Butane - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
The viscosity of a fluid is a measure of its resistance to gradual deformation by shear stress or tensile stress .
For further definitions, go to Absolute (dynamic) and kinematic viscosity . Absolute or dynamic viscosity is used to calculate Reynold's Number to determine if a fluid flow is laminar, transient or turbulent.
Tabulated values of butane viscosity and viscosity units conversion are given below the figures.
Online Butane Viscosity Calculator
The calculator below can be used to estimate butane dynamic or kinematic viscosity at given temperatures and atmospheric pressure.
The output dynamic viscosity is given as Pa*s, N*s/m2, cP, mPa*s, lbf *s/ft2and lbm /(ft*h),
while the kinematic viscosity is given as cSt, m2/s, and ft2/s
Choose the actual unit of temperature:
See also other properties of Butane at varying temperature and pressure: Density and specific weight , Specific Heat (Heat Capacity) and Thermal conductivity , and Thermophysical properties at standard conditions ,
as well as dynamic and kinematic viscosity of air , ammonia , benzene , carbon dioxide , ethane , ethanol , ethylene , methane , methanol , nitrogen , oxygen , propane and water .
Dynamic and kinematic viscosity of gaseous butane at atmospheric pressure and varying temperature:
Dynamic and kinematic viscosity of liquid butane at atmospheric pressure and varying temperature:
Dynamic viscosity of butane at varying temperature and 1, 10, 50 and 100 bara (14.5, 145, 725 and 1450 psia):
Kinematic viscosity of butane at varying temperature and 1, 10, 50 and 100 bara (14.5, 145, 725 and 1450 psia):
Dynamic viscosity of butane at gas-liquid equilibrium pressure:
Kinematic viscosity of butane at gas-liquid equilibrium pressure:
Dynamic (absolute) and kinematic viscosity of butane at given temperatures and pressures, SI and Imperial units:
For full table with Dynamic and Kinematic Viscosity - rotate the screen!
State | Temperature | Pressure | Dynamic (Absolute) Viscosity | Kinematic Viscosity | ||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|
[K] | [°C] | [°F] | [bara] | [psia] | [μPa s] | [cP] | [x10-6 lbf s/ft2] | [x10-6 lbm /ft s] | [lbm /ft h] | [cSt], [x10-6 m2/s] | [x10-6 ft2/s] | |
Liquid at equilibrium |
134.9 | -138.25 | -216.85 | 6.7E-06 | 9.7E-05 | 2304 | 2.304 | 48.12 | 1548 | 5.574 | 3.13 | 33.7 |
150 | -123 | -190 | 8.6E-05 | 1.2E-03 | 1370 | 1.370 | 28.61 | 920.6 | 3.314 | 1.90 | 20.5 | |
200 | -73 | -100 | 0.0194 | 0.281 | 496.5 | 0.4965 | 10.37 | 333.6 | 1.201 | 0.737 | 7.93 | |
