Datasets
-
Mole fraction (4)
-
η - Viscosity, Pa*s (4)
-
Pvap - Vapor or sublimation pressure, kPa (4)
-
ρl - Mass density, kg/m3 (4)
-
Binary diffusion coefficient, m2/s (2)
-
Vapor or sublimation pressure, kPa (2)
Mole fraction of Carbon dioxide (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
313.15 |
1320.00 |
0.1190 |
338.15 |
1650.00 |
0.1190 |
363.15 |
1920.00 |
0.1190 |
313.15 |
2100.00 |
0.2990 |
338.15 |
2650.00 |
0.2990 |
363.15 |
3140.00 |
0.2990 |
313.15 |
4290.00 |
0.5190 |
338.15 |
5560.00 |
0.5190 |
363.15 |
6780.00 |
0.5190 |
Mole fraction of Squalane (1)
[ref]
Fixed |
Measured |
Mole fraction of Squalane (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Squalane (1) - Gas |
0.1160 |
373.70 |
0.0071 |
0.1240 |
343.15 |
0.0066 |
0.1300 |
343.15 |
0.0068 |
0.1440 |
426.00 |
0.0050 |
0.1530 |
343.15 |
0.0036 |
0.1690 |
343.15 |
0.0045 |
0.2030 |
343.15 |
0.0008 |
0.2060 |
343.15 |
0.0023 |
0.2150 |
373.70 |
0.0006 |
0.2450 |
343.15 |
0.0003 |
0.2700 |
426.00 |
0.0007 |
0.2950 |
343.15 |
0.0001 |
0.3060 |
373.10 |
0.0001 |
0.3420 |
343.15 |
0.0001 |
0.3770 |
423.10 |
0.0003 |
0.3860 |
373.70 |
0.0000 |
0.4180 |
343.15 |
0.0001 |
0.4470 |
426.00 |
0.0002 |
0.4950 |
343.15 |
0.0001 |
0.5640 |
423.10 |
0.0002 |
0.6510 |
343.15 |
0.0001 |
0.7970 |
343.15 |
0.0005 |
0.8280 |
313.15 |
0.0015 |
0.8310 |
313.15 |
0.0045 |
0.8380 |
343.15 |
0.0026 |
0.8430 |
313.15 |
0.0041 |
0.8460 |
313.15 |
0.0024 |
0.8460 |
313.15 |
0.0028 |
0.8690 |
343.15 |
0.0062 |
0.8710 |
343.15 |
0.0081 |
0.8780 |
343.15 |
0.0075 |
Mole fraction of Carbon dioxide (2)
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
313.15 |
1320.00 |
0.1190 |
338.15 |
1650.00 |
0.1190 |
363.15 |
1920.00 |
0.1190 |
313.15 |
2100.00 |
0.2990 |
338.15 |
2650.00 |
0.2990 |
363.15 |
3140.00 |
0.2990 |
313.15 |
4290.00 |
0.5190 |
338.15 |
5560.00 |
0.5190 |
363.15 |
6780.00 |
0.5190 |
Mole fraction of Squalane (1)
[ref]
Fixed |
Measured |
Mole fraction of Squalane (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Squalane (1) - Gas |
0.1160 |
373.70 |
0.0071 |
0.1240 |
343.15 |
0.0066 |
0.1300 |
343.15 |
0.0068 |
0.1440 |
426.00 |
0.0050 |
0.1530 |
343.15 |
0.0036 |
0.1690 |
343.15 |
0.0045 |
0.2030 |
343.15 |
0.0008 |
0.2060 |
343.15 |
0.0023 |
0.2150 |
373.70 |
0.0006 |
0.2450 |
343.15 |
0.0003 |
0.2700 |
426.00 |
0.0007 |
0.2950 |
343.15 |
0.0001 |
0.3060 |
373.10 |
0.0001 |
0.3420 |
343.15 |
0.0001 |
0.3770 |
423.10 |
0.0003 |
0.3860 |
373.70 |
0.0000 |
0.4180 |
343.15 |
0.0001 |
0.4470 |
426.00 |
0.0002 |
0.4950 |
343.15 |
0.0001 |
0.5640 |
423.10 |
0.0002 |
0.6510 |
343.15 |
0.0001 |
0.7970 |
343.15 |
0.0005 |
0.8280 |
313.15 |
0.0015 |
0.8310 |
313.15 |
0.0045 |
0.8380 |
343.15 |
0.0026 |
0.8430 |
313.15 |
0.0041 |
0.8460 |
313.15 |
0.0024 |
0.8460 |
313.15 |
0.0028 |
0.8690 |
343.15 |
0.0062 |
0.8710 |
343.15 |
0.0081 |
0.8780 |
343.15 |
0.0075 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Viscosity, Pa*s - Liquid |
0.1990 |
313.15 |
2790.00 |
0.0114 |
0.1990 |
313.15 |
12560.00 |
0.0134 |
0.1990 |
313.15 |
23440.00 |
0.0161 |
0.1990 |
313.15 |
45240.00 |
0.0229 |
0.1990 |
313.15 |
60140.00 |
0.0287 |
0.1990 |
313.15 |
74430.00 |
0.0359 |
0.1990 |
338.15 |
3100.00 |
0.0056 |
0.1990 |
338.15 |
11690.00 |
0.0064 |
0.1990 |
338.15 |
21990.00 |
0.0076 |
0.1990 |
338.15 |
42870.00 |
0.0105 |
0.1990 |
338.15 |
57570.00 |
0.0128 |
0.1990 |
338.15 |
69970.00 |
0.0154 |
0.1990 |
363.15 |
2670.00 |
0.0032 |
0.1990 |
363.15 |
11090.00 |
0.0037 |
0.1990 |
363.15 |
21420.00 |
0.0043 |
0.1990 |
363.15 |
42490.00 |
0.0057 |
0.1990 |
363.15 |
56730.00 |
0.0068 |
0.1990 |
363.15 |
70780.00 |
0.0081 |
0.2990 |
313.15 |
3900.00 |
0.0092 |
0.2990 |
313.15 |
12320.00 |
0.0105 |
0.2990 |
313.15 |
23100.00 |
0.0125 |
0.2990 |
313.15 |
44510.00 |
0.0171 |
0.2990 |
313.15 |
58570.00 |
0.0216 |
0.2990 |
313.15 |
73410.00 |
0.0265 |
0.2990 |
338.15 |
3320.00 |
0.0047 |
0.2990 |
338.15 |
11180.00 |
0.0054 |
0.2990 |
338.15 |
21990.00 |
0.0062 |
0.2990 |
338.15 |
42690.00 |
0.0083 |
0.2990 |
338.15 |
57330.00 |
0.0101 |
0.2990 |
338.15 |
71030.00 |
0.0122 |
0.2990 |
363.15 |
3820.00 |
0.0029 |
0.2990 |
363.15 |
10840.00 |
0.0031 |
0.2990 |
363.15 |
21180.00 |
0.0036 |
0.2990 |
363.15 |
42250.00 |
0.0048 |
0.2990 |
363.15 |
56390.00 |
0.0057 |
0.2990 |
363.15 |
70320.00 |
0.0068 |
0.5190 |
313.15 |
5300.00 |
0.0051 |
0.5190 |
313.15 |
11290.00 |
0.0056 |
0.5190 |
313.15 |
21910.00 |
0.0065 |
0.5190 |
313.15 |
42900.00 |
0.0086 |
0.5190 |
313.15 |
57150.00 |
0.0105 |
0.5190 |
313.15 |
71140.00 |
0.0125 |
0.5190 |
338.15 |
6440.00 |
0.0030 |
0.5190 |
338.15 |
10860.00 |
0.0032 |
0.5190 |
338.15 |
21260.00 |
0.0036 |
0.5190 |
338.15 |
42140.00 |
0.0048 |
0.5190 |
338.15 |
56660.00 |
0.0057 |
