Which of the following types of reactors is the safest from operation point of view?

Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?

A liquid phase reactor

Pot type reactor

A vapor phase reactor

A liquid phase catalytic reactor

A liquid phase reactor

Pot type reactor

A vapor phase reactor

A liquid phase catalytic reactor

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

Reverse

Split

Cross

Cascade

Reverse

Split

Cross

Cascade

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Process Equipment and Plant Design
Column support for the roof of cylindrical storage tank must be provided for

Small diameter tall tanks

Large diameter tanks

All of these

Small diameter tanks

Small diameter tall tanks

Large diameter tanks

All of these

Small diameter tanks

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Process Equipment and Plant Design
Cylindrical pressure vessels in horizontal condition is generally supported on a __________ support.

Skirt

Guy wire

Lug

Saddle

Skirt

Guy wire

Lug

Saddle

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Process Equipment and Plant Design
Steam economy is defined as the amount of evaporation per unit amount of steam used, while the capacity is the total evaporation obtained per hour. Use of multiple effect in evaporation

Does not affect the capacity

Increases capacity

Both B & C

Increases economy

Does not affect the capacity

Increases capacity

Both B & C

Increases economy

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Process Equipment and Plant Design
In case of design of a shell and tube heat exchanger,

Minimum cleaning lane of 6.5 mm is provided, when tubes are on a square pitch

O.D. of the tube is 6 to 40 mm while the tube lengths used are 0.5, 2.5, 3.0, 4.0, 5.0, 6 metres

Minimum tube sheet thickness (in which tubes are fixed) is equal to the O.D. of the tube upto 15 mm tube diameter; and for > 15 mm tube diameter, tube sheet thickness is smaller than tube diameter

All of these

Minimum cleaning lane of 6.5 mm is provided, when tubes are on a square pitch

O.D. of the tube is 6 to 40 mm while the tube lengths used are 0.5, 2.5, 3.0, 4.0, 5.0, 6 metres

Minimum tube sheet thickness (in which tubes are fixed) is equal to the O.D. of the tube upto 15 mm tube diameter; and for > 15 mm tube diameter, tube sheet thickness is smaller than tube diameter

All of these

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Process Equipment and Plant Design

Process Equipment and Plant Design Which of the following types of reactors is the safest from operation point of view?

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

Process Equipment and Plant Design Column support for the roof of cylindrical storage tank must be provided for

Process Equipment and Plant Design Cylindrical pressure vessels in horizontal condition is generally supported on a __________ support.

Process Equipment and Plant Design Steam economy is defined as the amount of evaporation per unit amount of steam used, while the capacity is the total evaporation obtained per hour. Use of multiple effect in evaporation

Process Equipment and Plant Design In case of design of a shell and tube heat exchanger,

Process Equipment and Plant Design
Which of the following types of reactors is the safest from operation point of view?

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

Process Equipment and Plant Design
Column support for the roof of cylindrical storage tank must be provided for

Process Equipment and Plant Design
Cylindrical pressure vessels in horizontal condition is generally supported on a __________ support.

Process Equipment and Plant Design
Steam economy is defined as the amount of evaporation per unit amount of steam used, while the capacity is the total evaporation obtained per hour. Use of multiple effect in evaporation

Process Equipment and Plant Design
In case of design of a shell and tube heat exchanger,