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  <titleInfo>
    <title>Denitrification of toxic nitrogenous wastewater</title>
  </titleInfo>
  <name type="personal">
    <namePart>Krongtong Sripruitkait</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Annachhatre, Ajit P.</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Takizawa, Satoshi</namePart>
    <role>
      <roleTerm type="text">Examination committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Eckhardt, Ing Heinz</namePart>
    <role>
      <roleTerm type="text">Examination committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>Asian Institute of Technology Partial Scholarship</namePart>
    <role>
      <roleTerm type="text">Scholarship donor</roleTerm>
    </role>
  </name>
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  <originInfo>
    <place>
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    <place>
      <placeTerm type="text">Bangkok</placeTerm>
    </place>
    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1998</dateIssued>
    <issuance>monographic</issuance>
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  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
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  <physicalDescription>
    <extent>123 leaves</extent>
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  <abstract>Denitrification with using aniline as a carbon source was investigated in the upflow  denitrification reactor. Synthetic wastewater comprising of N03-N, aniline and nutrients was  used as feed. Investigations were carried out to ascertain the effect of upflow velocity, N03-N  load and N03-N concentration on denitrification rate with aniline as a carbon source. A 2.8 L  upflow denitrification reactor was operated at ambient temperature of about 28-32°C and  maintained ML VSS of about 10,000-11,000 mg/L.  The results obtained indicated that aniline could be successfully used as a carbon  source by denitrifiers. Aniline required for denitrification was estimated as 1.1  g aniline/g N03-N. The denitrification rates achieved were about 70 to 90 mg N03-N/L·d based  on volumetric load and were about 9 to 12 mg N03-N/g MLVSS·d based on sludge load. The  experiments also showed that denitrification rate is affected due to upflow velocity, influent  N03-N load and N03-N concentration.  At constant influent N03-N concentration of about 90-95 mg/L, upflow velocity  between 3 to 4 cm/hr was found to be optimum for achieving denitrification rate of about 90  mg N03-N/L·d based on volumetric load and about 12 mg N03-N/g MLVSS·d based on sludge  load. Increase in upflow velocity to 5 cm/hr resulted in reduced denitrification rate.  Maximum denitrification rate of about 90 mg N03-N/L'd based on volumetric load and  about 12 mg N03-N/g MLVSS·d based on sludge load was achieved for upflow velocity of 3  cm/hr at the N03-N loading of about 95 mg N03-N/L·d based on volumetric load and about 13  mg N03-N/g ML VSS·d based on sludge load.  At constant upflow velocity of 4 cm/hr, the maximum denitrification rate of about 85  mg N03-N/L·d based on volumetric load and about 12 mg N03-N/g MLVSS·d based on sludge  load were achieved at influent N03-N concentration between 70 to 90 mg/L. </abstract>
  <note>A thesis submitted in partial fulfillment of the requirement 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>Nitrogen removal</topic>
  </subject>
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    <titleInfo>
      <title>Thesis ; no. EV-98-19</title>
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      <namePart>Asian Institute of Technology.</namePart>
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  <identifier type="uri">http://203.159.5.9/ait-thesis/detail.php?q=B12739</identifier>
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    <recordCreationDate encoding="marc">011298</recordCreationDate>
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