0.5190 |
338.15 |
70400.00 |
0.0066 |
0.5190 |
363.15 |
7280.00 |
0.0019 |
0.5190 |
363.15 |
10740.00 |
0.0021 |
0.5190 |
363.15 |
21340.00 |
0.0023 |
0.5190 |
363.15 |
42180.00 |
0.0030 |
0.5190 |
363.15 |
56170.00 |
0.0034 |
0.5190 |
363.15 |
70120.00 |
0.0041 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Viscosity, Pa*s - Liquid |
0.4233 |
303.15 |
10060.00 |
0.0091 |
0.4233 |
303.15 |
10070.00 |
0.0092 |
0.4233 |
303.15 |
30380.00 |
0.0127 |
0.4233 |
303.15 |
50510.00 |
0.0173 |
0.4233 |
303.15 |
70400.00 |
0.0230 |
0.4233 |
303.15 |
90250.00 |
0.0305 |
0.4233 |
303.15 |
110380.00 |
0.0401 |
0.4233 |
303.15 |
130280.00 |
0.0523 |
0.4233 |
303.15 |
150080.00 |
0.0678 |
0.4233 |
303.15 |
170210.00 |
0.0859 |
0.4233 |
348.25 |
10070.00 |
0.0030 |
0.4233 |
348.25 |
10100.00 |
0.0030 |
0.4233 |
348.25 |
30440.00 |
0.0040 |
0.4233 |
348.25 |
50590.00 |
0.0051 |
0.4233 |
348.25 |
70530.00 |
0.0064 |
0.4233 |
348.25 |
90610.00 |
0.0080 |
0.4233 |
348.25 |
110610.00 |
0.0098 |
0.4233 |
348.25 |
130400.00 |
0.0119 |
0.4233 |
348.25 |
150670.00 |
0.0145 |
0.4233 |
348.25 |
169670.00 |
0.0173 |
0.4233 |
398.31 |
10790.00 |
0.0014 |
0.4233 |
398.31 |
10830.00 |
0.0014 |
0.4233 |
398.31 |
30180.00 |
0.0018 |
0.4233 |
398.31 |
50350.00 |
0.0022 |
0.4233 |
398.31 |
70500.00 |
0.0027 |
0.4233 |
398.31 |
90450.00 |
0.0033 |
0.4233 |
398.31 |
110290.00 |
0.0039 |
0.4233 |
398.31 |
130350.00 |
0.0046 |
0.4233 |
398.31 |
150520.00 |
0.0054 |
0.4233 |
398.31 |
170000.00 |
0.0062 |
0.4233 |
448.35 |
11450.00 |
0.0008 |
0.4233 |
448.35 |
11570.00 |
0.0008 |
0.4233 |
448.35 |
30330.00 |
0.0010 |
0.4233 |
448.35 |
50410.00 |
0.0013 |
0.4233 |
448.35 |
70450.00 |
0.0016 |
0.4233 |
448.35 |
90670.00 |
0.0019 |
0.4233 |
448.35 |
110310.00 |
0.0022 |
0.4233 |
448.35 |
130440.00 |
0.0025 |
0.4233 |
448.35 |
150510.00 |
0.0029 |
0.4233 |
448.35 |
169900.00 |
0.0033 |
0.6039 |
303.18 |
10600.00 |
0.0049 |
0.6039 |
303.18 |
30810.00 |
0.0066 |
0.6039 |
303.18 |
50820.00 |
0.0086 |
0.6039 |
303.18 |
70800.00 |
0.0110 |
0.6039 |
303.18 |
91100.00 |
0.0140 |
0.6039 |
303.18 |
100670.00 |
0.0156 |
0.6039 |
303.18 |
111110.00 |
0.0175 |
0.6039 |
303.18 |
130850.00 |
0.0217 |
0.6039 |
303.18 |
150500.00 |
0.0265 |
0.6039 |
303.18 |
170440.00 |
0.0320 |
0.6039 |
348.11 |
10450.00 |
0.0019 |
0.6039 |
348.11 |
10480.00 |
0.0019 |
0.6039 |
348.11 |
30310.00 |
0.0025 |
0.6039 |
348.11 |
50270.00 |
0.0031 |
0.6039 |
348.11 |
70180.00 |
0.0039 |
0.6039 |
348.11 |
90320.00 |
0.0047 |
0.6039 |
348.11 |
110880.00 |
0.0056 |
0.6039 |
348.11 |
130860.00 |
0.0067 |
0.6039 |
348.11 |
150870.00 |
0.0079 |
0.6039 |
348.11 |
170910.00 |
0.0093 |
0.6039 |
398.13 |
10940.00 |
0.0010 |
0.6039 |
398.13 |
11100.00 |
0.0010 |
0.6039 |
398.13 |
30870.00 |
0.0013 |
0.6039 |
398.13 |
50550.00 |
0.0016 |
0.6039 |
398.13 |
70810.00 |
0.0019 |
0.6039 |
398.13 |
91230.00 |
0.0023 |
0.6039 |
398.13 |
110700.00 |
0.0027 |
0.6039 |
398.13 |
131240.00 |
0.0031 |
0.6039 |
398.13 |
150740.00 |
0.0036 |
0.6039 |
398.13 |
170660.00 |
0.0041 |
0.6039 |
448.13 |
10630.00 |
0.0007 |
0.6039 |
448.13 |
11010.00 |
0.0007 |
0.6039 |
448.13 |
30730.00 |
0.0009 |
0.6039 |
448.13 |
50590.00 |
0.0011 |
0.6039 |
448.13 |
70380.00 |
0.0012 |
0.6039 |
448.13 |
91380.00 |
0.0014 |
0.6039 |
448.13 |
111050.00 |
0.0016 |
0.6039 |
448.13 |
130810.00 |
0.0018 |
0.6039 |
448.13 |
150960.00 |
0.0021 |
0.6039 |
448.13 |
171000.00 |
0.0024 |
0.7882 |
303.17 |
30190.00 |
0.0024 |
0.7882 |
303.17 |
30740.00 |
0.0022 |
0.7882 |
303.17 |
50100.00 |
0.0028 |
0.7882 |
303.17 |
70730.00 |
0.0034 |
0.7882 |
303.17 |
90490.00 |
0.0042 |
0.7882 |
303.17 |
110640.00 |
0.0050 |
0.7882 |
303.17 |
130570.00 |
0.0059 |
0.7882 |
303.17 |
151340.00 |
0.0069 |
0.7882 |
303.17 |
170570.00 |
0.0081 |
0.7882 |
348.25 |
30390.00 |
0.0011 |
0.7882 |
348.25 |
30610.00 |
0.0011 |
0.7882 |
348.25 |
50540.00 |
0.0013 |
0.7882 |
348.25 |
70650.00 |
0.0016 |
0.7882 |
348.25 |
90680.00 |
0.0019 |
0.7882 |
348.25 |
110350.00 |
0.0022 |
0.7882 |
348.25 |
130530.00 |
0.0026 |
0.7882 |
348.25 |
150600.00 |
0.0029 |
0.7882 |
348.25 |
170310.00 |
0.0033 |
0.7882 |
398.33 |
30150.00 |
0.0006 |
0.7882 |
398.33 |
30500.00 |
0.0006 |
0.7882 |
398.33 |
50500.00 |
0.0008 |
0.7882 |
398.33 |
70580.00 |
0.0009 |
0.7882 |
398.33 |
90510.00 |
0.0011 |
0.7882 |
398.33 |
110760.00 |
0.0013 |
0.7882 |
398.33 |
130550.00 |
0.0015 |
0.7882 |
398.33 |
150620.00 |
0.0016 |
0.7882 |
398.33 |
170310.00 |
0.0018 |
0.7882 |
448.41 |
30160.00 |
0.0004 |
0.7882 |
448.41 |
30820.00 |
0.0004 |
0.7882 |
448.41 |
50450.00 |
0.0005 |
0.7882 |
448.41 |
70350.00 |
0.0006 |
0.7882 |
448.41 |
90420.00 |
0.0007 |
0.7882 |
448.41 |
110590.00 |
0.0008 |
0.7882 |
448.41 |
130360.00 |
0.0010 |
0.7882 |
448.41 |
