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1 0 . 3 4 . Make use of Eqs. ( 3 . 3 6 ) , ( 3 . 6 1 ) , (

10.34. Make use of Eqs. (3.36),(3.61),(3.62),(6.54),(6.55),(6.56),(6.70),(6.71),(10.62), and (10.69)-(10.74), to estimate V, HR, SR, and GR for one of the following binary vapor mixtures:
(a) Acetone(1)/1,3-butadiene (2) with mole fractions y1=0.28 and y2=0.72 at t =60\deg C and P =170 kPa (b) Acetonitrile(1)/diethyl ether (2) with mole fractions y1=0.37 and y2=0.63 at t=50\deg C and P =120 kPa
(c) Methyl chloride(1)/ethyl chloride(2) with mole fractions y1=0.45 and y2=0.55 at t =25\deg C and P =100 kPa (d) Nitrogen(1)/ammonia(2) with mole fractions y1=0.83 and y2=0.17 at 1=20\deg C and P =300 kPa
(e) Sulfur dioxide(1)/ethylene(2) with mole fractions y1=0.32 and y2=0.68 at t =25\deg C and P =420 kPa Note: Set ky-0 in Eq.(10.71).
Where
Eq 3.36 Z=PV/RT=1+BP/RT
Eq 3.61 B^0=0.083-0.422/(T_r^1.6)
Eq 3.62 B^1=0.139-0.172/(T_r^4.2)
Eq 6.54 G^R/RT=BP/RT
Eq 6.55 H^R/RT=P/R (B/T-dB/dT)
Eq 6.56 S^R/R=-P/R dB/dT
Eq 6.70(dB^0)/(dT_r )=0.675/(T_r^2.6)
Eq 6.71(dB^1)/(dT_r )=0.722/(T_r^5.2)
Eq 10.62 B=y_1^2 B_11+2y_1 y_2 B_12+y_2^2 B_22
Eq 10.69a B _ij=B^0+w_ij B^1
Eq 10.69b B _ij=(B_ij P_cij)/(RT_cij )
Eq 10.70 w_ij=((w_i+w_j ))/2
Eq 10.71 T_cij=(T_ci T_cj )^(1/2)(1-k_ij )
Eq 10.72 P_cij=(Z_cij RT_cij)/V_cij
Eq 10.73 Z_cij=(Z_ci+Z_cj)/2
Eq 10.74 V_cij=(((V_ci^(1/3)+V_cj^(1/3)))/2)^310.34. Make use of Eqs. (3.36),(3.61),(3.62),(6.54),(6.55),(6.56),(6.70),(6.71),(10.62), and (10.69)-(10.74), to estimate V,HR,SR,
and GR for one of the following binary vapor mixtures:
(a) Acetone(1)/1,3-butadiene(2) with mole fractions y1=0.28 and y2=0.72 at t=60C and P=170kPa
(b) Acetonitrile(1)/diethyl ether(2) with mole fractions y1=0.37 and y2=0.63 at t=50C and P=120kPa
(c) Methyl chloride(1)/ethyl chloride(2) with mole fractions y1=0.45 and y2=0.55 at t=25C and P=100kPa
(d) Nitrogen(1)/ammonia(2) with mole fractions y1=0.83 and y2=0.17 at t=20C and P=300kPa
(e) Sulfur dioxide(1)/ethylene(2) with mole fractions y1=0.32 and y2=0.68 at t=25C and P=420kPa
Note: Set kij=0 in Eq.(10.71).
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