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연료전지용 소형 금속 열교환기의 성능에 대한 실험 및 이론적 연구

Study on Experimental and Theroretical performances for a Compact Metallic Heat Exchanger for Fuel Cell Systems

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참고문헌

키워드

주제분류기타공학

초록

Thisstudyassessedtheperformanceofacompactheatexchangerwithstaggeredtubebanksforrecuperation ofhightemperatureexhaustthermalenergyforSOFCfuelcellsystem.Thecompactheatexchangerinthisstudy istwopasssystem whichconsistsof315×202.5×48.5㎣ and132tubesof6.0㎜Φ foreachheatexchanger.From experimentsofthe2passheatexchangersystem,airtemperaturewasincreasedfrom 60~85℃ to402~482℃ while gas temperature was decreased from 600℃ to 305~402℃ according to mass flow rates of3.9~7.8 g/s.The experimentalheattransferratesoftheheatexchangerwerecomparedwithCFD numericalsolutionswiththe conventionalξ-NTU method.From the comparisons,the following conclusions were obtained.Forthe heat exchangersystem,therelativeerrorsofheattransferratebyCFD solutionwerefrom 7.1to27%,andthoseby ξ-NTU methodwerefrom 0.6% to21% comparedwithexperimentaldata.From thecomparisons,itcanbesaid thatbothofCFD andξ-NTU methodalmostsimulatedtoexperimentaldataexceptspecificconditions.Pressure dropsthrough airtubesand gaspassageswerecalculated with both oftheCFD computation and head loss equations.Thedifferencesbetweenthem werefrom 14to22%.

Abstract

Thisstudyassessedtheperformanceofacompactheatexchangerwithstaggeredtubebanksforrecuperation ofhightemperatureexhaustthermalenergyforSOFCfuelcellsystem.Thecompactheatexchangerinthisstudy istwopasssystem whichconsistsof315×202.5×48.5㎣ and132tubesof6.0㎜Φ foreachheatexchanger.From experimentsofthe2passheatexchangersystem,airtemperaturewasincreasedfrom 60~85℃ to402~482℃ while gas temperature was decreased from 600℃ to 305~402℃ according to mass flow rates of3.9~7.8 g/s.The experimentalheattransferratesoftheheatexchangerwerecomparedwithCFD numericalsolutionswiththe conventionalξ-NTU method.From the comparisons,the following conclusions were obtained.Forthe heat exchangersystem,therelativeerrorsofheattransferratebyCFD solutionwerefrom 7.1to27%,andthoseby ξ-NTU methodwerefrom 0.6% to21% comparedwithexperimentaldata.From thecomparisons,itcanbesaid thatbothofCFD andξ-NTU methodalmostsimulatedtoexperimentaldataexceptspecificconditions.Pressure dropsthrough airtubesand gaspassageswerecalculated with both oftheCFD computation and head loss equations.Thedifferencesbetweenthem werefrom 14to22%.

참고문헌 (8)

  1. Chan,S.H, "ModellingforPartLoad Operation ofSolid OxideFuelCell-gas TurbineHybridPowerPlant", Journalof PowerSource, 114, pp.213~227 (2003)
  2. Wimkler,Loreaz, "TheDesignofStationary and Mobile Soild Oxide FuelCell-gas Turbine System", Journal of Power Source, 105, pp.222~227 (2002)
  3. Bourisa,D, "Design ofaNovel IntensifiedHeatExchangerforReduced Fouling Rates", Inter.J.HeatandMass Transfer, 48(18), pp.318~382 (2005)
  4. Tsuzuki,N, "Ishiduka,HighPerformance PrintedCircuitHeatExchanger", AppliedThermal Engineering, 27(10), pp.1702~1707 (2007)
  5. 곽재수, "고온용 핀-휜 열교환기 개발 Part1:설계 및 제 작", 대한기계학회 춘계학술대회 논문집, pp.2136~2141 (2005)
  6. 곽재수, "고온용 핀-휜 열교환기 개발 Part2:시험 및 분석", 대한기계학회 춘계학술대회 논문집, pp.2142~2147 (2005)
  7. YunasA, "Cengel,HeatTransferapractical approach" (2008), McGraw-Hill
  8. Kays,W.M, "Compact HeatExchanger" (1984), McGraw-Hill

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