The ratio of volumes of the mixed reactor to the plug flow reactor (for identical feed composition, flow rate, conversion, and for all positive reaction orders) is always

Process Equipment and Plant Design
The ratio of volumes of the mixed reactor to the plug flow reactor (for identical feed composition, flow rate, conversion, and for all positive reaction orders) is always

1

>1

< 1

Equal to the order of reaction

1

>1

< 1

Equal to the order of reaction

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Process Equipment and Plant Design
Vertical condenser is advantageous to the horizontal condenser from operation point of view, when

Only the function of condensation is to be carried out

Sub cooling of condensate is desired

Hydrostatic head is required for refluxing the condensate

Both the functions of condensation & sub cooling are carried out in a single unit

Only the function of condensation is to be carried out

Sub cooling of condensate is desired

Hydrostatic head is required for refluxing the condensate

Both the functions of condensation & sub cooling are carried out in a single unit

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

Diameter of the vessel

Operating pressure and welding/joint efficiency

All of these

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

Diameter of the vessel

Operating pressure and welding/joint efficiency

All of these

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

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Process Equipment and Plant Design
Vertical vessels are not supported by

Skirts

Brackets

Saddles

Columns

Skirts

Brackets

Saddles

Columns

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Process Equipment and Plant Design
In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Layout

Pitch

Neither A nor B

Both A & B

Layout

Pitch

Neither A nor B

Both A & B

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Process Equipment and Plant Design
Value of Peclet number = 0, is the representative of

Complete back mixing

Laminar flow

Eddy diffusivity = 0

Plug flow

Complete back mixing

Laminar flow

Eddy diffusivity = 0

Plug flow

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Process Equipment and Plant Design

Process Equipment and Plant Design The ratio of volumes of the mixed reactor to the plug flow reactor (for identical feed composition, flow rate, conversion, and for all positive reaction orders) is always

Process Equipment and Plant Design Vertical condenser is advantageous to the horizontal condenser from operation point of view, when

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

Process Equipment and Plant Design Vertical vessels are not supported by

Process Equipment and Plant Design In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Process Equipment and Plant Design Value of Peclet number = 0, is the representative of

Process Equipment and Plant Design
The ratio of volumes of the mixed reactor to the plug flow reactor (for identical feed composition, flow rate, conversion, and for all positive reaction orders) is always

Process Equipment and Plant Design
Vertical condenser is advantageous to the horizontal condenser from operation point of view, when

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

Process Equipment and Plant Design
Vertical vessels are not supported by

Process Equipment and Plant Design
In a heat exchanger, shell side fluid velocity can be changed by changing the tube

Process Equipment and Plant Design
Value of Peclet number = 0, is the representative of