Which of the following is not a valid assumption in continuous binary distillation for calculating the number of equilibrium stages by Mc-Cabe-Thiele's method?

Process Equipment and Plant Design
Which of the following is not a valid assumption in continuous binary distillation for calculating the number of equilibrium stages by Mc-Cabe-Thiele's method?

Molar latent heat of the two components are equal

Heat of mixing of normal liquid is assumed to be zero

Sensible heat changes for vapour & liquid are negligibly small

Reflux is not a saturated liquid

Molar latent heat of the two components are equal

Heat of mixing of normal liquid is assumed to be zero

Sensible heat changes for vapour & liquid are negligibly small

Reflux is not a saturated liquid

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Process Equipment and Plant Design
The operating pressure drop range in a bag filter is about __________ mm water gauge.

500-1500

50-150

43961

1500-2500

500-1500

50-150

43961

1500-2500

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Process Equipment and Plant Design
The diameter of a propeller agitator used in agitation tank ranges from __________ percent of the tank diameter and its peripherial speed is normally 300 to 500 metres/minute.

5 to 10

55 to 75

15 to 30

40 to 50

5 to 10

55 to 75

15 to 30

40 to 50

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

Small

Tall but empty

Large horizontal cylindrical

Thick walled tall

Small

Tall but empty

Large horizontal cylindrical

Thick walled tall

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Process Equipment and Plant Design
Vertical vessels are not supported by

Brackets

Saddles

Skirts

Columns

Brackets

Saddles

Skirts

Columns

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Process Equipment and Plant Design
The LMTD correction factor (FT) is applied in __________ heat exchangers.

Double pipe

1-1 cocurrent

All multipass

All of these

Double pipe

1-1 cocurrent

All multipass

All of these

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Process Equipment and Plant Design

Process Equipment and Plant Design Which of the following is not a valid assumption in continuous binary distillation for calculating the number of equilibrium stages by Mc-Cabe-Thiele's method?

Process Equipment and Plant Design The operating pressure drop range in a bag filter is about __________ mm water gauge.

Process Equipment and Plant Design The diameter of a propeller agitator used in agitation tank ranges from __________ percent of the tank diameter and its peripherial speed is normally 300 to 500 metres/minute.

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

Process Equipment and Plant Design Vertical vessels are not supported by

Process Equipment and Plant Design The LMTD correction factor (FT) is applied in __________ heat exchangers.

Process Equipment and Plant Design
Which of the following is not a valid assumption in continuous binary distillation for calculating the number of equilibrium stages by Mc-Cabe-Thiele's method?

Process Equipment and Plant Design
The operating pressure drop range in a bag filter is about __________ mm water gauge.

Process Equipment and Plant Design
The diameter of a propeller agitator used in agitation tank ranges from __________ percent of the tank diameter and its peripherial speed is normally 300 to 500 metres/minute.

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

Process Equipment and Plant Design
Vertical vessels are not supported by

Process Equipment and Plant Design
The LMTD correction factor (FT) is applied in __________ heat exchangers.