150480.00 |
0.0011 |
0.7882 |
448.41 |
169720.00 |
0.0012 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Viscosity, Pa*s - Liquid |
0.1990 |
313.15 |
2790.00 |
0.0114 |
0.1990 |
313.15 |
12560.00 |
0.0134 |
0.1990 |
313.15 |
23440.00 |
0.0161 |
0.1990 |
313.15 |
45240.00 |
0.0229 |
0.1990 |
313.15 |
60140.00 |
0.0287 |
0.1990 |
313.15 |
74430.00 |
0.0359 |
0.1990 |
338.15 |
3100.00 |
0.0056 |
0.1990 |
338.15 |
11690.00 |
0.0064 |
0.1990 |
338.15 |
21990.00 |
0.0076 |
0.1990 |
338.15 |
42870.00 |
0.0105 |
0.1990 |
338.15 |
57570.00 |
0.0128 |
0.1990 |
338.15 |
69970.00 |
0.0154 |
0.1990 |
363.15 |
2670.00 |
0.0032 |
0.1990 |
363.15 |
11090.00 |
0.0037 |
0.1990 |
363.15 |
21420.00 |
0.0043 |
0.1990 |
363.15 |
42490.00 |
0.0057 |
0.1990 |
363.15 |
56730.00 |
0.0068 |
0.1990 |
363.15 |
70780.00 |
0.0081 |
0.2990 |
313.15 |
3900.00 |
0.0092 |
0.2990 |
313.15 |
12320.00 |
0.0105 |
0.2990 |
313.15 |
23100.00 |
0.0125 |
0.2990 |
313.15 |
44510.00 |
0.0171 |
0.2990 |
313.15 |
58570.00 |
0.0216 |
0.2990 |
313.15 |
73410.00 |
0.0265 |
0.2990 |
338.15 |
3320.00 |
0.0047 |
0.2990 |
338.15 |
11180.00 |
0.0054 |
0.2990 |
338.15 |
21990.00 |
0.0062 |
0.2990 |
338.15 |
42690.00 |
0.0083 |
0.2990 |
338.15 |
57330.00 |
0.0101 |
0.2990 |
338.15 |
71030.00 |
0.0122 |
0.2990 |
363.15 |
3820.00 |
0.0029 |
0.2990 |
363.15 |
10840.00 |
0.0031 |
0.2990 |
363.15 |
21180.00 |
0.0036 |
0.2990 |
363.15 |
42250.00 |
0.0048 |
0.2990 |
363.15 |
56390.00 |
0.0057 |
0.2990 |
363.15 |
70320.00 |
0.0068 |
0.5190 |
313.15 |
5300.00 |
0.0051 |
0.5190 |
313.15 |
11290.00 |
0.0056 |
0.5190 |
313.15 |
21910.00 |
0.0065 |
0.5190 |
313.15 |
42900.00 |
0.0086 |
0.5190 |
313.15 |
57150.00 |
0.0105 |
0.5190 |
313.15 |
71140.00 |
0.0125 |
0.5190 |
338.15 |
6440.00 |
0.0030 |
0.5190 |
338.15 |
10860.00 |
0.0032 |
0.5190 |
338.15 |
21260.00 |
0.0036 |
0.5190 |
338.15 |
42140.00 |
0.0048 |
0.5190 |
338.15 |
56660.00 |
0.0057 |
0.5190 |
338.15 |
70400.00 |
0.0066 |
0.5190 |
363.15 |
7280.00 |
0.0019 |
0.5190 |
363.15 |
10740.00 |
0.0021 |
0.5190 |
363.15 |
21340.00 |
0.0023 |
0.5190 |
363.15 |
42180.00 |
0.0030 |
0.5190 |
363.15 |
56170.00 |
0.0034 |
0.5190 |
363.15 |
70120.00 |
0.0041 |
Viscosity, Pa*s
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Viscosity, Pa*s - Liquid |
0.4233 |
303.15 |
10060.00 |
0.0091 |
0.4233 |
303.15 |
10070.00 |
0.0092 |
0.4233 |
303.15 |
30380.00 |
0.0127 |
0.4233 |
303.15 |
50510.00 |
0.0173 |
0.4233 |
303.15 |
70400.00 |
0.0230 |
0.4233 |
303.15 |
90250.00 |
0.0305 |
0.4233 |
303.15 |
110380.00 |
0.0401 |
0.4233 |
303.15 |
130280.00 |
0.0523 |
0.4233 |
303.15 |
150080.00 |
0.0678 |
0.4233 |
303.15 |
170210.00 |
0.0859 |
0.4233 |
348.25 |
10070.00 |
0.0030 |
0.4233 |
348.25 |
10100.00 |
0.0030 |
0.4233 |
348.25 |
30440.00 |
0.0040 |
0.4233 |
348.25 |
50590.00 |
0.0051 |
0.4233 |
348.25 |
70530.00 |
0.0064 |
0.4233 |
348.25 |
90610.00 |
0.0080 |
0.4233 |
348.25 |
110610.00 |
0.0098 |
0.4233 |
348.25 |
130400.00 |
0.0119 |
0.4233 |
348.25 |
150670.00 |
0.0145 |
0.4233 |
348.25 |
169670.00 |
0.0173 |
0.4233 |
398.31 |
10790.00 |
0.0014 |
0.4233 |
398.31 |
10830.00 |
0.0014 |
0.4233 |
398.31 |
30180.00 |
0.0018 |
0.4233 |
398.31 |
50350.00 |
0.0022 |
0.4233 |
398.31 |
70500.00 |
0.0027 |
0.4233 |
398.31 |
90450.00 |
0.0033 |
0.4233 |
398.31 |
110290.00 |
0.0039 |
0.4233 |
398.31 |
130350.00 |
0.0046 |
0.4233 |
398.31 |
150520.00 |
0.0054 |
0.4233 |
398.31 |
170000.00 |
0.0062 |
0.4233 |
448.35 |
11450.00 |
0.0008 |
0.4233 |
448.35 |
11570.00 |
0.0008 |
0.4233 |
448.35 |
30330.00 |
0.0010 |
0.4233 |
448.35 |
50410.00 |
0.0013 |
0.4233 |
448.35 |
70450.00 |
0.0016 |
0.4233 |
448.35 |
90670.00 |
0.0019 |
0.4233 |
448.35 |
110310.00 |
0.0022 |
0.4233 |
448.35 |
130440.00 |
0.0025 |
0.4233 |
448.35 |
150510.00 |
0.0029 |
0.4233 |
448.35 |
169900.00 |
0.0033 |
0.6039 |
303.18 |
10600.00 |
0.0049 |
0.6039 |
303.18 |
30810.00 |
0.0066 |
0.6039 |
303.18 |
50820.00 |
0.0086 |
0.6039 |
303.18 |
70800.00 |
0.0110 |
0.6039 |
303.18 |
91100.00 |
0.0140 |
0.6039 |
303.18 |
100670.00 |
0.0156 |
0.6039 |
303.18 |
111110.00 |
0.0175 |
0.6039 |
303.18 |
130850.00 |
0.0217 |
0.6039 |
303.18 |
150500.00 |
0.0265 |
0.6039 |
303.18 |
170440.00 |
0.0320 |
0.6039 |
348.11 |
10450.00 |
0.0019 |
0.6039 |
348.11 |
10480.00 |
0.0019 |
0.6039 |
348.11 |
30310.00 |
0.0025 |
0.6039 |
348.11 |
50270.00 |
0.0031 |
0.6039 |
348.11 |
70180.00 |
0.0039 |
0.6039 |
348.11 |
90320.00 |
0.0047 |
0.6039 |
348.11 |
110880.00 |
0.0056 |
0.6039 |
348.11 |
130860.00 |
0.0067 |
0.6039 |
348.11 |
150870.00 |
0.0079 |
0.6039 |
348.11 |
170910.00 |
0.0093 |
0.6039 |
398.13 |
10940.00 |
0.0010 |
0.6039 |
398.13 |
11100.00 |
0.0010 |
0.6039 |
398.13 |
30870.00 |
0.0013 |
0.6039 |
398.13 |
50550.00 |
0.0016 |
