Contents
-
Physical Properties
-
Temperature Dependent Properties
-
Pressure Dependent Properties
-
Datasets
-
Correlations
-
Similar Compounds
-
Mixtures
-
Sources
Physical Properties
Temperature Dependent Properties
Property |
Value |
Unit |
Temperature (K) |
Source |
Cp,gas |
[156.27; 206.94] |
J/mol×K |
[333.85; 468.90] |
|
|
Cp,gas |
156.27 ± 0.31 |
J/mol×K |
333.85 |
NIST
|
Cp,gas |
168.28 ± 0.34 |
J/mol×K |
365.15 |
NIST
|
Cp,gas |
181.17 ± 0.36 |
J/mol×K |
398.85 |
NIST
|
Cp,gas |
194.10 ± 0.39 |
J/mol×K |
433.70 |
NIST
|
Cp,gas |
206.94 ± 0.41 |
J/mol×K |
468.90 |
NIST
|
Cp,liquid |
[184.20; 265.20] |
J/mol×K |
[293.50; 308.35] |
|
|
Cp,liquid |
193.30 |
J/mol×K |
293.50 |
NIST
|
Cp,liquid |
191.60 |
J/mol×K |
295.10 |
NIST
|
Cp,liquid |
195.64 |
J/mol×K |
297.32 |
NIST
|
Cp,liquid |
196.10 |
J/mol×K |
297.32 |
NIST
|
Cp,liquid |
194.10 |
J/mol×K |
298.00 |
NIST
|
Cp,liquid |
196.20 |
J/mol×K |
298.00 |
NIST
|
Cp,liquid |
195.10 |
J/mol×K |
298.00 |
NIST
|
Cp,liquid |
189.10 |
J/mol×K |
298.10 |
NIST
|
Cp,liquid |
195.33 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
195.80 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
195.33 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
194.96 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
195.80 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
195.80 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
197.66 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
195.84 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
195.76 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
195.64 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
197.66 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
197.66 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
198.50 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
195.52 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
194.97 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
265.20 |
J/mol×K |
298.15 |
NIST
|
Cp,liquid |
196.10 |
J/mol×K |
299.80 |
NIST
|
Cp,liquid |
184.20 |
J/mol×K |
300.00 |
NIST
|
Cp,liquid |
186.20 |
J/mol×K |
300.70 |
NIST
|
Cp,liquid |
203.00 |
J/mol×K |
308.35 |
NIST
|
η |
[0.0000655; 0.0003495] |
Pa×s |
[283.15; 473.15] |
|
|
η |
0.0003495 |
Pa×s |
283.15 |
Liquid ...
|
η |
0.0003163 |
Pa×s |
293.15 |
Viscosi...
|
η |
0.0003190 |
Pa×s |
293.15 |
Densiti...
|
η |
0.0003020 |
Pa×s |
293.15 |
Excess ...
|
η |
0.0003100 |
Pa×s |
293.15 |
Dynamic...
|
η |
0.0003127 |
Pa×s |
293.15 |
Liquid ...
|
η |
0.0002979 |
Pa×s |
293.15 |
Viscosi...
|
η |
0.0003036 |
Pa×s |
298.15 |
Viscosi...
|
η |
0.0003010 |
Pa×s |
298.15 |
Dynamic...
|
η |
0.0002944 |
Pa×s |
298.15 |
Measure...
|
η |
0.0002886 |
Pa×s |
298.15 |
Excess ...
|
η |
0.0003040 |
Pa×s |
298.15 |
Densiti...
|
η |
0.0002865 |
Pa×s |
298.15 |
Viscosi...
|
η |
0.0002990 |
Pa×s |
298.15 |
Densiti...
|
η |
0.0002937 |
Pa×s |
298.20 |
Viscosi...
|
η |
0.0002900 |
Pa×s |
303.15 |
Densiti...
|
η |
0.0002914 |
Pa×s |
303.15 |
Viscosi...
|
η |
0.0002830 |
Pa×s |
303.15 |
Density...
|
η |
0.0002809 |
Pa×s |
303.15 |
Liquid ...
|
η |
0.0002774 |
Pa×s |
303.15 |
Excess ...
|
η |
0.0002850 |
Pa×s |
303.15 |
Densiti...
|
η |
0.0002810 |
Pa×s |
303.15 |
Dynamic...
|
η |
0.0002798 |
Pa×s |
303.16 |
Viscosi...
|
η |
0.0002669 |
Pa×s |
308.13 |
Viscosi...
|
η |
0.0002690 |
Pa×s |
308.15 |
Density...
|
η |
0.0002730 |
Pa×s |
308.15 |
Densiti...
|
η |
0.0002797 |
Pa×s |
308.15 |
Viscosi...
|
η |
0.0002520 |
Pa×s |
313.15 |
Density...
|
η |
0.0002600 |
Pa×s |
313.15 |
Densiti...
|
η |
0.0002685 |
Pa×s |
313.15 |
Viscosi...
|
η |
0.0002546 |
Pa×s |
313.15 |
Liquid ...
|
η |
0.0002504 |
Pa×s |
313.15 |
Excess ...
|
η |
0.0002537 |
Pa×s |
313.15 |
Measure...
|
η |
0.0002560 |
Pa×s |
313.15 |
Dynamic...
|
η |
0.0002490 |
Pa×s |
318.15 |
Densiti...
|
η |
0.0002580 |
Pa×s |
318.15 |
Viscosi...
|
η |
0.0002340 |
Pa×s |
323.15 |
Liquid ...
|
η |
0.0002380 |
Pa×s |
323.15 |
Densiti...
|
η |
0.0002482 |
Pa×s |
323.15 |
Viscosi...
|
η |
0.0002339 |
Pa×s |
323.15 |
Excess ...
|
η |
0.0002391 |
Pa×s |
328.15 |
Viscosi...
|
η |
0.0002300 |
Pa×s |
328.15 |
Densiti...
|
η |
0.0002308 |
Pa×s |
333.15 |
Viscosi...
|
η |
0.0002114 |
Pa×s |
333.15 |
Excess ...
|
η |
0.0001905 |
Pa×s |
348.15 |
Liquid ...
|
η |
0.0001550 |
Pa×s |
373.15 |
Liquid ...
|
η |
0.0001268 |
Pa×s |
398.15 |
Liquid ...
|
η |
0.0001026 |
Pa×s |
423.15 |
Liquid ...
|
η |
0.0000837 |
Pa×s |
448.15 |
Liquid ...
|
η |
0.0000655 |
Pa×s |
473.15 |
Liquid ...
|
ΔfusH |
[12.34; 13.08] |
kJ/mol |
[177.80; 178.60] |
|
|
ΔfusH |
13.08 |
kJ/mol |
177.80 |
NIST
|
ΔfusH |
13.08 |
kJ/mol |
177.80 |
NIST
|
ΔfusH |
13.08 |
kJ/mol |
177.84 |
NIST
|
ΔfusH |
12.34 |
kJ/mol |
177.90 |
NIST
|
ΔfusH |
13.03 |
kJ/mol |
177.90 |
NIST
|
ΔfusH |
12.58 |
kJ/mol |
178.60 |
NIST
|
ΔsubH |
50.80 |
kJ/mol |
178.00 |
NIST
|
ΔvapH |
[8.90; 35.70] |
kJ/mol |
[221.50; 498.00] |
|
|
ΔvapH |
32.50 |
kJ/mol |
221.50 |
NIST
|
ΔvapH |
35.70 |
kJ/mol |
224.00 |
NIST
|
ΔvapH |
34.90 |
kJ/mol |
268.00 |
NIST
|
ΔvapH |
31.88 |
kJ/mol |
298.00 |
Enthalp...
|
ΔvapH |
30.90 ± 0.10 |
kJ/mol |
309.00 |
NIST
|
ΔvapH |
31.60 |
kJ/mol |
310.50 |
NIST
|
ΔvapH |
30.70 ± 0.10 |
kJ/mol |
313.00 |
NIST
|
ΔvapH |
30.50 ± 0.20 |
kJ/mol |
313.00 |
NIST
|
ΔvapH |
32.00 |
kJ/mol |
314.50 |
NIST
|
ΔvapH |
30.90 |
kJ/mol |
318.00 |
NIST
|
ΔvapH |
31.50 |
kJ/mol |
320.50 |
NIST
|
ΔvapH |
29.80 ± 0.10 |
kJ/mol |
328.00 |
NIST
|
ΔvapH |
29.50 ± 0.10 |
kJ/mol |
333.00 |
NIST
|
ΔvapH |
29.00 ± 0.20 |
kJ/mol |
333.00 |
NIST
|
ΔvapH |
28.85 |
kJ/mol |
341.90 |
KDB
|
ΔvapH |
28.85 |
kJ/mol |
341.90 |
NIST
|
ΔvapH |
28.20 ± 0.10 |
kJ/mol |
353.00 |
NIST
|
ΔvapH |
28.20 ± 0.20 |
kJ/mol |
353.00 |
NIST
|
ΔvapH |
30.10 |
kJ/mol |
359.00 |
NIST
|
ΔvapH |
26.60 |
kJ/mol |
373.00 |
NIST
|
ΔvapH |
29.30 |
kJ/mol |
412.50 |
NIST
|
ΔvapH |
22.50 |
kJ/mol |
423.00 |
NIST
|
ΔvapH |
15.70 |
kJ/mol |
473.00 |
NIST
|
ΔvapH |
29.40 |
kJ/mol |
476.50 |
NIST
|
ΔvapH |
8.90 |
kJ/mol |
498.00 |
NIST
|
ν |
[0.0000004; 0.0000005] |
m2/s |
[283.15; 313.15] |
|
|
ν |
0.0000005 |
m2/s |
283.15 |
Kinemat...
|
ν |
0.0000005 |
m2/s |
283.15 |
Experim...
|
ν |
0.0000004 |
m2/s |
298.15 |
Kinemat...
|
ν |
0.0000004 |
m2/s |
298.15 |
Experim...
|
ν |
0.0000004 |
m2/s |
313.15 |
Kinemat...
|
ν |
0.0000004 |
m2/s |
313.15 |
Experim...
|
Pvap |
[12.89; 2876.83] |
kPa |
[288.15; 504.04] |
|
|
Pvap |
12.89 |
kPa |
288.15 |
Article...
|
Pvap |
17.00 |
kPa |
288.24 |
Isother...
|
Pvap |
15.88 |
kPa |
292.98 |
Measure...
|
Pvap |
21.00 |
kPa |
296.23 |
Isother...
|
Pvap |
18.39 |
kPa |
296.27 |
Measure...
|
Pvap |
20.22 |
kPa |
298.15 |
(Vapour...
|
Pvap |
20.22 |
kPa |
298.15 |
Thermop...
|
Pvap |
20.22 |
kPa |
298.15 |
Article...
|
Pvap |
20.69 |
kPa |
298.95 |
Measure...
|
Pvap |
23.81 |
kPa |
302.20 |
Measure...
|
Pvap |
25.16 |
kPa |
303.15 |
Measure...
|
Pvap |
25.01 |
kPa |
303.15 |
Phase e...
|
Pvap |
25.04 |
kPa |
303.16 |
Isobari...
|
Pvap |
26.19 |
kPa |
304.49 |
Measure...
|
Pvap |
27.50 |
kPa |
305.43 |
Isobari...
|
Pvap |
28.77 |
kPa |
306.76 |
Measure...
|
Pvap |
29.95 |
kPa |
307.43 |
Isobari...
|
Pvap |
30.01 |
kPa |
307.66 |
Measure...
|
Pvap |
30.00 |
kPa |
307.66 |
Measure...
|
Pvap |
30.70 |
kPa |
308.15 |
Article...
|
Pvap |
30.68 |
kPa |
308.28 |
Measure...
|
Pvap |
32.44 |
kPa |
309.54 |
Isobari...
|
Pvap |
32.97 |
kPa |
310.14 |
Measure...
|
Pvap |
35.07 |
kPa |
311.47 |
Isobari...
|
Pvap |
35.01 |
kPa |
311.56 |
Measure...
|
Pvap |
35.53 |
kPa |
311.96 |
Measure...
|
Pvap |
37.04 |
kPa |
313.15 |
Vapor-L...
|
Pvap |
37.19 |
kPa |
313.15 |
Charact...
|
Pvap |
37.27 |
kPa |
313.15 |
Vapour ...
|
Pvap |
37.54 |
kPa |
313.15 |
Phase e...
|
Pvap |
37.42 |
kPa |
313.15 |
Measure...
|
Pvap |
37.90 |
kPa |
313.20 |
Isother...
|
Pvap |
37.51 |
kPa |
313.25 |
Isobari...
|
Pvap |
37.95 |
kPa |
313.70 |
Measure...
|
Pvap |
39.98 |
kPa |
314.84 |
Isobari...
|
Pvap |
40.01 |
kPa |
315.02 |
Measure...
|
Pvap |
40.10 |
kPa |
315.07 |
Measure...
|
Pvap |
41.16 |
kPa |
315.74 |
Vapour ...
|
Pvap |
42.30 |
kPa |
316.51 |
Measure...
|
Pvap |
42.44 |
kPa |
316.52 |
Isobari...
