Our website is made possible by displaying online advertisements to our visitors. Please consider supporting us by whitelisting our website.

CHEMICAL ENGINEERING

Nusselt number for full developed, laminar, constant property flow in a pipe at uniform heat flux is

Question: Nusselt number for full developed, laminar, constant property flow in a pipe at uniform heat flux is
[A].

0.72

[B].

4.364

[C].

18

[D].

83

Answer: Option B

Explanation:

No answer description available for this question.

Nusselt number for full developed, laminar, constant property flow in a pipe at uniform heat flux is Read More »

CHEMICAL ENGINEERING, Heat Transfer

“The ratio of the total emissive power to the absorptivity for all bodies is same at ther-mal equilibrium”. This is __________ law.

Question: “The ratio of the total emissive power to the absorptivity for all bodies is same at ther-mal equilibrium”. This is __________ law.
[A].

Kirchoffs

[B].

Planck’s

[C].

Wien’s displacement

[D].

Stefan-Boltzman

Answer: Option A

Explanation:

No answer description available for this question.

“The ratio of the total emissive power to the absorptivity for all bodies is same at ther-mal equilibrium”. This is __________ law. Read More »

CHEMICAL ENGINEERING, Heat Transfer

In a liquid-liquid heat exchanger, for the same process temperature, the ratio of the LMTD in parallel flow to the LMTD in counter flow is always

Question: In a liquid-liquid heat exchanger, for the same process temperature, the ratio of the LMTD in parallel flow to the LMTD in counter flow is always
[A].

< 1

[B].

> 1

[C].

1

[D].

Answer: Option A

Explanation:

No answer description available for this question.

In a liquid-liquid heat exchanger, for the same process temperature, the ratio of the LMTD in parallel flow to the LMTD in counter flow is always Read More »

CHEMICAL ENGINEERING, Heat Transfer

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