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In a shell and tube heat exchanger, the tube side heat transfer co-efficient just at the entrance of the tube is

Question: In a shell and tube heat exchanger, the tube side heat transfer co-efficient just at the entrance of the tube is
[A].

infinity.

[B].

zero.

[C].

same as average heat transfer co-efficient for tube side.

[D].

none of these.

Answer: Option A

Explanation:

No answer description available for this question.

In a shell and tube heat exchanger, the tube side heat transfer co-efficient just at the entrance of the tube is Read More »

CHEMICAL ENGINEERING, Heat Transfer

The average heat transfer co-efficient for laminar film condensation on vertical surface is inversely proportional to (where, ΔT = Temperature drop across condensate film )

Question: The average heat transfer co-efficient for laminar film condensation on vertical surface is inversely proportional to (where, ΔT = Temperature drop across condensate film )
[A].

(ΔT)2

[B].

ΔT

[C].

(ΔT)1/4

[D].

(ΔT)3/2

Answer: Option C

Explanation:

No answer description available for this question.

The average heat transfer co-efficient for laminar film condensation on vertical surface is inversely proportional to (where, ΔT = Temperature drop across condensate film ) Read More »

CHEMICAL ENGINEERING, Heat Transfer

Conductance is given by(where, x = thickness, A = heat flow area, K = thermal conductivity.)

Question: Conductance is given by(where, x = thickness, A = heat flow area, K = thermal conductivity.)
[A].

x/KA

[B].

KA/x

[C].

K/Ax

[D].

A/Kx

Answer: Option B

Explanation:

No answer description available for this question.

Conductance is given by(where, x = thickness, A = heat flow area, K = thermal conductivity.) Read More »

CHEMICAL ENGINEERING, Heat Transfer

LMTD can’t be used as such without a correction factor for the

Question: LMTD can’t be used as such without a correction factor for the
[A].

multipass heat exchanger.

[B].

baffled heat exchanger.

[C].

condensation of mixed vapour in a condenser.

[D].

all (a) (b) and (c).

Answer: Option D

Explanation:

No answer description available for this question.

LMTD can’t be used as such without a correction factor for the Read More »

CHEMICAL ENGINEERING, Heat Transfer