Question 3.101: Reconsider Prob. 3-100. Using EES (or other) software, compa......

Reconsider Prob. 3-100. Using EES (or other) software, compare the pressure results of the ideal-gas and Beattie-Bridgeman equations with nitrogen data supplied by EES. Plot temperature versus specific volume for a pressure of 1000 \mathrm{~kPa} with respect to the saturated liquid and saturated vapor lines of nitrogen over the range of 110 \mathrm{~K}<T<150 \mathrm{~K}.

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EES Problem 3.100 is reconsidered. Using EES (or other) software, the pressure results of the ideal gas and Beattie-Bridgeman equations with nitrogen data supplied by EES are to be compared. The temperature is to be plotted versus specific volume for a pressure of 1000 kPa with respect to the saturated liquid and saturated vapor lines of nitrogen over the range of 110 \mathrm{~K}<T<150 \mathrm{~K}.

Analysis The problem is solved using EES, and the solution is given below.

Function BeattBridg(T,v,M,R_u)
v_bar=v*M "Conversion from m^3/kg to m^3/kmol"
"The constants for the Beattie-Bridgeman equation of state are found in text"
Ao=136.2315; aa=0.02617; Bo=0.05046; bb=-0.00691; cc=4.20*1E4
B=Bo*(1-bb/v_bar)
A=Ao*(1-aa/v_bar)
"The Beattie-Bridgeman equation of state is"
BeattBridg:=R_u*T/(v_bar**2)*(1-cc/(v_bar*T**3))*(v_bar+B)-A/v_bar**2
End

 

T=150 [K]
v=0.041884 [m^3/kg]
P_exper=1000 [kPa]
T_table=T; T_BB=T;T_idealgas=T
P_table=PRESSURE(Nitrogen,T=T_table,v=v) “EES data for nitrogen as a real gas”
{T_table=temperature(Nitrogen, P=P_table,v=v)}
M=MOLARMASS(Nitrogen)
R_u=8.314 [kJ/kmol-K] “Universal gas constant”
R=R_u/M “Particular gas constant”
P_idealgas=R*T_idealgas/v “Ideal gas equation”
P_BB=BeattBridg(T_BB,v,M,R_u) “Beattie-Bridgeman equation of state Function”
3-101
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\mathrm{P}_\text{BB} [kPa] \mathrm{P}_\text{table} [kPa] \mathrm{P} _\text{ideal gas} [kPa] V [m³/kg] \mathrm{T}_\text{BB} [K] \mathrm{T}_\text{ideal gas} [K] \mathrm{T} _\text{table} [K]
1000 1000 1000 0.01 91.23 33.69 103.8
1000 1000 1000 0.02 95.52 67.39 103.8
1000 1000 1000 0.025 105 84.23 106.1
1000 1000 1000 0.03 116.8 101.1 117.2
1000 1000 1000 0.035 130.1 117.9 130.1
1000 1000 1000 0.04 144.4 134.8 144.3
1000 1000 1000 0.05 174.6 168.5 174.5

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