220 | -53 | -64 | 0.0781 | 1.13 | 373.4 | 0.3734 | 7.799 | 250.9 | 0.9033 | 0.570 | 6.14 | |
240 | -33.2 | -28 | 0.241 | 3.49 | 290.9 | 0.2909 | 6.076 | 195.5 | 0.7037 | 0.458 | 4.93 | |
260 | -13.2 | 8.3 | 0.610 | 8.84 | 232.3 | 0.2323 | 4.852 | 156.1 | 0.5620 | 0.378 | 4.07 | |
280 | 6.9 | 44.3 | 1.33 | 19.3 | 189.0 | 0.1890 | 3.947 | 127.0 | 0.4572 | 0.319 | 3.43 | |
300 | 26.9 | 80.3 | 2.58 | 37.4 | 155.6 | 0.1556 | 3.250 | 104.6 | 0.3764 | 0.273 | 2.93 | |
320 | 46.9 | 116 | 4.56 | 66.2 | 129.1 | 0.1291 | 2.696 | 86.75 | 0.3123 | 0.236 | 2.54 | |
340 | 66.9 | 152 | 7.52 | 109 | 107.2 | 0.1072 | 2.239 | 72.04 | 0.2593 | 0.206 | 2.22 | |
360 | 86.9 | 188 | 11.7 | 170 | 88.54 | 0.08854 | 1.849 | 59.50 | 0.2142 | 0.181 | 1.95 | |
380 | 106.9 | 224 | 17.4 | 252 | 71.86 | 0.07186 | 1.501 | 48.29 | 0.1738 | 0.158 | 1.70 | |
400 | 126.9 | 260 | 25.0 | 362 | 55.96 | 0.05596 | 1.169 | 37.60 | 0.1354 | 0.137 | 1.47 | |
420 | 146.9 | 296 | 34.9 | 506 | 37.39 | 0.03739 | 0.7809 | 25.12 | 0.09045 | 0.114 | 1.23 | |
425.13 | 151.98 | 305.56 | 38.0 | 551 | 23.90 | 0.02390 | 0.4992 | 16.06 | 0.05782 | 0.105 | 1.13 | |
Gas at equilibrium |
134.9 | -138.25 | -216.85 | 6.7E-06 | 9.7E-05 | 3.321 | 0.00332 | 0.06936 | 2.232 | 0.00803 | 96261 | 1036142 |
150 | -123 | -190 | 8.6E-05 | 1.2E-03 | 3.709 | 0.00371 | 0.07746 | 2.492 | 0.00897 | 9284 | 99933 | |
200 | -73 | -100 | 0.0194 | 0.281 | 4.979 | 0.00498 | 0.1040 | 3.346 | 0.01204 | 73.3 | 789 | |
220 | -53 | -64 | 0.0781 | 1.13 | 5.477 | 0.00548 | 0.1144 | 3.680 | 0.01325 | 21.9 | 236 | |
240 | -33.2 | -28 | 0.241 | 3.49 | 5.966 | 0.00597 | 0.1246 | 4.009 | 0.01443 | 8.38 | 90.2 | |
260 | -13.2 | 8.3 | 0.610 | 8.84 | 6.450 | 0.00645 | 0.1347 | 4.334 | 0.01560 | 3.82 | 41.1 | |
280 | 6.9 | 44.3 | 1.33 | 19.3 | 6.935 | 0.00694 | 0.1448 | 4.660 | 0.01678 | 1.99 | 21.4 | |
300 | 26.9 | 80.3 | 2.58 | 37.4 | 7.436 | 0.00744 | 0.1553 | 4.997 | 0.01799 | 1.14 | 12.3 | |
320 | 46.9 | 116 | 4.56 | 66.2 | 7.978 | 0.00798 | 0.1666 | 5.361 | 0.01930 | 0.707 | 7.61 | |
340 | 66.9 | 152 | 7.52 | 109 | 8.601 | 0.00860 | 0.1796 | 5.780 | 0.02081 | 0.464 | 5.00 | |
360 | 86.9 | 188 | 11.7 | 170 | 9.369 | 0.00937 | 0.1957 | 6.296 | 0.02266 | 0.319 | 3.44 | |
380 | 107 | 224 | 17.4 | 252 | 10.41 | 0.01041 | 0.2174 | 6.995 | 0.02518 | 0.227 | 2.44 | |
400 | 127 | 260 | 25.0 | 362 | 12.03 | 0.01203 | 0.2513 | 8.084 | 0.02910 | 0.165 | 1.77 | |
420 | 147 | 296 | 34.9 | 506 | 15.96 | 0.01596 | 0.3333 | 10.72 | 0.03861 | 0.118 | 1.27 | |
425.13 | 151.98 | 305.56 | 38.0 | 551 | 23.90 | 0.02390 | 0.4992 | 16.06 | 0.05782 | 0.105 | 1.13 | |