|
Pvap |
44.59 |
kPa |
317.91 |
Measure...
|
Pvap |
45.02 |
kPa |
317.92 |
Isobari...
|
Pvap |
45.01 |
kPa |
318.15 |
Measure...
|
Pvap |
47.45 |
kPa |
319.49 |
Isobari...
|
Pvap |
47.35 |
kPa |
319.58 |
Measure...
|
Pvap |
50.01 |
kPa |
320.76 |
Isobari...
|
Pvap |
49.63 |
kPa |
320.83 |
Measure...
|
Pvap |
50.01 |
kPa |
321.03 |
Measure...
|
Pvap |
50.62 |
kPa |
321.32 |
Vapour ...
|
Pvap |
51.87 |
kPa |
322.02 |
Measure...
|
Pvap |
52.52 |
kPa |
322.26 |
Isobari...
|
Pvap |
53.91 |
kPa |
323.15 |
Vapor-L...
|
Pvap |
54.39 |
kPa |
323.15 |
Phase e...
|
Pvap |
54.11 |
kPa |
323.15 |
Measure...
|
Pvap |
55.03 |
kPa |
323.37 |
Isobari...
|
Pvap |
54.51 |
kPa |
323.45 |
Measure...
|
Pvap |
55.01 |
kPa |
323.68 |
Measure...
|
Pvap |
56.42 |
kPa |
324.35 |
Measure...
|
Pvap |
57.32 |
kPa |
324.59 |
Isobari...
|
Pvap |
59.15 |
kPa |
325.74 |
Measure...
|
Pvap |
60.07 |
kPa |
325.89 |
Isobari...
|
Pvap |
60.00 |
kPa |
326.11 |
Isobari...
|
Pvap |
60.01 |
kPa |
326.15 |
Measure...
|
Pvap |
62.46 |
kPa |
326.95 |
Isobari...
|
Pvap |
62.05 |
kPa |
327.09 |
Measure...
|
Pvap |
64.02 |
kPa |
327.99 |
Measure...
|
Pvap |
64.20 |
kPa |
328.02 |
Vapour ...
|
Pvap |
64.77 |
kPa |
328.09 |
Isobari...
|
Pvap |
65.01 |
kPa |
328.45 |
Measure...
|
Pvap |
66.61 |
kPa |
329.13 |
Measure...
|
Pvap |
67.22 |
kPa |
329.19 |
Isobari...
|
Pvap |
65.63 |
kPa |
329.22 |
P-x dat...
|
Pvap |
68.93 |
kPa |
330.14 |
Measure...
|
Pvap |
69.64 |
kPa |
330.16 |
Isobari...
|
Pvap |
70.01 |
kPa |
330.62 |
Measure...
|
Pvap |
70.86 |
kPa |
330.93 |
Measure...
|
Pvap |
72.45 |
kPa |
331.45 |
Isobari...
|
Pvap |
73.11 |
kPa |
331.87 |
Measure...
|
Pvap |
74.82 |
kPa |
332.28 |
Isobari...
|
Pvap |
74.53 |
kPa |
332.40 |
Vapour ...
|
Pvap |
75.62 |
kPa |
332.87 |
Measure...
|
Pvap |
76.32 |
kPa |
333.15 |
Vapor-L...
|
Pvap |
77.48 |
kPa |
333.48 |
Isobari...
|
Pvap |
78.04 |
kPa |
333.77 |
Measure...
|
Pvap |
79.84 |
kPa |
334.39 |
Isobari...
|
Pvap |
80.01 |
kPa |
334.60 |
Measure...
|
Pvap |
80.00 |
kPa |
334.61 |
Isobari...
|
Pvap |
80.11 |
kPa |
334.61 |
Measure...
|
Pvap |
82.31 |
kPa |
335.33 |
Isobari...
|
Pvap |
82.94 |
kPa |
335.65 |
Measure...
|
Pvap |
84.88 |
kPa |
336.26 |
Isobari...
|
Pvap |
84.85 |
kPa |
336.32 |
Vapour ...
|
Pvap |
85.40 |
kPa |
336.53 |
Measure...
|
Pvap |
87.26 |
kPa |
337.14 |
Isobari...
|
Pvap |
87.73 |
kPa |
337.38 |
Measure...
|
Pvap |
89.85 |
kPa |
338.02 |
Isobari...
|
Pvap |
89.92 |
kPa |
338.15 |
Vapor-L...
|
Pvap |
90.01 |
kPa |
338.21 |
Measure...
|
Pvap |
90.28 |
kPa |
338.26 |
Measure...
|
Pvap |
92.35 |
kPa |
338.91 |
Isobari...
|
Pvap |
93.18 |
kPa |
339.25 |
Measure...
|
Pvap |
94.85 |
kPa |
339.73 |
Isobari...
|
Pvap |
95.79 |
kPa |
340.10 |
Measure...
|
Pvap |
96.72 |
kPa |
340.39 |
Vapour ...
|
Pvap |
97.02 |
kPa |
340.44 |
Isobari...
|
Pvap |
98.28 |
kPa |
340.92 |
Measure...
|
Pvap |
99.08 |
kPa |
341.17 |
Measure...
|
Pvap |
100.00 |
kPa |
341.48 |
Isobari...
|
Pvap |
100.39 |
kPa |
341.60 |
Measure...
|
Pvap |
101.32 |
kPa |
341.76 |
Isobari...
|
Pvap |
101.32 |
kPa |
341.79 |
Isobari...
|
Pvap |
101.30 |
kPa |
341.79 |
Measure...
|
Pvap |
101.33 |
kPa |
341.85 |
Vapor-L...
|
Pvap |
101.31 |
kPa |
341.86 |
Vapour ...
|
Pvap |
101.32 |
kPa |
341.88 |
Measure...
|
Pvap |
101.30 |
kPa |
341.88 |
Isobari...
|
Pvap |
101.80 |
kPa |
342.02 |
Vapour ...
|
Pvap |
101.81 |
kPa |
342.08 |
Measure...
|
Pvap |
102.22 |
kPa |
342.15 |
Vapour ...
|
Pvap |
102.83 |
kPa |
342.34 |
Measure...
|
Pvap |
104.95 |
kPa |
343.01 |
Measure...
|
Pvap |
106.98 |
kPa |
343.62 |
Measure...
|
Pvap |
110.01 |
kPa |
344.52 |
Measure...
|
Pvap |
110.65 |
kPa |
344.69 |
Measure...
|
Pvap |
113.16 |
kPa |
345.43 |
Measure...
|
Pvap |
115.31 |
kPa |
346.05 |
Measure...
|
Pvap |
117.46 |
kPa |
346.66 |
Measure...
|
Pvap |
119.99 |
kPa |
347.36 |
Measure...
|
Pvap |
122.52 |
kPa |
348.05 |
Measure...
|
Pvap |
122.84 |
kPa |
348.15 |
Measure...
|
Pvap |
123.03 |
kPa |
348.15 |
Measure...
|
Pvap |
123.12 |
kPa |
348.15 |
Measure...
|
Pvap |
124.01 |
kPa |
348.44 |
Measure...
|
Pvap |
126.23 |
kPa |
349.04 |
Measure...
|
Pvap |
128.44 |
kPa |
349.61 |
Measure...
|
Pvap |
129.32 |
kPa |
349.82 |
Measure...
|
Pvap |
131.23 |
kPa |
350.34 |
Measure...
|
Pvap |
133.07 |
kPa |
350.82 |
Measure...
|
Pvap |
135.49 |
kPa |
351.42 |
Measure...
|
Pvap |
137.54 |
kPa |
351.93 |
Measure...
|
Pvap |
139.99 |
kPa |
352.53 |
Measure...
|
Pvap |
140.84 |
kPa |
352.74 |
Vapour ...
|
Pvap |
141.31 |
kPa |
352.83 |
Measure...
|
Pvap |
142.40 |
kPa |
353.15 |
Vapor L...
|
Pvap |
142.80 |
kPa |
353.22 |
Measure...
|
Pvap |
145.75 |
kPa |
353.87 |
Measure...
|
Pvap |
146.70 |
kPa |
354.14 |
Vapour ...
|
Pvap |
147.04 |
kPa |
354.23 |
Measure...
|
Pvap |
149.34 |
kPa |
354.71 |
Measure...
|
Pvap |
152.14 |
kPa |
355.40 |
Measure...
|
Pvap |
153.31 |
kPa |
355.66 |
Measure...
|
Pvap |
155.14 |
kPa |
356.04 |
Measure...
|
Pvap |
157.29 |
kPa |
356.52 |
Measure...
|
Pvap |
159.38 |
kPa |
357.01 |
Measure...
|
Pvap |
161.05 |
kPa |
357.38 |
Measure...
|
Pvap |
162.94 |
kPa |
357.80 |
Measure...
|
Pvap |
166.02 |
kPa |
358.47 |
Measure...
|
Pvap |
167.98 |
kPa |
358.88 |
Measure...
|
Pvap |
169.31 |
kPa |
359.18 |
Measure...
|
Pvap |
171.84 |
kPa |
359.69 |
Measure...
|
Pvap |
172.89 |
kPa |
359.90 |
Measure...
|
Pvap |
175.78 |
kPa |
360.51 |
Measure...
|
Pvap |
177.31 |
kPa |
360.80 |
Measure...
|
Pvap |
178.41 |
kPa |
361.06 |
Vapour ...
|
Pvap |
178.67 |
kPa |
361.09 |
Measure...
|
Pvap |
180.95 |
kPa |
361.54 |
Measure...
|
Pvap |
182.61 |
kPa |
361.86 |
Measure...
|
Pvap |
185.32 |
kPa |
362.43 |
Measure...
|
Pvap |
186.64 |
kPa |
362.68 |
Measure...
|
Pvap |
188.20 |
kPa |
362.98 |
Measure...
|
Pvap |
188.05 |
kPa |
363.15 |
Vapor-L...
|
Pvap |
189.72 |
kPa |
363.29 |
Vapour ...
|
Pvap |
191.05 |
kPa |
363.52 |
Measure...
|
Pvap |
193.35 |
kPa |
363.95 |
Measure...
|
Pvap |
214.05 |
kPa |
367.78 |
Vapour ...
|
Pvap |
247.22 |
kPa |
373.15 |
Measure...
|
Pvap |
245.99 |
kPa |
373.15 |
Measure...
|
Pvap |
245.79 |
kPa |
373.15 |
Measure...
|
Pvap |
254.29 |
kPa |
374.40 |
Vapour ...
|
Pvap |
281.37 |
kPa |
378.42 |
Vapour ...
|
Pvap |
284.18 |
kPa |
378.82 |
Vapour ...
|
Pvap |
324.95 |
kPa |
384.30 |
Vapour ...
|
Pvap |
378.71 |
kPa |
390.79 |
Vapour ...
|
Pvap |
410.00 |
kPa |
393.15 |
In Situ...
|
Pvap |
402.46 |
kPa |
393.44 |
Vapour ...
|
Pvap |
417.93 |
kPa |
395.10 |
Vapour ...
|
Pvap |
465.31 |
kPa |
399.91 |
Vapour ...
|
Pvap |
503.73 |
kPa |
403.55 |
Vapour ...
|
Pvap |
509.54 |
kPa |
404.08 |
Vapour ...
|
Pvap |
551.62 |
kPa |
407.80 |
Vapour ...
|
Pvap |
601.70 |
kPa |
411.96 |
Vapour ...
|
Pvap |
633.00 |
kPa |
413.15 |
In Situ...
|
Pvap |
664.70 |
kPa |
416.84 |
Vapour ...
|
Pvap |
695.49 |
kPa |
419.10 |
Vapour ...
|
Pvap |
720.50 |
kPa |
420.88 |
Vapour ...
|
Pvap |
796.06 |
kPa |
425.99 |
Vapour ...
|
Pvap |
829.29 |
kPa |
428.13 |
Vapour ...
|
Pvap |
871.03 |
kPa |
430.72 |
Vapour ...
|
Pvap |
918.00 |
kPa |
433.15 |
In Situ...
|
Pvap |
911.85 |
kPa |
433.17 |
Vapour ...
|
Pvap |
992.37 |
kPa |
437.76 |
Vapour ...
|
Pvap |
1031.74 |
kPa |
439.90 |
Vapour ...
|
Pvap |
1088.58 |
kPa |
442.89 |
Vapour ...
|
Pvap |
1170.51 |
kPa |
447.01 |
Vapour ...
|
Pvap |
1180.73 |
kPa |
447.50 |
Vapour ...
|
Pvap |
1301.00 |
kPa |
453.15 |
In Situ...
|
Pvap |
1310.01 |
kPa |
453.54 |
Vapour ...
|
Pvap |
1399.98 |
kPa |
457.47 |
Vapour ...
|
Pvap |
1504.52 |
kPa |
461.81 |
Vapour ...
|
Pvap |
1584.85 |
kPa |
465.00 |
Vapour ...
|
Pvap |
1725.01 |
kPa |
470.26 |
Vapour ...
|
Pvap |
1801.25 |
kPa |
472.99 |
Vapour ...
|
Pvap |
1961.15 |
kPa |
478.43 |
Vapour ...
