Process Heat Transfer: Principles and Applications

| Acceleration | 1 m/s 2 = 4.2520 10 7ft/h 2 |
| Area | 1m 2 = 10.764 ft 2 |
| Density | 1 kg/m 3 = 0.06243 lbm/ft 3 |
| Energy | 1J = 0.239 cal = 9.4787 10 ?4Btu |
| Force | 1N = 0.22481 lbf |
| Fouling factor | 1 m 2 K/W = 5.6779 h ft 2 F/Btu |
| Heat capacity flow rate | 1kW/K =1kW/ C = 1895.6 Btu/h F |
| Heat flux | 1W/m 2 =0.3171 Btu/h-ft 2 |
| Heat generation rate | 1 W/m 3 = 0.09665 Btu/h ft 3 |
| Heat transfer coefficient | 1 W/m 2 K = 0.17612 Btu/h ft 2 F |
| Heat transfer rate | 1W =3.4123 Btu/h |
| Kinematic viscosity and thermal diffusivity | 1 m 2/s = 3.875 10 4 ft 2/h |
| Latent heat and specific enthalpy | 1kJ/kg = 0.42995 Btu/lbm |
| Length | 1m = 3.2808 ft |
| Mass | 1kg = 2.2046 lbm |
| Mass flow rate | 1kg/s =7936.6lbm/h |
| Mass flux | 1 kg/s m 2 = 737.35 lbm/h ft 2 |
| Power | 1kW =3412 Btu/h = 1.341 hp |
| Pressure (stress) | 1 Pa (1 N/m 2) = 0.020886 lbf/ft 2 = 1.4504 10 ?4 psi = 4.015 10 ?3 in. H 2O |
| Pressure | 1.01325 10 5 Pa = 1 atm = 14.696 psi = 760torr = 406.8 in. H2O |
| Specific heat | 1 kJ/kg K = 0.2389 Btu/lbm F |
| Surface tension | 1N/m =1000 dyne/cm = 0.068523 lbf/ft |