Liquid | 150 | -123 | -190 | 1 | 14.5 | 1371 | 1.371 | 28.63 | 921.2 | 3.316 | 1.90 | 20.5 |
200 | -73.2 | -100 | 1 | 14.5 | 496.9 | 0.4969 | 10.38 | 333.9 | 1.202 | 0.737 | 7.94 | |
250 | -23.2 | -9.7 | 1 | 14.5 | 259.4 | 0.2594 | 5.418 | 174.3 | 0.6276 | 0.415 | 4.47 | |
272.31 | -0.8 | 30.5 | 1 | 14.5 | 204.2 | 0.2042 | 4.265 | 137.2 | 0.4940 | 0.339 | 3.65 | |
Gas | 272.31 | -0.8 | 30.5 | 1 | 14.5 | 6.748 | 0.00675 | 0.1409 | 4.534 | 0.01632 | 2.521 | 27.14 |
300 | 26.9 | 80.3 | 1 | 14.5 | 7.452 | 0.00745 | 0.1556 | 5.008 | 0.01803 | 3.11 | 33.43 | |
350 | 76.9 | 170 | 1 | 14.5 | 8.691 | 0.00869 | 0.1815 | 5.840 | 0.02102 | 4.28 | 46.03 | |
400 | 127 | 260 | 1 | 14.5 | 9.899 | 0.00990 | 0.2067 | 6.652 | 0.02395 | 5.60 | 60.30 | |
450 | 177 | 350 | 1 | 14.5 | 11.08 | 0.01108 | 0.2315 | 7.447 | 0.02681 | 7.08 | 76.23 | |
500 | 227 | 440 | 1 | 14.5 | 12.25 | 0.01225 | 0.2558 | 8.230 | 0.02963 | 8.72 | 93.82 | |
550 | 277 | 530 | 1 | 14.5 | 13.40 | 0.01340 | 0.2798 | 9.001 | 0.03240 | 10.502 | 113.04 | |
Liquid | 150 | -123 | -190 | 10 | 145 | 1381 | 1.381 | 28.85 | 928.2 | 3.341 | 1.91 | 20.6 |
200 | -73.2 | -100 | 10 | 145 | 500.6 | 0.5006 | 10.45 | 336.4 | 1.211 | 0.742 | 7.99 | |
250 | -23.2 | -9.7 | 10 | 145 | 261.8 | 0.2618 | 5.468 | 175.9 | 0.6333 | 0.418 | 4.50 | |
300 | 26.9 | 80.3 | 10 | 145 | 157.3 | 0.1573 | 3.285 | 105.7 | 0.3805 | 0.275 | 2.96 | |
350 | 76.9 | 170 | 10 | 145 | 97.70 | 0.09770 | 2.040 | 65.65 | 0.2363 | 0.193 | 2.08 | |
352.62 | 79.5 | 175 | 10 | 145 | 95.14 | 0.09514 | 1.987 | 63.93 | 0.2301 | 0.190 | 2.04 | |
Gas | 352.62 | 79.5 | 175 | 10 | 145 | 9.063 | 0.00906 | 0.1893 | 6.090 | 0.02192 | 0.365 | 3.93 |
400 | 127 | 260 | 10 | 145 | 10.16 | 0.01016 | 0.2121 | 6.825 | 0.02457 | 0.511 | 5.50 | |
450 | 177 | 350 | 10 | 145 | 11.32 | 0.01132 | 0.2365 | 7.609 | 0.02739 | 0.673 | 7.24 | |
500 | 227 | 440 | 10 | 145 | 12.48 | 0.01248 | 0.2605 | 8.383 | 0.03018 | 0.846 | 9.11 | |
550 | 277 | 530 | 10 | 145 | 13.61 | 0.01361 | 0.2843 | 9.146 | 0.03293 | 1.03 | 11.11 | |
Liquid | 150 | -123 | -190 | 50 | 725 | 1428 | 1.428 | 29.83 | 959.7 | 3.455 | 1.97 | 21.3 |
200 | -73.2 | -100 | 50 | 725 | 516.9 | 0.5169 | 10.80 | 347.3 | 1.250 | 0.763 | 8.21 | |
250 | -23.2 | -9.7 | 50 | 725 | 272.3 | 0.2723 | 5.687 | 183.0 | 0.6587 | 0.432 | 4.65 | |
300 | 26.9 | 80.3 | 50 | 725 | 166.0 | 0.1660 | 3.466 | 111.5 | 0.4015 | 0.287 | 3.09 | |
350 | 76.9 | 170 | 50 | 725 | 106.8 | 0.1068 | 2.230 | 71.74 | 0.2583 | 0.206 | 2.22 | |
400 | 127 | 260 | 50 | 725 | 65.43 | 0.06543 | 1.366 | 43.96 | 0.1583 | 0.150 | 1.61 | |
Supercritical phase |
