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Process Equipment and Plant Design

Process Equipment and Plant Design
In the design of a paddle agitator, the ratio (paddle dia/tank dia) is normally taken as

0.5
0.8
0.1
0.25

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Process Equipment and Plant Design
With increase in the reflux ratio for a fixed production from a continuous binary distillation column, the __________ decreases.

Vapour & liquid load both
Fixed charges initially
Running cost of steam for reboiler
Running cost of cooling water for condenser

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Process Equipment and Plant Design
Maximum plate efficiency is achieved in case of __________ flow.

Cascade
Reverse
Cross
Split

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Process Equipment and Plant Design
Steam side heat transfer co-efficient for design consideration under ordinary condition can be assumed to be about __________ kcal/hr.m².°C.

7500
15000
1250
2500

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Process Equipment and Plant Design
In a shell and tube heat exchanger having triangular pitch, the shell side equivalent diameter is given by

(p² - πd²/4)/πd
4(0.86p² - πd²)/πd
(4p² - πd²/4)/πd
4(0.86p² - πd²/4)/πd

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Process Equipment and Plant Design
Saddle supports are used for supporting __________ vessels.

Horizontal cylinderical
Thick walled vertical
Tall vertical
Thick spherical

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