|
Pvap |
2057.52 |
kPa |
481.54 |
Vapour ...
|
Pvap |
2106.53 |
kPa |
483.08 |
Vapour ...
|
Pvap |
2109.00 |
kPa |
483.15 |
Measure...
|
Pvap |
2195.23 |
kPa |
485.80 |
Vapour ...
|
Pvap |
2278.56 |
kPa |
488.27 |
Vapour ...
|
Pvap |
2450.36 |
kPa |
493.14 |
Vapour ...
|
Pvap |
2453.00 |
kPa |
493.15 |
Measure...
|
Pvap |
2623.45 |
kPa |
497.75 |
Vapour ...
|
Pvap |
2701.96 |
kPa |
499.76 |
Vapour ...
|
Pvap |
2764.64 |
kPa |
501.32 |
Vapour ...
|
Pvap |
2838.00 |
kPa |
503.15 |
Measure...
|
Pvap |
2876.83 |
kPa |
504.04 |
Vapour ...
|
n0 |
[1.36150; 1.37590] |
|
[293.15; 318.15] |
|
|
n0 |
1.37590 |
|
293.15 |
Physica...
|
n0 |
1.37486 |
|
293.15 |
Isobari...
|
n0 |
1.37490 |
|
293.15 |
Vapour ...
|
n0 |
1.37250 |
|
293.15 |
Isother...
|
n0 |
1.37480 |
|
293.15 |
Isobari...
|
n0 |
1.37480 |
|
293.15 |
Vapor L...
|
n0 |
1.37495 |
|
293.15 |
Mixing ...
|
n0 |
1.37510 |
|
293.15 |
Solubil...
|
n0 |
1.37520 |
|
293.15 |
A novel...
|
n0 |
1.37500 |
|
293.20 |
Liquid ...
|
n0 |
1.37514 |
|
298.10 |
Vapor-L...
|
n0 |
1.37440 |
|
298.10 |
Excess ...
|
n0 |
1.37226 |
|
298.15 |
KDB
|
n0 |
1.37374 |
|
298.15 |
Vapor-l...
|
n0 |
1.37320 |
|
298.15 |
Physica...
|
n0 |
1.37374 |
|
298.15 |
Experim...
|
n0 |
1.37360 |
|
298.15 |
Excess ...
|
n0 |
1.37240 |
|
298.15 |
Phase e...
|
n0 |
1.37287 |
|
298.15 |
Thiophe...
|
n0 |
1.37230 |
|
298.15 |
(Vapor ...
|
n0 |
1.37230 |
|
298.15 |
Physica...
|
n0 |
1.37217 |
|
298.15 |
A study...
|
n0 |
1.37217 |
|
298.15 |
Mixing ...
|
n0 |
1.37226 |
|
298.15 |
Effect ...
|
n0 |
1.37234 |
|
298.15 |
Extract...
|
n0 |
1.37241 |
|
298.15 |
Ethanol...
|
n0 |
1.37510 |
|
298.15 |
Ternary...
|
n0 |
1.37220 |
|
298.15 |
Volumet...
|
n0 |
1.37240 |
|
298.15 |
Isother...
|
n0 |
1.37237 |
|
298.15 |
Liquid ...
|
n0 |
1.37287 |
|
298.15 |
Phase b...
|
n0 |
1.37226 |
|
298.15 |
Separat...
|
n0 |
1.37250 |
|
298.15 |
Measure...
|
n0 |
1.37280 |
|
298.15 |
Liquid-...
|
n0 |
1.37280 |
|
298.15 |
Liquid-...
|
n0 |
1.37280 |
|
298.15 |
Density...
|
n0 |
1.37230 |
|
298.15 |
Vapor-L...
|
n0 |
1.37287 |
|
298.15 |
Liquid-...
|
n0 |
1.37220 |
|
298.15 |
Solubil...
|
n0 |
1.37470 |
|
298.15 |
Solubil...
|
n0 |
1.37220 |
|
298.15 |
Solubil...
|
n0 |
1.37230 |
|
298.15 |
Densiti...
|
n0 |
1.37240 |
|
298.15 |
Vapor-L...
|
n0 |
1.37240 |
|
298.15 |
Solubil...
|
n0 |
1.37230 |
|
298.15 |
Vapor-L...
|
n0 |
1.37287 |
|
298.15 |
Extract...
|
n0 |
1.37234 |
|
298.15 |
Separat...
|
n0 |
1.37450 |
|
298.15 |
Densiti...
|
n0 |
1.37230 |
|
298.15 |
Multipr...
|
n0 |
1.37240 |
|
298.15 |
Physica...
|
n0 |
1.37234 |
|
298.15 |
Liquid-...
|
n0 |
1.36980 |
|
303.15 |
Density...
|
n0 |
1.36936 |
|
303.15 |
Mixing ...
|
n0 |
1.37070 |
|
303.15 |
Excess ...
|
n0 |
1.37090 |
|
303.15 |
Physica...
|
n0 |
1.36700 |
|
308.15 |
Density...
|
n0 |
1.36760 |
|
308.15 |
Excess ...
|
n0 |
1.36150 |
|
318.15 |
Multipr...
|
ρl |
[617.07; 677.18] |
kg/m3 |
[273.15; 338.15] |
|
|
ρl |
677.18 |
kg/m3 |
273.15 |
Experim...
|
ρl |
672.79 |
kg/m3 |
278.15 |
Experim...
|
ρl |
668.37 |
kg/m3 |
283.15 |
Experim...
|
ρl |
663.91 |
kg/m3 |
288.15 |
Experim...
|
ρl |
659.00 |
kg/m3 |
293.00 |
KDB
|
ρl |
659.40 |
kg/m3 |
293.15 |
Solubil...
|
ρl |
660.00 |
kg/m3 |
293.15 |
Experim...
|
ρl |
659.40 |
kg/m3 |
293.15 |
Densiti...
|
ρl |
660.51 |
kg/m3 |
293.15 |
Surface...
|
ρl |
659.42 |
kg/m3 |
293.15 |
Experim...
|
ρl |
659.40 |
kg/m3 |
293.15 |
A therm...
|
ρl |
654.89 |
kg/m3 |
298.10 |
Excess ...
|
ρl |
655.07 |
kg/m3 |
298.15 |
Experim...
|
ρl |
655.00 |
kg/m3 |
298.15 |
VLE mea...
|
ρl |
655.07 |
kg/m3 |
298.15 |
Surface...
|
ρl |
655.07 |
kg/m3 |
298.15 |
Densiti...
|
ρl |
655.12 |
kg/m3 |
298.15 |
Liquid-...
|
ρl |
655.20 |
kg/m3 |
298.15 |
Capacit...
|
ρl |
655.09 |
kg/m3 |
298.15 |
Desulfu...
|
ρl |
654.89 |
kg/m3 |
298.15 |
Experim...
|
ρl |
655.25 |
kg/m3 |
298.15 |
Thermod...
|
ρl |
654.90 |
kg/m3 |
298.15 |
Vapor-L...
|
ρl |
655.20 |
kg/m3 |
298.15 |
Ionic l...
|
ρl |
655.42 |
kg/m3 |
298.15 |
Excess ...
|
ρl |
654.80 |
kg/m3 |
298.15 |
Viscosi...
|
ρl |
654.00 |
kg/m3 |
298.15 |
Isother...
|
ρl |
668.00 |
kg/m3 |
298.15 |
Liquid-...
|
ρl |
654.70 |
kg/m3 |
298.15 |
Thermop...
|
ρl |
654.80 |
kg/m3 |
298.15 |
Phase d...
|
ρl |
655.21 |
kg/m3 |
298.15 |
Volumet...
|
ρl |
655.09 |
kg/m3 |
298.15 |
Hexyl d...
|
ρl |
655.10 |
kg/m3 |
298.15 |
Evaluat...
|
ρl |
659.00 |
kg/m3 |
298.15 |
Liquid ...
|
ρl |
654.82 |
kg/m3 |
298.15 |
Excess ...
|
ρl |
654.82 |
kg/m3 |
298.15 |
Topolog...
|
ρl |
655.20 |
kg/m3 |
298.15 |
Applica...
|
ρl |
655.20 |
kg/m3 |
298.15 |
Cation ...
|
ρl |
655.19 |
kg/m3 |
298.15 |
Phase b...
|
ρl |
654.90 |
kg/m3 |
298.15 |
Excess ...
|
ρl |
654.90 |
kg/m3 |
298.15 |
Fully a...
|
ρl |
654.90 |
kg/m3 |
298.15 |
Densiti...
|
ρl |
654.70 |
kg/m3 |
298.15 |
Experim...
|
ρl |
654.76 |
kg/m3 |
298.15 |
Solubil...
|
ρl |
654.80 |
kg/m3 |
298.15 |
A therm...
|
ρl |
655.19 |
kg/m3 |
298.15 |
SAFT-.g...
|
ρl |
654.70 |
kg/m3 |
298.15 |
Surface...
|
ρl |
655.29 |
kg/m3 |
298.20 |
Isobari...
|
ρl |
655.04 |
kg/m3 |
298.20 |
Apparen...
|
ρl |
652.90 |
kg/m3 |
303.15 |
Unravel...
|
ρl |
650.64 |
kg/m3 |
303.15 |
Volumet...
|
ρl |
650.33 |
kg/m3 |
303.15 |
Experim...
|
ρl |
650.20 |
kg/m3 |
303.15 |
A therm...
|
ρl |
650.90 |
kg/m3 |
303.15 |
Volumet...
|
ρl |
650.21 |
kg/m3 |
303.15 |
Solubil...
|
ρl |
646.03 |
kg/m3 |
308.15 |
Volumet...
|
ρl |
645.40 |
kg/m3 |
308.15 |
A therm...
|
ρl |
645.43 |
kg/m3 |
308.15 |
Solubil...
|
ρl |
645.40 |
kg/m3 |
308.15 |
Thermop...
|
ρl |
645.73 |
kg/m3 |
308.15 |
Experim...
|
ρl |
642.00 |
kg/m3 |
313.15 |
Experim...
|
ρl |
641.37 |
kg/m3 |
313.15 |
Volumet...
|
ρl |
641.70 |
kg/m3 |
313.15 |
Volumet...
|
ρl |
641.20 |
kg/m3 |
313.15 |
Experim...
|
ρl |
640.70 |
kg/m3 |
313.15 |
A therm...
|
ρl |
641.08 |
kg/m3 |
313.15 |
Experim...
|
ρl |
640.75 |
kg/m3 |
313.15 |
Solubil...
|
ρl |
636.38 |
kg/m3 |
318.15 |
Experim...
|
ρl |
636.67 |
kg/m3 |
318.15 |
Volumet...
|
ρl |
636.20 |
kg/m3 |
318.15 |
Thermop...
|
ρl |
631.92 |
kg/m3 |
323.15 |
Volumet...
|
ρl |
630.90 |
kg/m3 |
323.15 |
Volumet...
|
ρl |
631.20 |
kg/m3 |
323.15 |
Thermop...
|
ρl |
631.64 |
kg/m3 |
323.15 |
Experim...
|
ρl |
626.84 |
kg/m3 |
328.15 |
Experim...
|
ρl |
626.40 |
kg/m3 |
328.15 |
Thermop...
|
ρl |
621.99 |
kg/m3 |
333.15 |
Experim...
|
ρl |
617.07 |
kg/m3 |
338.15 |
Experim...
|
ΔfusS |
[69.38; 73.54] |
J/mol×K |
[177.84; 178.60] |
|
ΔfusS |
73.54 |
J/mol×K |
177.84 |
NIST
|
ΔfusS |
69.38 |
J/mol×K |
177.90 |
NIST
|
ΔfusS |
73.30 |
J/mol×K |
177.90 |
NIST
|
ΔfusS |
70.44 |
J/mol×K |
178.60 |
NIST
|
csound,fluid |
[109.70; 1121.40] |
m/s |
[288.15; 506.15] |
|
|
csound,fluid |
1121.40 |
m/s |
288.15 |
Excess ...
|
csound,fluid |
1098.90 |
m/s |
293.15 |
Acousti...
|
csound,fluid |
1099.00 |
m/s |
293.15 |
Excess ...
|
csound,fluid |
1098.00 |
m/s |
293.15 |
Tempera...
|
csound,fluid |
1098.10 |
m/s |
293.15 |
Speed o...
|
csound,fluid |
1076.30 |
m/s |
298.15 |
Excess ...
|
csound,fluid |
1076.00 |
m/s |
298.15 |
Tempera...
|
csound,fluid |
1076.00 |
m/s |
298.15 |
Speed o...
|
csound,fluid |
1111.20 |
m/s |
300.09 |
Speed o...
|
csound,fluid |
1073.00 |
m/s |
300.15 |
Measure...
|
csound,fluid |
1054.30 |
m/s |
303.15 |
Speed o...
|
csound,fluid |
1054.00 |
m/s |
303.15 |
Tempera...
|
csound,fluid |
1053.60 |
m/s |
303.15 |
Excess ...
|
csound,fluid |
1032.00 |
m/s |
308.15 |
Tempera...
|
csound,fluid |
1031.10 |
m/s |
308.15 |
Excess ...
