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Process Equipment and Plant Design

Process Equipment and Plant Design
Cooling water fouling factors vary in the range of 0.001 to 0.003

(BTU/hr.ft² . °F)⁻¹
(kcal/hr. m. °C)⁻¹
(W/m².°K)⁻¹
(kcal/hr.m² .°C)⁻¹

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Process Equipment and Plant Design
Friction factor for turbulent flow in a new pipe is given by

f = 16/NRe
f = 0.22 NRe0.05
f = 0.04/NRe0.16
f = 25/NRe

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Process Equipment and Plant Design
Normally, the length to diameter ratio of rotary dryers varies form 4 to 10 and for its economic operation, the number of transfer units (NTU) for such dryers varies from

44119
3.5-5.5
1.5-2.5
7.5-10.0

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Process Equipment and Plant Design
Back-trapping in a distillation column results due to

High gas velocity
Low reflux ratio
Excessive liquid gradient over the tray
Low gas velocity

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Process Equipment and Plant Design
Rotary driers are most economically designed for the number of heat transfer units (HTU) from

0.01 to 1
5 to 10
1.5 to 2.5
10 to 20

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Process Equipment and Plant Design
Movement of pipeline caused by thermal expansion is taken care by providing

All of these
Changes in its direction
Change in the shape of pipeline
Expansion joint

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