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  <titleInfo>
    <title>Tapioca starch wastewater treatment by aerobic fluidized bed process</title>
  </titleInfo>
  <name type="personal">
    <namePart>Nguyen Trong Quang</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Samorn Muttamara</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Chongrak Polprasert</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Shin, Hang-Sik</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>
  <originInfo>
    <place>
      <placeTerm type="code" authority="marccountry">th</placeTerm>
    </place>
    <place>
      <placeTerm type="text">Bangkok</placeTerm>
    </place>
    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1986</dateIssued>
    <issuance>continuing</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
    <extent>74 p.</extent>
  </physicalDescription>
  <abstract>An aerobic tapered fluidized bed reactor was operated to  study its performance at variable organic loading rates.It was to  be measured in terms of organic removal efficiency and dissolved  oxygen concentrations maintained in the reactor. The uniqueness  of this process is the combined activity of suspended and attached growth microorganlsms ln or anic removal. Attached  lcroorganisms were pre omlnan ln the fluidized sand media while suspended microorganisms were dominant in the volume above the expanded bed in the reactor. The investigation shows the moderate organic carbon removal  efficiency (55-65 %) at medium dissolved pure oxygen of 16.9-18.6 mg/l and low detention time of 6 hours. It is deduced from  the study, that the removal efficiency is dependent upon the  initial waste strength, the influent dissolved oxygen and the reator sizes.  </abstract>
  <note>A research study submitted in partial fulfillment of the requirements for the degree of Master of Science, School of Environment, Resources and Development</note>
  <note>Thesis (M.Sc.) - Asian Institute of Technology, 1986</note>
  <subject authority="lcsh">
    <topic>Sewage</topic>
    <topic>Purification</topic>
    <topic>Biological treatment</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Factory and trade waste</topic>
  </subject>
  <relatedItem type="series">
    <titleInfo>
      <title>Thesis ; no. EV-86-4</title>
    </titleInfo>
    <name type="corporate">
      <namePart>Asian Institute of Technology.</namePart>
      <namePart/>
    </name>
  </relatedItem>
  <identifier type="uri">http://203.159.5.9/ait-thesis/detail.php?q=B19626</identifier>
  <location>
    <url displayLabel="Full-Text">http://203.159.5.9/ait-thesis/detail.php?q=B19626</url>
  </location>
  <recordInfo>
    <recordCreationDate encoding="marc">011298</recordCreationDate>
    <recordChangeDate encoding="iso8601">20260818223900.0</recordChangeDate>
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