|
csound,fluid |
1031.80 |
m/s |
308.15 |
Speed o...
|
csound,fluid |
1010.00 |
m/s |
313.15 |
Tempera...
|
csound,fluid |
1009.90 |
m/s |
313.15 |
Speed o...
|
csound,fluid |
993.00 |
m/s |
313.15 |
Measure...
|
csound,fluid |
988.00 |
m/s |
318.15 |
Tempera...
|
csound,fluid |
987.70 |
m/s |
318.15 |
Speed o...
|
csound,fluid |
965.70 |
m/s |
323.15 |
Speed o...
|
csound,fluid |
966.00 |
m/s |
323.15 |
Tempera...
|
csound,fluid |
944.00 |
m/s |
328.15 |
Tempera...
|
csound,fluid |
926.80 |
m/s |
328.15 |
Measure...
|
csound,fluid |
943.70 |
m/s |
328.15 |
Speed o...
|
csound,fluid |
921.30 |
m/s |
333.15 |
Speed o...
|
csound,fluid |
921.00 |
m/s |
333.15 |
Tempera...
|
csound,fluid |
899.70 |
m/s |
338.15 |
Speed o...
|
csound,fluid |
900.00 |
m/s |
338.15 |
Tempera...
|
csound,fluid |
882.70 |
m/s |
343.15 |
Measure...
|
csound,fluid |
877.80 |
m/s |
343.15 |
Speed o...
|
csound,fluid |
878.00 |
m/s |
343.15 |
Tempera...
|
csound,fluid |
856.00 |
m/s |
348.15 |
Tempera...
|
csound,fluid |
855.90 |
m/s |
348.15 |
Speed o...
|
csound,fluid |
898.50 |
m/s |
353.12 |
Speed o...
|
csound,fluid |
834.20 |
m/s |
353.15 |
Speed o...
|
csound,fluid |
834.00 |
m/s |
353.15 |
Tempera...
|
csound,fluid |
838.80 |
m/s |
353.15 |
Measure...
|
csound,fluid |
812.10 |
m/s |
358.15 |
Speed o...
|
csound,fluid |
812.00 |
m/s |
358.15 |
Tempera...
|
csound,fluid |
790.00 |
m/s |
363.15 |
Tempera...
|
csound,fluid |
790.30 |
m/s |
363.15 |
Speed o...
|
csound,fluid |
794.90 |
m/s |
363.15 |
Measure...
|
csound,fluid |
768.00 |
m/s |
368.15 |
Tempera...
|
csound,fluid |
768.40 |
m/s |
368.15 |
Speed o...
|
csound,fluid |
751.00 |
m/s |
373.15 |
Measure...
|
csound,fluid |
747.00 |
m/s |
373.15 |
Tempera...
|
csound,fluid |
746.60 |
m/s |
373.15 |
Speed o...
|
csound,fluid |
707.20 |
m/s |
383.15 |
Measure...
|
csound,fluid |
663.40 |
m/s |
393.15 |
Measure...
|
csound,fluid |
619.50 |
m/s |
403.15 |
Measure...
|
csound,fluid |
705.90 |
m/s |
403.17 |
Speed o...
|
csound,fluid |
575.60 |
m/s |
413.15 |
Measure...
|
csound,fluid |
531.60 |
m/s |
423.15 |
Measure...
|
csound,fluid |
487.50 |
m/s |
433.15 |
Measure...
|
csound,fluid |
443.10 |
m/s |
443.15 |
Measure...
|
csound,fluid |
420.70 |
m/s |
448.15 |
Measure...
|
csound,fluid |
513.00 |
m/s |
453.15 |
Speed o...
|
csound,fluid |
398.20 |
m/s |
453.15 |
Measure...
|
csound,fluid |
375.60 |
m/s |
458.15 |
Measure...
|
csound,fluid |
352.80 |
m/s |
463.15 |
Measure...
|
csound,fluid |
329.80 |
m/s |
468.15 |
Measure...
|
csound,fluid |
306.40 |
m/s |
473.15 |
Measure...
|
csound,fluid |
282.60 |
m/s |
478.15 |
Measure...
|
csound,fluid |
258.20 |
m/s |
483.15 |
Measure...
|
csound,fluid |
233.00 |
m/s |
488.15 |
Measure...
|
csound,fluid |
206.40 |
m/s |
493.15 |
Measure...
|
csound,fluid |
177.30 |
m/s |
498.15 |
Measure...
|
csound,fluid |
323.70 |
m/s |
503.13 |
Speed o...
|
csound,fluid |
142.00 |
m/s |
503.15 |
Measure...
|
csound,fluid |
109.70 |
m/s |
506.15 |
Measure...
|
γ |
[0.02; 0.02] |
N/m |
[283.15; 328.15] |
|
|
γ |
0.02 |
N/m |
283.15 |
Surface...
|
γ |
0.02 |
N/m |
283.15 |
Study o...
|
γ |
0.02 |
N/m |
288.15 |
Surface...
|
γ |
0.02 |
N/m |
288.15 |
Interfa...
|
γ |
0.02 |
N/m |
288.15 |
Study o...
|
γ |
0.02 |
N/m |
293.15 |
Surface...
|
γ |
0.02 |
N/m |
293.15 |
Surface...
|
γ |
0.02 |
N/m |
293.15 |
Study o...
|
γ |
0.02 |
N/m |
293.15 |
Surface...
|
γ |
0.02 |
N/m |
293.20 |
KDB
|
γ |
0.02 |
N/m |
298.15 |
Surface...
|
γ |
0.02 |
N/m |
298.15 |
Study o...
|
γ |
0.02 |
N/m |
298.15 |
Surface...
|
γ |
0.02 |
N/m |
298.15 |
Surface...
|
γ |
0.02 |
N/m |
298.15 |
Interfa...
|
γ |
0.02 |
N/m |
303.15 |
Study o...
|
γ |
0.02 |
N/m |
303.15 |
Surface...
|
γ |
0.02 |
N/m |
303.15 |
Surface...
|
γ |
0.02 |
N/m |
303.15 |
Surface...
|
γ |
0.02 |
N/m |
308.15 |
Surface...
|
γ |
0.02 |
N/m |
308.15 |
Surface...
|
γ |
0.02 |
N/m |
308.15 |
Surface...
|
γ |
0.02 |
N/m |
308.15 |
Interfa...
|
γ |
0.02 |
N/m |
308.15 |
Study o...
|
γ |
0.02 |
N/m |
313.15 |
Study o...
|
γ |
0.02 |
N/m |
313.15 |
Surface...
|
γ |
0.02 |
N/m |
313.15 |
Surface...
|
γ |
0.02 |
N/m |
313.15 |
Surface...
|
γ |
0.02 |
N/m |
318.15 |
Interfa...
|
γ |
0.02 |
N/m |
328.15 |
Interfa...
|
λ |
[0.01; 0.01] |
W/m×K |
[292.90; 322.74] |
|
|
λ |
0.01 |
W/m×K |
292.90 |
Thermal...
|
λ |
0.01 |
W/m×K |
296.63 |
Thermal...
|
λ |
0.01 |
W/m×K |
298.79 |
Thermal...
|
λ |
0.01 |
W/m×K |
313.06 |
Thermal...
|
λ |
0.01 |
W/m×K |
322.74 |
Thermal...
|
Pressure Dependent Properties
Property |
Value |
Unit |
Pressure (kPa) |
Source |
Tboil |
340.35 |
K |
96.60 |
Low cos...
|
Datasets
-
Molar heat capacity at constant pressure, J/K/mol (1)
-
Viscosity, Pa*s (1)
-
Mass density, kg/m3 (7)
-
Speed of sound, m/s (1)
-
Thermal conductivity, W/m/K (1)
Molar heat capacity at constant pressure, J/K/mol
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Molar heat capacity at constant pressure, J/K/mol - Liquid |
323.15 |
140.00 |
203.63 |
328.15 |
140.00 |
205.70 |
333.15 |
140.00 |
207.85 |
323.15 |
10090.00 |
200.62 |
328.15 |
10090.00 |
202.43 |
333.15 |
10090.00 |
204.49 |
338.15 |
10090.00 |
206.13 |
343.15 |
10090.00 |
208.11 |
348.15 |
10090.00 |
210.10 |
353.15 |
10090.00 |
211.91 |
358.15 |
10090.00 |
214.15 |
363.15 |
10090.00 |
216.04 |
368.15 |
10090.00 |
218.37 |
Reference
|
Viscosity, Pa*s
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Viscosity, Pa*s - Liquid |
273.15 |
100.00 |
0.0004 |
273.15 |
10000.00 |
0.0004 |
273.15 |
20000.00 |
0.0005 |
273.15 |
30000.00 |
0.0005 |
293.15 |
100.00 |
0.0003 |
293.15 |
10000.00 |
0.0003 |
293.15 |
20000.00 |
0.0004 |
293.15 |
30000.00 |
0.0004 |
313.15 |
100.00 |
0.0003 |
313.15 |
10000.00 |
0.0003 |
313.15 |
20000.00 |
0.0003 |
313.15 |
30000.00 |
0.0004 |
333.15 |
100.00 |
0.0002 |
333.15 |
10000.00 |
0.0002 |
333.15 |
20000.00 |
0.0003 |
333.15 |
30000.00 |
0.0003 |
Reference
|
Mass density, kg/m3
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
293.22 |
1999.00 |
661.4 |
293.22 |
3994.00 |
663.53 |
293.22 |
5999.00 |
665.43 |
293.22 |
8007.00 |
667.57 |
293.23 |
10003.00 |
669.41 |
293.23 |
13000.00 |
672.26 |
293.23 |
16006.00 |
675.2 |
293.23 |
19000.00 |
677.83 |
293.22 |
22004.00 |
680.38 |
293.23 |
25002.00 |
682.87 |
293.22 |
28004.00 |
685.01 |
293.23 |
30001.00 |
686.72 |
313.10 |
2005.00 |
643.6 |
313.10 |
3997.00 |
645.97 |
313.10 |
5999.00 |
648.24 |
313.10 |
8000.00 |
650.44 |
313.10 |
9999.00 |
652.57 |
313.10 |
12997.00 |
655.73 |
313.10 |
15999.00 |
659.0 |
313.10 |
18003.00 |
661.04 |
313.10 |
21999.00 |
664.77 |
313.10 |
24998.00 |
667.58 |
313.10 |
28001.00 |
670.32 |
313.10 |
30004.00 |
672.03 |
333.00 |
2004.00 |
624.85 |
333.00 |
4002.00 |
627.59 |
333.00 |
6003.00 |
630.29 |
333.00 |
8005.00 |
632.82 |
333.00 |
10008.00 |
635.78 |
333.00 |
12998.00 |
639.36 |
333.00 |
16002.00 |
642.74 |
333.00 |
19000.00 |
646.04 |
333.00 |
21993.00 |
649.32 |
333.00 |
25001.00 |
652.41 |
333.00 |
28000.00 |
655.31 |
333.00 |
30005.00 |
657.29 |
353.15 |
2003.00 |
605.15 |
353.14 |
4001.00 |
608.43 |
353.15 |
5997.00 |
611.57 |
353.14 |
8003.00 |
614.97 |
353.15 |
10009.00 |
618.0 |
353.15 |
13000.00 |
622.08 |
353.14 |
15997.00 |
625.92 |
353.15 |
19000.00 |
629.87 |
353.14 |
21998.00 |
633.46 |
Reference
|
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
278.15 |
100.00 |
673.3 |
278.15 |
1000.00 |
673.9 |
278.15 |
5000.00 |
677.6 |
278.15 |
10000.00 |
681.8 |
278.15 |
20000.00 |
689.6 |
278.15 |
30000.00 |
696.8 |
278.15 |
40000.00 |
703.2 |
278.15 |
50000.00 |
709.2 |
278.15 |
60000.00 |
715.0 |
298.15 |
100.00 |
656.1 |
298.15 |
1000.00 |
655.9 |
298.15 |
5000.00 |
660.1 |
298.15 |
10000.00 |
665.1 |
298.15 |
20000.00 |
673.9 |
298.15 |
30000.00 |
681.9 |
298.15 |
40000.00 |
689.0 |
298.15 |
50000.00 |
695.5 |
298.15 |
60000.00 |
701.7 |
323.15 |
100.00 |
631.7 |
323.15 |
1000.00 |
633.1 |
323.15 |
5000.00 |
638.2 |
323.15 |
10000.00 |
644.2 |
323.15 |
20000.00 |
654.7 |
323.15 |
30000.00 |
663.9 |
323.15 |
40000.00 |
671.9 |
323.15 |
50000.00 |
679.3 |
323.15 |
60000.00 |
686.1 |
348.15 |
1000.00 |
608.5 |
348.15 |
5000.00 |
614.9 |
348.15 |
10000.00 |
622.1 |
348.15 |
20000.00 |
634.6 |
348.15 |
30000.00 |
645.2 |
348.15 |
40000.00 |
654.4 |
348.15 |
50000.00 |
662.6 |
348.15 |
60000.00 |
670.2 |
373.15 |
1000.00 |
582.6 |
373.15 |
5000.00 |
591.0 |
373.15 |
10000.00 |
600.0 |
373.15 |
20000.00 |
614.8 |
373.15 |
30000.00 |
627.0 |
373.15 |
40000.00 |
637.4 |
373.15 |
50000.00 |
646.6 |
373.15 |
60000.00 |
654.9 |
423.15 |
1000.00 |
521.2 |
423.15 |
5000.00 |
536.9 |
423.15 |
10000.00 |
551.5 |
423.15 |
20000.00 |
573.2 |
423.15 |
30000.00 |
589.7 |
423.15 |
40000.00 |
603.2 |
423.15 |
50000.00 |
614.6 |
423.15 |
60000.00 |
624.8 |
463.15 |
5000.00 |
484.2 |
463.15 |
10000.00 |
508.5 |
463.15 |
20000.00 |
538.9 |
463.15 |
30000.00 |
559.8 |
463.15 |
40000.00 |
575.9 |
463.15 |
50000.00 |
589.3 |
463.15 |
60000.00 |
600.7 |
Reference
|
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
313.12 |
1019.00 |
642.2 |
313.12 |
2044.00 |
643.5 |
313.12 |
3023.00 |
644.6 |
313.12 |
4018.00 |
645.8 |
313.12 |
5016.00 |
647.0 |
313.12 |
6012.00 |
648.1 |
313.12 |
7016.00 |
649.2 |
313.12 |
8016.00 |
650.3 |
313.12 |
9020.00 |
651.4 |
313.12 |
10018.00 |
652.5 |
313.12 |
11020.00 |
653.5 |
313.12 |
12004.00 |
654.6 |
313.12 |
13007.00 |
655.6 |
313.12 |
14015.00 |
656.6 |
313.12 |
15006.00 |
657.6 |
313.12 |
16023.00 |
658.6 |
313.12 |
17015.00 |
659.6 |
313.12 |
18011.00 |
660.5 |
313.12 |
19009.00 |
661.4 |
313.12 |
20016.00 |
662.4 |
313.12 |
20995.00 |
663.3 |
313.12 |
22018.00 |
664.2 |
313.12 |
23018.00 |
665.1 |
313.12 |
24013.00 |
666.0 |
313.12 |
25002.00 |
666.8 |
323.05 |
1030.00 |
633.0 |
323.05 |
2010.00 |
634.3 |
323.05 |
3021.00 |
635.6 |
323.05 |
4018.00 |
636.9 |
323.05 |
5014.00 |
638.1 |
323.05 |
6007.00 |
639.4 |
323.05 |
7010.00 |
640.6 |
323.05 |
8012.00 |
641.8 |
323.05 |
9020.00 |
643.0 |
323.05 |
10008.00 |
644.1 |
323.05 |
11021.00 |
645.2 |
323.05 |
12011.00 |
646.4 |
323.05 |
13007.00 |
647.4 |
323.05 |
14007.00 |
648.5 |
323.05 |
15035.00 |
649.6 |
323.05 |
16011.00 |
650.6 |
323.05 |
17021.00 |
651.6 |
323.05 |
18020.00 |
652.7 |
323.05 |
19013.00 |
653.7 |
323.05 |
20001.00 |
654.6 |
323.05 |
21028.00 |
655.6 |
323.05 |
22004.00 |
656.6 |
323.05 |
23010.00 |
657.5 |
323.05 |
24021.00 |
658.5 |
323.05 |
25018.00 |
659.4 |
332.85 |
1020.00 |
623.5 |
332.85 |
2021.00 |
625.0 |
332.85 |
3022.00 |
626.5 |
332.85 |
4020.00 |
627.8 |
332.85 |
5011.00 |
629.2 |
332.85 |
6016.00 |
630.6 |
332.85 |
7012.00 |
631.9 |
332.85 |
8025.00 |
633.3 |
332.85 |
9012.00 |
634.5 |
332.85 |
10010.00 |
635.7 |
332.85 |
11012.00 |
636.9 |
332.85 |
12019.00 |
638.1 |
332.85 |
13007.00 |
639.2 |
332.85 |
14021.00 |
640.4 |
332.85 |
15014.00 |
641.6 |
332.85 |
16025.00 |
642.8 |
332.85 |
17011.00 |
643.8 |
332.85 |
18035.00 |
644.9 |
332.85 |
19014.00 |
646.0 |
332.85 |
20011.00 |
647.1 |
332.85 |
21015.00 |
648.1 |
332.85 |
22000.00 |
649.1 |
