1 Ocak 2007 Dergi makalesi Açık Erişim

Kaya, Durmus; Sarac, H. Ibrahim

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  <identifier identifierType="URL">https://aperta.ulakbim.gov.tr/record/97279</identifier>
  <creators>
    <creator>
      <creatorName>Kaya, Durmus</creatorName>
      <givenName>Durmus</givenName>
      <familyName>Kaya</familyName>
    </creator>
    <creator>
      <creatorName>Sarac, H. Ibrahim</creatorName>
      <givenName>H. Ibrahim</givenName>
      <familyName>Sarac</familyName>
    </creator>
  </creators>
  <titles>
    <title>Mathematical Modeling Of Multiple-Effect Evaporators And Energy Economy</title>
  </titles>
  <publisher>Aperta</publisher>
  <publicationYear>2007</publicationYear>
  <dates>
    <date dateType="Issued">2007-01-01</date>
  </dates>
  <resourceType resourceTypeGeneral="Text">Journal article</resourceType>
  <alternateIdentifiers>
    <alternateIdentifier alternateIdentifierType="url">https://aperta.ulakbim.gov.tr/record/97279</alternateIdentifier>
  </alternateIdentifiers>
  <relatedIdentifiers>
    <relatedIdentifier relatedIdentifierType="DOI" relationType="IsIdenticalTo">10.1016/j.energy.2006.09.002</relatedIdentifier>
  </relatedIdentifiers>
  <rightsList>
    <rights rightsURI="http://www.opendefinition.org/licenses/cc-by">Creative Commons Attribution</rights>
    <rights rightsURI="info:eu-repo/semantics/openAccess">Open Access</rights>
  </rightsList>
  <descriptions>
    <description descriptionType="Abstract">In this study, a mathematical model was developed for multiple-effect evaporators. These evaporators have cocurrent, countercurrent and parallel flow operation options. Each operation was investigated with and without pre-heaters. The effect of pre-heating on evaporation process was investigated from the point of energy economy. A sugar factory's data was used with the applied models as a case study. The results obtained for pre-heated and non-pre-heated situations were compared with each other. The maximum COP is found as 3.33 for countercurrent operation with pre-heating. The minimum COP is 2.57 for parallel flow operation without pre-heating. (c) 2006 Elsevier Ltd. All rights reserved.</description>
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