Agglomeration of silica sand in a fluidized bed gasifier operating on wheat straw
The effects of straw feed rate and ash composition on the agglomeration characteristics of the bed material (silica sand) in a fluidized bed gasification system were investigated. By changing the air flow rate and/or straw feed rate, the effects of four equivalence ratios (0.26, 0.38, 0.57 and 0.76)...
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Veröffentlicht in: | Biomass & bioenergy 1993, Vol.4 (2), p.135-147 |
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description | The effects of straw feed rate and ash composition on the agglomeration characteristics of the bed material (silica sand) in a fluidized bed gasification system were investigated. By changing the air flow rate and/or straw feed rate, the effects of four equivalence ratios (0.26, 0.38, 0.57 and 0.76) on agglomeration were investigated. The effect of straw ash content (0.0, 3.3, 27.8 and 43.5%) on the agglomeration of the bed material was also investigated at various temperatures (620, 740 and 850°C) using a high temperature furnace. It was found that a fluidized bed of silica sand agglomerated at around 800°C in the presence of straw ash, resulting in serious channelling and defluidization. A very hard and brittle structure was formed at 850°C. Changes in air velocity and/or fuel rate did not improve agglomeration characteristics. K
2O, which is present at a high weight percentage in the straw ash and has a relatively low melting temperature, was the major contributor to the agglomeration process. |
doi_str_mv | 10.1016/0961-9534(93)90034-2 |
format | Article |
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2O, which is present at a high weight percentage in the straw ash and has a relatively low melting temperature, was the major contributor to the agglomeration process.</description><subject>agglomeration</subject><subject>air flow rate</subject><subject>ash composition</subject><subject>ash content</subject><subject>channelling</subject><subject>defluidization</subject><subject>feed rate</subject><subject>fluidized bed</subject><subject>Gasification</subject><subject>pressure drop</subject><subject>silica sand</subject><subject>straw</subject><subject>temperature</subject><issn>0961-9534</issn><issn>1873-2909</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1993</creationdate><recordtype>article</recordtype><recordid>eNp9kEtLAzEUhYMoWKv_wEVWoovRvDrTbIRSfIEggq7DneRmjEwnNZla9Nc7bcWli8vdnO_A-Qg55eySM15eMV3yQk-kOtfyQjMmVSH2yIhPK1kIzfQ-Gf1FDslRzu-MccUUH5HnWdO0cYEJ-hA7Gj3NoQ0WaIbO0dBRoL5dBRe-0dF6uAZy8AETjcst1DV04NZvCD3NfYL1MTnw0GY8-f1j8np78zK_Lx6f7h7ms8fCyor3BZdCMicY1EJLVoMH9IiuLHmFUvhK8ArqiROV11P0wgIoPnVMeWC1rUHKMTnb9S5T_Fhh7s0iZIttCx3GVTZ8IpRUfBNUu6BNMeeE3ixTWED6MpyZjT-zkWM2coyWZuvPiAG73mE4jPgcFptsA3YWXUhoe-Ni-L_gB-qOeAc</recordid><startdate>1993</startdate><enddate>1993</enddate><creator>Ergudenler, A.</creator><creator>Ghaly, A.E.</creator><general>Elsevier Ltd</general><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>1993</creationdate><title>Agglomeration of silica sand in a fluidized bed gasifier operating on wheat straw</title><author>Ergudenler, A. ; Ghaly, A.E.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c371t-13230d20ab2930bafaefeed6617e32f7217ab5d27f98ef2caa418d04fa0bcba33</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1993</creationdate><topic>agglomeration</topic><topic>air flow rate</topic><topic>ash composition</topic><topic>ash content</topic><topic>channelling</topic><topic>defluidization</topic><topic>feed rate</topic><topic>fluidized bed</topic><topic>Gasification</topic><topic>pressure drop</topic><topic>silica sand</topic><topic>straw</topic><topic>temperature</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ergudenler, A.</creatorcontrib><creatorcontrib>Ghaly, A.E.</creatorcontrib><collection>CrossRef</collection><jtitle>Biomass & bioenergy</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ergudenler, A.</au><au>Ghaly, A.E.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Agglomeration of silica sand in a fluidized bed gasifier operating on wheat straw</atitle><jtitle>Biomass & bioenergy</jtitle><date>1993</date><risdate>1993</risdate><volume>4</volume><issue>2</issue><spage>135</spage><epage>147</epage><pages>135-147</pages><issn>0961-9534</issn><eissn>1873-2909</eissn><abstract>The effects of straw feed rate and ash composition on the agglomeration characteristics of the bed material (silica sand) in a fluidized bed gasification system were investigated. By changing the air flow rate and/or straw feed rate, the effects of four equivalence ratios (0.26, 0.38, 0.57 and 0.76) on agglomeration were investigated. The effect of straw ash content (0.0, 3.3, 27.8 and 43.5%) on the agglomeration of the bed material was also investigated at various temperatures (620, 740 and 850°C) using a high temperature furnace. It was found that a fluidized bed of silica sand agglomerated at around 800°C in the presence of straw ash, resulting in serious channelling and defluidization. A very hard and brittle structure was formed at 850°C. Changes in air velocity and/or fuel rate did not improve agglomeration characteristics. K
2O, which is present at a high weight percentage in the straw ash and has a relatively low melting temperature, was the major contributor to the agglomeration process.</abstract><pub>Elsevier Ltd</pub><doi>10.1016/0961-9534(93)90034-2</doi><tpages>13</tpages></addata></record> |
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source | ScienceDirect Journals (5 years ago - present) |
subjects | agglomeration air flow rate ash composition ash content channelling defluidization feed rate fluidized bed Gasification pressure drop silica sand straw temperature |
title | Agglomeration of silica sand in a fluidized bed gasifier operating on wheat straw |
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