332.85 |
23012.00 |
650.1 |
332.85 |
24022.00 |
651.2 |
332.85 |
25030.00 |
652.2 |
342.73 |
1010.00 |
613.9 |
342.73 |
2010.00 |
615.5 |
342.73 |
3011.00 |
617.1 |
342.73 |
4010.00 |
618.6 |
342.73 |
5005.00 |
620.0 |
342.73 |
6031.00 |
621.6 |
342.73 |
7020.00 |
623.0 |
342.73 |
8009.00 |
624.4 |
342.73 |
9015.00 |
625.7 |
342.73 |
10012.00 |
627.0 |
342.73 |
11006.00 |
628.4 |
342.73 |
12014.00 |
629.7 |
342.73 |
13011.00 |
630.9 |
342.73 |
14014.00 |
632.2 |
342.73 |
15008.00 |
633.4 |
342.73 |
16006.00 |
634.6 |
342.73 |
17021.00 |
635.7 |
342.73 |
18016.00 |
636.9 |
342.73 |
19025.00 |
638.0 |
342.73 |
20037.00 |
639.2 |
342.73 |
21025.00 |
640.3 |
342.73 |
22016.00 |
641.3 |
342.73 |
23010.00 |
642.5 |
342.73 |
24023.00 |
643.5 |
342.73 |
25006.00 |
644.5 |
352.56 |
1017.00 |
604.0 |
352.56 |
2028.00 |
605.8 |
352.56 |
3030.00 |
607.6 |
352.56 |
4024.00 |
609.2 |
352.56 |
5022.00 |
610.9 |
352.56 |
6024.00 |
612.5 |
352.56 |
7027.00 |
614.0 |
352.56 |
8021.00 |
615.5 |
352.56 |
9022.00 |
617.0 |
352.56 |
10020.00 |
618.4 |
352.56 |
11023.00 |
619.9 |
352.56 |
12003.00 |
621.2 |
352.56 |
13021.00 |
622.6 |
352.56 |
14012.00 |
623.9 |
352.56 |
15007.00 |
625.2 |
352.56 |
16016.00 |
626.5 |
352.56 |
17012.00 |
627.7 |
352.56 |
18015.00 |
629.0 |
352.56 |
19003.00 |
630.2 |
352.56 |
20040.00 |
631.4 |
352.56 |
21005.00 |
632.5 |
352.56 |
22035.00 |
633.8 |
352.56 |
23002.00 |
634.8 |
352.56 |
24039.00 |
636.0 |
352.56 |
25000.00 |
637.1 |
362.40 |
1029.00 |
593.8 |
362.40 |
2020.00 |
595.8 |
362.40 |
3028.00 |
597.6 |
362.40 |
4029.00 |
599.5 |
362.40 |
5040.00 |
601.3 |
362.40 |
6026.00 |
602.9 |
362.40 |
7026.00 |
604.7 |
362.40 |
8004.00 |
606.3 |
362.40 |
9007.00 |
607.9 |
362.40 |
10009.00 |
609.4 |
362.40 |
11009.00 |
610.9 |
362.40 |
12010.00 |
612.5 |
362.40 |
13000.00 |
614.0 |
362.40 |
14028.00 |
615.5 |
362.40 |
15017.00 |
616.8 |
362.40 |
16014.00 |
618.1 |
362.40 |
17004.00 |
619.5 |
362.40 |
18002.00 |
620.9 |
362.40 |
18988.00 |
622.1 |
362.40 |
20027.00 |
623.4 |
362.40 |
21002.00 |
624.7 |
362.40 |
22018.00 |
625.9 |
362.40 |
23013.00 |
627.1 |
362.40 |
24001.00 |
628.4 |
362.40 |
25000.00 |
629.5 |
Reference
|
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
283.15 |
100.00 |
668.07 |
283.15 |
2500.00 |
670.36 |
283.15 |
5000.00 |
672.69 |
283.15 |
10000.00 |
677.06 |
283.15 |
15000.00 |
681.19 |
283.15 |
20000.00 |
685.08 |
283.15 |
25000.00 |
688.82 |
283.15 |
30000.00 |
692.35 |
283.15 |
35000.00 |
695.65 |
293.15 |
100.00 |
659.18 |
293.15 |
2500.00 |
661.67 |
293.15 |
5000.00 |
664.17 |
293.15 |
10000.00 |
668.87 |
293.15 |
15000.00 |
673.27 |
293.15 |
20000.00 |
677.4 |
293.15 |
25000.00 |
681.33 |
293.15 |
30000.00 |
685.07 |
293.15 |
35000.00 |
688.63 |
298.15 |
100.00 |
654.61 |
298.15 |
2500.00 |
657.21 |
298.15 |
5000.00 |
659.81 |
298.15 |
10000.00 |
664.66 |
298.15 |
15000.00 |
669.24 |
298.15 |
20000.00 |
673.51 |
298.15 |
25000.00 |
677.56 |
298.15 |
30000.00 |
681.4 |
298.15 |
35000.00 |
685.02 |
303.15 |
100.00 |
649.97 |
303.15 |
2500.00 |
652.7 |
303.15 |
5000.00 |
655.36 |
303.15 |
10000.00 |
660.53 |
303.15 |
15000.00 |
665.23 |
303.15 |
20000.00 |
669.63 |
303.15 |
25000.00 |
673.81 |
303.15 |
30000.00 |
677.77 |
303.15 |
35000.00 |
681.45 |
313.15 |
100.00 |
640.82 |
313.15 |
2500.00 |
643.76 |
313.15 |
5000.00 |
646.69 |
313.15 |
10000.00 |
652.13 |
313.15 |
15000.00 |
657.16 |
313.15 |
20000.00 |
661.86 |
313.15 |
25000.00 |
666.28 |
313.15 |
30000.00 |
670.44 |
313.15 |
35000.00 |
674.41 |
323.15 |
100.00 |
631.41 |
323.15 |
2500.00 |
634.61 |
323.15 |
5000.00 |
637.8 |
323.15 |
10000.00 |
643.69 |
323.15 |
15000.00 |
649.12 |
323.15 |
20000.00 |
654.14 |
323.15 |
25000.00 |
658.84 |
323.15 |
30000.00 |
663.23 |
323.15 |
35000.00 |
667.4 |
333.15 |
100.00 |
621.8 |
333.15 |
2500.00 |
625.32 |
333.15 |
5000.00 |
628.77 |
333.15 |
10000.00 |
635.13 |
333.15 |
15000.00 |
640.94 |
333.15 |
20000.00 |
646.27 |
333.15 |
25000.00 |
651.23 |
333.15 |
30000.00 |
655.89 |
333.15 |
35000.00 |
660.3 |
Reference
|
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
278.15 |
100.00 |
670.8 |
278.15 |
5000.00 |
675.9 |
278.15 |
10000.00 |
680.5 |
278.15 |
15000.00 |
683.5 |
278.15 |
20000.00 |
688.7 |
283.15 |
100.00 |
667.5 |
283.15 |
5000.00 |
671.8 |
283.15 |
10000.00 |
676.2 |
283.15 |
15000.00 |
680.7 |
283.15 |
20000.00 |
684.4 |
288.15 |
100.00 |
664.0 |
288.15 |
5000.00 |
668.5 |
288.15 |
10000.00 |
672.9 |
288.15 |
15000.00 |
677.6 |
288.15 |
20000.00 |
681.3 |
293.15 |
100.00 |
658.8 |
293.15 |
5000.00 |
663.7 |
293.15 |
10000.00 |
668.8 |
293.15 |
15000.00 |
672.8 |
293.15 |
20000.00 |
677.4 |
298.15 |
100.00 |
654.2 |
298.15 |
5000.00 |
659.5 |
298.15 |
10000.00 |
664.7 |
298.15 |
15000.00 |
669.2 |
298.15 |
20000.00 |
673.2 |
303.15 |
100.00 |
649.8 |
303.15 |
5000.00 |
655.5 |
303.15 |
10000.00 |
660.2 |
303.15 |
15000.00 |
664.9 |
303.15 |
20000.00 |
669.3 |
308.15 |
100.00 |
645.1 |
308.15 |
5000.00 |
651.1 |
308.15 |
10000.00 |
656.3 |
308.15 |
15000.00 |
661.2 |
308.15 |
20000.00 |
666.0 |
313.15 |
100.00 |
641.3 |
313.15 |
5000.00 |
647.3 |
313.15 |
10000.00 |
652.8 |
313.15 |
15000.00 |
657.4 |
313.15 |
20000.00 |
662.5 |
Reference
|
Fixed |
Measured |
Pressure, kPa - Liquid |
Temperature, K - Liquid |
Mass density, kg/m3 - Liquid |
100.00 |
283.15 |
668.8 |
100.00 |
288.15 |
664.2 |
100.00 |
293.15 |
659.7 |
100.00 |
298.15 |
655.2 |
100.00 |
303.15 |
650.7 |
100.00 |
308.15 |
646.0 |
100.00 |
313.15 |
641.4 |
100.00 |
318.15 |
636.7 |
100.00 |
323.15 |
631.8 |
5000.00 |
283.15 |
673.2 |
5000.00 |
288.15 |
669.0 |
5000.00 |
293.15 |
664.7 |
5000.00 |
298.15 |
660.3 |
5000.00 |
303.15 |
655.9 |
5000.00 |
308.15 |
651.6 |
5000.00 |
313.15 |
647.2 |
5000.00 |
318.15 |
642.7 |
5000.00 |
323.15 |
638.1 |
10000.00 |
283.15 |
677.6 |
10000.00 |
288.15 |
673.5 |
10000.00 |
293.15 |
669.3 |
10000.00 |
298.15 |
665.2 |
10000.00 |
303.15 |
661.0 |
10000.00 |
308.15 |
656.8 |
10000.00 |
313.15 |
652.6 |
10000.00 |
318.15 |
648.3 |
10000.00 |
323.15 |
644.0 |
20000.00 |
283.15 |
685.7 |
20000.00 |
288.15 |
681.9 |
20000.00 |
293.15 |
678.0 |
20000.00 |
298.15 |
674.1 |
20000.00 |
303.15 |
670.2 |
20000.00 |
308.15 |
666.3 |
20000.00 |
313.15 |
662.4 |
20000.00 |
318.15 |
658.4 |
20000.00 |
323.15 |
654.4 |
30000.00 |
283.15 |
693.1 |
30000.00 |
288.15 |
689.4 |
30000.00 |
293.15 |
685.7 |
30000.00 |
298.15 |
682.1 |
30000.00 |
303.15 |
678.4 |
30000.00 |
308.15 |
674.7 |
30000.00 |
313.15 |
671.0 |
30000.00 |
318.15 |
667.3 |
30000.00 |
323.15 |
663.5 |
40000.00 |
283.15 |
699.8 |
40000.00 |
288.15 |
696.3 |
40000.00 |
293.15 |
692.9 |
40000.00 |
298.15 |
689.3 |
40000.00 |
303.15 |
685.9 |
40000.00 |
308.15 |
682.4 |
40000.00 |
313.15 |
678.9 |
40000.00 |
318.15 |
675.3 |
40000.00 |
323.15 |
671.7 |
50000.00 |
283.15 |
706.1 |
50000.00 |
288.15 |
702.8 |
50000.00 |
293.15 |
699.4 |
50000.00 |
298.15 |
696.1 |
50000.00 |
303.15 |
692.7 |
50000.00 |
308.15 |
689.3 |
50000.00 |
313.15 |
686.0 |
50000.00 |
318.15 |
682.5 |
50000.00 |
323.15 |
679.2 |
60000.00 |
283.15 |
711.5 |
60000.00 |
288.15 |
708.8 |
60000.00 |
293.15 |
705.6 |
60000.00 |
298.15 |
702.4 |
60000.00 |
303.15 |
699.1 |
60000.00 |
308.15 |
695.8 |
60000.00 |
313.15 |
692.7 |
60000.00 |
318.15 |
689.3 |
60000.00 |
323.15 |
686.0 |
Reference
|
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mass density, kg/m3 - Liquid |
298.15 |
20.22 |
654.96 |
Reference
|
Speed of sound, m/s
Fixed |
Measured |
Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Speed of sound, m/s - Fluid (supercritical or subcritical phases) |
509.17 |
3500.00 |
162.1 |
511.69 |
3500.00 |
138.7 |
514.46 |
3500.00 |
112.5 |
517.72 |
3500.00 |
95.8 |
519.87 |
3500.00 |
100.4 |
523.79 |
3500.00 |
112.7 |
527.85 |
3500.00 |
120.4 |
533.83 |
3500.00 |
134.2 |
538.84 |
3500.00 |
140.1 |
543.69 |
3500.00 |
145.3 |
548.31 |
3500.00 |
149.2 |
553.10 |
3500.00 |
155.1 |
558.44 |
3500.00 |
161.5 |
562.56 |
3500.00 |
164.9 |
568.21 |
3500.00 |
168.8 |
574.58 |
3500.00 |
174.8 |
578.77 |
3500.00 |
177.5 |
584.09 |
3500.00 |
183.0 |
588.59 |
3500.00 |
186.5 |
594.05 |
3500.00 |
188.6 |
598.83 |
3500.00 |
192.2 |
603.41 |
3500.00 |
195.9 |
608.96 |
3500.00 |
198.5 |
614.50 |
3500.00 |
203.1 |
618.79 |
3500.00 |
204.3 |
624.52 |
3500.00 |
206.1 |
629.29 |
3500.00 |
209.3 |
573.18 |
5500.00 |
150.0 |
578.22 |
5500.00 |
154.0 |
582.79 |
5500.00 |
157.3 |
588.07 |
5500.00 |
160.4 |
592.61 |
5500.00 |
164.2 |
597.98 |
5500.00 |
169.1 |
602.85 |
5500.00 |
172.0 |
608.05 |
5500.00 |
178.0 |
612.50 |
5500.00 |
180.2 |
618.05 |
5500.00 |
184.3 |
622.80 |
5500.00 |
186.5 |
628.11 |
5500.00 |
190.4 |
633.07 |
5500.00 |
193.6 |
636.04 |
5500.00 |
195.0 |
509.44 |
6500.00 |
331.1 |
511.27 |
6500.00 |
324.2 |
514.43 |
6500.00 |
314.1 |
517.58 |
6500.00 |
303.6 |
520.46 |
6500.00 |
289.0 |
523.63 |
6500.00 |
278.2 |
528.58 |
6500.00 |
263.2 |
533.48 |
6500.00 |
248.1 |
538.58 |
6500.00 |
231.5 |
543.14 |
6500.00 |
219.9 |
548.14 |
6500.00 |
207.4 |
553.55 |
6500.00 |
194.1 |
559.79 |
6500.00 |
180.9 |
633.86 |
3500.00 |
210.4 |
637.99 |
3500.00 |
211.6 |
509.40 |
4500.00 |
243.8 |
511.26 |
4500.00 |
232.7 |
514.50 |
4500.00 |
216.4 |
517.47 |
4500.00 |
201.9 |
520.36 |
4500.00 |
183.7 |
523.40 |
4500.00 |
168.4 |
527.66 |
4500.00 |
155.0 |
533.30 |
4500.00 |
131.7 |
538.14 |
4500.00 |
125.0 |
543.00 |
4500.00 |
125.6 |
547.96 |
4500.00 |
130.2 |
553.60 |
4500.00 |
134.9 |
558.48 |
4500.00 |
139.2 |
562.44 |
4500.00 |
142.8 |
567.95 |
4500.00 |
150.6 |
573.36 |
4500.00 |
155.7 |
578.08 |
4500.00 |
161.3 |
582.93 |
4500.00 |
164.7 |
587.91 |
4500.00 |
170.5 |
593.04 |
4500.00 |
174.8 |
597.84 |
4500.00 |
178.5 |
602.73 |
4500.00 |
181.2 |
608.03 |
4500.00 |
183.5 |
612.70 |
4500.00 |
187.0 |
617.91 |
4500.00 |
193.6 |
623.06 |
4500.00 |
195.6 |
628.15 |
4500.00 |
198.3 |
563.76 |
6500.00 |
171.7 |
568.59 |
6500.00 |
169.0 |
573.51 |
6500.00 |
165.9 |
578.65 |
6500.00 |
167.9 |
583.09 |
6500.00 |
165.5 |
588.45 |
6500.00 |
166.4 |
592.78 |
6500.00 |
168.5 |
598.14 |
6500.00 |
168.6 |
603.05 |
6500.00 |
173.4 |
608.12 |
6500.00 |
175.1 |
612.69 |
6500.00 |
179.7 |
618.21 |
6500.00 |
182.0 |
622.49 |
6500.00 |
184.8 |
628.16 |
6500.00 |
189.0 |
632.99 |
6500.00 |
192.3 |
635.50 |
6500.00 |
194.3 |
509.67 |
7500.00 |
361.3 |
511.34 |
7500.00 |
355.3 |
514.25 |
7500.00 |
347.2 |
517.46 |
7500.00 |
336.8 |
520.19 |
7500.00 |
328.5 |
523.93 |
7500.00 |
316.5 |
528.42 |
7500.00 |
304.2 |
533.43 |
7500.00 |
285.3 |
538.81 |
7500.00 |
270.8 |
543.52 |
7500.00 |
259.9 |
548.56 |
7500.00 |
248.3 |
553.44 |
7500.00 |
235.1 |
560.33 |
7500.00 |
222.2 |
632.52 |
4500.00 |
202.1 |
636.79 |
4500.00 |
204.9 |
509.57 |
5500.00 |
291.1 |
511.22 |
5500.00 |
286.1 |
514.60 |
5500.00 |
272.0 |
517.82 |
5500.00 |
260.2 |
520.54 |
5500.00 |
245.2 |
523.89 |
5500.00 |
229.4 |
528.22 |
5500.00 |
210.9 |
533.62 |
5500.00 |
194.1 |
538.33 |
5500.00 |
174.8 |
543.21 |
5500.00 |
165.4 |
