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njit-etd1961-002 - New Jersey Institute of Technology

njit-etd1961-002 - New Jersey Institute of Technology

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4log Ti φ(Tr) (αc 7) )(Tr) Equation (5)ErThe value <strong>of</strong> was determined using the knownnormal boiling point <strong>of</strong> formaldehyde at ¹ atmosphere.(F) Specific volumes <strong>of</strong> the saturated liquid weredetermined from -¹0 ° C. to ¹4¹ ° C. by the method <strong>of</strong>Watson ² . The data required for the calculationsare the critical temperature and critical compressibilityfactor and a single known accurate densitymeasurement as a reference state. The liquid densityat -²0°C. was available 7 , and was employed inconjunction with the reduced density table by thefollowing equation ² :DiD2(D, ) Equation (6)Specific volumes were then obtained by the reciprocals<strong>of</strong> the calculated liquid densities.(G) Specific volumes <strong>of</strong> the saturated and superheatedvapor were calculated using the generalizedcompressibility factors 4 which were derived fromthe correlation <strong>of</strong> Lydersen, Greenkorn and Hougen.Calculation was done using:PV ZRT Equation (7)(H) The saturated formaldehyde liquid at -¹9°C.was taken as the reference point for the zero value<strong>of</strong> enthalpy and entropy.(I) The latent heat <strong>of</strong> vaporization at the normalboiling point listed by Walker ¹6 as 5.57Kcal/g-mole at -¹9 ° C. was used to calculate thevalue <strong>of</strong> the latent heat <strong>of</strong> vaporization from-¹0 ° C. to the critical temperature. The equationderived by Watson ¹7 was used;

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