0.6039 |
398.13 |
70810.00 |
0.0019 |
0.6039 |
398.13 |
91230.00 |
0.0023 |
0.6039 |
398.13 |
110700.00 |
0.0027 |
0.6039 |
398.13 |
131240.00 |
0.0031 |
0.6039 |
398.13 |
150740.00 |
0.0036 |
0.6039 |
398.13 |
170660.00 |
0.0041 |
0.6039 |
448.13 |
10630.00 |
0.0007 |
0.6039 |
448.13 |
11010.00 |
0.0007 |
0.6039 |
448.13 |
30730.00 |
0.0009 |
0.6039 |
448.13 |
50590.00 |
0.0011 |
0.6039 |
448.13 |
70380.00 |
0.0012 |
0.6039 |
448.13 |
91380.00 |
0.0014 |
0.6039 |
448.13 |
111050.00 |
0.0016 |
0.6039 |
448.13 |
130810.00 |
0.0018 |
0.6039 |
448.13 |
150960.00 |
0.0021 |
0.6039 |
448.13 |
171000.00 |
0.0024 |
0.7882 |
303.17 |
30190.00 |
0.0024 |
0.7882 |
303.17 |
30740.00 |
0.0022 |
0.7882 |
303.17 |
50100.00 |
0.0028 |
0.7882 |
303.17 |
70730.00 |
0.0034 |
0.7882 |
303.17 |
90490.00 |
0.0042 |
0.7882 |
303.17 |
110640.00 |
0.0050 |
0.7882 |
303.17 |
130570.00 |
0.0059 |
0.7882 |
303.17 |
151340.00 |
0.0069 |
0.7882 |
303.17 |
170570.00 |
0.0081 |
0.7882 |
348.25 |
30390.00 |
0.0011 |
0.7882 |
348.25 |
30610.00 |
0.0011 |
0.7882 |
348.25 |
50540.00 |
0.0013 |
0.7882 |
348.25 |
70650.00 |
0.0016 |
0.7882 |
348.25 |
90680.00 |
0.0019 |
0.7882 |
348.25 |
110350.00 |
0.0022 |
0.7882 |
348.25 |
130530.00 |
0.0026 |
0.7882 |
348.25 |
150600.00 |
0.0029 |
0.7882 |
348.25 |
170310.00 |
0.0033 |
0.7882 |
398.33 |
30150.00 |
0.0006 |
0.7882 |
398.33 |
30500.00 |
0.0006 |
0.7882 |
398.33 |
50500.00 |
0.0008 |
0.7882 |
398.33 |
70580.00 |
0.0009 |
0.7882 |
398.33 |
90510.00 |
0.0011 |
0.7882 |
398.33 |
110760.00 |
0.0013 |
0.7882 |
398.33 |
130550.00 |
0.0015 |
0.7882 |
398.33 |
150620.00 |
0.0016 |
0.7882 |
398.33 |
170310.00 |
0.0018 |
0.7882 |
448.41 |
30160.00 |
0.0004 |
0.7882 |
448.41 |
30820.00 |
0.0004 |
0.7882 |
448.41 |
50450.00 |
0.0005 |
0.7882 |
448.41 |
70350.00 |
0.0006 |
0.7882 |
448.41 |
90420.00 |
0.0007 |
0.7882 |
448.41 |
110590.00 |
0.0008 |
0.7882 |
448.41 |
130360.00 |
0.0010 |
0.7882 |
448.41 |
150480.00 |
0.0011 |
0.7882 |
448.41 |
169720.00 |
0.0012 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.4738 |
353.23 |
5650.00 |
0.4738 |
362.59 |
6080.00 |
0.4738 |
374.10 |
6600.00 |
0.4738 |
382.73 |
6960.00 |
0.4738 |
392.97 |
7360.00 |
0.5622 |
332.80 |
6180.00 |
0.5622 |
342.83 |
6680.00 |
0.5622 |
353.27 |
7240.00 |
0.5622 |
363.39 |
7930.00 |
0.5622 |
373.41 |
8450.00 |
0.5622 |
383.47 |
8950.00 |
0.5622 |
393.67 |
9420.00 |
0.6030 |
322.98 |
6210.00 |
0.6030 |
333.48 |
7140.00 |
0.6030 |
343.23 |
7680.00 |
0.6030 |
352.60 |
8340.00 |
0.6030 |
364.11 |
8890.00 |
0.6030 |
373.13 |
9420.00 |
0.6030 |
382.75 |
9990.00 |
0.6030 |
393.48 |
10790.00 |
0.6854 |
303.40 |
6180.00 |
0.6854 |
313.28 |
7060.00 |
0.6854 |
323.20 |
8150.00 |
0.6854 |
333.23 |
8990.00 |
0.6854 |
343.08 |
9960.00 |
0.6854 |
353.33 |
10690.00 |
0.8002 |
313.15 |
10330.00 |
0.8002 |
323.52 |
11910.00 |
0.8002 |
333.13 |
13460.00 |
0.8002 |
343.22 |
14600.00 |
0.8002 |
353.20 |
16090.00 |
0.8002 |
363.05 |
17360.00 |
0.8002 |
373.15 |
18520.00 |
0.8002 |
383.15 |
19660.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.4738 |
353.25 |
5690.00 |
0.4738 |
362.55 |
6160.00 |
0.4738 |
374.15 |
6630.00 |
0.4738 |
382.75 |
6950.00 |
0.4738 |
392.85 |
7370.00 |
0.5622 |
332.75 |
6140.00 |
0.5622 |
342.85 |
6640.00 |
0.5622 |
353.25 |
7210.00 |
0.5622 |
363.45 |
7910.00 |
0.5622 |
373.65 |
8470.00 |
0.5622 |
383.45 |
8900.00 |
0.5622 |
393.65 |
9570.00 |
0.6030 |
323.25 |
6350.00 |
0.6030 |
333.45 |
7260.00 |
0.6030 |
343.35 |
7890.00 |
0.6030 |
352.65 |
8330.00 |
0.6030 |
364.25 |
8940.00 |
0.6030 |
373.15 |
9430.00 |
0.6030 |
382.75 |
10120.00 |
0.6854 |
304.05 |
6290.00 |
0.6854 |
313.25 |
7030.00 |
0.6854 |
323.25 |
8180.00 |
0.6854 |
333.15 |
8830.00 |
0.6854 |
342.95 |
9990.00 |
0.6854 |
353.25 |
10760.00 |
0.8002 |
313.15 |
10380.00 |
0.8002 |
323.45 |
11990.00 |
0.8002 |
333.15 |
12940.00 |
0.8002 |
343.15 |
14400.00 |
0.8002 |
353.35 |
15950.00 |
0.8002 |
363.05 |
17310.00 |
0.8002 |
373.15 |
18560.00 |
0.8002 |
383.25 |
19670.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.4738 |
353.23 |
5650.00 |
0.4738 |
362.59 |
6080.00 |
0.4738 |
374.10 |
6600.00 |
0.4738 |
382.73 |
6960.00 |
0.4738 |
392.97 |
7360.00 |
0.5622 |
332.80 |
6180.00 |
0.5622 |
342.83 |
6680.00 |
0.5622 |
353.27 |
7240.00 |
0.5622 |
363.39 |
7930.00 |
0.5622 |
373.41 |
8450.00 |
0.5622 |
383.47 |
8950.00 |
0.5622 |
393.67 |
9420.00 |
0.6030 |
322.98 |
6210.00 |
0.6030 |
333.48 |
7140.00 |
0.6030 |
343.23 |
7680.00 |
0.6030 |
352.60 |
8340.00 |
0.6030 |
364.11 |
8890.00 |
0.6030 |
373.13 |
9420.00 |
0.6030 |
382.75 |
9990.00 |
0.6030 |
393.48 |
10790.00 |
0.6854 |
303.40 |
6180.00 |
0.6854 |
313.28 |
7060.00 |
0.6854 |
323.20 |
8150.00 |
0.6854 |
333.23 |
8990.00 |
0.6854 |
343.08 |
9960.00 |
