Thermodynamic properties of glycerol: Experimental and theoretical study Verevkin, S.P.; Zaitsau, D.H.; Emel’yanenko, V.N.; Zhabina, A.A.; Fluid Phase Equilibria 2015, 397, 87-94
Data
T (K) P (kPa)
352.60 0.00528
387.39 0.06861
310.89 9.63e-05
306.03 5.56e-05
303.61 4.19e-05
304.56 4.68e-05
392.20 0.09367
397.02 0.12656
401.83 0.16943
406.64 0.22507
412.11 0.30891
416.92 0.40331
421.73 0.52244
426.53 0.6725
431.34 0.85826
357.42 0.00782
436.13 1.08735
433.73 0.96709
428.91 0.75864
424.11 0.59225
419.30 0.45853
414.48 0.35259
409.68 0.26875
404.23 0.1952
399.42 0.1462
394.61 0.1087
362.66 0.01179
389.80 0.07986
384.99 0.0582
380.17 0.04186
374.70 0.0286
369.89 0.0202
365.07 0.0141
359.80 0.00938
354.98 0.00639
352.57 0.00526
357.39 0.00777
367.48 0.01696
362.63 0.0117
367.45 0.01686
372.27 0.024
377.08 0.03379
382.55 0.04942
387.37 0.06807
392.18 0.09311
397.00 0.12585
401.81 0.16876
406.62 0.22422
372.29 0.02415
401.81 0.16869
406.62 0.22404
412.08 0.30801
416.89 0.40226
421.70 0.52095
426.50 0.6698
431.31 0.85646
436.11 1.0859
433.72 0.96525
428.91 0.75836
377.11 0.03408
424.10 0.59195
419.30 0.45835
414.49 0.35263
409.69 0.26896
404.26 0.19523
399.45 0.14643
394.64 0.10866
389.83 0.07998
385.01 0.05821
380.19 0.04192
382.59 0.04972
374.73 0.0286
369.91 0.02016
365.08 0.01409
359.82 0.00939
354.99 0.00641
352.58 0.00527
303.59 4.15e-05
308.43 7.28e-05
313.29 0.000125
318.12 0.0002107
377.77 0.03569
322.95 0.0003472
327.82 0.0005644
332.72 0.0009037
338.25 0.0015021
343.08 0.0023202
347.91 0.0035293
352.73 0.0053181
357.57 0.0078629
362.42 0.011457
364.82 0.0138
382.59 0.0496
360.01 0.009523
355.18 0.006488
350.34 0.00436
345.51 0.0028755
340.68 0.0018722
335.14 0.0011323
330.30 0.0007165
325.42 0.0004428
320.57 0.0002701
315.71 0.0001634
182; glycerol; 00100