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Heat exchangers operating, when the asymptotic range is reached,

Question: Heat exchangers operating, when the asymptotic range is reached,
[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.

Answer: Option B

Explanation:

No answer description available for this question.

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CHEMICAL ENGINEERING, Heat Transfer

In an extended surface heat exchanger, fluid having lower co-efficient

Question: In an extended surface heat exchanger, fluid having lower co-efficient
[A].

flows through the tube.

[B].

flows outside the tubes.

[C].

can flow either inside or outside the tubes.

[D].

should not be used as it gives very high pressure drop.

Answer: Option B

Explanation:

No answer description available for this question.

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CHEMICAL ENGINEERING, Heat Transfer

Baffle spacing

Question: Baffle spacing
[A].

is not the same as baffle pitch.

[B].

should be less than one fifth the diameter of the shell.

[C].

should be less than the inside diameter of the shell.

[D].

none of these.

Answer: Option C

Explanation:

The distance between the baffles is called baffle spacing. While the maximum baffle spacing is equal to the diameter of the shell, the minimum is l/5th the shell diameter.

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CHEMICAL ENGINEERING, Heat Transfer

In a shell and tube heat exchanger, square pitch compared to triangular pitch

Question: In a shell and tube heat exchanger, square pitch compared to triangular pitch
[A].

gives a higher shell side pressure drop.

[B].

gives a lower shell side pressure drop.

[C].

can pack more surface area into a shell of given diameter.

[D].

none of these.

Answer: Option B

Explanation:

No answer description available for this question.

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CHEMICAL ENGINEERING, Heat Transfer

In a shell and tube heat exchanger,

Question: In a shell and tube heat exchanger,
[A].

the temperature drops in the two fluids and the wall are proportional to individual resistances.

[B].

the temperature drop is inversely proportional to the resistance across which the drop occurs.

[C].

there is no relationship between temperature drop and resistance.

[D].

the relationship is not generalised.

Answer: Option A

Explanation:

No answer description available for this question.

In a shell and tube heat exchanger, Read More »

CHEMICAL ENGINEERING, Heat Transfer

In a heat exchanger, the rate of heat transfer from the hot fluid to the cold fluid

Question: In a heat exchanger, the rate of heat transfer from the hot fluid to the cold fluid
[A].

varies directly as the area and the LMTD.

[B].

directly proportional to LMTD and inversely proportional to the area.

[C].

varies as square of the area.

[D].

none of these.

Answer: Option A

Explanation:

No answer description available for this question.

In a heat exchanger, the rate of heat transfer from the hot fluid to the cold fluid Read More »

CHEMICAL ENGINEERING, Heat Transfer

Baffles in the shell side of a shell and tube heat exchanger

Question: Baffles in the shell side of a shell and tube heat exchanger
[A].

increase the cross-section of the shell side liquid.

[B].

force the liquid to flow parallel to the bank.

[C].

increase the shell side heat transfer co-efficient.

[D].

decrease the shell side heat transfer co-efficient.

Answer: Option C

Explanation:

No answer description available for this question.

Baffles in the shell side of a shell and tube heat exchanger Read More »

CHEMICAL ENGINEERING, Heat Transfer