0.6854 |
353.33 |
10690.00 |
0.8002 |
313.15 |
10330.00 |
0.8002 |
323.52 |
11910.00 |
0.8002 |
333.13 |
13460.00 |
0.8002 |
343.22 |
14600.00 |
0.8002 |
353.20 |
16090.00 |
0.8002 |
363.05 |
17360.00 |
0.8002 |
373.15 |
18520.00 |
0.8002 |
383.15 |
19660.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.4738 |
353.25 |
5690.00 |
0.4738 |
362.55 |
6160.00 |
0.4738 |
374.15 |
6630.00 |
0.4738 |
382.75 |
6950.00 |
0.4738 |
392.85 |
7370.00 |
0.5622 |
332.75 |
6140.00 |
0.5622 |
342.85 |
6640.00 |
0.5622 |
353.25 |
7210.00 |
0.5622 |
363.45 |
7910.00 |
0.5622 |
373.65 |
8470.00 |
0.5622 |
383.45 |
8900.00 |
0.5622 |
393.65 |
9570.00 |
0.6030 |
323.25 |
6350.00 |
0.6030 |
333.45 |
7260.00 |
0.6030 |
343.35 |
7890.00 |
0.6030 |
352.65 |
8330.00 |
0.6030 |
364.25 |
8940.00 |
0.6030 |
373.15 |
9430.00 |
0.6030 |
382.75 |
10120.00 |
0.6854 |
304.05 |
6290.00 |
0.6854 |
313.25 |
7030.00 |
0.6854 |
323.25 |
8180.00 |
0.6854 |
333.15 |
8830.00 |
0.6854 |
342.95 |
9990.00 |
0.6854 |
353.25 |
10760.00 |
0.8002 |
313.15 |
10380.00 |
0.8002 |
323.45 |
11990.00 |
0.8002 |
333.15 |
12940.00 |
0.8002 |
343.15 |
14400.00 |
0.8002 |
353.35 |
15950.00 |
0.8002 |
363.05 |
17310.00 |
0.8002 |
373.15 |
18560.00 |
0.8002 |
383.25 |
19670.00 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
0.1990 |
313.15 |
2790.00 |
796.7 |
0.1990 |
313.15 |
12560.00 |
804.5 |
0.1990 |
313.15 |
23440.00 |
812.5 |
0.1990 |
313.15 |
45240.00 |
826.3 |
0.1990 |
313.15 |
60140.00 |
834.5 |
0.1990 |
313.15 |
74430.00 |
841.6 |
0.1990 |
338.15 |
3100.00 |
780.2 |
0.1990 |
338.15 |
11690.00 |
787.3 |
0.1990 |
338.15 |
21990.00 |
795.1 |
0.1990 |
338.15 |
42870.00 |
808.7 |
0.1990 |
338.15 |
57570.00 |
817.1 |
0.1990 |
338.15 |
69970.00 |
823.5 |
0.1990 |
363.15 |
2670.00 |
763.2 |
0.1990 |
363.15 |
11090.00 |
770.2 |
0.1990 |
363.15 |
21420.00 |
778.2 |
0.1990 |
363.15 |
42490.00 |
792.2 |
0.1990 |
363.15 |
56730.00 |
800.5 |
0.1990 |
363.15 |
70780.00 |
807.9 |
0.2990 |
313.15 |
3900.00 |
799.1 |
0.2990 |
313.15 |
12320.00 |
805.8 |
0.2990 |
313.15 |
23100.00 |
813.6 |
0.2990 |
313.15 |
44510.00 |
828.1 |
0.2990 |
313.15 |
58570.00 |
836.5 |
0.2990 |
313.15 |
73410.00 |
844.9 |
0.2990 |
338.15 |
3320.00 |
782.1 |
0.2990 |
338.15 |
11180.00 |
788.3 |
0.2990 |
338.15 |
21990.00 |
796.2 |
0.2990 |
338.15 |
42690.00 |
810.4 |
0.2990 |
338.15 |
57330.00 |
819.2 |
0.2990 |
338.15 |
71030.00 |
826.9 |
0.2990 |
363.15 |
3820.00 |
766.2 |
0.2990 |
363.15 |
10840.00 |
771.7 |
0.2990 |
363.15 |
21180.00 |
779.2 |
0.2990 |
363.15 |
42250.00 |
793.2 |
0.2990 |
363.15 |
56390.00 |
801.8 |
0.2990 |
363.15 |
70320.00 |
809.6 |
0.5190 |
313.15 |
5300.00 |
804.5 |
0.5190 |
313.15 |
11290.00 |
810.3 |
0.5190 |
313.15 |
21910.00 |
819.7 |
0.5190 |
313.15 |
42900.00 |
836.1 |
0.5190 |
313.15 |
57150.00 |
846.0 |
0.5190 |
313.15 |
71140.00 |
854.8 |
0.5190 |
338.15 |
6440.00 |
787.1 |
0.5190 |
338.15 |
10860.00 |
791.5 |
0.5190 |
338.15 |
21260.00 |
801.0 |
0.5190 |
338.15 |
42140.00 |
817.7 |
0.5190 |
338.15 |
56660.00 |
827.7 |
0.5190 |
338.15 |
70400.00 |
836.4 |
0.5190 |
363.15 |
7280.00 |
769.5 |
0.5190 |
363.15 |
10740.00 |
772.7 |
0.5190 |
363.15 |
21340.00 |
782.5 |
0.5190 |
363.15 |
42180.00 |
799.3 |
0.5190 |
363.15 |
56170.00 |
809.2 |
0.5190 |
363.15 |
70120.00 |
818.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
0.4233 |
303.15 |
10060.00 |
814.8 |
0.4233 |
303.15 |
10070.00 |
815.3 |
0.4233 |
303.15 |
30380.00 |
828.0 |
0.4233 |
303.15 |
50510.00 |
839.2 |
0.4233 |
303.15 |
70400.00 |
849.3 |
0.4233 |
303.15 |
90250.00 |
856.5 |
0.4233 |
303.15 |
110380.00 |
862.1 |
0.4233 |
303.15 |
130280.00 |
867.8 |
0.4233 |
303.15 |
150080.00 |
869.4 |
0.4233 |
303.15 |
170210.00 |
882.8 |
0.4233 |
348.25 |
10070.00 |
783.6 |
0.4233 |
348.25 |
10100.00 |
783.4 |
0.4233 |
348.25 |
30440.00 |
799.2 |
0.4233 |
348.25 |
50590.00 |
812.2 |
0.4233 |
348.25 |
70530.00 |
823.5 |
0.4233 |
348.25 |
90610.00 |
833.7 |
0.4233 |
348.25 |
110610.00 |
842.8 |
0.4233 |
348.25 |
130400.00 |
851.3 |
0.4233 |
348.25 |
150670.00 |
859.3 |
0.4233 |
348.25 |
169670.00 |
866.3 |
0.4233 |
398.31 |
10790.00 |
749.0 |
0.4233 |
398.31 |
10830.00 |
755.3 |
0.4233 |
398.31 |
30180.00 |
768.1 |
0.4233 |
398.31 |
50350.00 |
784.0 |
0.4233 |
398.31 |
70500.00 |
797.4 |
0.4233 |
398.31 |
90450.00 |
808.9 |
0.4233 |
398.31 |
110290.00 |
819.1 |
0.4233 |
398.31 |
130350.00 |
828.4 |
0.4233 |
398.31 |
150520.00 |
837.2 |
0.4233 |
398.31 |
170000.00 |
845.0 |
0.4233 |
448.35 |
11450.00 |
715.2 |
0.4233 |
448.35 |
11570.00 |
720.6 |
0.4233 |
448.35 |
30330.00 |
737.6 |
0.4233 |
448.35 |
50410.00 |
756.5 |
0.4233 |
448.35 |
70450.00 |
771.8 |
0.4233 |
448.35 |
90670.00 |
785.2 |
0.4233 |
448.35 |
110310.00 |
796.6 |
0.4233 |
448.35 |