450 | 177 | 350 | 50 | 725 | 19.32 | 0.01932 | 0.4035 | 12.98 | 0.04674 | 0.107 | 1.15 |
500 | 227 | 440 | 50 | 725 | 14.78 | 0.01478 | 0.3086 | 9.928 | 0.03574 | 0.149 | 1.60 | |
550 | 277 | 530 | 50 | 725 | 14.93 | 0.01493 | 0.3118 | 10.03 | 0.03611 | 0.191 | 2.06 | |
Liquid | 150 | -123 | -190 | 100 | 1450 | 1488 | 1.488 | 31.08 | 1000 | 3.600 | 2.05 | 22.1 |
200 | -73.2 | -100 | 100 | 1450 | 537.3 | 0.5373 | 11.22 | 361.0 | 1.300 | 0.790 | 8.50 | |
250 | -23.2 | -9.7 | 100 | 1450 | 285.2 | 0.2852 | 5.956 | 191.6 | 0.6899 | 0.449 | 4.84 | |
300 | 26.9 | 80.3 | 100 | 1450 | 176.3 | 0.1763 | 3.683 | 118.5 | 0.4266 | 0.301 | 3.24 | |
350 | 76.9 | 170 | 100 | 1450 | 116.8 | 0.1168 | 2.439 | 78.48 | 0.2825 | 0.220 | 2.36 | |
400 | 127 | 260 | 100 | 1450 | 77.78 | 0.07778 | 1.625 | 52.27 | 0.1882 | 0.167 | 1.79 | |
450 | 177 | 350 | 100 | 1450 | 48.33 | 0.04833 | 1.009 | 32.47 | 0.1169 | 0.127 | 1.36 | |
Supercritical phase |
500 | 227 | 440 | 100 | 1450 | 27.08 | 0.02708 | 0.5655 | 18.19 | 0.06550 | 0.101 | 1.09 |
550 | 277 | 530 | 100 | 1450 | 19.39 | 0.01939 | 0.4049 | 13.03 | 0.04690 | 0.103 | 1.11 | |
Liquid | 150 | -123 | -190 | 300 | 4351 | 1748 | 1.748 | 36.51 | 1175 | 4.229 | 2.38 | 25.6 |
200 | -73.2 | -100 | 300 | 4351 | 619.2 | 0.6192 | 12.93 | 416.1 | 1.498 | 0.895 | 9.63 | |
250 | -23.2 | -9.7 | 300 | 4351 | 335.1 | 0.3351 | 6.998 | 225.1 | 0.8105 | 0.515 | 5.54 | |
300 | 26.9 | 80.3 | 300 | 4351 | 214.5 | 0.2145 | 4.481 | 144.2 | 0.5190 | 0.352 | 3.79 | |
350 | 76.9 | 170 | 300 | 4351 | 150.5 | 0.1505 | 3.142 | 101.1 | 0.3640 | 0.265 | 2.86 | |
400 | 127 | 260 | 300 | 4351 | 110.9 | 0.1109 | 2.316 | 74.53 | 0.2683 | 0.212 | 2.28 | |
450 | 177 | 350 | 300 | 4351 | 83.81 | 0.08381 | 1.750 | 56.32 | 0.2027 | 0.175 | 1.89 | |
Supercritical phase |
500 | 227 | 440 | 300 | 4351 | 64.10 | 0.06410 | 1.339 | 43.07 | 0.1551 | 0.148 | 1.59 |
550 | 277 | 530 | 300 | 4351 | 49.56 | 0.04956 | 1.035 | 33.30 | 0.1199 | 0.127 | 1.37 | |
Liquid | 150 | -123 | -190 | 650 | 9427 | 2300 | 2.300 | 48.04 | 1546 | 5.565 | 3.08 | 33.2 |
200 | -73.2 | -100 | 650 | 9427 | 766.5 | 0.7665 | 16.01 | 515.0 | 1.854 | 1.08 | 11.6 | |
250 | -23.2 | -9.7 | 650 | 9427 | 419.1 | 0.4191 | 8.754 | 281.6 | 1.014 | 0.623 | 6.71 | |
300 | 26.9 | 80.3 | 650 | 9427 | 275.1 | 0.2751 | 5.746 | 184.9 | 0.6656 | 0.431 | 4.64 | |
350 | 76.9 | 170 | 650 | 9427 | 199.8 | 0.1998 | 4.172 | 134.2 | 0.4833 | 0.331 | 3.56 | |
400 | 127 | 260 | 650 | 9427 | 154.3 | 0.1543 | 3.222 | 103.7 | 0.3731 | 0.270 | 2.90 | |
450 | 177 | 350 | 650 | 9427 | 123.8 | 0.1238 | 2.585 | 83.17 | 0.2994 | 0.229 | 2.47 | |
Supercritical phase |
