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This section includes 8247 Mcqs, each offering curated multiple-choice questions to sharpen your Engineering knowledge and support exam preparation. Choose a topic below to get started.
| 4751. |
Bulk diffusion in catalyst pore __________ with increase in pressure. |
| A. | increases |
| B. | decreases |
| C. | remains unchanged |
| D. | increases exponentially |
| Answer» C. remains unchanged | |
| 4752. |
The following half life data are available for the irreversible liquid phase reaction A products.The overall order of reaction is |
| A. | 0.5 |
| B. | 1 |
| C. | 1.5 |
| D. | 2 |
| Answer» D. 2 | |
| 4753. |
A non-catalytic chemical reaction of the type is called a __________ reaction. |
| A. | parallel |
| B. | series |
| C. | series-parallel |
| D. | none of these |
| Answer» D. none of these | |
| 4754. |
The unit of frequency factor in Arhenious equation is |
| A. | same as that of rate constant. |
| B. | same as that of activation energy. |
| C. | dimensionless. |
| D. | none of these. |
| Answer» B. same as that of activation energy. | |
| 4755. |
With increase in the order of reaction (for all positive reaction orders), the ratio of the volume of mixed reactor to the volume of plug flow reactor (for identical feed composition, flow rate and conversion) |
| A. | increases |
| B. | decreases |
| C. | remains same |
| D. | increases linearly |
| Answer» B. decreases | |
| 4756. |
Reaction of benzene with chlorine gas to produce tri-chlorobenzene exemplifies a/an __________ reaction. |
| A. | elementary |
| B. | parallel |
| C. | consecutive |
| D. | none of these |
| Answer» D. none of these | |
| 4757. |
Which of the following factors control the deactivation of a porous catalyst pellet ? |
| A. | Decay reactions. |
| B. | Pore diffusion. |
| C. | Form of surface attack by poison. |
| D. | All (a), (b) and (c). |
| Answer» E. | |
| 4758. |
A liquid phase reaction is to be carried out under isothermal conditions. The reaction rate as a function of conversion has been determined experimentally and is shown in the figure given below. What choice of reactor or combination of reactors will require the minimum overall reactor volume, if a conversion of 0.9 is desired ? |
| A. | CSTR followed by a PFR |
| B. | PFR followed by a CSTR |
| C. | CSTR followed by a PFR followed by a CSTR. |
| D. | PFR followed by a CSTR followed by a PFR. |
| Answer» E. | |
| 4759. |
If the time required for half change is inversely proportional to the square of initial concentration and the velocity depends on the units in which the concentration term is expressed, then the order of reaction is |
| A. | 1 |
| B. | 2 |
| C. | 3 |
| D. | 0 |
| Answer» D. 0 | |
| 4760. |
The experimentally determined overall order of the reaction, A + B C + D, is two. Then the |
| A. | reaction is elementary with a molecularity of 2. |
| B. | molecularity of the reaction is 2, but the reaction may not be elementary. |
| C. | reaction may be elementary with molecularity of 2. |
| D. | reaction is elementary but the molecularity may not be 2. |
| Answer» B. molecularity of the reaction is 2, but the reaction may not be elementary. | |
| 4761. |
In a continuous flow stirred tank reactor, the composition of the exit stream |
| A. | is same as that in the reactor. |
| B. | is different than that in the reactor. |
| C. | depends upon the flow rate of inlet stream. |
| D. | none of these. |
| Answer» B. is different than that in the reactor. | |
| 4762. |
Recycling back of outlet stream to the reactor from an ideal CSTR carrying out a first order liquid phase reaction will result in __________ in conversion. |
| A. | decrease |
| B. | increase |
| C. | no change |
| D. | either (a) or (b), depends on the type of reaction |
| Answer» D. either (a) or (b), depends on the type of reaction | |