130440.00 |
807.0 |
0.4233 |
448.35 |
150510.00 |
816.5 |
0.4233 |
448.35 |
169900.00 |
824.8 |
0.6039 |
303.18 |
10600.00 |
823.9 |
0.6039 |
303.18 |
30810.00 |
838.1 |
0.6039 |
303.18 |
50820.00 |
850.4 |
0.6039 |
303.18 |
70800.00 |
861.0 |
0.6039 |
303.18 |
91100.00 |
871.1 |
0.6039 |
303.18 |
100670.00 |
874.8 |
0.6039 |
303.18 |
111110.00 |
879.9 |
0.6039 |
303.18 |
130850.00 |
888.1 |
0.6039 |
303.18 |
150500.00 |
897.9 |
0.6039 |
303.18 |
170440.00 |
910.5 |
0.6039 |
348.11 |
10450.00 |
787.7 |
0.6039 |
348.11 |
10480.00 |
788.1 |
0.6039 |
348.11 |
30310.00 |
806.0 |
0.6039 |
348.11 |
50270.00 |
820.7 |
0.6039 |
348.11 |
70180.00 |
833.3 |
0.6039 |
348.11 |
90320.00 |
844.4 |
0.6039 |
348.11 |
110880.00 |
854.6 |
0.6039 |
348.11 |
130860.00 |
863.7 |
0.6039 |
348.11 |
150870.00 |
872.1 |
0.6039 |
348.11 |
170910.00 |
879.8 |
0.6039 |
398.13 |
10940.00 |
749.2 |
0.6039 |
398.13 |
11100.00 |
748.9 |
0.6039 |
398.13 |
30870.00 |
771.8 |
0.6039 |
398.13 |
50550.00 |
789.2 |
0.6039 |
398.13 |
70810.00 |
804.2 |
0.6039 |
398.13 |
91230.00 |
817.2 |
0.6039 |
398.13 |
110700.00 |
828.2 |
0.6039 |
398.13 |
131240.00 |
838.7 |
0.6039 |
398.13 |
150740.00 |
847.7 |
0.6039 |
398.13 |
170660.00 |
856.2 |
0.6039 |
448.13 |
10630.00 |
713.1 |
0.6039 |
448.13 |
11010.00 |
713.3 |
0.6039 |
448.13 |
30730.00 |
739.7 |
0.6039 |
448.13 |
50590.00 |
759.8 |
0.6039 |
448.13 |
70380.00 |
776.6 |
0.6039 |
448.13 |
91380.00 |
791.8 |
0.6039 |
448.13 |
111050.00 |
804.5 |
0.6039 |
448.13 |
130810.00 |
815.7 |
0.6039 |
448.13 |
150960.00 |
826.0 |
0.6039 |
448.13 |
171000.00 |
835.3 |
0.7882 |
303.17 |
30190.00 |
854.3 |
0.7882 |
303.17 |
30740.00 |
847.4 |
0.7882 |
303.17 |
50100.00 |
863.4 |
0.7882 |
303.17 |
70730.00 |
877.8 |
0.7882 |
303.17 |
90490.00 |
890.0 |
0.7882 |
303.17 |
110640.00 |
901.1 |
0.7882 |
303.17 |
130570.00 |
911.0 |
0.7882 |
303.17 |
151340.00 |
922.8 |
0.7882 |
303.17 |
170570.00 |
934.8 |
0.7882 |
348.25 |
30390.00 |
806.0 |
0.7882 |
348.25 |
30610.00 |
806.9 |
0.7882 |
348.25 |
50540.00 |
827.0 |
0.7882 |
348.25 |
70650.00 |
844.0 |
0.7882 |
348.25 |
90680.00 |
858.4 |
0.7882 |
348.25 |
110350.00 |
870.8 |
0.7882 |
348.25 |
130530.00 |
882.3 |
0.7882 |
348.25 |
150600.00 |
892.7 |
0.7882 |
348.25 |
170310.00 |
902.0 |
0.7882 |
398.33 |
30150.00 |
760.4 |
0.7882 |
398.33 |
30500.00 |
759.9 |
0.7882 |
398.33 |
50500.00 |
786.7 |
0.7882 |
398.33 |
70580.00 |
807.3 |
0.7882 |
398.33 |
90510.00 |
824.2 |
0.7882 |
398.33 |
110760.00 |
839.0 |
0.7882 |
398.33 |
130550.00 |
851.6 |
0.7882 |
398.33 |
150620.00 |
863.2 |
0.7882 |
398.33 |
170310.00 |
873.6 |
0.7882 |
448.41 |
30160.00 |
714.5 |
0.7882 |
448.41 |
30820.00 |
714.9 |
0.7882 |
448.41 |
50450.00 |
748.0 |
0.7882 |
448.41 |
70350.00 |
772.5 |
0.7882 |
448.41 |
90420.00 |
792.3 |
0.7882 |
448.41 |
110590.00 |
809.1 |
0.7882 |
448.41 |
130360.00 |
823.3 |
0.7882 |
448.41 |
150480.00 |
836.2 |
0.7882 |
448.41 |
169720.00 |
847.5 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
0.1990 |
313.15 |
2790.00 |
796.7 |
0.1990 |
313.15 |
12560.00 |
804.5 |
0.1990 |
313.15 |
23440.00 |
812.5 |
0.1990 |
313.15 |
45240.00 |
826.3 |
0.1990 |
313.15 |
60140.00 |
834.5 |
0.1990 |
313.15 |
74430.00 |
841.6 |
0.1990 |
338.15 |
3100.00 |
780.2 |
0.1990 |
338.15 |
11690.00 |
787.3 |
0.1990 |
338.15 |
21990.00 |
795.1 |
0.1990 |
338.15 |
42870.00 |
808.7 |
0.1990 |
338.15 |
57570.00 |
817.1 |
0.1990 |
338.15 |
69970.00 |
823.5 |
0.1990 |
363.15 |
2670.00 |
763.2 |
0.1990 |
363.15 |
11090.00 |
770.2 |
0.1990 |
363.15 |
21420.00 |
778.2 |
0.1990 |
363.15 |
42490.00 |
792.2 |
0.1990 |
363.15 |
56730.00 |
800.5 |
0.1990 |
363.15 |
70780.00 |
807.9 |
0.2990 |
313.15 |
3900.00 |
799.1 |
0.2990 |
313.15 |
12320.00 |
805.8 |
0.2990 |
313.15 |
23100.00 |
813.6 |
0.2990 |
313.15 |
44510.00 |
828.1 |
0.2990 |
313.15 |
58570.00 |
836.5 |
0.2990 |
313.15 |
73410.00 |
844.9 |
0.2990 |
338.15 |
3320.00 |
782.1 |
0.2990 |
338.15 |
11180.00 |
788.3 |
0.2990 |
338.15 |
21990.00 |
796.2 |
0.2990 |
338.15 |
42690.00 |
810.4 |
0.2990 |
338.15 |
57330.00 |
819.2 |
0.2990 |
338.15 |
71030.00 |
826.9 |
0.2990 |
363.15 |
3820.00 |
766.2 |
0.2990 |
363.15 |
10840.00 |
771.7 |
0.2990 |
363.15 |
21180.00 |
779.2 |
0.2990 |
363.15 |
42250.00 |
793.2 |
0.2990 |
363.15 |
56390.00 |
801.8 |
0.2990 |
363.15 |
70320.00 |
809.6 |
0.5190 |
313.15 |
5300.00 |
804.5 |
0.5190 |
313.15 |
11290.00 |
810.3 |
0.5190 |
313.15 |
21910.00 |
819.7 |
0.5190 |
313.15 |
42900.00 |
836.1 |
0.5190 |
313.15 |
57150.00 |
846.0 |
0.5190 |
313.15 |
71140.00 |
854.8 |
0.5190 |
338.15 |
6440.00 |
787.1 |
0.5190 |
338.15 |
10860.00 |
791.5 |
0.5190 |
338.15 |
21260.00 |
801.0 |
0.5190 |
338.15 |
42140.00 |
817.7 |
0.5190 |
338.15 |
56660.00 |
827.7 |
0.5190 |
338.15 |
