Formulario Seconda parte Advanced Heat and Mass Transfer

Metodo LMTD e heat rate transfer

UAATM RATETRANSFERHEATq = METODO LMTDItemUA FlowCOUNTERCf = piùstent:Ì conCÈR= HEAT fattoCAPACITYTao Ta ,D= - PERFORMANCEte ;UADTEMFTIPIR) Hitq > E-METODO NTU94mm{ EFFECTIVENESS= )(( Tai HTTri HA9mm - -minNTU NTV= (minCmim( RATIO⇐[ CmaxE- 1CrNTU CORRELAZIONEse -= 1- E E)( Creo correlazioneNTU 1-ln se= -

Pool bollinonatural connection

POOL BOLLINONATURAL CONNECTION"htfg ( )Nn Gzqg=D Prg14= correlazione,913ITL34}Gris =g TI, ONB%Ò 4 Approssimatafase singola Id 1mme- con ,n ?IÈ fgg Rstate vgcon = raggioe " NB"Pin" )ftp.csgfffgnjgfjj )↳ ronsenowftrstapprox97 0,013Csgmio water onlycon meo =,IÌNn 3Mt ROHSENON correlatori2> nestaff hggCpgJoe = )" "( %( :)%L' ho Fpe GORENFLO- »" 72,5 ITEFa -1,2ps pr pi.. 1- Perpr"0,9 -0,3Pamf : }6.tt?p-)piMf=d,9-q3piais("pi1,73Fere t Water the ( )9lb Ep20000Epo default-0,1 0,4 0,4pro > >- = È:{ """ "- -Mpinfeogpr ) «se55= ZEME 200-0,218g Ep-0,12m' ( )defaultlogep

DNB e film boiung

DNB CHFBURNOUT-""hggfgkfoglfg.gg ))9% 0,149 ZUBERe-. FILM BOIUNGh hctdfshr-_ lea.↳ -Ehi-anzsf%fE.sn?;; ! ; Y-.fYorlnsetubesand Berensonhorizontalflutsurf .L' ggeahggtoiocpghtsatµÌ¥¥%↳sàs) ""ha 0,62 Bromley= ' in9094,991%1%1%1 MFBn' ' zuser= () )" Arc( BERENSONTsatTNEB 9 hfb=- BerensonBerenson

Subcooledflow

SUBCOOLEDFLOW BollinomaiG dtsubi-tw-tgidtsafon.aegg TsatTonnong= = -) t49(Tg TgZ tetep.aze- i, GD Cpg4¥ Cpg Dtsubi SUBCOSLEDZs %Twlz hgoheat.tramsf.ae)) Tglz t pp-- .single PhaseIL [ % )Cps -zon and=, )Tfttonb( )Dtsub Tsatzona e- - paorsu,o)