| Component 1 | ethanol | ||
| Component 2 | water | ||
| p1s=PC1*exp(VPA1*x**3+VPB1*x**2+VPC1*x) | [bar] | ||
| x=1-1/(T/TC1) | |||
| PC1=61.4 [bar] | VPA1=-6.3405e-002 | VPB1=-1.3118e+000 | VPC1=8.2807e+000 |
| p2s=PC2*exp(VPA2*x**3+VPB2*x**2+VPC2*x) | [bar] | ||
| x=1-1/(T/TC2) | |||
| PC2=221.2 [bar] | VPA2=2.2244e-001 | VPB2=-5.2240e-002 | VPC2=7.1773e+000 |
| ---------------- A, B, C from Px datga ------ | |||
| A=a(Tr1)+b | a=1.6148e+000 | b=6.1880e-001 | ARD=4.500e-002 |
| B=a(Tr1)+b | a=-7.6540e-001 | b=1.4513e+000 | ARD=4.800e-002 |
| Tr1=T/TC1 | TC1=513.9 [K] | ||
| CTC=aX | a=2.963 | ||
| CTC=aX**2+bX | a=0.000e+000 | b=0.000e+000 | |
| CTC=aX**b | a=0.000e+000 | b=0.000e+000 | |
| CTC=(p1s*exp(C)-p2s)/(PC1-p2sTC1)-(p1s-p2s)/(PC1-p2sTC1) | |||
| ---------------- A, B, C from xy datga ------- | |||