(1)
Cp=k−1kar=1.667−11.667×38=77894.97=0.1221BTU/lbR Q=mcp(T2−T1)
300=3×0.1221(T2−560)
T2=1379=919°F
(B)
Q=mcp(T2−T1)=H
H=300BTU
(C)
W=p(v2−v1)=p(p2mRT−p1mRT1)
W=pmR(pT2−pT1)=mR(T2−T1)
W=3×38×(1379−560)=120.008BTU (D)
Cv=k−1R=1.677−138×7781=0.0732BTU/lb.R ∆U=mcv(T2−T1)
∆U=3×0.0732×(1379−560)=179.85BTU (e)
∆S=mcplnT2T2=4×0.1221ln5601379 ∆S=0.3301=BTU/R
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