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  <titleInfo>
    <title>Performance of tube-settlers in clarification of turbid tropical surface waters</title>
  </titleInfo>
  <name type="personal">
    <namePart>Amin, Mian Muhammad</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart> Pescod, M.B.</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Nguyen Cong Thanh</namePart>
    <role>
      <roleTerm type="text">Co-Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>British 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>1974</dateIssued>
    <issuance>monographic</issuance>
  </originInfo>
  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
  </language>
  <physicalDescription>
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    <extent>166 p.</extent>
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  <abstract>The research was conducted at. Pilot-.Plant scale to investigate  the performance of tube-settlers and develop design criteria for  treatment of tropical turbid waters. The evaluation of horizontal tube-settler was carried out using the "Neptune Microfloc" 10 gpm Pilot-Plant (5 degree inclination). ,-The tubes were of 1-in depth and  2 ft in length Inclined tube settler, with tubes 2 x 2 in. cross- v section, 3 ft in length and 60 degrees angle of inclination, was  specially designed for this study It was found that horizontal tube-settlers were efficient devices in turbidity removal but sludge storage capacity was a limitation on the system. At flow rates of 2.45 m3 /m2-hr (1.0 gpm/ft2 ) and above and with raw turbidities 50-80 Jackson units tubes were filled in about one hour. Flow-rates of 0.98 m3 /m2-hr (0.4 gpm/ft2 ) and 1.96 m3 /m2-hr (0.8 gpm/ft2 ) "with average raw turbidities of 60 JTU, gave run lengths of 24 and 8 hours respectively for 70-percent removal efficiency~ The  corresponding detention times were 37.5 and 18.9 minutes. Thus, under these conditions the advantages of short detention times were lost due to limitation of sludge storage capacity. Dual-media (Anthracite-Sand) filter did not perform satisfactorily when influent turbidities were 10  JTU and above.  The inclined tube settlers performed very well at flow rates- as high as 10_._Q_m3 /m2-hr (4.0 gpm/ft2 ) and detention time 5.5 minutes,  giving about 80 percent' turbidity removal operating at influent turbidities of 95 Jackson units. Thus, the high-rate capabilities of the tube-settling system were clearly demonstrated. ' The use of tube settlers in treatment plants affords substantial savings in space requirements and capital costs.</abstract>
  <note>A thesis submitted-in partial fulfillment of the requirements for the degree of Master of Engineering in the Asian Institute of Technology, Bangkok, Thailand.</note>
  <note>Thesis (M.Eng.) - Asian Institute of Technology, 1974</note>
  <subject authority="lcsh">
    <topic>Water reclamation</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Turbidity</topic>
  </subject>
  <subject authority="lcsh">
    <topic>Tubes</topic>
  </subject>
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    <titleInfo>
      <title>Thesis ; no. 636</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=B24190</identifier>
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    <url displayLabel="Full-Text">http://203.159.5.9/ait-thesis/detail.php?q=B24190</url>
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    <recordCreationDate encoding="marc">231297</recordCreationDate>
    <recordChangeDate encoding="iso8601">20260818171632.0</recordChangeDate>
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