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    Shell-and-Plate-Type Heat Exchangers for OTEC Plants

    Source: Journal of Solar Energy Engineering:;1984:;volume( 106 ):;issue: 003::page 286
    Author:
    H. Uehara
    ,
    H. Sumitomo
    ,
    H. Kusuda
    ,
    M. Monde
    ,
    T. Nakaoka
    DOI: 10.1115/1.3267597
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: New titanium, shell-and-plate type heat exchangers for ocean-thermal-energy-conversion (OTEC) plants have been developed which include three different plate types (fluted, impinging, and porous-surface) for the evaporator and two kinds of plates (No. 1 and No. 2) for the condenser. Performance tests with fresh water show that the overall heat transfer coefficient U of the evaporator using the porous plate is the highest among the three plates; it can reach 4000–4500 W/m2 K using ammonia as the working fluid and 3500–4000 W/m2 K for a Freon, R-22. The U of the condenser using the No. 2 plate is higher than that using the No. 1 plate; it can reach 3800–4500 W/m2 K for ammonia and 2000–3500 W/m2 K for R-22.
    keyword(s): Industrial plants , Shells , Heat exchangers , Ocean thermal energy conversion , Plates (structures) , Condensers (steam plant) , Heat transfer coefficients , Testing performance , Titanium , Water AND Fluids ,
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      Shell-and-Plate-Type Heat Exchangers for OTEC Plants

    URI
    http://yetl.yabesh.ir/yetl1/handle/yetl/98962
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    • Journal of Solar Energy Engineering

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    contributor authorH. Uehara
    contributor authorH. Sumitomo
    contributor authorH. Kusuda
    contributor authorM. Monde
    contributor authorT. Nakaoka
    date accessioned2017-05-08T23:18:45Z
    date available2017-05-08T23:18:45Z
    date copyrightAugust, 1984
    date issued1984
    identifier issn0199-6231
    identifier otherJSEEDO-28169#286_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/98962
    description abstractNew titanium, shell-and-plate type heat exchangers for ocean-thermal-energy-conversion (OTEC) plants have been developed which include three different plate types (fluted, impinging, and porous-surface) for the evaporator and two kinds of plates (No. 1 and No. 2) for the condenser. Performance tests with fresh water show that the overall heat transfer coefficient U of the evaporator using the porous plate is the highest among the three plates; it can reach 4000–4500 W/m2 K using ammonia as the working fluid and 3500–4000 W/m2 K for a Freon, R-22. The U of the condenser using the No. 2 plate is higher than that using the No. 1 plate; it can reach 3800–4500 W/m2 K for ammonia and 2000–3500 W/m2 K for R-22.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleShell-and-Plate-Type Heat Exchangers for OTEC Plants
    typeJournal Paper
    journal volume106
    journal issue3
    journal titleJournal of Solar Energy Engineering
    identifier doi10.1115/1.3267597
    journal fristpage286
    journal lastpage290
    identifier eissn1528-8986
    keywordsIndustrial plants
    keywordsShells
    keywordsHeat exchangers
    keywordsOcean thermal energy conversion
    keywordsPlates (structures)
    keywordsCondensers (steam plant)
    keywordsHeat transfer coefficients
    keywordsTesting performance
    keywordsTitanium
    keywordsWater AND Fluids
    treeJournal of Solar Energy Engineering:;1984:;volume( 106 ):;issue: 003
    contenttypeFulltext
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