Nitrogen - Thermal Diffusivity vs. Temperature and Pressure
Thermal diffusivity is the rate of transfer of heat of a material from the hot side to the cold side - a measure of how quickly a material can absorb heat from its surroundings . It can be calculated by taking the thermal conductivity divided by density and specific heat capacity at constant pressure.
Thermal diffusivity has the SI derived unit of [m²/s] , and is usually denoted α but a, κ, K, and D are also used. The formula is:
α =k /(ρ CP ) [1]
where
k = is thermal conductivity [W/(m·K)]
ρ = density [kg/m³]
CP = specific heat capacity [J/(kg·K)]
Below, thermal diffusivity of nitrogen 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 Nitrogen at varying temperature and pressure : Density and specific weight , Dynamic and kinematic viscosity , Prandtl number , Specific heat (Heat capacity) and Thermal conductivity , and thermophysical properties at standard conditions ,
as well as thermal diffusivity of air , propane and water .
Thermal diffusivity of nitrogen at 1, 10, 50 and 100 bara (14.5, 145, 725 and 1450 psia), and varying temperature given as °C or °F:
Thermal diffusivity of nitrogen at gas-liquid equilibrium pressure and varying temperature given as °C or °F:
Thermal diffusivity of gaseous nitrogen at atmospheric pressure and given temperature, SI and Imperial units:
Temperature | Thermal diffusivity | Temperature | Thermal diffusivity | |||||
---|---|---|---|---|---|---|---|---|
[K] | [°C] | [x10-6 m2/s] | [m2/h] | [K] | [°F] | [x10 -5 ft2/s] | [ ft2/h] | |
78 | -195 | 1.489 | 0.00536 | 78 | -320 | 1.577 | 0.05679 | |
98 | -175 | 2.447 | 0.00881 | 89 | -300 | 2.118 | 0.07626 | |
123 | -150 | 3.934 | 0.01416 | 116 | -250 | 3.775 | 0.1359 | |
148 | -125 | 5.727 | 0.02062 | 144 | -200 | 5.843 | 0.2103 | |
173 | -100 | 7.807 | 0.02811 | 172 | -150 | 8.298 | 0.2987 | |
198 | -75 | 10.16 | 0.03658 | 200 | -100 | 11.11 | 0.4001 | |
223 | -50 | 12.77 | 0.04597 | 228 | -50 | 14.27 | 0.5137 | |
231 | -42 | 13.65 | 0.04916 | 231 | -44 | 14.67 | 0.5281 | |
248 | -25 | 15.62 | 0.05622 | 244 | -20 | 16.32 | 0.5874 | |
263 | -10 | 17.44 | 0.06277 | 255 | 0 | 17.74 | 0.6387 | |
268 | -5 | 18.06 | 0.06501 | 266 | 20 | 19.21 | 0.6917 | |
278 | 5 | 19.33 | 0.06960 | 278 | 40 | 20.73 | 0.7464 | |
283 | 10 | 19.98 | 0.07193 | 283 | 50 | 21.51 | 0.7743 | |
293 | 20 | 21.30 | 0.07670 | 294 | 70 | 23.09 | 0.8313 | |
298 | 25 | 21.98 | 0.07912 | 300 | 80 | 23.90 | 0.8604 | |
303 | 30 | 22.66 | 0.08158 | 305 | 90 | 24.72 | 0.8899 | |
323 | 50 | 25.46 | 0.09167 | 311 | 100 | 25.55 | 0.9198 | |
348 | 75 | 29.14 | 0.1049 | 339 | 150 | 29.85 | 1.074 | |
373 | 100 | 32.99 | 0.1187 | 366 | 200 | 34.38 | 1.238 | |
398 | 125 | 37.00 | 0.1332 | 394 | 250 | 39.14 | 1.409 | |
423 | 150 | 41.16 | 0.1482 | 422 | 300 | 44.10 | 1.588 | |
448 | 175 | 45.47 | 0.1637 | 478 | 400 | 54.59 | 1.965 | |
473 | 200 | 49.91 | 0.1797 | 533 | 500 | 65.75 | 2.367 | |
573 | 300 | 68.88 | 0.2480 | 644 | 700 | 89.74 | 3.231 | |
623 | 350 | 78.99 | 0.2844 | 700 | 800 | 102.5 | 3.689 | |
673 | 400 | 89.46 | 0.3221 | 755 | 900 | 115.6 | 4.163 | |
