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Talk to SalesThe Review of Physical Chemistry of Japan Vol. 38 No. 2 (1968)
88
M. Srichand and M. A. Tirunarayanan
square method. The values of and , so obtained, are given in Table 2 with the standard deviation, , and the probable error, P. E., calculated by the equation
In Fig. 3, the excess viscosity of Freon-12 and Freon-22 vapours is plotted versus density.
Zero-density viscosity of Freon-12 and Freon-22 vapours
It is important to realize that the determination of viscosity at any temperature and density requires information regarding the temperature dependence of zero-density viscosity. The temperature dependence of zero-density viscosity may be represented by an equation of the form
where the constants, and , depend on the nature of the vapour.
The constants, and , for Freon-12 and Freon-22 vapours are evaluated by matching equation (6) to the zero-density viscosity-temperature data presented in Table 1 using the method of least squares. The values of and , so obtained, are given in Table 3. The standard deviation is calculated by equation (4) and the probable error by equation (5).
Table 3. Constants, , and reliability information for Freon-12 and Freon-22 vapours based on zero-density viscosity data given in Table 1
| Refrigerant | Constant | Constant | Standard deviation | Probable error |
|---|---|---|---|---|
|
Poise/ |
Poise |
Poise |
P. E.
Poise |
|
| Freon-12 | 10.57 | 59.77 | 1.6643 | 1.1226 |
| Freon-22 | 13.25 | 102.65 | 0.5334 | 0.3598 |
Fig. 3 Variation of excess viscosity of Freon-12 and Freon-22 vapours with density
Fig. 4 Zero-density viscosity of Freon-12 and Freon-22 vapours