500 | 227 | 440 | 650 | 9427 | 101.8 | 0.1018 | 2.126 | 68.39 | 0.2462 | 0.200 | 2.15 |
550 | 277 | 530 | 650 | 9427 | 85.08 | 0.08508 | 1.777 | 57.17 | 0.2058 | 0.177 | 1.90 |
Viscosity Dynamic, Absolute
Absolute or Dynamic Viscosity Unit Converter
centipoise [cP], gram/(centimeter second) [g/(cm s)] = poise [P], kilogram/meter second [kg/m s]=newton second/square meter [N s/m2]= pascal second [Pa s], pound/(foot hour) [lb/(ft h)], pound/(foot second) [lb/(ft s)], reyn [reyn]
- 1 cP = 0.001 Pa s = 0.01 P = = 0.01 g/(cm sec) = 6.72197x10-4 lb/(ft s) = 2.4191 lb/(ft h)
- 1 lb/(ft h) = 0.00027778 lb/(ft s) = 0.00041338 Pa s = 0.0041338 P = 0.41338 cP
- 1 lb/(ft s) = 3600 lb/(ft h) = 1.48816 Pa s = 14.8816 P = 1488.16 cP
- 1 kg/(m s ) = 1 (N s)/m2= 1 Pa s = 10 P = 1000 cP = 0.672197 lb/(ft s) = 2419.09 lb/(ft h)
- 1 (N s)/m2= 1 kg/(m s ) = 1 Pa s = 10 P = 1000 cP = 0.672197 lb/(ft s) = 2419.09 lb/(ft h)
- 1 P = 1 g/(cm s) = 0.1 Pa s = 100 cP = 0.067197 lb/(ft s) = 241.909 lb/(ft h)
- 1 Pa s = 1 kg/(m s) = 1 (N s)/m2= 10 P = 1000 cP = 0.672197 lb/(ft s) = 2419.08 lb/(ft h) = 0.00014504 reyn
- 1 reyn = 6894.76 Pa s
Viscosity Kinematic
Kinematic Viscosity Unit Converter
centistoke [cSt] = square millimeter/second [mm2/s], square foot/hour [ft2/h], square foot/second [ft2/s], square inch/second [in2/s], square meter/hour [m2/h], square meter/second [m2/s], stoke [St] = square centimeter/second [cm2/s]
- 1 cm2/s = 1 St = 100 mm2/s = 100 cSt = 1x10-4 m2/s = 0.36 m2/h = 1.07639x10-3 ft2/s = 3.875008 ft2/h = 0.1550003 in2/s
- 1 cSt = 1 mm2/s = 0.01 St = 1x10-6 m2/s = 0.0036 m2/h = 1.07639x10 -5 ft2/s = 0.03875008 ft2/h = 0.001550003 in2/s
- 1 ft2/h = 2.7778x10-4 ft2/s = 0.04 in2/s = 2.58064x10 -5 m2/s = 0.09290304 m2/h = 25.8064 cS = 0.258064 St
- 1 ft2/s = 3600 ft2/h = 144 in2/s = 0.09290304 m2/s = 334.451 m2/h = 92903.04 cSt = 929.0304 St
- 1 in2/s = 0.0069444 ft2/s = 25 ft2/h = 0.00064516 m2/s = 2.322576 m2/h = 645.16 cSt = 6.4516 St
- 1 m2/h = 1/3600 m2/s = 2.7778x10-4 m2/s = 2.7778 cm2/s = 277.78 mm2/s = 277.78 cSt = 2.7778 St = 0.00298998 ft2/s = 10.7639 ft2/h = 0.430556 in2/s
- 1 m2/s = 3600 m2/h = 1x104 cm2/s = 1x104 St = 1x106 mm2/s = 1x106 cSt = 10.7639 ft2/s = 38750.08 ft2/h = 1550003 in2/s
- 1 mm2/s = 1 cSt = 1x10-6 m2/s = 0.0036 m2/h = 0.01 cm2/s = 0.01 St = 1.07639x10 -5 ft2/s = 0.03875008 ft2/h = 0.001550003 in2/s
- 1 St = 1 cm2/s = 100 cSt = 100 mm2/s = 1x10-4 m2/s = 0.36 m2/h = 1.076x10-3 ft2/s = 3.875008 ft2/h = 0.1550003 in2/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.
• Viscosities
Viscosities of products and chemical species at varying conditions.
