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231223s2009 xx |||||o 00| ||eng c |
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|a 10.1177/0734242X08091553
|2 doi
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|a pubmed24n0628.xml
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|a (DE-627)NLM188350683
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|a (NLM)19423576
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|a DE-627
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|a eng
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|a Gao, Ningbo
|e verfasserin
|4 aut
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|a Research into fine powder and large particle tyre pyrolysis
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|c 2009
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|a Text
|b txt
|2 rdacontent
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|a ƒaComputermedien
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|2 rdamedia
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|a ƒa Online-Ressource
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|2 rdacarrier
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|a Date Completed 11.08.2009
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|a Date Revised 15.05.2009
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|a published: Print-Electronic
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|a Citation Status MEDLINE
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|a This paper investigates the kinetics of the pyrolysis of scrap tyre using thermogravimetry and a small batch laboratory-scale externally heated fixed-bed. Five particle sizes (20-40, 40-60, 60-80, 80-100, 100-200 mesh) and five heating rates (5, 10, 15, 20, 40 K min(-1)) were investigated. The results show that there is no obvious distinction on weight loss for different sizes. With increasing heating rate the weight loss regions shift to a higher temperature range and the weight loss rate increases. The activation energy (E) and pre-exponential factor constant (A) were calculated using the Arrhenius type kinetic model. The heat value of pyrolysis gases is in the range of 12 to 22 MJ Nm(-3). The yields of solid, liquid and gas of pyrolysis scrap tyre and tyre cube at 800 degrees C were investigated, the ratio of pyrolysis production composition of scrap tyre and tyre cube for gas, oil and char is found to be 35 : 23 : 42 and 10 : 31 : 59, respectively
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|a Journal Article
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|a Air Pollutants
|2 NLM
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|a Powders
|2 NLM
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|a Li, Aimin
|e verfasserin
|4 aut
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|a Li, Wanjing
|e verfasserin
|4 aut
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|i Enthalten in
|t Waste management & research : the journal of the International Solid Wastes and Public Cleansing Association, ISWA
|d 1991
|g 27(2009), 3 vom: 01. Mai, Seite 242-50
|w (DE-627)NLM098164791
|x 1096-3669
|7 nnns
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|g volume:27
|g year:2009
|g number:3
|g day:01
|g month:05
|g pages:242-50
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|u http://dx.doi.org/10.1177/0734242X08091553
|3 Volltext
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