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  <titleInfo>
    <title>Thermophilic treatment of high strength wastewater by modified Upflow Anaerobic Sludge Blanket reactor (U.A.S.B.)</title>
  </titleInfo>
  <name type="personal">
    <namePart>Chen, Ann-cheng</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Harada, Hideki</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Tran, Francis T.</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Verink, Johan</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>Chinese Taipei Government</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>
    <place>
      <placeTerm type="code" authority="marccountry">th</placeTerm>
    </place>
    <place>
      <placeTerm type="text">Bangkok</placeTerm>
    </place>
    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1991</dateIssued>
    <issuance>continuing</issuance>
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  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
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  <physicalDescription>
    <extent>70 p.</extent>
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  <abstract>This study was aimed to cultivate thermophilic organisms  which can perform optimally at 55°c, and to utilize their  increased reaction rate at increased temperature. A semi-pilot modified U.A.S.B. reactor were operated at  different organic loading of 2 to 24 Kg COD/m3.day corresponding  to H.R.T.:12o hr to 10 hr and using distillery wastewater as  feed substrate which was inherently at high temperature.  Investigations on gas production rate, biogas composition, COD  balance, sulfur balance, microbial and physico-chemical mechanism  of granular sludge formation were made. It was determined that organic loading up to 24 Kg  COD/m3.day could be handled with satisfactory efficiency. High  methane production rate was linearly increasing correspondingly  with increasing organic loading. Higher organic loading was  still imposed continuously, that is, maximum organic loading was  not obtained yet. It was found that limiting step of thermophilic U.A.S.B. reactor was propionate degradation. The interspecies hydrogen  transfer in the system was very important factor for process  performance. Based on COD balance, 68% of removal COD was  converted to methane gas. Also it was found that sulfate reducing  bacteria can not compete with methanogenic bacteria in the  system. Both Methanosarcina-like and Methanothrix-like  methanogens were coexisting in granular sludge.</abstract>
  <note>A thesis submitted in partial fulfillment of the requirements for  the degree of Master of Engineering</note>
  <note>Thesis (M.Eng.) - Asian Institute of Technology, 1991</note>
  <subject authority="lcsh">
    <topic>Sewage</topic>
    <topic>Purification</topic>
    <topic>Activated sludge process</topic>
  </subject>
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    <titleInfo>
      <title>Thesis ; no. EV-91-20</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=B17411</identifier>
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    <recordCreationDate encoding="marc">170399</recordCreationDate>
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