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  <titleInfo>
    <title>Upflow anaerobic sludge blanket reactor with inclined tube settlers</title>
  </titleInfo>
  <name type="personal">
    <namePart>Lee, Keng-pang</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Shin, Hang-Sik</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Hanaki, K.</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Vigneswaran, Saravanamuthu</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>Chinese Petroleum Corporation,  Republic of China</namePart>
    <role>
      <roleTerm type="text">Scholarship Donor</roleTerm>
    </role>
  </name>
  <typeOfResource>text</typeOfResource>
  <originInfo>
    <place>
      <placeTerm type="code" authority="marccountry">th</placeTerm>
    </place>
    <place>
      <placeTerm type="text">Bangkok</placeTerm>
    </place>
    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1987</dateIssued>
    <issuance>monographic</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
    <extent>89 p.</extent>
  </physicalDescription>
  <abstract>This study was aimed to compare the operation of UASB  (Upflow An aerobic Sludge BlanKet) reactor having incline d tube  settlers (ITS) with that of conventiona1- OSAB reactor.  UASB reactors without and with ITS were operated at  different HRT of 4 h to 48 h. using brewery· wastewater a s feed  substrate . Investigation on gas production rate , methane  content, COD and solids removal efficiencies were made.  Over a wide range of COD loading rates tried in this study,  it was determined that organic loadings up to 10 kg COD/ m3-d  could be handled with high efficiency . COD removal was more than  95 percent, and methane production was more than 150 l /Kg COD  added when t he hydraulic retention time was 12 h. Shorter  detention time, that is, higher organic loading rate hampered the  performance o f the reactors , in terms of COD removal and a mount  of gas produced per kg of COD added.  It was found that inclined tub setter provided better gas  production and solids removal efficiency and more methane  content. Especially, higher solids removal was observed during  low hydraulic retention period.</abstract>
  <note> A thesis submitted in partial fulfilment 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,1987</note>
  <subject authority="lcsh">
    <topic>Sewage</topic>
    <topic>Purification</topic>
    <topic>Biological treatment</topic>
  </subject>
  <relatedItem type="series">
    <titleInfo>
      <title>Thesis ; no. EV-87-22</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=B19245</identifier>
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    <url displayLabel="Full-Text">http://203.159.5.9/ait-thesis/detail.php?q=B19245</url>
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    <recordCreationDate encoding="marc">011298</recordCreationDate>
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