bed steam gasification pilot plant at TU Wien are presented and discussed. The results of ten different experiments were compared. Quartz, olivine and feldspar were mixed with limestone in mass ratios of 100/0, 90/10, 50/50 and 0/100. Limestone was used due to its catalytic activity at high temperatures as CaO and thus enhanced tar, char and water conversion of quartz, olivine and feldspar. The admixture of limestone to quartz, olivine and feldspar shifted the product gas compositions towards higher hydrogen and carbon dioxide and lower carbon monoxide contents. By using 100 wt.-% limestone as bed material a hydrogen content of 47.4 vol.-% could be generated. Additionally, the tar concentrations as well as the tar dew points decreased and especially the heavy tar compounds could be reduced. Already small amounts of limestone (
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The results of ten different experiments were compared. Quartz, olivine and feldspar were mixed with limestone in mass ratios of 100/0, 90/10, 50/50 and 0/100. Limestone was used due to its catalytic activity at high temperatures as CaO and thus enhanced tar, char and water conversion of quartz, olivine and feldspar. The admixture of limestone to quartz, olivine and feldspar shifted the product gas compositions towards higher hydrogen and carbon dioxide and lower carbon monoxide contents. By using 100 wt.-% limestone as bed material a hydrogen content of 47.4 vol.-% could be generated. Additionally, the tar concentrations as well as the tar dew points decreased and especially the heavy tar compounds could be reduced. Already small amounts of limestone (&lt;10 wt.-%) to the bed material mixture influenced tar reduction in a positive way. The low abrasion resistance of limestone resulted in increasing dust contents by increasing its amount. However, this could be balanced by the specific design of the separation system of the advanced pilot plant. [Display omitted] •100 kWth dual fluidized bed steam gasification pilot plant at TU Wien.•Mixtures of quartz, olivine and feldspar with limestone as bed material.•Increasing tar destruction and H2 content by increasing limestone content.•Rising share of limestone in bed material mixture reduced heavy tar compounds.•Already low amounts of limestone showed significant effects on product gas and tar.</description><identifier>ISSN: 0360-5442</identifier><identifier>EISSN: 1873-6785</identifier><identifier>DOI: 10.1016/j.energy.2018.05.158</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Abrasion ; Abrasion resistance ; Admixtures ; Carbon dioxide ; Carbon monoxide ; Catalysis ; Catalytic activity ; Dew point ; Feldspar ; Fluidized bed combustion ; Fluidized beds ; Gasification ; High temperature ; Limestone ; Limestone/CaO ; Mass ratios ; Olivine ; Pilot plants ; Quartz ; Softwoods ; Steam ; Tar ; Tar reduction</subject><ispartof>Energy (Oxford), 2018-08, Vol.157, p.957-968</ispartof><rights>2018 Elsevier Ltd</rights><rights>Copyright Elsevier BV Aug 15, 2018</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c371t-2c533f40301fe11ce08343d3bf5c49d7beebe497ab26cea729f741a5883435903</citedby><cites>FETCH-LOGICAL-c371t-2c533f40301fe11ce08343d3bf5c49d7beebe497ab26cea729f741a5883435903</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0360544218310028$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids></links><search><creatorcontrib>Mauerhofer, A.M.</creatorcontrib><creatorcontrib>Benedikt, F.</creatorcontrib><creatorcontrib>Schmid, J.C.</creatorcontrib><creatorcontrib>Fuchs, J.</creatorcontrib><creatorcontrib>Müller, S.</creatorcontrib><creatorcontrib>Hofbauer, H.</creatorcontrib><title>Influence of different bed material mixtures on dual fluidized bed steam gasification</title><title>Energy (Oxford)</title><description>Within this paper, investigations to convert softwood with four different types of bed materials in the 100 kWth dual fluidized bed steam gasification pilot plant at TU Wien are presented and discussed. 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subjects Abrasion
Abrasion resistance
Admixtures
Carbon dioxide
Carbon monoxide
Catalysis
Catalytic activity
Dew point
Feldspar
Fluidized bed combustion
Fluidized beds
Gasification
High temperature
Limestone
Limestone/CaO
Mass ratios
Olivine
Pilot plants
Quartz
Softwoods
Steam
Tar
Tar reduction
title Influence of different bed material mixtures on dual fluidized bed steam gasification
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