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  <titleInfo>
    <title>Mathematical modelling of a down draft wood gasifier</title>
  </titleInfo>
  <name type="personal">
    <namePart>Navaratnam, Sivasakthy</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Bhattacharya, Sribas C.</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Prida Wibulswas</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Tentscher, Wolfgang</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>CIDA</namePart>
    <role>
      <roleTerm type="text">Scholarship Donor</roleTerm>
    </role>
  </name>
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  <originInfo>
    <place>
      <placeTerm type="code" authority="marccountry">th</placeTerm>
    </place>
    <place>
      <placeTerm type="text">Bangkok</placeTerm>
    </place>
    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1986</dateIssued>
    <issuance>monographic</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
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  <physicalDescription>
    <extent>81 p.</extent>
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  <abstract>In this study, a review of the available literature on kinetics of wood  pyrolysis has been made. Available literature shows wood pyrolysis is a  complex process and need to be studied further experimentally, to develop a  fairly realistic theoretical model for pyrolysis zone of a wood gasifier.  Since no data are available on pyrolysis product distribution in fixed  bed wood gasifier, an attempt was made to estimate the pyrolysis product  distribution theoretically assuming pyrolysis reactions to be autothermic.  Thermal Analysis was carried out to analyze the kinetics of pyrolysis  process qualitatively. The results show that heat of reaction of pyrolysis  process is different at different temperatures. Major weight loss occurred  in the .temperature range of 280 to 450 C.  A steady state model for a downdraft wood gasifier has been developed  based on kinetics and mechanisms of chemical reactions, mass and heat  transfer and conservation of mass and energy. Wood gasifier model is subjected to constraints such as pyrolysis product composition. Parametric  studies were made on wood and air flow rates, reaction multiplier and particle diameter.  Also, an attempt has been made to incorporate porosity effect, in the  model developed by BASAK(1985) for charcoal gasifier. Incorporation of  porosity effect was found to improve the reaction rates .</abstract>
  <note>A thesis submitted in partial fulfillment of the requirements for the degree of Master of Engineering, School of Environment, Resources and Development</note>
  <note>Thesis (M.Eng.) - Asian Institute of Technology, 1986</note>
  <subject authority="lcsh">
    <topic>Pyrolysis</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Biomass energy</topic>
  </subject>
  <relatedItem type="series">
    <titleInfo>
      <title>Thesis ; no. ET-86-7</title>
    </titleInfo>
    <name type="corporate">
      <namePart>Asian Institute of Technology.</namePart>
      <namePart/>
    </name>
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  <identifier type="uri">http://203.159.5.9/ait-thesis/detail.php?q=B19621</identifier>
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    <url displayLabel="Full-Text">http://203.159.5.9/ait-thesis/detail.php?q=B19621</url>
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