547.89 |
5500.00 |
158.2 |
554.09 |
5500.00 |
150.9 |
558.90 |
5500.00 |
144.8 |
563.13 |
5500.00 |
143.4 |
568.40 |
5500.00 |
146.5 |
563.92 |
7500.00 |
215.1 |
568.54 |
7500.00 |
205.6 |
573.12 |
7500.00 |
201.1 |
579.07 |
7500.00 |
191.7 |
583.30 |
7500.00 |
190.5 |
589.01 |
7500.00 |
188.8 |
593.24 |
7500.00 |
187.8 |
598.52 |
7500.00 |
186.2 |
603.44 |
7500.00 |
186.0 |
608.49 |
7500.00 |
185.6 |
613.43 |
7500.00 |
187.8 |
618.56 |
7500.00 |
190.1 |
622.59 |
7500.00 |
191.0 |
628.12 |
7500.00 |
194.6 |
633.06 |
7500.00 |
196.8 |
635.27 |
7500.00 |
198.0 |
Reference
|
Thermal conductivity, W/m/K
Fixed |
Measured |
Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Thermal conductivity, W/m/K - Fluid (supercritical or subcritical phases) |
508.17 |
2949.00 |
0.0646 |
508.17 |
2953.00 |
0.0651 |
508.17 |
2956.00 |
0.0651 |
508.17 |
2963.00 |
0.0660 |
508.17 |
2966.00 |
0.0663 |
508.17 |
2970.00 |
0.0668 |
508.17 |
2974.00 |
0.0673 |
508.17 |
2979.00 |
0.0683 |
508.17 |
2982.00 |
0.0687 |
508.17 |
2990.00 |
0.0704 |
508.17 |
2991.00 |
0.0707 |
508.17 |
2995.00 |
0.0713 |
508.17 |
2998.00 |
0.0722 |
508.17 |
3002.00 |
0.0732 |
508.17 |
3007.00 |
0.0744 |
508.17 |
3009.00 |
0.0749 |
508.17 |
3013.00 |
0.0758 |
508.17 |
3015.00 |
0.0765 |
508.17 |
3017.00 |
0.0770 |
508.17 |
3021.00 |
0.0782 |
508.17 |
3022.00 |
0.0785 |
508.17 |
3024.00 |
0.0792 |
508.17 |
3026.00 |
0.0799 |
508.17 |
3029.00 |
0.0807 |
508.17 |
3031.00 |
0.0819 |
508.17 |
3033.00 |
0.0829 |
508.17 |
3034.00 |
0.0834 |
508.17 |
3036.00 |
0.0847 |
508.17 |
3037.00 |
0.0847 |
508.17 |
3038.00 |
0.0860 |
508.17 |
3039.00 |
0.0857 |
508.17 |
3040.00 |
0.0873 |
508.17 |
3041.00 |
0.0865 |
508.17 |
3041.00 |
0.0882 |
508.17 |
3042.00 |
0.0910 |
508.17 |
3043.00 |
0.0920 |
508.17 |
3045.00 |
0.0940 |
508.17 |
3046.00 |
0.0950 |
508.17 |
3047.00 |
0.0961 |
508.17 |
3048.00 |
0.0983 |
508.17 |
3049.00 |
0.0994 |
508.17 |
3050.00 |
0.1017 |
508.17 |
3051.00 |
0.1048 |
508.17 |
3052.00 |
0.1081 |
508.17 |
3053.00 |
0.1119 |
508.17 |
3054.00 |
0.1168 |
508.17 |
3055.00 |
0.1226 |
508.17 |
3056.00 |
0.1319 |
508.17 |
3057.00 |
0.1487 |
508.17 |
3058.00 |
0.1625 |
508.17 |
3059.00 |
0.1438 |
508.17 |
3060.00 |
0.1319 |
508.17 |
3061.00 |
0.1231 |
508.17 |
3062.00 |
0.1168 |
508.17 |
3063.00 |
0.1123 |
508.17 |
3064.00 |
0.1088 |
508.17 |
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508.17 |
3067.00 |
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3068.00 |
0.1006 |
508.17 |
3069.00 |
0.0994 |
508.17 |
3070.00 |
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508.17 |
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508.17 |
3074.00 |
0.0951 |
508.17 |
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508.17 |
3076.00 |
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508.17 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
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508.92 |
6000.00 |
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508.92 |
6100.00 |
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508.92 |
6200.00 |
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508.92 |
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508.92 |
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0.0753 |
508.92 |
7000.00 |
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508.92 |
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508.92 |
8000.00 |
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508.92 |
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508.92 |
9000.00 |
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508.92 |
9500.00 |
0.0791 |
508.92 |
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0.0795 |
509.85 |
2686.00 |
0.0464 |
509.85 |
2700.00 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
2760.00 |
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509.85 |
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509.85 |
2780.00 |
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509.85 |
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509.85 |
2800.00 |
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509.85 |
2805.00 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
2965.00 |
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509.85 |
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509.85 |
2975.00 |
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509.85 |
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509.85 |
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509.85 |
2990.00 |
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509.85 |
2995.00 |
0.0565 |
509.85 |
3000.00 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
3040.00 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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0.0643 |
509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
3110.00 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
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509.85 |
3160.00 |
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509.85 |
3170.00 |
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509.85 |
3180.00 |
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509.85 |
3190.00 |
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509.85 |
3200.00 |
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509.85 |
3210.00 |
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509.85 |
3220.00 |
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509.85 |
3230.00 |
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509.85 |
3240.00 |
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509.85 |
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509.85 |
3260.00 |
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509.85 |
3270.00 |
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509.85 |
3280.00 |
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509.85 |
3290.00 |
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509.85 |
3300.00 |
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509.85 |
3310.00 |
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509.85 |
3320.00 |
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509.85 |
3330.00 |
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509.85 |
3340.00 |
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509.85 |
3390.00 |
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509.85 |
3400.00 |
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509.85 |
3450.00 |
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509.85 |
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509.85 |
3600.00 |
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509.85 |
3800.00 |
0.0703 |
509.85 |
4000.00 |
0.0706 |
509.85 |
4200.00 |
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509.85 |
4400.00 |
0.0713 |
509.85 |
4600.00 |
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509.85 |
4800.00 |
0.0722 |
509.85 |
5000.00 |
0.0725 |
509.85 |
5200.00 |
0.0728 |
509.85 |
5400.00 |
0.0732 |
509.85 |
5600.00 |
0.0736 |
509.85 |
5800.00 |
0.0739 |
509.85 |
6000.00 |
0.0742 |
509.85 |
6200.00 |
0.0745 |
509.85 |
6400.00 |
0.0748 |
509.85 |
6600.00 |
0.0751 |
509.85 |
6800.00 |
0.0754 |
509.85 |
7000.00 |
0.0757 |
509.85 |
7200.00 |
0.0760 |
509.85 |
7400.00 |
0.0762 |
509.85 |
7600.00 |
0.0765 |
509.85 |
7800.00 |
0.0767 |
509.85 |
8000.00 |
0.0768 |
509.85 |
8200.00 |
0.0770 |
509.85 |
8500.00 |
0.0774 |
509.85 |
9000.00 |
0.0780 |
509.85 |
9500.00 |
0.0786 |
509.85 |
10000.00 |
0.0791 |
510.36 |
245.00 |
0.0379 |
510.36 |
1000.00 |
0.0385 |
510.36 |
2245.00 |
0.0418 |
510.36 |
2715.00 |
0.0466 |
510.36 |
3110.00 |
0.0680 |
510.36 |
3112.00 |
0.0682 |
510.36 |
3114.00 |
0.0688 |
510.36 |
3116.00 |
0.0694 |
510.36 |
3118.00 |
0.0703 |
510.36 |
3120.00 |
0.0709 |
510.36 |
3122.00 |
0.0715 |
510.36 |
3124.00 |
0.0724 |
510.36 |
3126.00 |
0.0734 |
510.36 |
3128.00 |
0.0740 |
510.36 |
3130.00 |
0.0747 |
510.36 |
3132.00 |
0.0754 |
510.36 |
3133.00 |
0.0761 |
510.36 |
3134.00 |
0.0762 |
510.36 |
3137.00 |
0.0784 |
510.36 |
3138.00 |
0.0791 |
510.36 |
3139.00 |
0.0799 |
510.36 |
3140.00 |
0.0806 |
510.36 |
3141.00 |
0.0812 |
510.36 |
3142.00 |
0.0820 |
510.36 |
3143.00 |
0.0827 |
510.36 |
3144.00 |
0.0833 |
510.36 |
3145.00 |
0.0839 |
510.36 |
3146.00 |
0.0846 |
510.36 |
3147.00 |
0.0850 |
510.36 |
3148.00 |
0.0855 |
510.36 |
3150.00 |
0.0863 |
510.36 |
3151.00 |
0.0866 |
510.36 |
3152.00 |
0.0867 |
510.36 |
3153.00 |
0.0869 |
510.36 |
3154.00 |
0.0871 |
510.36 |
3155.00 |
0.0870 |
510.36 |
3156.00 |
0.0869 |
510.36 |
3157.00 |
0.0868 |
510.36 |
3158.00 |
0.0866 |
510.36 |
3159.00 |
0.0863 |
510.36 |
3160.00 |
0.0860 |
510.36 |
3161.00 |
0.0858 |
510.36 |
3162.00 |
0.0855 |
510.36 |
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0.0852 |
510.36 |
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0.0848 |
510.36 |
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510.36 |
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510.36 |
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510.36 |
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510.36 |
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510.36 |
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510.36 |
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511.55 |
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511.55 |
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511.55 |
1100.00 |
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511.55 |
1200.00 |
0.0386 |
511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
1800.00 |
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511.55 |
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511.55 |
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0.0409 |
511.55 |
2100.00 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
2462.00 |
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511.55 |
2466.00 |
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511.55 |
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511.55 |
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511.55 |
2700.00 |
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511.55 |
2800.00 |
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511.55 |
2900.00 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
3110.00 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
3245.00 |
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511.55 |
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511.55 |
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511.55 |
3260.00 |
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511.55 |
3265.00 |
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511.55 |
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511.55 |
3275.00 |
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511.55 |
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511.55 |
