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  <titleInfo>
    <title>Application of membrane separation to chlorinated phenols treatment</title>
  </titleInfo>
  <name type="personal">
    <namePart>Chan, Tik-yuen</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Yamamoto, K.</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Ahn, Kyu-Hong</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Tran, Francis T.</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>The Government of Japan</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>1989</dateIssued>
    <issuance>monographic</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
    <extent>85 p.</extent>
  </physicalDescription>
  <abstract>Ethylene hollow fiber membranes of 0.2 æm pore size were used as direct  solid/liquid separation device in laboratory-scale aeration tanks for the  treatment of phenol, 2-chlorophenol, 2,4,6-trichlorophenol and pentachlorophenol.  Phenol-adapted sludge was used. The biodegradability of the chlorinated phenols  was dependent on the acclimation period and the chemical properties of the  compounds. 2-chlorophenol and 2,4,6-trichlorophenol were readily degraded after  13 days acclimation, while pentachlorophenol required an acclimation period of  20 days. The removal efficiency of the chlorophenols increased with a longer  adaptation period and higher volumetric organic loading.  Removal rate of phenol and 2-chlorophenol was much faster than  2,4,6- trichlorophenol and pentachlorophenol. Utilization rates of phenol and  2-chlorophenol (kg phenols/(kg MLSS.d)) were over 0.04 and 0.004 d -t respectively,  while that of 2,4,6-trichlorophenol and pentachlorophenol wer e around the range  of 2.2 x 10 -J d - 1 {u2022}  The direct membrane separation activated sludge system was shown to be  very stable against shock loadings due to a high MLSS concentration achieved by  membrane separation. Good effluent quality was attained as well, owing to the  membranes' ability to retain macromolecules from cell lysis.</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, 1989</note>
  <subject authority="lcsh">
    <topic>Sewage</topic>
    <topic>Purification</topic>
    <topic>Phenol removal</topic>
  </subject>
  <relatedItem type="series">
    <titleInfo>
      <title>Thesis ; no. EV-89-6</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=B17981</identifier>
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    <url displayLabel="Full-Text">http://203.159.5.9/ait-thesis/detail.php?q=B17981</url>
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    <recordCreationDate encoding="marc">120399</recordCreationDate>
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