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njit-etd1961-002 - New Jersey Institute of Technology

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10predicted and given. —over, most <strong>of</strong> the other methodsare not recommended for values <strong>of</strong> Zc less than 0.23 orboiling point less than 250 ° K. This method <strong>of</strong> vaporpressure correlation has ±107 accuracy.In the absence <strong>of</strong> any experimental data, the heatcapacity data for formaldehyde were calculated byWalker 16 based ou. pectroscopic measurements. Thesedata can be represeroc ,1 by the following equation as afunction <strong>of</strong> temperature between 0 to 400 ° C.Cp = 9.48 + 0.00914T - 6.4 x 10 -7 T 2The accuracy <strong>of</strong> the . , boqe equation is not known. However,formaldehyde poss ee no internal rotation and this factmakes the use <strong>of</strong> the )rincipleD <strong>of</strong> statistical mechanicspossible for predicting accurate heat capacity andabsolute entropy for the ideal gaseous state fromspectroscopic measurement For this reason, the resultsobtained by using the rIkt.)e heat capacity equation tocalculate the enthalpy ind entropy <strong>of</strong> the ideal gas arebelieved to have :or y accuracy.The. ,,orrelations <strong>of</strong> Lydersen, Greenkorn,and Hauge,. wer- n -ied to obtain the values <strong>of</strong> thespecific volume, ek iJalpy and entropy in both the saturatedand superhcatr, d re. These correlations were basedon the ),,)nding states which pro thatall pure I,I sibility faLf - orsand departui L, ,1 LetHvior <strong>of</strong> enthalpy andentropy when F14,=,. , , , 0,4,, tomt,-; reclined conditions <strong>of</strong>pressure and tic,p ,,n,a and au the value <strong>of</strong> Zc.The specific volumes <strong>of</strong> the saturated liquid wereevaluated by the method <strong>of</strong> Watson 2 .. This method is notsensitive to errors in D c or Zc. The average error inestimating liquid densities by this method is about 1%.

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