A. Conduction
B. Natural convection
C. Forced convection
D. None of these
A. Agitated film evaporator
B. Long tube vertical evaporator
C. Open pan evaporator
D. None of these
A. Provide very large heat transfer co-efficient
B. Results in making part of the heating surface inactive
C. Results in abruptly increased velocity
D. None of these
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. Increases the heating area required
B. Reduces the economy
C. Both A. and B.
D. Decreases the heating area required
A. Boiling point elevations
B. Temperature of the feed
C. Rate of heat transfer
D. Ratio of the weight of the thin liquor to thick liquor
A. Decreased capacity
B. Increase in liquor film co-efficient
C. Decreased effect of hydrostatic head
D. Increased true temperature drop
A. Cube
B. Plate
C. Sphere
D. All will cool at the same rate