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511.55 |
3290.00 |
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511.55 |
3295.00 |
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511.55 |
3300.00 |
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511.55 |
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511.55 |
3310.00 |
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511.55 |
3315.00 |
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511.55 |
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511.55 |
3330.00 |
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511.55 |
3335.00 |
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511.55 |
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511.55 |
3345.00 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
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511.55 |
3900.00 |
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511.55 |
3950.00 |
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511.55 |
4000.00 |
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511.55 |
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511.55 |
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511.55 |
4300.00 |
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511.55 |
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511.55 |
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511.55 |
4600.00 |
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511.55 |
4700.00 |
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511.55 |
4800.00 |
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511.55 |
5000.00 |
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511.55 |
5100.00 |
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511.55 |
5300.00 |
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511.55 |
5500.00 |
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511.55 |
5800.00 |
0.0728 |
511.55 |
6000.00 |
0.0731 |
511.55 |
6200.00 |
0.0734 |
511.55 |
6400.00 |
0.0737 |
511.55 |
6600.00 |
0.0741 |
511.55 |
6800.00 |
0.0744 |
511.55 |
6900.00 |
0.0746 |
511.55 |
7100.00 |
0.0748 |
511.55 |
7200.00 |
0.0750 |
511.55 |
7300.00 |
0.0751 |
511.55 |
7500.00 |
0.0762 |
511.55 |
7800.00 |
0.0766 |
511.55 |
8000.00 |
0.0769 |
511.55 |
8200.00 |
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511.55 |
8300.00 |
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511.55 |
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511.55 |
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0.0775 |
511.55 |
8600.00 |
0.0776 |
511.55 |
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0.0777 |
511.55 |
9000.00 |
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511.55 |
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0.0781 |
511.55 |
9200.00 |
0.0782 |
511.55 |
9300.00 |
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511.55 |
9400.00 |
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511.55 |
9700.00 |
0.0787 |
511.55 |
10000.00 |
0.0790 |
511.79 |
1600.00 |
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511.79 |
1800.00 |
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511.79 |
1900.00 |
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511.79 |
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511.79 |
2090.00 |
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511.79 |
2100.00 |
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511.79 |
2110.00 |
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511.79 |
2200.00 |
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511.79 |
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511.79 |
2400.00 |
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511.79 |
2500.00 |
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511.79 |
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511.79 |
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511.79 |
2800.00 |
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511.79 |
2817.00 |
0.0486 |
511.79 |
2911.00 |
0.0508 |
511.79 |
2958.00 |
0.0520 |
511.79 |
2987.00 |
0.0528 |
511.79 |
3000.00 |
0.0534 |
511.79 |
3049.00 |
0.0556 |
511.79 |
3076.00 |
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511.79 |
3093.00 |
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511.79 |
3101.00 |
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511.79 |
3113.00 |
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511.79 |
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511.79 |
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511.79 |
3143.00 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
3216.00 |
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511.79 |
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511.79 |
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511.79 |
3223.00 |
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511.79 |
3226.00 |
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511.79 |
3231.00 |
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511.79 |
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511.79 |
3236.00 |
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511.79 |
3237.00 |
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511.79 |
3240.00 |
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511.79 |
3243.00 |
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511.79 |
3246.00 |
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511.79 |
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511.79 |
3247.00 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
3269.00 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
3300.00 |
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511.79 |
3301.00 |
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511.79 |
3306.00 |
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511.79 |
3310.00 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
3321.00 |
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511.79 |
3325.00 |
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511.79 |
3327.00 |
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511.79 |
3330.00 |
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511.79 |
3332.00 |
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511.79 |
3335.00 |
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511.79 |
3340.00 |
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511.79 |
3346.00 |
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511.79 |
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511.79 |
3353.00 |
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511.79 |
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511.79 |
3360.00 |
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511.79 |
3365.00 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
3395.00 |
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511.79 |
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511.79 |
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511.79 |
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511.79 |
3440.00 |
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511.79 |
3460.00 |
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511.79 |
3500.00 |
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511.79 |
3600.00 |
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511.79 |
3657.00 |
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511.79 |
3700.00 |
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511.79 |
3750.00 |
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511.79 |
3800.00 |
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511.79 |
3850.00 |
0.0697 |
511.79 |
3900.00 |
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511.79 |
3950.00 |
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511.79 |
3980.00 |
0.0698 |
511.79 |
4000.00 |
0.0699 |
511.79 |
4030.00 |
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511.79 |
4100.00 |
0.0701 |
511.79 |
4180.00 |
0.0704 |
511.79 |
4190.00 |
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511.79 |
4200.00 |
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511.79 |
4400.00 |
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511.79 |
4600.00 |
0.0716 |
511.79 |
4800.00 |
0.0718 |
511.79 |
5400.00 |
0.0730 |
511.79 |
6000.00 |
0.0740 |
511.79 |
7000.00 |
0.0757 |
511.79 |
8000.00 |
0.0770 |
511.79 |
9000.00 |
0.0781 |
511.79 |
10000.00 |
0.0792 |
513.09 |
2634.00 |
0.0455 |
513.09 |
2645.00 |
0.0456 |
513.09 |
2653.00 |
0.0457 |
513.09 |
2654.00 |
0.0457 |
513.09 |
2655.00 |
0.0457 |
513.09 |
2661.00 |
0.0459 |
513.09 |
2722.00 |
0.0455 |
513.09 |
2740.00 |
0.0468 |
513.09 |
2760.00 |
0.0471 |
513.09 |
2763.00 |
0.0470 |
513.09 |
2839.00 |
0.0483 |
513.09 |
2849.00 |
0.0486 |
513.09 |
2879.00 |
0.0492 |
513.09 |
2894.00 |
0.0493 |
513.09 |
2909.00 |
0.0496 |
513.09 |
2931.00 |
0.0501 |
513.09 |
2953.00 |
0.0505 |
513.09 |
2983.00 |
0.0515 |
513.09 |
3010.00 |
0.0524 |
513.09 |
3034.00 |
0.0532 |
513.09 |
3054.00 |
0.0539 |
513.09 |
3098.00 |
0.0560 |
513.09 |
3114.00 |
0.0568 |
513.09 |
3152.00 |
0.0594 |
513.09 |
3163.00 |
0.0604 |
513.09 |
3169.00 |
0.0609 |
513.09 |
3176.00 |
0.0615 |
513.09 |
3180.00 |
0.0622 |
513.09 |
3184.00 |
0.0626 |
513.09 |
3186.00 |
0.0629 |
513.09 |
3193.00 |
0.0631 |
513.09 |
3195.00 |
0.0631 |
513.09 |
3200.00 |
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553.00 |
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553.00 |
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553.00 |
3600.00 |
0.0505 |
553.00 |
3700.00 |
0.0513 |
553.00 |
3800.00 |
0.0519 |
553.00 |
3900.00 |
0.0525 |
553.00 |
4000.00 |
0.0532 |
553.00 |
4100.00 |
0.0539 |
553.00 |
4200.00 |
0.0547 |
553.00 |
4268.00 |
0.0552 |
553.00 |
4390.00 |
0.0562 |
553.00 |
4700.00 |
0.0589 |
553.00 |
4800.00 |
0.0599 |
553.00 |
4900.00 |
0.0607 |
553.00 |
5000.00 |
0.0617 |
553.00 |
5300.00 |
0.0642 |
553.00 |
5500.00 |
0.0656 |
553.00 |
5800.00 |
0.0675 |
553.00 |
6000.00 |
0.0684 |
553.00 |
6300.00 |
0.0697 |
553.00 |
6500.00 |
0.0702 |
553.00 |
6800.00 |
0.0711 |
553.00 |
7000.00 |
0.0717 |
553.00 |
7200.00 |
0.0720 |
553.00 |
7500.00 |
0.0727 |
553.00 |
7800.00 |
0.0733 |
553.00 |
8000.00 |
0.0736 |
553.00 |
8300.00 |
0.0743 |
553.00 |
8500.00 |
0.0743 |
553.00 |
8800.00 |
0.0755 |
553.00 |
9000.00 |
0.0755 |
553.00 |
9250.00 |
0.0756 |
553.00 |
9500.00 |
0.0758 |
553.00 |
9800.00 |
0.0762 |
553.00 |
10000.00 |
0.0764 |
553.00 |
10300.00 |
0.0765 |
553.00 |
10500.00 |
0.0769 |
553.00 |
10800.00 |
0.0772 |
553.00 |
11000.00 |
0.0773 |
553.00 |
11500.00 |
0.0778 |
553.00 |
12000.00 |
0.0783 |
553.00 |
12300.00 |
0.0787 |
553.00 |
12870.00 |
0.0791 |
553.00 |
13500.00 |
0.0798 |
553.00 |
14000.00 |
0.0802 |
553.00 |
14500.00 |
0.0807 |
553.00 |
15000.00 |
0.0812 |
Reference
|
Correlations
Similar Compounds
Find more compounds similar to n-Hexane.
