- (A) Temperature gradient
- (B) Mechanical strength of the equipment
- (C) Heat transfer area
- (D) Heat transfer co-efficient
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- (A) Pool
- (B) Nucleate
- (C) Transition
- (D) Film
- (A) K/h0
- (B) 2K/h0
- (C) hi/K
- (D) 2hi/K
- (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

