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  <titleInfo>
    <title>Carbon oxidation-nitrification in attached growth activated sludge process</title>
  </titleInfo>
  <name type="personal">
    <namePart>Baskaran, Kanagaratnam</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Chongrak Polprasert</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>I, Fude</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>The Roya l Netherland Government</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>1988</dateIssued>
    <issuance>monographic</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
    <extent>100 p.</extent>
  </physicalDescription>
  <abstract>Laboratory experiments were carried out on Attached Growth Activated Sludge Process (AGASP) with volume of attached-growth media  in the aeration tank varied at 5%, 10%, and 15% of the aeration tank  volume. Different organic loadings (F /M ratio) and different solid  retention time(9 ) of the reactors were operated to investigate the  c  process kinetics and process efficiency. The experiments were carried  out in three phases. In the first phase, the 9 were varied from 5 days c  to 20 days at a constant organic loading of 0. 3 kg COD/ (kg MLSS. d).  In the second phase the optimum 9 was fixed while the organic loadings c  were varied from 0. 3 to 1. 0 kg COD/ (kg MLSS. d). Synthetic waste  (sodium acetate and ammonium sulfate as main ingredients for carbon  and nitrogen sources) was utilized as feed. The hydraulic retention  time(9) and influent NH3 -N concentration were maintained at 8 hours  and 65 mg/L, respectively, throughout the first two phases of experiments. In the third phase the 9 and the Organic Loading were fixed  c  at 10 days and 0.3 kg COD/(kg MLSS.d), respectively while the in fluent NH3 -N concentration was increased to 100 mg/L .  Experimental results from the first phase revealed that the 9  c  of 10 days in all AGASP reactors provided the optimum process efficiency with respect to Carbonaceous and nitrogenous compound removal.  At this 9c the carbon (COD) removal was 97% and NH3 -N concentration  in the effluent was not detectable. In the second phase, complete  NH3 -N removal was observed in the AGASP reactors with 5% and 10%  media at organic loadings between 0.3 - 1.0 kg COD/(kg MLSS . d). The COD  removal in all four reactors we re between 94% - 98%. In third phase,  when the AGASP reactors were fed with a high strength nitrogenous waste  (NH3 -N = 100 mg/L). The AGASP reactor with 15% media gave t he optimum  NH3 -N removal efficiency of 95%.  The experimental results obtained suggested that the installation  of 10% media in the aeration tank of an activated sludge reactor will  provide a high degree of COD and NH3 -N removal. AGASP with 10% media  was found to produce an effluent which should  effluent standards when operated at organic  1 . 0 kg COD/(kg MLSS.d) .  satisfy most stringent  loadings be tween 0.3 - A mathematical model established based on a comination of MONOD expression and diffusion equation could predict the effluent  quality of t h e AGASP .</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, 1988</note>
  <subject authority="lcsh">
    <topic>Sewage</topic>
    <topic>Purification</topic>
    <topic>Activated sludge process</topic>
  </subject>
  <relatedItem type="series">
    <titleInfo>
      <title>Thesis ; no. EV-88-10</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=B18880</identifier>
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    <url displayLabel="Full-Text">http://203.159.5.9/ait-thesis/detail.php?q=B18880</url>
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  <recordInfo>
    <recordCreationDate encoding="marc">120399</recordCreationDate>
    <recordChangeDate encoding="iso8601">20260817172215.0</recordChangeDate>
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