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Chemical Reaction Engineering

Chemical Reaction Engineering
Non-catalytic fluid-solid reactions are represented by __________ model.

Unreacted core
Neither A and B
Continuous reaction
Both A and B

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Chemical Reaction Engineering
According to Arhenious equation of temperature dependency of rate constant for an elementary reaction

None of these
K ∝ √T
K ∝ T e-E/RT
K ∝ e-E/RT

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Chemical Reaction Engineering
Carbon particles accummulated on the catalyst used in the gas oil cracking lies in the category of __________ poison.

Deposited
Stability
Selectivity
Chemisorbed

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Chemical Reaction Engineering
In the hydrodealkylation of toluene to benzene, the following reactions occur:C₇H₈ + H₂ → C₆H₆ + CH₄2C₆H₆ ⇋ C₁₂H₁₀ + H₂Toluene and hydrogen are fed to a reactor in a molar ratio 1:5.80% of the toluene gets converted and the selectivity of benzene(defined as moles of benzene formed/moles of toluene converted) is 90%. The fractional conversion of hydrogen is

0.136
0.152
0.144
0.16

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Chemical Reaction Engineering
Which of the following is an independent variable for a batch tank reactor with uniform concentration and temperature?

Diameter of the reactor
Time
Useful volume of the tank
None of these

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Chemical Reaction Engineering
With increase in temperature, the equilibrium conversion of a reversible exothermic reaction

Increases
Remains unaffected
Decreases linearily with temperature
Decreases

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