A. (ΔT)1/4
B. (ΔT)1/2
C. (ΔT)5/4
D. (ΔT)3/4
Chemical Heat Transfer
Chemical Heat Transfer
A. Viscosity
B. Density
C. Thermal conductivity
D. Heat capacity
A. 555
B. 55.5
C. 0.55
D. 0.15
A. Prandtl
B. Nusselt
C. Stanton
D. Grashoff
A. Zero
B. One
C. ∞
D. Between 0 and ∞
A. 5.6697 × 10-8W/m2.°K4
B. 0.1714 × 10-8W/m2.°K4
C. 5.6697 × 10-8kcal/m2. °K4
D. 0.1714 × 10-8kcal/m2. °K4
A. 5.6
B. 0.025
C. 3.5
D. 0.0035
A. Plate type
B. Double pipe type with fin on steam side
C. Double pipe type with fin on air side
D. Shell and tube type
A. Agitated film evaporator
B. Long tube vertical evaporator
C. Open pan evaporator
D. None of these
A. 1000
B. 727
C. 800
D. 1200
