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  • Plate type heat exchangers are widely used in process industries for gas/gas applications. Typically, these exchangers proved to be very efficient especially as air preheaters in process furnaces or as equipment of units for environmental protection (e.g. in units for thermal disposal of wastes). From economic reasons of these industries there is a need for a new optimization approach for plate type heat exchanger design and operation. The objective function is of achieving minimum total annual cost of heat exchangers. Pressure drop and heat transfer are interdependent and both of them strongly influence capital and operating costs of any heat transfer system. During the designing a heat exchanger it is necessary to determine optimum dimensions of apparatus which is connected with given conditions of the equipment operation. The goal is to obtain the most economically optimum design. An economic assessment allows a comparable estimation of various alternatives. The total annual cost consisting of fi
  • Plate type heat exchangers are widely used in process industries for gas/gas applications. Typically, these exchangers proved to be very efficient especially as air preheaters in process furnaces or as equipment of units for environmental protection (e.g. in units for thermal disposal of wastes). From economic reasons of these industries there is a need for a new optimization approach for plate type heat exchanger design and operation. The objective function is of achieving minimum total annual cost of heat exchangers. Pressure drop and heat transfer are interdependent and both of them strongly influence capital and operating costs of any heat transfer system. During the designing a heat exchanger it is necessary to determine optimum dimensions of apparatus which is connected with given conditions of the equipment operation. The goal is to obtain the most economically optimum design. An economic assessment allows a comparable estimation of various alternatives. The total annual cost consisting of fi (en)
Title
  • Alternative Approach in Optimization of Plate Type Heat Exchangers
  • Alternative Approach in Optimization of Plate Type Heat Exchangers (en)
skos:prefLabel
  • Alternative Approach in Optimization of Plate Type Heat Exchangers
  • Alternative Approach in Optimization of Plate Type Heat Exchangers (en)
skos:notation
  • RIV/00216305:26210/04:PU48212!RIV11-MSM-26210___
http://linked.open...avai/riv/aktivita
http://linked.open...avai/riv/aktivity
  • P(GA101/01/0191), P(OC E26.001), P(OK 264), V, Z(MSM 262100004)
http://linked.open...iv/cisloPeriodika
  • 5
http://linked.open...vai/riv/dodaniDat
http://linked.open...aciTvurceVysledku
http://linked.open.../riv/druhVysledku
http://linked.open...iv/duvernostUdaju
http://linked.open...titaPredkladatele
http://linked.open...dnocenehoVysledku
  • 553939
http://linked.open...ai/riv/idVysledku
  • RIV/00216305:26210/04:PU48212
http://linked.open...riv/jazykVysledku
http://linked.open.../riv/klicovaSlova
  • Plate heat exchanger, optimization (en)
http://linked.open.../riv/klicoveSlovo
http://linked.open...odStatuVydavatele
  • US - Spojené státy americké
http://linked.open...ontrolniKodProRIV
  • [5B16F68F02BF]
http://linked.open...i/riv/nazevZdroje
  • Heat Transfer Engineering
http://linked.open...in/vavai/riv/obor
http://linked.open...ichTvurcuVysledku
http://linked.open...cetTvurcuVysledku
http://linked.open...vavai/riv/projekt
http://linked.open...UplatneniVysledku
http://linked.open...v/svazekPeriodika
  • 25
http://linked.open...iv/tvurceVysledku
  • Jegla, Zdeněk
  • Stehlík, Petr
  • Kohoutek, Josef
http://linked.open...n/vavai/riv/zamer
issn
  • 0145-7632
number of pages
http://localhost/t...ganizacniJednotka
  • 26210
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