| 4763. |
The energy balance equation over a tubular reactor under transient conditions is |
| A. | an ordinary non-linear differential equation. |
| B. | an algebric differential equation. |
| C. | a linear partial differential equation. |
| D. | a non-linear partial differential equation. |
| Answer» D. a non-linear partial differential equation. | |
| 4764. |
In Langmuir treatment of adsorption, |
| A. | whole surface of the catalyst does not have the same activity for adsorption and there is attraction between the adsorbed molecule. |
| B. | whole surface of the catalyst is essentially uniform and the adsorbed molecule has no effect on the rate of adsorption per site. |
| C. | all the adsorption does not take place by the same mechanism. |
| D. | extent of adsorption is more than one complete monomolecular layer on the surface. |
| Answer» C. all the adsorption does not take place by the same mechanism. | |
| 4765. |
Organic catalysts differ from the inorganic catalyst in the sense that the former is |
| A. | active at cryogenic temperatures only. |
| B. | prohibitively costly. |
| C. | proteinous in nature. |
| D. | active at very high temperature only. |
| Answer» D. active at very high temperature only. | |
| 4766. |
The equilibrium constant K of a chemical reaction depends on |
| A. | temperature only. |
| B. | pressure only. |
| C. | temperature and pressure. |
| D. | ratio of reactants. |
| Answer» B. pressure only. | |
| 4767. |
The reaction rate almost gets doubled for 10 C rise in temperature. This is due to the fact that the |
| A. | increased temperature reduces the activation energy. |
| B. | fraction of molecules having threshold energy increases. |
| C. | collision frequency increases. |
| D. | value of threshold energy decreases. |
| Answer» C. collision frequency increases. | |
| 4768. |
Which of the following is not a unit of reaction rate ? |
| A. | Moles for med/(surface of catalyst) (time) |
| B. | Moles formed/volume of reactor) (time) |
| C. | Mole formed/volume of catalyst) (time) |
| D. | None of these |
| Answer» E. | |
| 4769. |
Brunaur, Emmet and Teller (BET) equation is used to determine the specific surface area of a porous particle but not the pore volume & the porosity of the catalyst bed. Which of the following postulates is not used to derive BET equation ? |
| A. | Langmuir's assumption applies to every adsorbed layer. |
| B. | There is no dynamic equilibrium between successive layer. |
| C. | The adsorbed layer may be polymolecular in thickness and the heat of adsorption in each layer (except the first one) is involved in each of the evaporation process. |
| D. | none of these. |
| Answer» C. The adsorbed layer may be polymolecular in thickness and the heat of adsorption in each layer (except the first one) is involved in each of the evaporation process. | |
| 4770. |
The sequence in which three CSTR's of volumes 5, 10 and 15 m3 will be connected in series to obtain the maximum production in a second order irreversible reaction is |
| A. | 15, 10, 5 |
| B. | 5, 10, 15 |
| C. | 10, 5, 15 |
| D. | 10, 15, 5 |
| Answer» B. 5, 10, 15 | |
| 4771. |
With the same reaction time, initial concentration and feed rate, the reaction 2A B is carried out separately in CSTR and P.F. reactor of equal volumes. The conversion will be |
| A. | higher in P.F. reactor |
| B. | higher in CSTR |
| C. | same in both the reactors |
| D. | data insufficient; can't be predicted |
| Answer» B. higher in CSTR | |
| 4772. |
The use of space time is preferred over the mean residence time in the design of a/an |
| A. | batch reactor |
| B. | ideal tubular-flow reactor |
| C. | slurry reactor |
| D. | CSTR |
| Answer» C. slurry reactor | |
| 4773. |
Autocatalytic reactions are best carried out in a |
| A. | CSTR |
| B. | CSTR in series |
| C. | plug flow reactor |