773 | 500 | 111.4 | 0.4011 | 811 | 1000 | 129.2 | 4.652 |
Thermal diffusivity of nitrogen at given temperature and pressure, SI and Imperial units:
State | Temperature | Pressure | Thermal diffusivity | ||||||
---|---|---|---|---|---|---|---|---|---|
[K] | [°C] | [°F] | [bara] | [psia] | [*10-6 m2/s] | [m2/h] | [x10 -5 ft2/s] | [ ft2/h] | |
Liquid at equilibrium |
63.15 | -210.0 | -346.0 | 0.125 | 1.82 | 0.09987 | 3.60E-04 | 0.1075 | 0.00387 |
69 | -204 | -335 | 0.332 | 4.82 | 0.09523 | 3.43E-04 | 0.1025 | 0.00369 | |
75 | -198 | -325 | 0.760 | 11.0 | 0.09011 | 3.24E-04 | 0.09699 | 0.00349 | |
79 | -194 | -317 | 1.22 | 17.8 | 0.08644 | 3.11E-04 | 0.09304 | 0.00335 | |
85 | -188 | -307 | 2.29 | 33.2 | 0.08053 | 2.90E-04 | 0.08668 | 0.00312 | |
89 | -184 | -299 | 3.31 | 47.9 | 0.07624 | 2.74E-04 | 0.08206 | 0.00295 | |
95 | -178 | -289 | 5.41 | 78.4 | 0.06918 | 2.49E-04 | 0.07447 | 0.00268 | |
99 | -174 | -281 | 7.26 | 105 | 0.06401 | 2.30E-04 | 0.06890 | 0.00248 | |
105 | -168 | -271 | 10.8 | 157 | 0.05539 | 1.99E-04 | 0.05962 | 0.00215 | |
109 | -164 | -263 | 13.8 | 201 | 0.04891 | 1.76E-04 | 0.05265 | 0.00190 | |
115 | -158 | -253 | 19.4 | 281 | 0.03766 | 1.36E-04 | 0.04054 | 0.00146 | |
121 | -152 | -242 | 26.4 | 383 | 0.02302 | 8.29E-05 | 0.02478 | 0.00089 | |
Gas at equilibrium |
63.15 | -210.0 | -346.0 | 0.125 | 1.82 | 7.877 | 0.02836 | 8.478 | 0.30523 |
69 | -204 | -335 | 0.332 | 4.82 | 3.506 | 0.01262 | 3.774 | 0.13585 | |
75 | -198 | -325 | 0.760 | 11.0 | 1.763 | 0.00635 | 1.897 | 0.06830 | |
79 | -194 | -317 | 1.22 | 17.8 | 1.182 | 0.00426 | 1.273 | 0.04582 | |
85 | -188 | -307 | 2.29 | 33.2 | 0.6937 | 0.00250 | 0.7467 | 0.02688 | |
89 | -184 | -299 | 3.31 | 47.9 | 0.5022 | 0.00181 | 0.5406 | 0.01946 | |
95 | -178 | -289 | 5.41 | 78.4 | 0.3198 | 0.00115 | 0.3442 | 0.01239 | |
99 | -174 | -281 | 7.26 | 105 | 0.2398 | 8.63E-04 | 0.2581 | 0.00929 | |
105 | -168 | -271 | 10.8 | 157 | 0.1562 | 5.62E-04 | 0.1681 | 0.00605 | |
109 | -164 | -263 | 13.8 | 201 | 0.1159 | 4.17E-04 | 0.1248 | 0.00449 | |
115 | -158 | -253 | 19.4 | 281 | 0.06909 | 2.49E-04 | 0.07437 | 0.00268 | |
121 | -152 | -242 | 26.4 | 383 | 0.03166 | 1.14E-04 | 0.03407 | 0.00123 | |
Liquid | 63.17 | -210.0 | -346.0 | 1 | 14.5 | 0.09991 | 3.60E-04 | 0.1075 | 0.00387 |
77.24 | -195.9 | -320.6 | 1 | 14.5 | 0.08808 | 3.17E-04 | 0.09481 | 0.00341 | |
Gas | 77.24 | -195.9 | -320.6 | 1 | 14.5 | 1.402 | 0.00505 | 1.509 | 0.05433 |
80 | -193.2 | -315.7 | 1 | 14.5 | 1.529 | 0.00550 | 1.645 | 0.05923 | |
100 | -173.2 | -279.7 | 1 | 14.5 | 2.548 | 0.00917 | 2.743 | 0.09875 | |
120 | -153.2 | -243.7 | 1 | 14.5 | 3.754 | 0.01352 | 4.041 | 0.1455 | |
140 | -133.2 | -207.7 | 1 | 14.5 | 5.151 | 0.01854 | 5.544 | 0.1996 | |
160 | -113.2 | -171.7 | 1 | 14.5 | 6.721 | 0.02420 | 7.234 | 0.2604 | |
180 | -93.2 | -135.7 | 1 | 14.5 | 8.464 | 0.03047 | 9.110 | 0.3280 | |
200 | -73.2 | -99.7 | 1 | 14.5 | 10.38 | 0.03738 | 11.18 | 0.4023 | |
220 | -53.2 | -63.7 | 1 | 14.5 | 12.44 | 0.04478 | 13.39 | 0.4820 | |
240 | -33.2 | -27.7 | 1 | 14.5 | 14.67 | 0.05282 | 15.79 | 0.5685 | |
260 | -13.2 | 8.3 | 1 | 14.5 | 17.03 | 0.06129 | 18.33 | 0.6598 | |
