k = is thermal conductivity [W/(m·K)]
ρ = density [kg/m³]
C P = specific heat capacity [J/(kg·K)]
Below, thermal diffusivity of propane at varying temperatures and 1, 10, 50 and 100 bara (14.5, 145, 725 and 1450 psia) are given in figures and tables .
See also other properties of propane at varying temperature and pressure: Density and specific weight , Dynamic and Kinematic Viscosity , Prandtl number , Specific heat (heat capacity) , Thermal conductivity , and Thermophysical properties at standard conditions ,
as well as thermal diffusivity of air , nitrogen and water .
Thermal diffusivity of propane at 1, 10 and 100 bara (14.5, 145 and 1450 psia), and varying temperature given as °C or °F:
Thermal diffusivity of propane at atmospheric pressure and given temperature, SI and Imperial units:
State | Temperature | Thermal diffusivity | Temperature | Thermal diffusivity | |||||
[K] | [°C] | [x10 -6 m2/s] | [m 2 /h] | [K] | [°F] | [x10 -5 ft 2 /s] | [ ft 2 /h] | ||
Liquid | 123 | -150 | 0.142 | 0.000510 | 116 | -250 | 0.154 | 0.00555 | |
148 | -125 | 0.134 | 0.000482 | 144 | -200 | 0.146 | 0.00524 | ||
173 | -100 | 0.124 | 0.000448 | 172 | -150 | 0.134 | 0.00484 | ||
198 | -75 | 0.114 | 0.000410 | 200 | -100 | 0.122 | 0.00438 | ||
223 | -50 | 0.103 | 0.000369 | 228 | -50 | 0.108 | 0.00390 | ||
231 | -42 | 0.09896 | 0.000356 | 231 | -44 | 0.107 | 0.00384 | ||
Gas | 231 | -42 | 3.68 | 0.0132 | 231 | -44 | 3.88 | 0.140 | |
248 | -25 | 4.33 | 0.0156 | 244 | -20 | 4.88 | 0.176 | ||
263 | -10 | 4.94 | 0.0178 | 255 | 0 | 5.76 | 0.207 | ||
268 | -5 | 5.14 | 0.0185 | 266 | 20 | 6.69 | 0.241 | ||
273 | 0 | 5.35 | 0.0193 | 272 | 30 | 7.18 | 0.259 | ||
278 | 5 | 5.56 | 0.0200 | 278 | 40 | 7.68 | 0.276 | ||
283 | 10 | 5.78 | 0.0208 | 283 | 50 | 8.19 | 0.295 | ||
293 | 20 | 6.22 | 0.0224 | 294 | 70 | 9.26 | 0.333 | ||
298 | 25 | 6.44 | 0.0232 | 300 | 80 | 9.82 | 0.353 | ||
303 | 30 | 6.67 | 0.0240 | 305 | 90 | 10.4 | 0.374 | ||
323 | 50 | 7.61 | 0.0274 | 311 | 100 | 11.0 | 0.395 | ||
348 | 75 | 8.86 | 0.0319 | 339 | 150 | 14.1 | 0.509 | ||
373 | 100 | 10.2 | 0.0367 | 366 | 200 | 17.8 | 0.639 | ||
398 | 125 | 11.6 | 0.0418 | 394 | 250 | 21.8 | 0.786 | ||
423 | 150 | 13.1 | 0.0473 | 422 | 300 | 26.4 | 0.951 | ||
448 | 175 | 14.8 | 0.0532 | 478 | 400 | 37.3 | 1.34 | ||
473 | 200 | 16.5 | 0.0594 | 533 | 500 | 50.7 | 1.83 | ||
523 | 250 | 20.3 | 0.0730 | 589 | 600 | 67.0 | 2.41 | ||
573 | 300 | 24.5 | 0.0884 | 644 | 700 | 86.4 | 3.11 | ||
623 | 350 | 29.3 | 0.106 | 700 | 800 | 109 | 3.94 | ||
673 | 400 | 34.7 | 0.125 | 755 | 900 | 136 | 4.90 | ||
773 | 500 | 47.1 | 0.170 | 811 | 1000 | 167 | 6.02 |
Thermal diffusivity of propane at given temperature and pressure, SI and Imperial units:
