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 |
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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 ( |
doi_str_mv | 10.1016/j.energy.2018.05.158 |
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[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. 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 (<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><subject>Abrasion</subject><subject>Abrasion resistance</subject><subject>Admixtures</subject><subject>Carbon dioxide</subject><subject>Carbon monoxide</subject><subject>Catalysis</subject><subject>Catalytic activity</subject><subject>Dew point</subject><subject>Feldspar</subject><subject>Fluidized bed combustion</subject><subject>Fluidized beds</subject><subject>Gasification</subject><subject>High temperature</subject><subject>Limestone</subject><subject>Limestone/CaO</subject><subject>Mass ratios</subject><subject>Olivine</subject><subject>Pilot plants</subject><subject>Quartz</subject><subject>Softwoods</subject><subject>Steam</subject><subject>Tar</subject><subject>Tar reduction</subject><issn>0360-5442</issn><issn>1873-6785</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><recordid>eNp9kE1LxDAQhoMouK7-Aw8Bz62ZpmnaiyCLHwsLXtxzSNPJkrJt16QV9debUs-eBobnfYd5CLkFlgKD4r5NsUd_-E4zBmXKRAqiPCMrKCVPClmKc7JivGCJyPPsklyF0DLGRFlVK7Lf9vY4YW-QDpY2zlr02I-0xoZ2ekTv9JF27mucPAY69LSZ4iJGXON-IjNzYUTd0YMOzjqjRzf01-TC6mPAm7-5Jvvnp_fNa7J7e9luHneJ4RLGJDOCc5szzsAigEFW8pw3vLbC5FUja8Qa80rqOisMaplVVuagRTljomJ8Te6W3pMfPiYMo2qHyffxpMoAQEiQVRWpfKGMH0LwaNXJu077bwVMzQJVqxaBahaomFBRYIw9LDGMH3w69CoYN5tqnEczqmZw_xf8AiRie8U</recordid><startdate>20180815</startdate><enddate>20180815</enddate><creator>Mauerhofer, A.M.</creator><creator>Benedikt, F.</creator><creator>Schmid, J.C.</creator><creator>Fuchs, J.</creator><creator>Müller, S.</creator><creator>Hofbauer, H.</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SP</scope><scope>7ST</scope><scope>7TB</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>KR7</scope><scope>L7M</scope><scope>SOI</scope></search><sort><creationdate>20180815</creationdate><title>Influence of different bed material mixtures on dual fluidized bed steam gasification</title><author>Mauerhofer, A.M. ; Benedikt, F. ; Schmid, J.C. ; Fuchs, J. ; Müller, S. ; Hofbauer, H.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c371t-2c533f40301fe11ce08343d3bf5c49d7beebe497ab26cea729f741a5883435903</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>Abrasion</topic><topic>Abrasion resistance</topic><topic>Admixtures</topic><topic>Carbon dioxide</topic><topic>Carbon monoxide</topic><topic>Catalysis</topic><topic>Catalytic activity</topic><topic>Dew point</topic><topic>Feldspar</topic><topic>Fluidized bed combustion</topic><topic>Fluidized beds</topic><topic>Gasification</topic><topic>High temperature</topic><topic>Limestone</topic><topic>Limestone/CaO</topic><topic>Mass ratios</topic><topic>Olivine</topic><topic>Pilot plants</topic><topic>Quartz</topic><topic>Softwoods</topic><topic>Steam</topic><topic>Tar</topic><topic>Tar reduction</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><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><collection>CrossRef</collection><collection>Electronics & Communications Abstracts</collection><collection>Environment Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Environment Abstracts</collection><jtitle>Energy (Oxford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mauerhofer, A.M.</au><au>Benedikt, F.</au><au>Schmid, J.C.</au><au>Fuchs, J.</au><au>Müller, S.</au><au>Hofbauer, H.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Influence of different bed material mixtures on dual fluidized bed steam gasification</atitle><jtitle>Energy (Oxford)</jtitle><date>2018-08-15</date><risdate>2018</risdate><volume>157</volume><spage>957</spage><epage>968</epage><pages>957-968</pages><issn>0360-5442</issn><eissn>1873-6785</eissn><abstract>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 (<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.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.energy.2018.05.158</doi><tpages>12</tpages></addata></record> |
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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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