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  <titleInfo>
    <nonSort>A </nonSort>
    <title>study of phenol and 2,4-dichlorophenol treatment by BAC-SBR system</title>
  </titleInfo>
  <name type="personal">
    <namePart>Liu, Qishan</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Ha, Sung-Ryong</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Eckhardt, Ing. Heinz</namePart>
    <role>
      <roleTerm type="text">Examination committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Takizawa, Satoshi</namePart>
    <role>
      <roleTerm type="text">Examination committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>Asian Institute of Technology</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>1998</dateIssued>
    <issuance>monographic</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
    <extent>54, A15, B6, C7, D1 leaves</extent>
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  <abstract>Treatibility of phenol and 2,4-DCP by BAC-SBR and SBR system were studied in six  reactors using synthetic wastewater. Phenol and 2,4-DCP were fed to the reactors as only  carbon sources and the influent concentration was varied according to the experimental  objectives. Totally 5 runs (3 phases) of experiments were conducted. Different reaction time  and sludge retention time was used in different Run.  When the influent concentration of 116 mg/L of phenol and 100 mg/L of2,4-DCP was  used, both BAC-SBR and SBR systems reach 90% .of COD and 99% of total phenol removal  except for SBRI with SRT of 3 days. BAC-SBR system shows lower effluent COD and  phenol at beginning of the operation than SBR system and stable effluent throughout the  operation. When the influent concentration of 2,4-DCP was increased to 200 mg/L, its toxic  effect to reactor performance was checked. The BAC-SBR system shows high tolerance  ability than SBR system.  In the last Run, the influent concentration of 162 mg/L of phenol and 140 mg/L of 2,4- DCP was used. The effluent COD and phenol from BAC-SBR system is lower than from SBR  system with same SRT. Short sludge retention time gives high effluent. Based on the data  obtained, a mathematical model was used to simulate the reactor performance. Some empirical  constants such as a, p, y were calculated as 1.031 , 2.225 and 1.1764 respectively. The model  can be used to predict the performance of the BAC-SBR system. </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, 1998</note>
  <subject authority="lcsh">
    <topic>Sewage</topic>
    <topic>Purification</topic>
    <topic>Phenol removal</topic>
  </subject>
  <relatedItem type="series">
    <titleInfo>
      <title>Thesis ; no. EV-98-7</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=B12735</identifier>
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    <url displayLabel="Full-Text">http://203.159.5.9/ait-thesis/detail.php?q=B12735</url>
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    <recordCreationDate encoding="marc">301198</recordCreationDate>
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