4.7 Article

Characterization of products obtained from pyrolysis and steam gasification of wood waste, RDF, and RPF

期刊

WASTE MANAGEMENT
卷 34, 期 2, 页码 402-410

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.wasman.2013.10.009

关键词

Gasification; Pyrolysis; RDF; RPF; Wood waste

资金

  1. global COE program of Yokohama University
  2. National Institute for Environmental Studies

向作者/读者索取更多资源

Pyrolysis and steam gasification of woody biomass chip (WBC) obtained from construction and demolition wastes, refuse-derived fuel (RDF), and refuse paper and plastic fuel (RPF) were performed at various temperatures using a lab-scale instrument. The gas, liquid, and solid products were examined to determine their generation amounts, properties, and the carbon balance between raw material and products. The amount of product gas and its hydrogen concentration showed a considerable difference depending on pyrolysis and steam gasification at higher temperature. The reaction of steam and solid product, char, contributed to an increase in gas amount and hydrogen concentration. The amount of liquid products generated greatly depended on temperature rather than pyrolysis or steam gasification. The compositions of liquid product varied relying on raw materials used at 500 degrees C but the polycyclic aromatic hydrocarbons became the major compounds at 900 degrees C irrespective of the raw materials used. Almost fixed carbon (FC) of raw materials remained as solid products under pyrolysis condition whereas FC started to decompose at 700 degrees C under steam gasification condition. For WBC, both char utilization by pyrolysis at low temperature (500 degrees C) and syngas recovery by steam gasification at higher temperature (900 degrees C) might be practical options. From the results of carbon balance of RDF and RPF, it was confirmed that the carbon conversion to liquid products conspicuously increased as the amount of plastic increased in the raw material. To recover feedstock from RPF, pyrolysis for oil recovery at low temperature (500 degrees C) might be one of viable options. Steam gasification at 900 degrees C could be an option but the method of tar reforming (e.g. catalyst utilization) should be considered. (C) 2013 Elsevier Ltd. All rights reserved.

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