70400.00 |
836.4 |
0.5190 |
363.15 |
7280.00 |
769.5 |
0.5190 |
363.15 |
10740.00 |
772.7 |
0.5190 |
363.15 |
21340.00 |
782.5 |
0.5190 |
363.15 |
42180.00 |
799.3 |
0.5190 |
363.15 |
56170.00 |
809.2 |
0.5190 |
363.15 |
70120.00 |
818.0 |
Mass density, kg/m3
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (2) - Liquid |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
0.4233 |
303.15 |
10060.00 |
814.8 |
0.4233 |
303.15 |
10070.00 |
815.3 |
0.4233 |
303.15 |
30380.00 |
828.0 |
0.4233 |
303.15 |
50510.00 |
839.2 |
0.4233 |
303.15 |
70400.00 |
849.3 |
0.4233 |
303.15 |
90250.00 |
856.5 |
0.4233 |
303.15 |
110380.00 |
862.1 |
0.4233 |
303.15 |
130280.00 |
867.8 |
0.4233 |
303.15 |
150080.00 |
869.4 |
0.4233 |
303.15 |
170210.00 |
882.8 |
0.4233 |
348.25 |
10070.00 |
783.6 |
0.4233 |
348.25 |
10100.00 |
783.4 |
0.4233 |
348.25 |
30440.00 |
799.2 |
0.4233 |
348.25 |
50590.00 |
812.2 |
0.4233 |
348.25 |
70530.00 |
823.5 |
0.4233 |
348.25 |
90610.00 |
833.7 |
0.4233 |
348.25 |
110610.00 |
842.8 |
0.4233 |
348.25 |
130400.00 |
851.3 |
0.4233 |
348.25 |
150670.00 |
859.3 |
0.4233 |
348.25 |
169670.00 |
866.3 |
0.4233 |
398.31 |
10790.00 |
749.0 |
0.4233 |
398.31 |
10830.00 |
755.3 |
0.4233 |
398.31 |
30180.00 |
768.1 |
0.4233 |
398.31 |
50350.00 |
784.0 |
0.4233 |
398.31 |
70500.00 |
797.4 |
0.4233 |
398.31 |
90450.00 |
808.9 |
0.4233 |
398.31 |
110290.00 |
819.1 |
0.4233 |
398.31 |
130350.00 |
828.4 |
0.4233 |
398.31 |
150520.00 |
837.2 |
0.4233 |
398.31 |
170000.00 |
845.0 |
0.4233 |
448.35 |
11450.00 |
715.2 |
0.4233 |
448.35 |
11570.00 |
720.6 |
0.4233 |
448.35 |
30330.00 |
737.6 |
0.4233 |
448.35 |
50410.00 |
756.5 |
0.4233 |
448.35 |
70450.00 |
771.8 |
0.4233 |
448.35 |
90670.00 |
785.2 |
0.4233 |
448.35 |
110310.00 |
796.6 |
0.4233 |
448.35 |
130440.00 |
807.0 |
0.4233 |
448.35 |
150510.00 |
816.5 |
0.4233 |
448.35 |
169900.00 |
824.8 |
0.6039 |
303.18 |
10600.00 |
823.9 |
0.6039 |
303.18 |
30810.00 |
838.1 |
0.6039 |
303.18 |
50820.00 |
850.4 |
0.6039 |
303.18 |
70800.00 |
861.0 |
0.6039 |
303.18 |
91100.00 |
871.1 |
0.6039 |
303.18 |
100670.00 |
874.8 |
0.6039 |
303.18 |
111110.00 |
879.9 |
0.6039 |
303.18 |
130850.00 |
888.1 |
0.6039 |
303.18 |
150500.00 |
897.9 |
0.6039 |
303.18 |
170440.00 |
910.5 |
0.6039 |
348.11 |
10450.00 |
787.7 |
0.6039 |
348.11 |
10480.00 |
788.1 |
0.6039 |
348.11 |
30310.00 |
806.0 |
0.6039 |
348.11 |
50270.00 |
820.7 |
0.6039 |
348.11 |
70180.00 |
833.3 |
0.6039 |
348.11 |
90320.00 |
844.4 |
0.6039 |
348.11 |
110880.00 |
854.6 |
0.6039 |
348.11 |
130860.00 |
863.7 |
0.6039 |
348.11 |
150870.00 |
872.1 |
0.6039 |
348.11 |
170910.00 |
879.8 |
0.6039 |
398.13 |
10940.00 |
749.2 |
0.6039 |
398.13 |
11100.00 |
748.9 |
0.6039 |
398.13 |
30870.00 |
771.8 |
0.6039 |
398.13 |
50550.00 |
789.2 |
0.6039 |
398.13 |
70810.00 |
804.2 |
0.6039 |
398.13 |
91230.00 |
817.2 |
0.6039 |
398.13 |
110700.00 |
828.2 |
0.6039 |
398.13 |
131240.00 |
838.7 |
0.6039 |
398.13 |
150740.00 |
847.7 |
0.6039 |
398.13 |
170660.00 |
856.2 |
0.6039 |
448.13 |
10630.00 |
713.1 |
0.6039 |
448.13 |
11010.00 |
713.3 |
0.6039 |
448.13 |
30730.00 |
739.7 |
0.6039 |
448.13 |
50590.00 |
759.8 |
0.6039 |
448.13 |
70380.00 |
776.6 |
0.6039 |
448.13 |
91380.00 |
791.8 |
0.6039 |
448.13 |
111050.00 |
804.5 |
0.6039 |
448.13 |
130810.00 |
815.7 |
0.6039 |
448.13 |
150960.00 |
826.0 |
0.6039 |
448.13 |
171000.00 |
835.3 |
0.7882 |
303.17 |
30190.00 |
854.3 |
0.7882 |
303.17 |
30740.00 |
847.4 |
0.7882 |
303.17 |
50100.00 |
863.4 |
0.7882 |
303.17 |
70730.00 |
877.8 |
0.7882 |
303.17 |
90490.00 |
890.0 |
0.7882 |
303.17 |
110640.00 |
901.1 |
0.7882 |
303.17 |
130570.00 |
911.0 |
0.7882 |
303.17 |
151340.00 |
922.8 |
0.7882 |
303.17 |
170570.00 |
934.8 |
0.7882 |
348.25 |
30390.00 |
806.0 |
0.7882 |
348.25 |
30610.00 |
806.9 |
0.7882 |
348.25 |
50540.00 |
827.0 |
0.7882 |
348.25 |
70650.00 |
844.0 |
0.7882 |
348.25 |
90680.00 |
858.4 |
0.7882 |
348.25 |
110350.00 |
870.8 |
0.7882 |
348.25 |
130530.00 |
882.3 |
0.7882 |
348.25 |
150600.00 |
892.7 |
0.7882 |
348.25 |
170310.00 |
902.0 |
0.7882 |
398.33 |
30150.00 |
760.4 |
0.7882 |
398.33 |
30500.00 |
759.9 |
0.7882 |
398.33 |
50500.00 |
786.7 |
0.7882 |
398.33 |
70580.00 |
807.3 |
0.7882 |
398.33 |
90510.00 |
824.2 |
0.7882 |
398.33 |
110760.00 |
839.0 |
0.7882 |
398.33 |
130550.00 |
851.6 |
0.7882 |
398.33 |
150620.00 |
863.2 |
0.7882 |
398.33 |
170310.00 |
873.6 |
0.7882 |
448.41 |
30160.00 |
714.5 |
0.7882 |
448.41 |
30820.00 |
714.9 |
0.7882 |
448.41 |
50450.00 |
748.0 |
0.7882 |
448.41 |
70350.00 |
772.5 |
0.7882 |
448.41 |
90420.00 |
792.3 |
0.7882 |
448.41 |
110590.00 |
809.1 |
0.7882 |
448.41 |
130360.00 |
823.3 |
0.7882 |
448.41 |
150480.00 |
836.2 |
0.7882 |
448.41 |
169720.00 |
847.5 |