Related Documents
Absolute or Dynamic Viscosity Online Converter
Convert between dynamic or absolute viscosity units - Poiseuille, Poise, centPoise and more.
Air - Dynamic and Kinematic Viscosity
Online calculator, figures and tables with dynamic (absolute) and kinematic viscosity for air at temperatures ranging -100 to 1600°C (-150 to 2900°F) and at pressures ranging 1 to 10 000 bara (14.5 - 145000 psia) - SI and Imperial Units.
Ammonia - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
Online calculator, figures and tables showing dynamic (absolute) and kinematic viscosity of gasous and liquid ammonia at temperatures ranging from -73 to 425°C (-100 to 800°F) at pressure ranging from 1 to 1000 bara (14.5 - 14500 psia) - SI and Imperial Units.
Benzene - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
Online calculator, figures and table showing dynamic and kinematic viscosity of benzene, C6H6, at varying temperature and pressure - Imperial and SI Units.
Butane - Density and Specific Weight vs. Temperature and Pressure
Online calculators, figures and tables showing density and specific weight of liquid and gaseous butane, C4H10, at varying temperarure and pressure, SI and Imperial units.
Butane - Specific Heat vs. Temperature and Pressure
Online calculators, figures and tables showing specific heat, Cp and Cv, of gasous and liquid butane, C4H10, at varying temperarure and pressure, SI and Imperial units.
Butane - Thermal Conductivity vs. Temperature and Pressure
Online calculators, figures and tables showing thermal conductivity of liquid and gaseous butane, C4H10, at varying temperature and pressure, SI and Imperial units.
Butane - Thermophysical Properties
Chemical, physical and thermal properties of n-Butane.
Carbon Dioxide - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
Online calculator, figures and table showing dynamic and kinematic viscosity of carbon dioxide, CO2, at varying temperature and pressure - Imperial and SI Units.
Ethane - Dynamic and Kinematic Viscosity
Online calculator, figures and tables showing dynamic and kinematic viscosity of ethane, C2H6, at varying temperature and pressure - Imperial and SI Units
Ethanol - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
Online calculator, figures and tables showing dynamic and kinematic viscosity of ethanol, C2H5OH, at varying temperature and pressure - Imperial and SI Units.
Ethylene - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
Online calculator, figures and tables showing dynamic and kinematic viscosity of ethylene, C2H4, also called ethene or acetene, at varying temperature and pressure - Imperial and SI Units.
Fuel Gases - Combustion Values
Combustion values for fuel gases like natural gas, propane and butane - Btu per cubic feet.
Fuel Gases - Flame Temperatures
Adiabatic flame temperatures for common fuel gases - propane, butane, acetylene and more - in air or oxygen atmospheres.
Gases - Gross and Net Heat Values
Gross heat and net heat values for gases like hydrogen, methane and more.
Hydrocarbons - Vapor Pressures
Vapor pressure vs. temperature for propane, n-butane, n-heptane and n-pentane hydrocarbons.
Kinematic Viscosity - Online Converter
Convert between kinematic viscosity units like centistokes, poise, lentor and more.
Methane - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
Online calculator, figures and tables showing dynamic and kinematic viscosity of methane, CH4, at varying temperature and pressure - Imperial and SI Units.
Methanol - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
Online calculator, figures and tables showing dynamic and kinematic viscosity of liquid methanol,CH3OH, at varying temperature - 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.
Oxygen - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
Online calculator, figures and tables showing dynamic and kinematic viscosity of oxygen, O2, at varying temperature and pressure - Imperial and SI Units.
Propane - Dynamic and Kinematic Viscosity vs. Temperature and Pressure
Online calculators, figures and tables showing dynamic and kinematic viscosity of liquid and gaseous propane at varying temperarure and pressure, SI and Imperial units.
Propane Butane Mixture - Evaporation Pressure
Evaporation pressure of propane butane mixture vs. temperature.
Reynolds Number
Introduction and definition of the dimensionless Reynolds Number - online calculators.
Viscosity - Absolute (Dynamic) vs. Kinematic
Vicosity is a fluid's resistance to flow and can be valued as dynamic (absolute) or kinematic.
Water - Dynamic (Absolute) and Kinematic Viscosity vs. Temperature and Pressure
Free online calculator - figures and tables with viscosity of water at temperatures ranging 0 to 360°C (32 to 675°F) - Imperial and SI Units.