State | Temperature | Pressure | Thermal diffusivity | ||||
[K] | [°C] | [°F] | [bara] | [psia] | [x10 -6 m 2 /s] | [x10 -5 ft 2 /s] | |
Liquid at equilibrium | 100 | -173 | -280 | 2.5E-07 | 3.7E-06 | 0.149 | 0.160 |
130 | -143 | -226 | 0.000176 | 0.00255 | 0.140 | 0.151 | |
160 | -113 | -172 | 0.00850 | 0.1233 | 0.130 | 0.140 | |
190 | -83.2 | -118 | 0.1055 | 1.530 | 0.117 | 0.126 | |
220 | -53.2 | -63.7 | 0.6058 | 8.787 | 0.104 | 0.112 | |
250 | -23.2 | -9.7 | 2.180 | 31.62 | 0.0902 | 0.0971 | |
280 | 6.9 | 44.3 | 5.817 | 84.37 | 0.0772 | 0.0831 | |
310 | 36.9 | 98.3 | 12.73 | 184.6 | 0.0650 | 0.0699 | |
320 | 46.9 | 116 | 15.99 | 231.9 | 0.0609 | 0.0656 | |
340 | 66.9 | 152 | 24.32 | 352.7 | 0.0512 | 0.0551 | |
355 | 81.9 | 179 | 32.43 | 470.4 | 0.0394 | 0.0425 | |
360 | 86.9 | 188 | 35.55 | 515.6 | 0.0345 | 0.0371 | |
Gas at equilibrium | 100 | -173 | -280 | 2.5E-07 | 3.7E-06 | 1921257 | 2068022 |
130 | -143 | -226 | 0.000176 | 0.00255 | 5460 | 5877 | |
160 | -113 | -172 | 0.00850 | 0.1233 | 187 | 201 | |
190 | -83.2 | -118 | 0.1055 | 1.530 | 22.2 | 23.9 | |
220 | -53.2 | -63.7 | 0.6058 | 8.787 | 5.13 | 5.52 | |
250 | -23.2 | -9.7 | 2.180 | 31.62 | 1.73 | 1.86 | |
280 | 6.9 | 44.3 | 5.817 | 84.37 | 0.729 | 0.785 | |
310 | 36.9 | 98.3 | 12.73 | 184.6 | 0.341 | 0.367 | |
320 | 46.9 | 116 | 15.99 | 231.9 | 0.264 | 0.284 | |
340 | 66.9 | 152 | 24.32 | 352.7 | 0.151 | 0.163 | |
355 | 81.9 | 179 | 32.43 | 470.4 | 0.0800 | 0.0861 | |
360 | 86.9 | 188 | 35.55 | 515.6 | 0.0552 | 0.0594 | |
Liquid | 85.53 | -187.62 | -305.72 | 1 | 14.5 | 0.148 | 0.159 |
100 | -173 | -280 | 1 | 14.5 | 0.147 | 0.158 | |
120 | -153 | -244 | 1 | 14.5 | 0.142 | 0.153 | |
140 | -133 | -208 | 1 | 14.5 | 0.137 | 0.147 | |
160 | -113 | -172 | 1 | 14.5 | 0.130 | 0.139 | |
180 | -93.2 | -136 | 1 | 14.5 | 0.122 | 0.131 | |
200 | -73.2 | -99.7 | 1 | 14.5 | 0.113 | 0.122 | |
220 | -53.2 | -63.7 | 1 | 14.5 | 0.104 | 0.112 | |
230.74 | -42.41 | -44.34 | 1 | 14.5 | 0.0992 | 0.107 | |
Gas | 230.74 | -42.41 | -44.34 | 1 | 14.5 | 3.36 | 3.62 |
240 | -33.2 | -27.7 | 1 | 14.5 | 3.70 | 3.98 | |
260 | -13.2 | 8.3 | 1 | 14.5 | 4.46 | 4.80 | |
280 | 6.9 | 44.3 | 1 | 14.5 | 5.26 | 5.66 | |
300 | 26.9 | 80.3 | 1 | 14.5 | 6.09 | 6.56 | |
320 | 46.9 | 116 | 1 | 14.5 | 6.96 | 7.50 | |
340 | 66.9 | 152 | 1 | 14.5 | 7.88 | 8.48 | |
360 | 86.9 | 188 | 1 | 14.5 | 8.84 | 9.51 | |
400 | 127 | 260 | 1 | 14.5 | 10.9 | 11.7 | |
500 | 227 | 440 | 1 | 14.5 | 17.1 | 18.4 | |
600 | 327 | 620 | 1 | 14.5 | 25.1 | 27.0 | |
700 | 427 | 800 | 1 | 14.5 | 35.1 | 37.7 | |
800 | 527 | 980 | 1 | 14.5 | 47.3 | 50.9 | |
900 | 627 | 1160 | 1 | 14.5 | 62.1 | 66.8 | |
1000 | 727 | 1340 | 1 | 14.5 | 79.6 | 85.7 | |
Liquid | 85.62 | -187.53 | -305.55 | 10 | 145 | 0.148 | 0.159 |
