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  <titleInfo>
    <title>Effect of operating parameters on anaerobic (upflow) filter performance</title>
  </titleInfo>
  <name type="personal">
    <namePart>Koirala, Ramesh</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Vigneswaran, Saravanamuthu</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Hanaki, K.</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Samorn Muttamara</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>Royal Government of the Netherlands</namePart>
    <role>
      <roleTerm type="text">Scholarship Donor</roleTerm>
    </role>
  </name>
  <typeOfResource>text</typeOfResource>
  <originInfo>
    <place>
      <placeTerm type="code" authority="marccountry">u</placeTerm>
    </place>
    <place>
      <placeTerm type="text">Bangkok</placeTerm>
    </place>
    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1987</dateIssued>
    <issuance>monographic</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
    <extent>78 p.</extent>
  </physicalDescription>
  <abstract>A laboratory- scale AF was studied to find the effect of  various design parameters i.e. hydraulic loadings &amp; hydraulic  retention times , influent concentrations and filter depths on the  performance of AF. The AF was fed with commercial grade glucose  synthetic waste. The effects of the se de sign parameters were  measured in terms of COO removal efficiency and gas production . The ratio of methane to carbon dioxide in the gas produced was  also found out by using Gas Chromatograph (Sichromat 2 , made in  Germany),  The COO removal efficiency decrease d with the increase in  hydraulic loading. The gas produced per kg of COO removed also  decreased with the increase in hydraulic loading.  The inverse relationship proposed by YOUNG and  McCARTYC1 968) did not exist in higher values of HRTs C144-24h) . But , it held good after a HRT value of 24h up to 6h. Hence , a  relations hip , based on the regression analysis of experimental  values , was proposed between the COO removal efficiency an d the  HRT for HRT range of 24-6h. The gas production was also affected  by the variation of HRT values .  The change in influent concentration at a constant  hydraulic loading did not have significant effect on the COO  removal efficiency and gas production capacity of the AF. It did  not show any significant effect on the methane content or gas  al so.  A filter depth of 120 cm was found to be sufficient enough  to provide COO removal efficiency of 97 . 2- 72.2% at hydraulic  loading range of 0.11 -2.7 m3 /(n12 .d) and an average influent  concentration of 3000 mg/L of synthetic waste (glucose being the  ma in substrate) {u2022}</abstract>
  <note>A thesis submitted in partial fulfillment of the requirements for  the degree of Master of Engineering, School of Environment, Resources and Technology</note>
  <note>Thesis (M.Eng.) - Asian Institute of Technology, 1987</note>
  <subject authority="lcsh">
    <topic>Sewage</topic>
    <topic>Purification</topic>
    <topic>Filtration</topic>
  </subject>
  <relatedItem type="series">
    <titleInfo>
      <title>Thesis ; no. EV-87-13</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=B19229</identifier>
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    <url displayLabel="Full-Text">http://203.159.5.9/ait-thesis/detail.php?q=B19229</url>
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    <recordCreationDate encoding="marc">011298</recordCreationDate>
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