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Process Equipment and Plant Design

Process Equipment and Plant Design
The maximum liquid gradient over a tray must not exceed

Half the tray spacing
2"-3.5"
0.5" -1.25"
5"

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Process Equipment and Plant Design
Diameter of the seive tray column is determined by the

Hole diameter of the seive tray
Lower limit of vapour velocity
Height of the plate spacing
Upper limit of the vapour velocity

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Process Equipment and Plant Design
In a distillation column, bubble caps are located on trays with a pitch of __________ times the outside diameter of the caps.

1.6 to 2
1.5 to 3
2.5
1.3 to 2

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Process Equipment and Plant Design
The ends of a cylinderical vessel can be closed by a head, which can be one of the four shapes. For the same thickness, choose the one which can withstand the highest pressure.

Torispherical
Ellipsoidal
Hemispherical
Flat plate

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Process Equipment and Plant Design
Vertical vessels are not supported by

Saddles
Brackets
Columns
Skirts

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Process Equipment and Plant Design
Lug support is meant for supporting __________ vessels.

Small
Thick walled tall
Tall but empty
Large horizontal cylindrical

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