A. Δt
B. Δt2
C. Δt3
D. √(Δt)
A. Δt
B. Δt2
C. Δt3
D. √(Δt)
A. 50 -100 Kcal/hr.m2.°C
B. 50 -100 W/m2.°K
C. 50 -100 BTU/hr. ft.2°F
D. 1000 – 1500 BTU/hr. ft.2°F
A. Basket type
B. Horizontal tube
C. Calandria
D. None of these
A. Increases
B. Decreases
C. Is not affected
D. May increase or decrease; depends on the feed
A. Increases the heating area required
B. Reduces the economy
C. Both A. and B.
D. Decreases the heating area required
A. Baffle spacing & shell diameter
B. Tube diameter & pitch
C. Viscosity, density & mass velocity of shell side fluid
D. None of these
A. Coated
B. Oily
C. Glazed & polished
D. Smooth
A. 0.35
B. 0.45
C. 0.55
D. 0.85
A. K/h0
B. 2K/h0
C. h0/K
D. h0/2K
A. Same velocity profile or equal eddy diffusivities
B. Thermal or pressure mass diffusion
C. Viscous heating or chemical reaction
D. Both B. and C.