Question #213790

Two vessels, A and B each of volume 4m3 are connected by a tube of negligible volume. Vessel

A contains air at 0.8MPa, 1050C, while vessel B contains air at 0.45MPa, 2250C. When A is allowed

to mix with B and assuming the mixing to be complete and adiabatic, determine (a) the final

pressure and temperature of air after mixing, (b) the amount of entropy generation and (c) the

irreversibilities in the process. Take, T0=300C



Expert's answer

(a) The final pressure and temperature of air after mixing

M=PVRTM = \frac{PV}{RT}

MA=80040.287375=29.73kgM_A = \frac{800*4}{0.287*375}=29.73 kg

MB=45040.287498=12.59kgM_B = \frac{450*4}{0.287*498}=12.59 kg

(MAcvTA+MBcvTB)=(MAcv+MBcv)TF(M_Ac_vT_A+M_Bc_vT_B)= (M_Ac_v+M_Bc_v)T_F

(29.730.718375+12.590.718498)=(29.730.718+12.590.718)TF(29.73*0.718*375+12.59*0.718*498)= (29.73*0.718+12.59*0.718)T_F

(29.730.718+12.590.718)TF30.38576=12506.5332630.38576\frac{\left(29.73\cdot \:0.718+12.59\cdot \:0.718\right)T_F}{30.38576}=\frac{12506.53326}{30.38576}

TF=12506.5332630.38576=411.59190CT_F=\frac{12506.53326}{30.38576} =411.5919^0C

PFVF=MFRTF    PF=(29.73+12.59)0.287411.598=624.89kPaP_FV_F =M_FRT_F \implies P_F = \frac{(29.73+12.59)*0.287*411.59}{8}=624.89 kPa

(b) The amount of entropy generation

ΔS=ΔSA+ΔSB=(mA(CplnTFTARlnPFPA))+(mB(CplnTFTBRlnPFPB))\Delta S=\Delta S_A +\Delta S_B = (m_A(C_p \ln \frac{T_F}{T_A} -R \ln \frac{P_F}{P_A} ))+(m_B(C_p \ln \frac{T_F}{T_B}-R \ln \frac{P_F}{P_B} ))

ΔS=(29.73(1.005ln411.593750.287ln624.89103800))+(12.59(1.005ln411.594980.287ln624.89103450))\Delta S= (29.73(1.005 \ln \frac{411.59}{375} -0.287 \ln \frac{624.89*10^3}{800} ))+(12.59(1.005 \ln \frac{411.59}{498}-0.287\ln \frac{624.89*10^3}{450} ))

ΔS=(29.730.1645)+(12.590.2858)\Delta S = (29.73*0.1645)+(12.59*-0.2858)

ΔS=1.2924kJ/kg.K\Delta S = 1.2924 kJ/kg.K

(c) the irreversibilities in the process

dU=TdSdW=1.29243003000.2858=301.98kJdU = TdS - dW = 1.2924*300- 300*0.2858 = 301.98 kJ


LATEST TUTORIALS
APPROVED BY CLIENTS