Property Calculation
⇒ Saturated Vapor Pressure
⇒ Saturated Liquid Density
⇒ Liquid Dynamic Viscosity
⇒ Surface Tension
⇒ Heat of Vaporization
Property Estimation
⇒ UNIFAC
⇒ MOSCED
⇒ Joback
Group Assignment
⇒ UNIFAC and PSRK

Saturated Liquid Density

Calculation by DIPPR105 Equation

Component
Temperature Unit 
Property Unit
Temperatures
(optional)




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Component Details
 #DDB  Name  CAS-No.   Formula 
 21   Ethyl acetate   141-78-6   C4H8O2 

DIPPR105 Equation Parameters (Density in kg/m3, T in K)
No.  A   B   C   D   Tmin   Tmax 
 (1)   72.568   0.247526   523.354   0.266298   253   522 
DIPPR105 Equation

Calculation Over Validity Range
Temperature [K] Density(1) [kg/m3]
253 945.578
258.38 939.685
263.76 933.741
269.14 927.745
274.52 921.694
279.9 915.587
285.28 909.422
290.66 903.196
296.04 896.907
301.42 890.553
306.8 884.131
312.18 877.639
317.56 871.073
322.94 864.43
328.32 857.708
333.7 850.902
339.08 844.008
344.46 837.023
349.84 829.942
355.22 822.76
360.6 815.471
365.98 808.071
371.36 800.552
376.74 792.908
382.12 785.131
387.5 777.214
392.88 769.146
398.26 760.918
403.64 752.519
409.02 743.935
414.4 735.152
419.78 726.155
425.16 716.925
430.54 707.441
435.92 697.678
441.3 687.607
446.68 677.197
452.06 666.406
457.44 655.186
462.82 643.48
468.2 631.215
473.58 618.297
478.96 604.609
484.34 589.989
489.72 574.218
495.1 556.975
500.48 537.762
505.86 515.743
511.24 489.287
516.62 454.323
522 390.147
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