280 | 6.9 | 44.3 | 1 | 14.5 | 19.56 | 0.07040 | 21.05 | 0.7578 | |
300 | 26.9 | 80.3 | 1 | 14.5 | 22.21 | 0.07997 | 23.91 | 0.8608 | |
320 | 46.9 | 116.3 | 1 | 14.5 | 24.96 | 0.08987 | 26.87 | 0.9673 | |
340 | 66.9 | 152.3 | 1 | 14.5 | 27.88 | 0.1004 | 30.01 | 1.080 | |
360 | 86.9 | 188.3 | 1 | 14.5 | 30.89 | 0.1112 | 33.25 | 1.197 | |
400 | 126.9 | 260.3 | 1 | 14.5 | 37.28 | 0.1342 | 40.13 | 1.445 | |
500 | 226.9 | 440.3 | 1 | 14.5 | 54.88 | 0.1976 | 59.08 | 2.127 | |
600 | 326.9 | 620.3 | 1 | 14.5 | 74.31 | 0.2675 | 79.99 | 2.880 | |
700 | 426.9 | 800.3 | 1 | 14.5 | 95.24 | 0.3429 | 102.5 | 3.691 | |
800 | 526.9 | 980.3 | 1 | 14.5 | 117.5 | 0.4231 | 126.5 | 4.554 | |
900 | 626.9 | 1160.3 | 1 | 14.5 | 141.1 | 0.5081 | 151.9 | 5.469 | |
1000 | 726.9 | 1340.3 | 1 | 14.5 | 166.3 | 0.5986 | 179.0 | 6.444 | |
Liquid | 63.37 | -210 | -346 | 10 | 145 | 0.1003 | 3.61E-04 | 0.1079 | 0.00388 |
80 | -193 | -316 | 10 | 145 | 0.08632 | 3.11E-04 | 0.09292 | 0.00334 | |
100 | -173 | -280 | 10 | 145 | 0.06318 | 2.27E-04 | 0.06800 | 0.00245 | |
103.8 | -169.4 | -272.9 | 10 | 145 | 0.05728 | 2.06E-04 | 0.06166 | 0.00222 | |
Gas | 103.8 | -169.4 | -272.9 | 10 | 145 | 0.1710 | 6.15E-04 | 0.1840 | 0.00662 |
140.0 | -133.2 | -207.7 | 10 | 145 | 0.4573 | 0.00165 | 0.4922 | 0.01772 | |
160 | -113 | -172 | 10 | 145 | 0.6261 | 0.00225 | 0.6739 | 0.02426 | |
180 | -93 | -136 | 10 | 145 | 0.8087 | 0.00291 | 0.8704 | 0.03134 | |
200 | -73.2 | -99.7 | 10 | 145 | 1.007 | 0.00363 | 1.084 | 0.03903 | |
240 | -33.2 | -27.7 | 10 | 145 | 1.448 | 0.00521 | 1.559 | 0.05613 | |
300 | 26.9 | 80.3 | 10 | 145 | 2.218 | 0.00798 | 2.387 | 0.08593 | |
400 | 127 | 260 | 10 | 145 | 3.730 | 0.01343 | 4.015 | 0.1445 | |
500 | 227 | 440 | 10 | 145 | 5.489 | 0.01976 | 5.908 | 0.2127 | |
600 | 327 | 620 | 10 | 145 | 7.464 | 0.02687 | 8.035 | 0.2892 | |
800 | 527 | 980 | 10 | 145 | 11.76 | 0.04232 | 12.65 | 0.4555 | |
1100 | 827 | 1520 | 10 | 145 | 19.35 | 0.06966 | 20.83 | 0.7498 | |
1600 | 1327 | 2420 | 10 | 145 | 35.06 | 0.1262 | 37.74 | 1.359 | |
Liquid | 100 | -173 | -280 | 50 | 725 | 0.07101 | 2.56E-04 | 0.07643 | 0.00275 |
Supercritical phase |
600 | 327 | 620 | 50 | 725 | 1.529 | 0.00550 | 1.646 | 0.05925 |
1100 | 827 | 1520 | 50 | 725 | 3.933 | 0.01416 | 4.233 | 0.1524 | |
1600 | 1327 | 2420 | 50 | 725 | 7.093 | 0.02553 | 7.635 | 0.2748 | |
Liquid | 65.32 | -208 | -342 | 100 | 1450 | 0.1035 | 3.73E-04 | 0.1114 | 0.00401 |
80 | -193 | -316 | 100 | 1450 | 0.09376 | 3.38E-04 | 0.1009 | 0.00363 | |
100 | -173 | -280 | 100 | 1450 | 0.07813 | 2.81E-04 | 0.084 | 0.00303 | |
Supercritical phase |
200 | -73.2 | -99.7 | 100 | 1450 | 0.09050 | 3.26E-04 | 0.097 | 0.00351 |
300 | 26.9 | 80.3 | 100 | 1450 | 0.2333 | 8.40E-04 | 0.2511 | 0.00904 | |
400 | 127 | 260 | 100 | 1450 | 0.4001 | 0.00144 | 0.4307 | 0.01550 | |
500 | 227 | 440 | 100 | 1450 | 0.5882 | 0.00212 | 0.6331 | 0.02279 | |
600 | 327 | 620 | 100 | 1450 | 0.7922 | 0.00285 | 0.8527 | 0.03070 | |
1100 | 827 | 1520 | 100 | 1450 | 2.008 | 0.00723 | 2.162 | 0.07782 | |
1600 | 1327 | 2420 | 100 | 1450 | 3.598 | 0.01295 | 3.873 | 0.1394 |
Unit conversion thermal diffusivity:
