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  <titleInfo>
    <title>Application of direct membrane separation to activated sludge process</title>
  </titleInfo>
  <name type="personal">
    <namePart>Mahmood, Talat</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>Orth, Hermann M.</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
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  <name type="personal">
    <namePart>Vigneswaran, Saravanamuthu</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>The Royal Norwegian Government  (Norade Scholarship)</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>
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  <physicalDescription>
    <extent>111 p.</extent>
  </physicalDescription>
  <abstract>Feasibility of . hollow fiber microfiltration for solid  liquid separation from the aeration tank of an activated  sludge process was investigated. The study was divided into  short term experiments and a long term experiment. From the  short term experiments results. cyclic operation was found  effective against inter' module clogginq and hence resulting  in stable membrane flux.  Out of three different organic loadings given in the  long term experiment. 3 kg/Cm3. d) was found to be the  critical one. concerning solid liquid separation. 2  kg/( m3. d) was the most suitable loading. Membrane permeate  was free of turbidity, free of bacteria, completely  nitrified, partially denitrified and very low in effluent  COD concentration. The process operated at very high MLSS  concentration without sludge wastage. Low values of kinetic  coefficients (kd and Y) and F/M ratio were obtained showing  little sludge production at steady state.  0. 45 æm membranes operated at '1ower suction pressures  than 0.1 æm membranes. The · highest pressure requirement  during, around 4 months of operational period was within 0. 5  m head of water employing O'. 45 æm membranes. This idea  motivated the use of elevation difference as a · driving force  for membrane separation, precluding the pump suction.  The proposed system showed better quality of effluent  with much lower HRT. and high enough organic 1oading, when  compared with the extended aeration process, in context of  sludge production.</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-88-25</title>
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    <name type="corporate">
      <namePart>Asian Institute of Technology.</namePart>
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    </name>
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  <identifier type="uri">http://203.159.5.9/ait-thesis/detail.php?q=B18895</identifier>
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