chemical engineering chemical reaction Mcqs
254. Slurry reactors are characterised by the_________________?
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A. Lack of intraparticle diffusion resistance

B. Presence of two mobile phases

C. Both A. and B.

D. Neither A. nor B.

255. Pick out the wrong statement ?
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A. The residence time for all the elements of fluid in case of a P.F.R. need not be same

B. A flat velocity profile exists in a plug flow reactor

C. Chemical reactions with high activation energy are very temperature sensitive

D. n one

E. Half life of a reaction increases with increased initial concentration for reaction orders more

260. Half-life period for a first order reaction is _____________ the initial concentration of the reactant?
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A. Inversely proportional to

B. Independent of

C. Directly proportional to

D. None of these

261. Pick out the wrong statement ?
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A. In a batch reactor, which is exclusively used for liquid phase reactions; temperature pressure and composition may vary with time

B. In a semi-batch reactor, one reactant is charged batch wise, while the other reactant is fed continuously

C. In a continuous flow reactor, uniform concentration cannot be maintained throughout the vessel even in a well agitated system

D. In a continuous flow reactor, both the reactants and the products flow out continuously

266. The effect of increasing pressure on the gaseous equilibrium of the reaction 2X + 3Y ? 3X + 2Y indicates that____________________?
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A. None of these

B. Forward reaction is favoured

C. Pressure has no effect

D. Backward reaction is favoured

267. In an ideal mixed reactor (at steady state), the ___________________?
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A. All A., B. and C.

B. Space time is equivalent to holding time for constant density systems

C. Composition throughout the reactor remains same

D. Exit stream has the same composition as the fluid within the reactor

268. Rate of a chemical reaction is not influenced by the__________________?
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A. Temperature

B. Number of molecules of reactants taking part in a reaction

C. Catalyst

D. Reactants concentration

271. Which of the following factors control the design of a fluid-solid reactor ?
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A. Size distribution of solids being treated

B. Reaction kinetics for single particle

C. All A., B. and C.

D. Flow patterns of solids and fluid in the reactor

272. The importance of diffusion in a catalyst are increased by ____________________?
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A. Small pore diameter

B. All A., B. and C.

C. Large catalyst particle size

D. An active surface of the catalyst

273. Pick out the correct statement ?
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A. A chemical reaction accompanied by evolution of heat is called an endothermic reaction

B. The rate constant for a first order reaction does not change on changing the concentration units

C. A chemical reaction accompanied by absorption of heat is called an exothermic reaction

D. Chemical equilibrium state is dynamic in nature

275. A backmix reactor_________________?
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A. Is most suitable for gas phase reaction

B. Employs mixing in axial direction only

C. Is same as ideal stirred tank reactor

D. Is same as plug-flow reactor

280. For multiple reactions, the flow pattern within the vessel affects the ____________________?
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A. Size requirement

B. Distribution of reaction products

C. Both A. and B.

D. Neither A. nor B.

281. The equilibrium constant for the reversible reaction as shown in the bellow figure, is affected by the__________________?
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A. Presence or absence of inerts

B. Temperature of the system

C. Pressure of the system

D. Kinetics of the reaction

282. The rate at which a chemical substance reacts is proportional to its _____________________?
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A. Equivalent weight

B. Molecular weight

C. Atomic weight

D. Active mass
284. Pick out the wrong statement?
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A. mentary

B. concentration of A decreases and the rate is proportional to the concentration of A

C. In a first order reaction, A ? products; the reaction becomes slower as it proceeds, because

D. Transition state theory approaches the problem of calculating reaction rates by concentrating

E. e of an eddy to the solute decreases</strong>

F. the idea of activated complexes

286. Photochemical reaction rate does not depend significantly on temperature, because____________________?
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A. It is a reversible reaction

B. It is an exothermic reaction

C. The energy of reacting molecules exceeds the activation energy by absorption of light

D. None of these

287. ______________ explains the mechanism of catalysis?
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A. None of these

B. Collision theory

C. Thermodynamics

D. Activated complex theory
288. Pick out the wrong statement?
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A. Activation energy for a reaction is obtained from the intercept of the Arrhenius plot

B. Alumina is added as a promoter to iron catalyst in ammonia synthesis reaction

C. Presence of inerts affects the equilibrium conversion of

D. Use of different catalysts in a reversible catalytic chemical reaction does not change the

E. ilibrium composition

290. Pick out the wrong statement ?
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A. A batch reactor cannot be used to study the kinetics of catalytic reaction

B. For studying a chemical reaction, it is desirable to monitor the reactants during initial stages

C. Study of non-ideal flow reactor is done experimentally by stimulus-response technique

D. Hold back is defined as the fraction of material that stays longer than the mean residence time

E. the products during the final stages of reaction

294. Pick out the wrong statement ?
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A. For a second order reaction, the slope of the graph/plot between rate and (concentration) is

B. Visible radiation provides the necessary activation energy in photochemical reactions

C. Molecularity of the reaction is always a whole number greater than zero

D. The order and molecularity of a complex reaction may not be the same

E. al to the rate constant (k)

296. For a vapour phase catalytic reaction (A + B ? P) which follows the Ridel mechanism and the reaction step is rate controlling, the rate of reaction is given by (reaction rate is irreversible, product also absorbs) ?
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A. -rA = (k . PA . PB)/(1 + KAPA + KPPP)

B. #8211; k1PP)/(1 + KAPA + KPPP)

C. -rA = (k . PA . PB)/(1 + KAPA)

D. -rA = (k . PA . PB)/(1 + KAPB + KBPB . KPPP)

E. -rA = (k . PA

298. The energy balance equation over a tubular reactor under transient conditions is________________?
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A. A linear partial differential equation

B. An algebraic differential equation

C. A non-linear partial differential equation

D. An ordinary non-linear differential equation