Mixtures
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Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
- Measurements of the Liquid Viscosities of Mixtures of n-Butane, n-Hexane, and n-Octane with Squalane to 30MPa
- Liquid-Liquid Coexistence Curve of n-Perfluorohexane - n-Hexane System
- Kinematic Viscosities for Ether + Alkane Mixtures: Experimental Results and UNIFAC-VISCO Parameters
- Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
- Acoustic and Thermophysical Properties of Binary Liquid Mixtures of Primary Butanols with Hexane and Cyclohexane at 293.15 K
- Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
- High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
- Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
- Vapour pressures and excess functions of (3,5; 2,6)dimethylpyridine + n-hexane, n-heptane and n-octane measurement and prediction
- Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
- Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of (ethanol or 1-butanol), triethylamine and n-hexane
- Vapour liquid equilibrium of carboxylic acid systems: Propionic acid + valeric acid and isobutyric acid + valeric acid
- Vapor liquid equilibrium of methane and methane + nitrogen and an equimolar hexane + decane mixture under isothermal conditions
- Experimental liquid liquid equilibria of 1-methylimidazole with hydrocarbons and ethers
- Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
- Vapour liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15K
- Excess molar enthalpies for mixtures of carbon dioxide + a modifier (5 mol% methanol or 1-octanol) and hexane at 308.15K and 12.40MPa
- Liquid liquid equilibrium of (perfluoroalkane + alkane) binary mixtures
- Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
- Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
- Phase behaviour of I-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium based ionic liquids with alcohols, water, ketones and hydrocarbons: The effect of cation and anion on solubility
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Liquid liquid equilibria and partitioning in organic aqueous systems
- Determination and correlation of liquid liquid equilibria for four binary N,N-dimethylformamide + hydrocarbon systems
- Isobaric vapor liquid and vapor liquid liquid equilibrium data for the water ethanol hexane system
- Solution thermodynamics near the liquid liquid critical point I. First-order excess derivatives
- Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
- Separation of aromatic hydrocarbons from alkanes using ammonium ionic liquid C2NTf2 at T = 298.15K
- Phase behaviour of 1-methyl-3-octylimidazolium bis[trifluoromethylsulfonyl]imide with thiophene and aliphatic hydrocarbons: The influence of n-alkane chain length
- Ternary liquid liquid equilibria for mixtures of an ionic liquid + n-hexane + an organic compound involved in the kinetic resolution of rac-1-phenyl ethanol (rac-1-phenyl ethanol, vinyl propionate, rac-1-phenylethyl propionate or propionic acid) at 298.2K and atmospheric pressure
- Liquid liquid equilibria of lactam containing binary systems
- A study on the liquid liquid equilibria of 1-alkyl-3-methylimidazolium hexafluorophosphate with ethanol and alkanes
- Thiophene separation from aliphatic hydrocarbons using the 1-ethyl-3-methylimidazolium ethylsulfate ionic liquid
- Solubility of hydrocarbons in water: Experimental measurements and modeling using a group contribution with association equation of state (GCA-EoS)
- Isobaric vapor liquid equilibria for the n-hexane + 2-isopropoxyethanol and n-heptane + 2-isopropoxyethanol systems
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
- Measurement and prediction of activity coefficients at infinite dilution ( ), vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
- Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
- (Solid + liquid) and (liquid + liquid) phase equilibria measurements and correlation of the binary systems {tri-iso-butyl(methyl)phosphonium tosylate + alcohol, or +hydrocarbon}
- Solubility of pyrene in simple and mixed solvent systems
- Liquid liquid equilibria for {hexane + benzene + 1-ethyl-3-methylimidazolium ethylsulfate} at (298.2, 313.2 and 328.2)K
- Activity coefficients at infinite dilution of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
- Solubilities of cholesterol and desmosterol in binary solvent mixtures of n-hexane + ethanol
- Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
- Measurement and correlation of solid-liquid equilibria of Irganox 1010 with n-hexane
- Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
- Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons
- Alkylsulfate-based ionic liquids to separate azeotropic mixtures
- Ionic liquids on desulfurization of fuel oils
- (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
- Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
- Infinite dilution activity coefficient and vapour liquid equilibrium measurements for dimethylsulphide and tetrahydrothiophene with hydrocarbons
- Alkylsulfate-based ionic liquids to separate azeotropic mixtures
- Application of [EMpy][ESO4] ionic liquid as solvent for the liquid extraction of xylenes from hexane
- Liquid-liquid equilibrium data for binary perfluoroalkane (C6 and C8) + n-alkane systems
- Measurements of binary diffusion coefficients for metal complexes in organic solvents by the Taylor dispersion method
- Experimental data on binary and ternary mixtures of perfluoro-1,3-dimethylcyclohexane with normal alkanes at 373.15 K
- Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
- Influence of anion structure on the liquid-liquid equilibria of 1-(3-hydroxypropyl)pyridinium cation based ionic liquid-hydrocarbon binary systems
- Influence of temperature on the (liquid + liquid) equilibria of {methanol + benzene + hexane} ternary system
- Study of [EMim][ESO4] ionic liquid as solvent in the liquid-liquid extraction of xylenes from their mixtures with hexane
- Physical properties of 3-methyl-N-butylpyridinium tricyanomethanide and ternary LLE data with an aromatic and an aliphatic hydrocarbon at T = (303.2 and 328.2) K and p = 0.1 MPa
- Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
- Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
- Measurement and theoretical prediction of the vapor-liquid equilibrium, densities and interfacial tensions of the system hexane + 2-methoxy-2-methylbutane
- P-x data for binary systems using a novel static total pressure apparatus
- Hexyl dimethylpyridinium ionic liquids for desulfurization of fuels. Effect of the position of the alkyl side chains
- Vapor-liquid equilibrium for the ternary carbon dioxide + ethanol + n-hexane and quaternary carbon dioxide + ethanol + n-hexane + thiophene systems
- LLE, VLE and VLLE data for the water n-butanol n-hexane system at atmospheric pressure
- Experimental determination and theoretical modeling of the vapor-liquid equilibrium and surface tensions of hexane + tetrahydro-2H-pyran
- Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
- Vapour-liquid equilibrium (VLE) for the systems furan + n-hexane and furan + toluene. Measurements, data treatment and modeling using molecular models
- Ionic liquids as solvents to separate the azeotropic mixture hexane/ethanol
- A novel static analytical apparatus for phase equilibrium measurements
- Ternary (liquid liquid) equilibria of nitrate based ionic liquid + alkane + benzene at 298.15 K: Experiments and correlation
- Measurement and correlation of vapor-liquid equilibria for alkane + alkanol andalkane + alkanediol systems with group contribution COSMOSPACE model
- Capacity of two 1-butyl-1-methylpyrrolidinium-based ionic liquidsfor the extraction of ethanol from its mixtures with heptane and hexane
- Desulfurization of fuels by liquid-liquid extraction with1-ethyl-3-methylimidazolium ionic liquids
- Viscosity of liquid systems involving hydrogenated and fluorinated substances: Liquid mixtures of (hexane + perfluorohexane)
- Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
- Vapor-liquid equilibrium and interfacial tensions of the system ethanol + hexane + tetrahydro-2H-Pyran
- Extraction of toluene from alkane using [Bmim][NO3] or [Omim][NO3] ionic liquid at 298.15 K and atmospheric pressure
- Prediction and measurement of phase equilibria for the extraction of BTX from naphtha reformate using BMIMPF6 ionic liquid
- Liquid-liquid equilibrium data for ternary mixtures composed of n-hexane, benzene and acetonitrile at (298.15, 308.15, and 318.15) K
- Solid-liquid equilibrium and thermodynamic of 2,5-thiophenedicarboxylic acid in different organic solvents
- Study of critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures of aromatic hydrocarbons with alkanes and cycloalkanes
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Measurement, correlation and prediction of isothermal vapor liquid equilibria of different systems containing vegetable oils
- Determination and correlation of solubility and solution thermodynamics of coumarin in different pure solvents
- The ionic liquid 1-ethyl-3-methylimidazolium tris(pentafluoroethyl) trifluorophosphate as alternative extractant for BTEX separation
- Experimental study on liquid - liquid equilibria of ionic liquids + alkane + ethyl benzene or p-xylene at 298.15 K
- Novel liquid-liquid equilibrium data for six ternary systems containing IL, hydrocarbon and thiophene at 25 C
- Liquid-liquid equilibria in the ternary and multicomponent systems involving hydrocarbons, thiophene or pyridine and ionic liquid (1-benzyl-3-metylimidazolium bis(trifluorometylsulfonyl)imide)
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- Liquid-liquid equilibrium data for (n-hexane + ethyl acetate + acetonitrile) ternary system at (298.15, 308.15, and 318.15) K
- Characterizing second generation biofuels: Excess enthalpies and vapour-liquid equilibria of the binary mixtures containing 1-pentanol or 2-pentanol and n-hexane
- Separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [EMIM]-based ionic liquids
- Preferential solvation and mixing behaviour of the essential oil 1,8-cineole with short-chain hydrocarbons
- Equilibrium data and GC-PC SAFT predictions for furanic extraction
- Equilibrium study and diversified models of drug Norfloxacin in eight pure organic and binary solvents at T = (278.15 to 328.15) K
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Liquid-liquid equilibrium data for extractive desulfurization using 1-butyl-3-methyl imidazolium thiocyanate, n-alkane and thiophene
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Ternary liquid-liquid equilibrium of an azeotropic mixture (hexane + methanol) with different imidazolium-based ionic liquids at T = 298.15 K and 101.325 kPa
- Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
- Ternary LLE measurements for the separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [DCA]-based ionic liquids
- Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- Thermal conductivity of gaseous and liquid n-hexane
- Vapor-liquid equilibrium in the binary and ternary systems containing ethyl propionate, ethanol and alkane at 101.3 kPa
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Unravelling various types of non-covalent interactions of benzyl amine with ethers in n-hexane at 303.15 K by ultrasonic and DFT methods
- Experimental measurement of carbon dioxide solubility in 1-methylpyrrolidin-2-one (NMP) + 1-butyl-3-methyl-1H-imidazol-3-ium tetrafluoroborate ([bmim][BF4]) mixtures using a new static-synthetic cell
- Experimental measurement and thermodynamic modeling of phase equilibria of {CO2 + tetralin + n-alkanes (with n = 6, 16)} and its binary systems
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Measurements of the thermal conductivity of n-hexane in the supercritical region
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
- VLE measurements and modelling for the binary systems of (CF4 + C6F14) and (CF4 + C8F18)
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- Measurement of the speed of sound in supercritical n-hexane at temperatures from (509.17-637.99) K and pressures from (3.5-7.5) MPa
- High-pressure experimental vapour-liquid-liquid equilibrium measurements and modelling for natural gas processing: Equipment validation, and the system CH4 + nC6H14 + H2O
- The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
- Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
- Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
- Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K
- Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
- Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
- (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
- Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
- Vapour pressures of n-hexane determined by comparative ebulliometry
- Experimental measurements and prediction of liquid densities for n-alkane mixtures
- Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
- Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
- Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of 1-butanol, a tertiary amine (tri-n-butylamine or tri-n-octylamine) and n-hexane: Experimental results and ERAS-model calculations
- Physical properties of (propyl propanoate + hexane + toluene) at 298.15 K