| D. | recycle reactor |
| Answer» E. | |
| 4774. |
The gas phase reaction 2A B is carried out in an isothermal plug flow reactor. The feed consists of 80 mole % A and 20 mole % inerts. If the conversion of A at the reactor exit is 50%, then CA/CA0 at the outlet of the reactor is |
| A. | 2/3 |
| B. | 5/8 |
| C. | 1/3 |
| D. | 3/8 |
| Answer» C. 1/3 | |
| 4775. |
The rate constant of a reaction is a function of the |
| A. | time of reaction. |
| B. | temperature of the system. |
| C. | extent of reaction. |
| D. | initial concentration of the reactants. |
| Answer» C. extent of reaction. | |
| 4776. |
Mean residence time is equal to the space time, when |
| A. | the feed rate is measured at temperature and pressure in the reactor. |
| B. | the temperature, pressure and the density of reaction mixture remains constant throughout the reactor. |
| C. | there is no change in number of moles in gaseous reaction. |
| D. | all (a), (b) and (c). |
| Answer» E. | |
| 4777. |
The value of 'n' for a chemical reaction A B, whose reaction rate is CAn, will be __________ if the rate of the reaction increases by a factor of 8, when the concentration of is doubled. |
| A. | 0 |
| B. | 1 |
| C. | 2 |
| D. | 3 |
| Answer» E. | |
| 4778. |
Non-catalytic fluid-solid reactions are represented by __________ model. |
| A. | continuous reaction |
| B. | unreacted core |
| C. | both (a) and (b) |
| D. | neither (a) and (b) |
| Answer» D. neither (a) and (b) | |
| 4779. |
A pulse tracer is introduced in an ideal CSTR (with a mean residence time ) at time, t = 0. The time taken for the exit concentration of the tracer to reach half of its initial value will be |
| A. | 2 |
| B. | 0.5 |
| C. | /0.693 |
| D. | 0.693 |
| Answer» B. 0.5 | |
| 4780. |
In a first order reaction, the time required to reduce the concentration of reactant from 1 mole/litre to 0.5 mole/litre will be __________ that required to reduce it from 10 moles/litre to 5 moles/litre in the same volume. |
| A. | more than |
| B. | less than |
| C. | same as |
| D. | data insufficient; can't be predicted. |
| Answer» D. data insufficient; can't be predicted. | |
| 4781. |
Photo-chemical reactions occur in presence of |
| A. | sunlight. |
| B. | darkness, |
| C. | solid catalysts. |
| D. | monochromatic radiation only. |
| Answer» B. darkness, | |
| 4782. |
Fractional conversion __________ for an exothermic reversible chemical reaction, when the temperature is maximum. |
| A. | increases |
| B. | remains unchanged |
| C. | decreases |
| D. | unpredictable from the data |
| Answer» D. unpredictable from the data | |
| 4783. |
With increase in temperature, the equilibrium conversion of a reversible exothermic reaction |
| A. | decreases |
| B. | increases |
| C. | remains unaffected |
| D. | decreases linearily with temperature |
| Answer» B. increases | |
| 4784. |
In a CSTR __________ varies with time. |
| A. | reaction rate |
| B. | concentration |
| C. | both (a) & (b) |
| D. | neither (a) nor (b) |
| Answer» E. | |
| 4785. |
The following gas phase reactions are carried out isothermally in a CSTR.A 2R ; r1 = k1pA ;k1 = 20mole/(sec.m3 bar)A 3S ; r2 = k2 pA ;k2 = 40mole/(sec.m3 .bar)What is the maximum possible value of FR(mole/sec.) ? |
| A. | 1/3 |
| B. | 1/2 |
| C. | 2/3 |
| D. | 2 |
| Answer» D. 2 | |
| 4786. |
As the chemical reaction proceeds, the rate of reaction |
| A. | increases. |
| B. | decreases. |
| C. | remains same. |
| D. | may increase or decrease depending on the type of reaction. |
| Answer» C. remains same. | |
| 4787. |
Pure A in gas phase enters a reactor 50% of this A is converted to B through the reaction, A 3B. Mole fraction of A in the exit stream is |
| A. | 1/2 |
| B. | 1/3 |
| C. | 1/4 |
| D. | 1/5 |
| Answer» C. 1/4 | |
| 4788. |
The rate of reaction does not decrease appreciably as the reaction proceeds in case of __________ reactions. |
