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  <titleInfo>
    <title>Application of ultra low pressure reverse osmosis (ULPRO) membrane for electroplating effluent treatment</title>
  </titleInfo>
  <name type="personal">
    <namePart>Wilasinee Saktaywin</namePart>
    <role>
      <roleTerm authority="marcrelator" type="text">creator</roleTerm>
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  </name>
  <name type="personal">
    <namePart>Ozaki, H.</namePart>
    <role>
      <roleTerm type="text">Chairperson</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Visvanathan, C.</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="personal">
    <namePart>Preeda Pakpian</namePart>
    <role>
      <roleTerm type="text">Examination Committee</roleTerm>
    </role>
  </name>
  <name type="corporate">
    <namePart>The Royal Netherlands Government</namePart>
    <role>
      <roleTerm type="text">Scholarship donor</roleTerm>
    </role>
  </name>
  <typeOfResource>text</typeOfResource>
  <genre authority="marc">series</genre>
  <genre authority="marc">technical report</genre>
  <originInfo>
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    </place>
    <place>
      <placeTerm type="text">Bangkok</placeTerm>
    </place>
    <publisher>Asian Institute of Technology</publisher>
    <dateIssued>1999</dateIssued>
    <issuance>continuing</issuance>
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  <language>
    <languageTerm authority="iso639-2b" type="code">eng</languageTerm>
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    <extent>100 leaves : ill.</extent>
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  <abstract>In an effort to determine the potential application of ultra low pressure reverse osmosis  (ULPRO) membrane in electroplating processes, experimental investigations were conducted  to evaluate the performance of ULPRO membrane for the removal of nickel, copper and  chromium. The influences of pressure, initial feed concentration, pH, competing compounds  and operation period on ULPRO membrane performance were also determined.  In this study, the experiment had been divided into two parts. The first part consisted of  the uses of synthetic wastewater containing heavy metal (Ni, Cu or Cr). The ULPRO  membrane model ES20 was used in the experiments. The experimental study ranges of  pressure, concentration, pH, competing compounds (Ca2 + and Mg2 +) were 0.1-0.5 MPa, 50  mg/L Ni, Cu and Cr and 5, 50 and 500 mg/L NaCl, pH 3-9, 5-30 mg/L Ca2 +, 3-15 mg/L Mg2 +  according! y.  Results showed that the removal efficiency for ULPRO membrane could be obtained  97 to 99.4% for Ni, 97.3 to 99.4% for Cu and 98 to 99.9% for Cr. Higher pressure, higher feed  concentration and higher pH showed positive response, while presence of competing  compounds showed negative response on Ni, Cu and Cr rejection.  In the second part of this study using real wastewater from the small electroplating  shop. The experimental study used ultra low pressure type composite reverse osmosis  membrane (ES20), RO membrane (NTR-759HR) and NF membrane (LFlO and NTR-729HF).  The study used of pressure and pH were 0.45 and 0.9 MPa, pH 3 and 7 for combined  wastewater and Cr rinse water.  Results showed that ES20 membrane gave the highest flux and rejection. All results  shown that the ES20 membrane requires about half of the operating pressure of NTR-759HR,  LFlO and NTR-729HF membrane to achieve the same level of metal ions removal.  Transmission electron micrographs of the membrane surface demonstrate that the structure of  the membrane skin layer is the reason for improved performance.</abstract>
  <note>A thesis submitted in partial fulfillment of the requirements for the degree of Master of Science, School of Environment, Resources and Development</note>
  <note>Thesis (M.Sc.) - Asian Institute of Technology, 1999</note>
  <subject authority="lcsh">
    <topic>Sewage</topic>
    <topic>Purification</topic>
    <topic>Reverse osmosis process</topic>
  </subject>
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    <titleInfo>
      <title>Thesis ; no. EV-99-25</title>
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      <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=B12091</identifier>
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    <recordCreationDate encoding="marc">041199</recordCreationDate>
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