Solution.
p2 = 1 bar;
p1 = 5 bar;
T3 = 283 K;
T1 = 298K;
pv1.3=constant;
L/d = 1.5;
cp = 1.005 kJ/kgK;
cv = 0.71 kJ/kgK;
T2T1=(p2p1)γγ−1;
T2298=(15)1.351.35−1=1.52;
T2=298/1.52=196K;
theoreticalC.O.P=T1−T2T2;
theoreticalC.O.P=298−196196=1.92 ;
actualC.O.P=0.5⋅1.92=0.96;
Refrigeratingeffectperkgofair=cp(T3–T2)=1.005(283–196)=87.44kJ/kg.
V3=p2mRT;
R=(cp–cv)=1.005–0.71=0.295kJ/kgK;
Refrigeratingeffectproducedbytherefrigeratingmachine=6×14000=84000kJ/h;
Hencemassofairincirculation=84000/(87.44⋅60)=16.01kg/min.
V3=(16.01⋅0.295⋅1000⋅283)/1.0⋅105=13.36m3/min;
Swept volume per stroke =13.36/(2⋅ 300) =0.02m3;
V = 0.02⋅ 0.85 = 0.019 m3;
π/4⋅d2⋅l=0.019;l=1.5d;
d=0.016m;l=0.024m;
Answer: theoretical C.O.P =1.92;
actual C.O.P = 0.96;
d=0.016m;
l = 0.024 m.
Comments