| A. | autocatalytic |
| B. | exothermic |
| C. | endothermic |
| D. | autothermal |
| Answer» B. exothermic | |
| 4789. |
Fluidised bed reactor is characterised by |
| A. | uniformity of temperature. |
| B. | comparatively smaller equipment. |
| C. | very small pressure drop. |
| D. | absence of continuous catalyst regeneration facility. |
| Answer» B. comparatively smaller equipment. | |
| 4790. |
Space time equals the mean residence time |
| A. | when the density of the reaction mixture is constant. |
| B. | for large diameter tubular reactor. |
| C. | for narrow diameter tubular reactor. |
| D. | for CSTR. |
| Answer» B. for large diameter tubular reactor. | |
| 4791. |
A liquid decomposes by irreversible first order kinetics and the half life period of this reaction is 8 minutes. The time required for 75% conversion of the liquid will be __________ minutes. |
| A. | 4 |
| B. | 8 |
| C. | 12 |
| D. | 16 |
| Answer» E. | |
| 4792. |
For a __________ order chemical reaction, , the fractional conversion of reactant 'A' is proportional to time. |
| A. | zero |
| B. | first |
| C. | second |
| D. | third |
| Answer» B. first | |
| 4793. |
Backmixing is most predominant in |
| A. | a well stirred batch reactor. |
| B. | a plug-flow reactor. |
| C. | a single CSTR. |
| D. | CSTR's connected in series. |
| Answer» D. CSTR's connected in series. | |
| 4794. |
If helium is introduced in a reactor containing O2, SO2 and SO3 at equilibrium, so that total pressure increases while volume and temperature remains constant. In this case the dissociation of SO3 (as per Le Chatlier principle) |
| A. | decreases |
| B. | increases |
| C. | remains unaltered |
| D. | changes unpredictably. |
| Answer» B. increases | |
| 4795. |
Consider a reversible exothermic reaction in a plug flow reactor. The maximum and minimum permissible temperatures are Tmax and Tmin respectively. Which of the following temperature (T) profiles will require the shortest residence time to achieve the desired conversion. |
| A. | <img src="/_files/images/chemical-engineering/chemical-reaction-engineering/478-497-1.png"> |
| B. | <img src="/_files/images/chemical-engineering/chemical-reaction-engineering/478-497-2.png"> |
| C. | <img src="/_files/images/chemical-engineering/chemical-reaction-engineering/478-497-3.png"> |
| D. | <img src="/_files/images/chemical-engineering/chemical-reaction-engineering/478-497-4.png"> |
| Answer» C. <img src="/_files/images/chemical-engineering/chemical-reaction-engineering/478-497-3.png"> | |
| 4796. |
With increase in initial concentration, the fractional conversion of a first order reaction in a given time |
| A. | increases |
| B. | decreases |
| C. | remains constant |
| D. | unpredictable |
| Answer» D. unpredictable | |
| 4797. |
The rate of reaction of a/an __________ reaction is not affected by temperature rise. |
| A. | autocatalytic |
| B. | photochemical |
| C. | consecutive |
| D. | zero order. |
| Answer» C. consecutive | |
| 4798. |
Half-life period for a first order reaction is __________ the initial concentration of the reactant. |
| A. | directly proportional to |
| B. | inversely proportional to |
| C. | independent of |
| D. | none of these |
| Answer» D. none of these | |
| 4799. |
Carbon particles accummulated on the catalyst used in the gas oil cracking lies in the category of __________ poison. |
| A. | deposited |
| B. | chemisorbed |
| C. | selectivity |
| D. | stability |
| Answer» B. chemisorbed | |
| 4800. |
What is the order of chemical reaction , if itis found that the reaction rate doubles on doubling the concentration of B and also the reaction rate doubles when the concentrations of both A & B were doubled and quandrupled when the concentrations of both B & C were doubled ? |
| A. | 1 |
| B. | 2 |
| C. | 3 |
| D. | 4 |
| Answer» C. 3 | |