Heat Transfer coefficients – Overal Heat Transfer Coefficient –U
Used for informational reference only
Types | Application | Overall Heat Transfer Coefficient - U - | |
---|---|---|---|
W/(m2 K) | Btu/(ft2 oF h) | ||
"Tubular, heating or cooling" | Gas at atmospheric pressure inside and outside tubes | May-35 | 6-Jan |
Gas at high pressure inside and outside tubes | 150 - 500 | 25 - 90 | |
Liquid outside (inside) and gas at atmospheric pressure inside (outside) tubes | 15 - 70 | 15-Mar | |
Gas at high pressure inside and liquid outside tubes | 200 - 400 | 35 - 70 | |
Liquids inside and outside tubes | 150 - 1200 | 25 - 200 | |
Steam outside and liquid inside tubes | 300 - 1200 | 50 - 200 | |
"Tubular, condensation" | Steam outside and cooling water inside tubes | 1500 - 4000 | 250 - 700 |
Organic vapors or ammonia outside and cooling water inside tubes | 300 - 1200 | 50 - 200 | |
"Tubular, evaporation" | "steam outside and high-viscous liquid inside tubes, natural circulation" | 300 - 900 | 50 - 150 |
"steam outside and low-viscous liquid inside tubes, natural circulation" | 600 - 1700 | 100 - 300 | |
"steam outside and liquid inside tubes, forced circulation" | 900 - 3000 | 150 - 500 | |
Air-cooled heat exchangers | Cooling of water | 600 - 750 | 100 - 130 |
Cooling of liquid light hydrocarbons | 400 - 550 | 70 - 95 | |
Cooling of tar | 30 - 60 | 10-May | |
Cooling of air or flue gas | 60 - 180 | 30-Oct | |
Cooling of hydrocarbon gas | 200 - 450 | 35 - 80 | |
Condensation of low pressure steam | 700 - 850 | 125 - 150 | |
Condensation of organic vapors | 350 - 500 | 65 - 90 | |
Plate heat exchanger | liquid to liquid | 1000 - 4000 | 150 - 700 |
Spiral heat exchanger | liquid to liquid | 700 - 2500 | 125 - 500 |
condensing vapor to liquid | 900 - 3500 | 150 - 700 |