A. Counter flow with process stream on shell side
B. Counter flow with process stream on tube side
C. Parallel flow with process stream on shell side
D. Parallel flow with process stream on tube side
A. Counter flow with process stream on shell side
B. Counter flow with process stream on tube side
C. Parallel flow with process stream on shell side
D. Parallel flow with process stream on tube side
A. Grashoff number
B. Peclet number
C. Reynolds number
D. Prandtl number
A. BTU/hr. ft2°F
B. BTU/hr. °F. ft
C. BTU/hr. °F
D. BTU/hr. ft
A. 40.5
B. 34.4
C. 26.8
D. 25
A. P and Q
B. P and R
C. P and S
D. R and S
A. Finned tube heat exchanger with air inside and steam outside
B. Finned tube heat exchanger with air outside and steam inside
C. Shell and tube heat exchanger with air inside tubes and steam on shell side
D. Shell and tube heat exchanger with air on shell side and steam inside tubes
A. Plain carbon steel
B. Stainless steel
C. Lead
D. Copper
A. W/m.k
B. W/m
C. W/m.k2
D. None, ‘a’ is just a number
A. 0.001 to 1
B. 0.6 to 120
C. 0.5 to 5
D. 120 to 400
A. 0.06 to 120
B. 0.6 to 120
C. 1 to 103
D. 1 to 50