10701112859194442 THT ,¥¥HW5 I , Ps = f- ( FFL - A . = f- ( Eph ( CET ( Eth - Cp , - Tl p ) ves=¥¥¥ vet=¥¥; . ÷i¥¥¥iE÷ ( = T ( - Ethnicity . I = 2 (Ttip rx Cp # . V VIT - - . # P) ( Ff ) DP dV=¥HpdTt , ( Ff ) H " Va up - t v ( Yp ) = , - = - , (IIT ) Yap - - p * EIGIL 1¥71 - - . , Eft xtvldfph = ( Eff Ptv LIFT ) - . , , H 3 H Vp - VL , (a) 5=5 ds =L Tds LT P) . Tdp # Ipd Tt ( = { ¥4 Sgp = - I = - p - reversible process Cpd T = DT = Kdp at # constant P (ft )p=¥ Va lb ) ds OS ' DT = = Cpln IT , i reversible 05=0 = 18 - = & - Vxdp Val Pa - Pi ) adiabatic cpln - VL ( Pz - Pi ) (1-100)×105 "ymy .no/ex#g%aeyxl n TI t k-18m3m/oTexl 0 -bmI m I x 2xi o -%eegx dg 18 * In Tf = 295.54k = # 18×10-42×10 " x ( - 991×105 V (IIT ) , 4- tap ) EH 5- Elp Yehia: t - i = # " ¥4 ' . # ' Tds EY ) p Epp c It's valid for . LEAP 5 = Cpd T for Vd = P constant If = law gas any other or under the condition of only ' Sgp ideal apply : I don't ' = restrictions P constant substance . and do the S and reversible . , # la ) i l ll free expansion i ' { A V = ' . . TS - o G = H - A = = OH = A = OG = OU = OH = OG o o = OH G = = - 0 o # Tos = - S Rtn = O - # OS = 2 Rlm 2 t Rlnz = Rtn 8 # RT In 8 # (3) o A O = = OS # O = O # # (4) OU OA = = OH OG = = O - # 05=2 Rlm RT In # 2 t 3 2 t R Thr 4 # TS (2) OU U o Rlm 5- = Rlm Rlm 2 = Rtn 4 # proof (b) free expansion n' ' OS Rlm - (c) - Tos oU=q/°W Cv ( Tz = C - , Rbnz # = oA=oG= 00=01-1--0 # ' c = RTln2 # adiabatic ) ' ' - . 05=0 OA Ti ) # - - = OH Cp ( Tz = - Ti ) # OG = = (d) OU OH G W - Cpt - i' A. G ' , paths " - × desire ) OU ou OH - - cut opt Ti ) . . - Til , 6 Ti ) # OH SOT OH - S ( Ta T1 ) - # oS=fEfIdT=¥dT=Cpln¥ into # state the 2 Ti , → Ta isothermal : " off OU = - - OH III ! ! !!:L:'m 't ' n # ( Tz - - Ita OA OG # oS=fs8÷dT=fI¥dT =aln¥ - entropy ) dH=S8p=CpdT # adiabatic i path - S ( Tz - constant , ( e) - 50T ( - - OG - ' . path l y Ti functions of are we - Ti ) # divide the process ' c ( Tz Cv = - - OU l : adiabatic ) # - - = Ti ) Si - - Tiki ou OH - - Taos # - Taos - it - . ( Tz - Tiki Ti ) Si # - - . Ta # , ills DS -_ SIT V) , = Tds ( f. = - f- ( ¥4 ( ¥ )vdTt ( Itv) , DV - =Sqr=CvdT { ⇐h=l u= - a, Tds = f- ( IF )p Credit reversible process Fie , ) at constant DV V # (ft ) If Taos Taos # # (2) LT 5=5 . P) dS=l¥tpdT -11¥ dp - , Tds Sgp = { ¥4 Tds - - - - ( = (3) 5- SIP V . - p Cpd T - - reversible process Cpd T at P constant (ft )p=¥ Va TVLDP # ) (F) udptlftulpdv Eph I # HIFI Exeat dS= Tds cuffed Pt = DV # - { (Fulp 7 - -_ - pl Ef )p=¥x¥ ( Tds . Tds = DV Cud Tt ↳g=cuezdPtvdV Tds - - = Cpd T We Tva dp - want to know the T A Bi → B→ C ' a constant T constant P , , Vt St TT ST is: : : ::::i: : : 8 ( Tc it . TB ) > .. . . Ps = - Il # Is . A = - f- ( Ft , ves=¥¥¥ verify . ¥¥¥¥iE¥÷ = = h÷= ( Flux (Ttip E Cp - r# - Tl # he # CITY . I relationship of Ty T S - " # - s # Ehs IET ' = LET) d tf v - I - ¥1 I - Ehs = JOIN THE DARKSIDE