Investigation on Liquid Density Data at the Bubble Point and Equations for the Refrigerant HFC-404A over a Wide Temperature Range Qiao, X.g.; Xu, Y.j.; Han, X.h.; Journal of Chemical & Engineering Data 2014, 59, 2872-2878
Data
wi = 0.44 g g-1, wi = 0.52 g g-1
T (K) ρ (kg m-3)
227.25 1311.81
248.80 1243.21
251.46 1234.49
253.53 1227.39
256.20 1218.32
258.87 1209.06
261.54 1199.78
264.32 1189.72
267.17 1179.44
269.53 1170.43
272.30 1159.85
229.00 1306.65
274.85 1149.89
277.35 1139.93
279.96 1129.44
282.79 1118.41
285.27 1107.93
287.82 1097.24
290.35 1086.13
292.99 1074.43
295.62 1062.34
298.31 1049.79
231.13 1299.96
300.94 1037.02
303.74 1022.97
306.35 1009.51
309.09 994.81
311.74 980.42
314.35 965.08
316.99 948.95
319.60 931.51
322.18 912.66
324.88 892.87
233.65 1292.07
327.98 867.04
330.72 843.76
333.30 816.24
335.45 793.34
337.95 762.75
340.20 734.21
341.31 713.96
236.65 1282.7
238.93 1275.33
241.17 1268.12
243.67 1260.13
246.15 1251.99
4783; ethane, pentafluoro- + 1,1,1-trifluoroethane + ethane, 1,1,1,2-tetrafluoro-; 00219:00223:00303