A. Surrounding temperature
B. Average temperature of the fin
C. Temperature of the fin end
D. Constant temperature equal to that of the base
Chemical Heat Transfer
Chemical Heat Transfer
A. Feed
B. Depth of liquid over heating surface
C. Pressure difference between steam chest and vapour space
D. All A., B. and C.
A. Length
B. Area
C. Volume
D. None of these
A. Remove condensate from the steam pipelines
B. Create vacuum
C. Superheat the steam
D. None of these
A. Vertical heat exchanger with steam on tube side
B. Vertical heat exchanger with steam on shell side
C. Horizontal heat exchanger with steam on tube side
D. Horizontal heat exchanger with steam on shell side
A. Gases
B. Solids
C. Liquids
D. Both B. and C.
A. Isothermal
B. Non-isothermal
C. Both A. and B.
D. Neither A. and B.
A. 0.5
B. 0.05
C. 0.1
D. 0.15
A. √(ΔT1 . ΔT2)
B. 2 (ΔT1 . ΔT2)/(ΔT1 + ΔT2)
C. 2 (ΔT1 . ΔT2)/(ΔT1 – ΔT2)
D. (ΔT1 – ΔT2)/(ΔT1 . ΔT2)
A. ha = hl
B. ha = 2hl
C. ha = 0.5 hl
D. ha = 0.75 hl