Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

Process Equipment and Plant Design
Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

More

Same

Less

More or less depending upon the pressure & temperature inside the vessel and the nature of the fluid contained therein

More

Same

Less

More or less depending upon the pressure & temperature inside the vessel and the nature of the fluid contained therein

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Process Equipment and Plant Design
The necessary wall thickness for a metallic storage vessel is a function of the

Ultimate tensile strength (or yield point) of the material and operating temperature

Diameter of the vessel

All of these

Operating pressure and welding/joint efficiency

Ultimate tensile strength (or yield point) of the material and operating temperature

Diameter of the vessel

All of these

Operating pressure and welding/joint efficiency

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Process Equipment and Plant Design
If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

Decrease by 22

None of these

Increase by 1.8

Increase by 21.6

Decrease by 22

None of these

Increase by 1.8

Increase by 21.6

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Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

0.75-0.85

0.60-0.90

0.5-0.65

0.15-030

0.75-0.85

0.60-0.90

0.5-0.65

0.15-030

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Process Equipment and Plant Design
Practical dividing line between a ductile and brittle materials is suggested, when the ultimate elongation is about 5%. Generally, larger the knuckle radius, stronger is the corner torus section of a head. The knuckle radius provided should be less than __________ of the head.

3 times the thickness

Either A or B, whichever is larger

Either A or B, whichever is smaller

6% of I.D.

3 times the thickness

Either A or B, whichever is larger

Either A or B, whichever is smaller

6% of I.D.

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

Lower limit of vapour velocity

Hole diameter of the seive tray

Height of the plate spacing

Upper limit of the vapour velocity

Lower limit of vapour velocity

Hole diameter of the seive tray

Height of the plate spacing

Upper limit of the vapour velocity

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Process Equipment and Plant Design

Process Equipment and Plant Design Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

Process Equipment and Plant Design The necessary wall thickness for a metallic storage vessel is a function of the

Process Equipment and Plant Design If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

Process Equipment and Plant Design The raio, (properller agitator dia/tank dia) is normally taken as

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

Process Equipment and Plant Design
Normally, the plate thickness of the bottoms and roofs of vertically cylindrical storage vessels as compared to that of the cylindrical shell is

Process Equipment and Plant Design
The necessary wall thickness for a metallic storage vessel is a function of the

Process Equipment and Plant Design
If a single tube pass heat exchanger is converted to two passes; for the same flow rate, the pressure drop per unit length in tube side will __________ times.

Process Equipment and Plant Design
The raio, (properller agitator dia/tank dia) is normally taken as

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