Binary diffusion coefficient, m2/s
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
298.00 |
1100.00 |
0.0000 |
298.00 |
10000.00 |
0.0000 |
298.00 |
32000.00 |
0.0000 |
298.00 |
52000.00 |
0.0000 |
298.00 |
66000.00 |
0.0000 |
323.00 |
1100.00 |
0.0000 |
323.00 |
10000.00 |
0.0000 |
323.00 |
30000.00 |
0.0000 |
323.00 |
52000.00 |
0.0000 |
323.00 |
64000.00 |
0.0000 |
348.00 |
1000.00 |
0.0000 |
348.00 |
11000.00 |
0.0000 |
348.00 |
31000.00 |
0.0000 |
348.00 |
50000.00 |
0.0000 |
348.00 |
67000.00 |
0.0000 |
373.00 |
1000.00 |
0.0000 |
373.00 |
10000.00 |
0.0000 |
373.00 |
30000.00 |
0.0000 |
373.00 |
47000.00 |
0.0000 |
373.00 |
66000.00 |
0.0000 |
398.00 |
1000.00 |
0.0000 |
398.00 |
11000.00 |
0.0000 |
398.00 |
31000.00 |
0.0000 |
398.00 |
50000.00 |
0.0000 |
398.00 |
66000.00 |
0.0000 |
423.00 |
1000.00 |
0.0000 |
423.00 |
11000.00 |
0.0000 |
423.00 |
30000.00 |
0.0000 |
423.00 |
50000.00 |
0.0000 |
423.00 |
67000.00 |
0.0000 |
Binary diffusion coefficient, m2/s
[ref]
Operational condition: Mole fraction =
0 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Binary diffusion coefficient, m2/s - Liquid |
298.00 |
1100.00 |
0.0000 |
298.00 |
10000.00 |
0.0000 |
298.00 |
32000.00 |
0.0000 |
298.00 |
52000.00 |
0.0000 |
298.00 |
66000.00 |
0.0000 |
323.00 |
1100.00 |
0.0000 |
323.00 |
10000.00 |
0.0000 |
323.00 |
30000.00 |
0.0000 |
323.00 |
52000.00 |
0.0000 |
323.00 |
64000.00 |
0.0000 |
348.00 |
1000.00 |
0.0000 |
348.00 |
11000.00 |
0.0000 |
348.00 |
31000.00 |
0.0000 |
348.00 |
50000.00 |
0.0000 |
348.00 |
67000.00 |
0.0000 |
373.00 |
1000.00 |
0.0000 |
373.00 |
10000.00 |
0.0000 |
373.00 |
30000.00 |
0.0000 |
373.00 |
47000.00 |
0.0000 |
373.00 |
66000.00 |
0.0000 |
398.00 |
1000.00 |
0.0000 |
398.00 |
11000.00 |
0.0000 |
398.00 |
31000.00 |
0.0000 |
398.00 |
50000.00 |
0.0000 |
398.00 |
66000.00 |
0.0000 |
423.00 |
1000.00 |
0.0000 |
423.00 |
11000.00 |
0.0000 |
423.00 |
30000.00 |
0.0000 |
423.00 |
50000.00 |
0.0000 |
423.00 |
67000.00 |
0.0000 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Squalane (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Gas |
0.1160 |
373.70 |
30400.00 |
0.1200 |
373.80 |
30050.00 |
0.1240 |
343.15 |
28400.00 |
0.1300 |
343.15 |
30100.00 |
0.1440 |
426.00 |
30300.00 |
0.1530 |
343.15 |
23600.00 |
0.1690 |
343.15 |
24800.00 |
0.2030 |
343.15 |
16750.00 |
0.2060 |
343.15 |
19500.00 |
0.2150 |
373.70 |
19600.00 |
0.2450 |
343.15 |
13100.00 |
0.2700 |
426.00 |
19350.00 |
0.2950 |
343.15 |
10900.00 |
0.3060 |
373.10 |
13900.00 |
0.3150 |
422.90 |
18000.00 |
0.3420 |
343.15 |
9300.00 |
0.3770 |
423.10 |
14100.00 |
0.3860 |
373.70 |
10100.00 |
0.4180 |
343.15 |
7200.00 |
0.4470 |
426.00 |
10750.00 |
0.4950 |
343.15 |
5650.00 |
0.5640 |
423.10 |
7900.00 |
0.6510 |
343.15 |
3500.00 |
0.7970 |
343.15 |
15000.00 |
0.8280 |
313.15 |
15000.00 |
0.8310 |
313.15 |
20000.00 |
0.8380 |
343.15 |
20000.00 |
0.8430 |
313.15 |
25000.00 |
0.8460 |
313.15 |
30000.00 |
0.8460 |
313.15 |
35000.00 |
0.8690 |
343.15 |
25000.00 |
0.8710 |
343.15 |
35000.00 |
0.8780 |
343.15 |
30000.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Squalane (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Gas |
0.1160 |
373.70 |
30400.00 |
0.1200 |
373.80 |
30050.00 |
0.1240 |
343.15 |
28400.00 |
0.1300 |
343.15 |
30100.00 |
0.1440 |
426.00 |
30300.00 |
0.1530 |
343.15 |
23600.00 |
0.1690 |
343.15 |
24800.00 |
0.2030 |
343.15 |
16750.00 |
0.2060 |
343.15 |
19500.00 |
0.2150 |
373.70 |
19600.00 |
0.2450 |
343.15 |
13100.00 |
0.2700 |
426.00 |
19350.00 |
0.2950 |
343.15 |
10900.00 |
0.3060 |
373.10 |
13900.00 |
0.3150 |
422.90 |
18000.00 |
0.3420 |
343.15 |
9300.00 |
0.3770 |
423.10 |
14100.00 |
0.3860 |
373.70 |
10100.00 |
0.4180 |
343.15 |
7200.00 |
0.4470 |
426.00 |
10750.00 |
0.4950 |
343.15 |
5650.00 |
0.5640 |
423.10 |
7900.00 |
0.6510 |
343.15 |
3500.00 |
0.7970 |
343.15 |
15000.00 |
0.8280 |
313.15 |
15000.00 |
0.8310 |
313.15 |
20000.00 |
0.8380 |
343.15 |
20000.00 |
0.8430 |
313.15 |
25000.00 |
0.8460 |
313.15 |
30000.00 |
0.8460 |
313.15 |
35000.00 |
0.8690 |
343.15 |
25000.00 |
0.8710 |
343.15 |
35000.00 |
0.8780 |
343.15 |
30000.00 |
Sources
-
Diffusion Coefficients of Carbon Dioxide in Eight Hydrocarbon Liquids at Temperatures between (298.15 and 423.15) K at Pressures up to 69 MPa
-
Vapor Liquid Equilibrium Measurements for Carbon Dioxide + Cyclohexene + Squalane at High Pressures Using a Synthetic Method
-
Measurements and Modeling of Phase Behavior, Density, and Viscosity of Oil + Carbon Dioxide: Squalane + CO2 at Temperatures (313 to 363) K and Pressures up to 77 MPa
-
Viscosity and Density of Carbon Dioxide + 2,6,10,15,19,23-Hexamethyltetracosane (Squalane)
-
Phase Equilibrium of Hydrogen, Carbon Dioxide, Squalene, and Squalane