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  <titleInfo>
    <nonSort>A </nonSort>
    <title>comparative study of different designs of spouted bed reactor</title>
  </titleInfo>
  <name type="personal">
    <namePart>Rasul, Md. Golam</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>Mora, Jean-Claude</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Bo, Khin</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>The Government of France</namePart>
    <role>
      <roleTerm type="text">Scholarship Donor</roleTerm>
    </role>
  </name>
  <typeOfResource>text</typeOfResource>
  <genre authority="marc">series</genre>
  <genre authority="marc">technical report</genre>
  <originInfo>
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    <place>
      <placeTerm type="text">Bangkok</placeTerm>
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    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1990</dateIssued>
    <issuance>continuing</issuance>
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  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
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  <physicalDescription>
    <extent>89 leaves.</extent>
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  <abstract>In this study, two new/unconventional spouted bed reactor designs have been  compared with the conventional design having a central gas (air) inlet jet. In one  of these designs, air is introduced into a rectangular column through a rectangular  slit while in the other design air is introduced into a cylindrical column through  a circular slit. The column and the air inlet areas were the same in all the designs  compared.  Tests, carried out with dry sand samples, displayed hysteresis typical of all  spouted beds with characteristic differences in shape depending upon particle size.  Effects of particle size, bed weight and column geometry were evaluated. The  maximum pressure drop was obtained in the design with circular slit and the  minimum in the design with rectangular slit.  Experiments were carried out to determine the contact efficiency, mass transfer  flux, and combustion efficiency loss due to CO formation for the different reactor  designs. The contact efficiency based on gas (air) exit and bed temperature, and  combustion efficiency loss due to CO formation showed similar results and it was  found that the highest contact efficiency and lowest co loss was achieved in the  design with circular slit and lowest contact efficiency and highest CO loss was  achieved in the design with rectangular slit. Mass transfer flux was found to  decrease with increasing particle diameter and it was maximum in the design with  central jet and minimum in the design with circular slit.</abstract>
  <note>A Research Study Submitted in Partial fulfilment of the requirement for the degree of Master of Engineering, School of Environment, Resources and Development</note>
  <note>Research Studies Project Report (M. Eng.) - Asian Institute of Technology, 1990</note>
  <subject authority="lcsh">
    <topic>Fluidized reactors</topic>
  </subject>
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    <titleInfo>
      <title>Research studies project report ; no. ET-90-3</title>
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    <name type="corporate">
      <namePart>Asian Institute of Technology.</namePart>
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    </name>
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  <identifier type="uri">http://203.159.5.9/ait-thesis/detail.php?q=B18165</identifier>
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    <url displayLabel="Full-Text">http://203.159.5.9/ait-thesis/detail.php?q=B18165</url>
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