Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa Ye, C.; Dong, X.; Zhu, W.; Cai, D.; Qiu, T.; Fluid Phase Equilibria 2014, 367, 45-50
Data
T (K) x (mol mol-1) x (mol mol-1)
330.5 1 1.0
337.3 0.7343 0.9639
338.4 0.6973 0.9586
338.6 0.6898 0.9572
339.4 0.6653 0.9528
340.8 0.6223 0.9437
340.7 0.6244 0.9444
343.1 0.5596 0.9286
345.1 0.5111 0.9157
349.1 0.4275 0.8851
351.7 0.3803 0.8619
331.0 0.9909 0.9987
353.9 0.3449 0.8406
357.7 0.2858 0.793
364.4 0.2265 0.7213
368.2 0.1728 0.6481
373.6 0.1261 0.5404
379.2 0.0836 0.4128
380.9 0.0717 0.3698
384.1 0.0511 0.2862
388.2 0.0260 0.1611
390.1 0.0153 0.0991
331.5 0.9699 0.9954
392.9 0.0004 0.0033
393.3 0 0.0
332.1 0.9468 0.9923
332.6 0.9244 0.9892
333.4 0.8900 0.9845
334.1 0.8624 0.9818
334.7 0.8370 0.9786
336.5 0.7657 0.9687
7251; methyl ethanoate + 1-methoxy-2-propanol; 00022:00550