Chemical Engineering
GATE CH purpose:exam-prep PYQs
Build your understanding with focused practice from past exam papers.
Questions 471–480 of 650. Imported answers require independent review unless marked reviewed.
Question 6
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For a fully-developed turbulent hydrodynamic boundary layer for flow past a flat plate, the thickness of the boundary layer increases with distance
from the leading edge of the plate, along the free-stream flow direction, asYour answerChoose one option.
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Consider a cylinder (diameter
and length
), a sphere (diameter
) and a cube (side length
). Which of the following statements concerning the sphericity (
) of the above objects is true:Your answerChoose one option.
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Prandtl number signifies the ratio of
Your answerChoose one option.
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Pool boiling equipment operating above ambient temperature is usually designed to operate
Your answerChoose one option.
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The desired liquid-phase reaction
is accompanied by an undesired side reaction
Four isothermal reactor schemes (CSTR: ideal Continuous-Stirred Tank Reactor; PFR: ideal Plug Flow Reactor) for processing equal molar feed rates of D and E are shown in figure. Each scheme is designed for the same conversion. The scheme that gives the most favorable product distribution is:
Your answerChoose one option.
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For a first order reaction in a porous spherical catalyst pellet, diffusional effects are most likely to lower the observed rate of reaction for
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A thermocouple senses temperature based on the
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The correct expression for the Colburn
-factor for mass transfer that relates Sherwood number (Sh), Reynolds number (Re) and Schmidt number (Sc) isYour answerChoose one option.
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In the drying of non-dissolving solids at constant drying conditions, the internal movement of moisture in the solid has a dominant effect on the drying rate during
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Open questionCHMCQ1 markNeeds review
Three distillation schemes for separating an equimolar, constant relative volatility ABC mixture into nearly pure components are shown. The usual simplifying assumptions such as constant molal overflow, negligible heat loss, ideal trays are valid. All the schemes are designed for minimum total reboiler duty. Given that the relative volatilities are in the ratio
, the correct option that arranges the optimally-designed schemes in ascending order of total reboiler duty is 
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