100 | -173 | -280 | 10 | 145 | 0.147 | 0.158 | |
120 | -153 | -244 | 10 | 145 | 0.143 | 0.154 | |
140 | -133 | -208 | 10 | 145 | 0.137 | 0.147 | |
160 | -113 | -172 | 10 | 145 | 0.130 | 0.140 | |
180 | -93.2 | -136 | 10 | 145 | 0.122 | 0.131 | |
200 | -73.2 | -99.7 | 10 | 145 | 0.113 | 0.122 | |
220 | -53.2 | -63.7 | 10 | 145 | 0.105 | 0.112 | |
240 | -33.2 | -27.7 | 10 | 145 | 0.0955 | 0.103 | |
260 | -13.2 | 8.3 | 10 | 145 | 0.0866 | 0.0933 | |
280 | 6.9 | 44.3 | 10 | 145 | 0.0779 | 0.0839 | |
300.09 | 26.94 | 80.49 | 10 | 145 | 0.0692 | 0.0745 | |
Gas | 300.09 | 26.94 | 80.49 | 10 | 145 | 0.435 | 0.468 |
320 | 46.9 | 116 | 10 | 145 | 0.553 | 0.595 | |
340 | 66.9 | 152 | 10 | 145 | 0.668 | 0.719 | |
360 | 86.9 | 188 | 10 | 145 | 0.782 | 0.842 | |
400 | 127 | 260 | 10 | 145 | 1.02 | 1.10 | |
500 | 227 | 440 | 10 | 145 | 1.69 | 1.81 | |
600 | 327 | 620 | 10 | 145 | 2.51 | 2.70 | |
700 | 427 | 800 | 10 | 145 | 3.54 | 3.81 | |
800 | 527 | 980 | 10 | 145 | 4.78 | 5.15 | |
900 | 627 | 1160 | 10 | 145 | 6.28 | 6.76 | |
1000 | 727 | 1340 | 10 | 145 | 8.05 | 8.67 | |
Liquid | 100 | -173 | -280 | 50 | 725 | 0.150 | 0.161 |
200 | -73.2 | -99.7 | 50 | 725 | 0.115 | 0.124 | |
300 | 26.9 | 80.3 | 50 | 725 | 0.0734 | 0.0790 | |
Supercritical phase | 400 | 127 | 260 | 50 | 725 | 0.102 | 0.110 |
500 | 227 | 440 | 50 | 725 | 0.300 | 0.322 | |
Liquid | 86.45 | -187 | -304 | 100 | 1450 | 0.149 | 0.160 |
100 | -173 | -280 | 100 | 1450 | 0.148 | 0.159 | |
120 | -153 | -244 | 100 | 1450 | 0.144 | 0.155 | |
140 | -133 | -208 | 100 | 1450 | 0.139 | 0.150 | |
160 | -113 | -172 | 100 | 1450 | 0.133 | 0.143 | |
180 | -93.2 | -136 | 100 | 1450 | 0.125 | 0.135 | |
200 | -73.2 | -99.7 | 100 | 1450 | 0.117 | 0.126 | |
220 | -53.2 | -63.7 | 100 | 1450 | 0.109 | 0.117 | |
240 | -33.2 | -27.7 | 100 | 1450 | 0.101 | 0.108 | |
260 | -13.2 | 8.3 | 100 | 1450 | 0.0925 | 0.0996 | |
280 | 6.9 | 44.3 | 100 | 1450 | 0.0849 | 0.0913 | |
300 | 26.9 | 80.3 | 100 | 1450 | 0.0779 | 0.0838 | |
320 | 46.9 | 116 | 100 | 1450 | 0.0716 | 0.0771 | |
340 | 66.9 | 152 | 100 | 1450 | 0.0660 | 0.0711 | |
360 | 86.9 | 188 | 100 | 1450 | 0.0611 | 0.0658 | |
Supercritical phase | 400 | 127 | 260 | 100 | 1450 | 0.0538 | 0.0579 |
500 | 227 | 440 | 100 | 1450 | 0.128 | 0.137 | |
600 | 327 | 620 | 100 | 1450 | 0.235 | 0.253 | |
700 | 427 | 800 | 100 | 1450 | 0.357 | 0.384 | |
800 | 527 | 980 | 100 | 1450 | 0.501 | 0.539 | |
900 | 627 | 1160 | 100 | 1450 | 0.669 | 0.720 | |
1000 | 727 | 1340 | 100 | 1450 | 0.865 | 0.931 |
Unit conversion thermal diffusivity:
square feet/second [ft 2 /s], square feet/hour [ft 2 /h], square meter/hour [m 2 /h], square meter/second [m 2 /s]
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