square feet/second [ft2/s], square feet/hour [ft2/h], square meter/hour [m2/h], square meter/second [m2/s]
- 1 ft2/h = 2.7778x10-4 ft2/s = 0.09290 m2/h = 2.581x10 -5 m2/s
- 1 ft2/s = 3600 ft2/h = 334.45 m2/h = 0.09290 m2/s
- 1 m2/h = 2.7778x10-4 m2/s = 10.7639 ft2/h = 0.002990 ft2/s
- 1 m2/s = 3600 m2/h = 38750.1 ft2/h = 10.7639 ft2/s
Related Topics
• Fluid Mechanics
The study of fluids - liquids and gases. Involving velocity, pressure, density and temperature as functions of space and time.
• Material Properties
Properties of gases, fluids and solids. Densities, specific heats, viscosities and more.
• Thermodynamics
Work, heat and energy systems.
Related Documents
Air - Composition and Molecular Weight
Dry air is a mechanical mixture of nitrogen, oxygen, argon and several other gases in minor amounts.
Air - Thermal Diffusivity vs. Temperature and Pressure
Figures and tables withdry air thermal diffusivity vs. temperarure and pressure. SI and Imperial units.
Conductive Heat Transfer
Conductive heat transfer takes place in a solid if there is a temperature gradient.
Cryogenic Fluids and Liquefied Gas Properties
Cryogenic properties as density, boiling points and heat of evaporation for fluids like hydrogen, methane, oxygen, nitrogen, fluorine and helium.
Density vs. Specific Weight and Specific Gravity
An introduction to density, specific weight and specific gravity.
Heat Capacity
The amount of heat required to change the temperature of a substance by one degree.
Liquids - Thermal Conductivities
Some fluids and their thermal conductivities.
Nitrogen - Enthalpy, Internal Energy and Entropy vs. Temperature
Enthalpy, internal energy and entropy of Nitrogen as an ideal gas.
Nitrogen - Density and Specific Weight vs. Temperature and Pressure
Online calculator, figures and tables showing density and specific weight of nitrogen, N2, at temperatures ranging from -175 to 1325 °C (-280 to 2400 °F) at atmospheric and higher pressure - Imperial and SI Units.
Nitrogen - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
Online calculator, figures and tables showing dynamic and kinematic viscosity of nitrogen, N2, at varying temperature and pressure - Imperial and SI Units.
Nitrogen - Prandtl number vs. Temperature and Pressure
Figures and tables showing Prandtl number of nitrogen at varying temperarure and pressure, SI and Imperial units.
Nitrogen - Thermal Conductivity vs. Temperature and Pressure
Online calculator, figures and tables showing thermal conductivity of nitrogen, N2, at varying temperarure and pressure, SI and Imperial units.
Nitrogen - Thermophysical Properties
Chemical, Physical and Thermal Properties of Nitrogen - N2.
Nitrogen Gas - Specific Heat vs. Temperature
Specific heat of Nitrogen Gas - N2 - at temperatures ranging 175 - 6000 K
Propane - Thermal Diffusivity vs. Temperature and Pressure
Figures and tables showing thermal diffusivity of liquid and gaseous propane at varying temperarure and pressure, SI and Imperial units.
Water - Thermal Diffusivity vs. Temperature and Pressure
Figures and tables with thermal diffusivity of liquids and gaseous water at varying temperarures and pressures - SI and Imperial units.