ChE Reaction Flashcards

(250 cards)

1
Q

Which of the following will give maximum gas conversion?

A. Fixed bed reactor.
B. Fluidized bed reactor.
C. Semi-fluidized bed reactor.
D. Plug-flow catalytic reactor.

A

C. Semi-fluidized bed reactor.

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2
Q

__________ explains the mechanism of catalysis.

A. Activated complex theory
B. Collision theory
C. Thermodynamics
D. None of these

A

A. Activated complex theory

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3
Q

The fractional volume change of the system for the isothermal gas phase reaction, A → 3B, between no conversion and complete conversion is

A. 0.5
B. 1
C. 2
D. 3

A

C. 2

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4
Q

A catalyst

A. initiates a reaction.
B. lowers the activation energy of reacting molecules.
C. is capable of reacting with any one of the reactants.
D. cannot be recovered chemically unchanged at the end of a chemical reaction.

A

B. lowers the activation energy of reacting molecules.

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5
Q

What is the order of a chemical reaction, A + 2B → C, if the rate of formation of ‘C’, increases by a factor of 2.82 on doubling the concentration of ‘A’ and increases by a factor of 9 on trebling the concentration of ‘B’?

A. 7/2
B. 7/4
C. 5/2
D. 5/4

A

A. 7/2

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6
Q

For high conversion in a highly exothermic solid catalyzed reaction, use a __________ bed reactor.

A. fixed
B. fluidized bed reactor followed by a fixed
C. fixed bed reactor followed by a fluidized
D. fluidized

A

B. fluidized bed reactor followed by a fixed

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7
Q

For every 10°C rise in temperature, the rate of chemical reaction doubles. When the temperature is increased from 30 to 70°C, the rate of reaction increases __________ times.

A. 8
B. 12
C. 16
D. 32

A

C. 16

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8
Q

A first order reaction requires two equal sized CSTR. The conversion is

A. less when they are connected in series.
B. more when they are connected in series.
C. more when they are connected in parallel.
D. same whether they are connected in series or in parallel.

A

B. more when they are connected in series.

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9
Q

In case of physical adsorption, the heat of adsorption is of the order of __________ kcal/kg-mole.

A. 100
B. 1000
C. 10000
D. 100000

A

B. 1000

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10
Q

The most unsuitable reactor for carrying out reactions in which high reactant concentration favors high yields is

A. backmix reactor
B. plug flow reactor
C. series of CSTR
D. PFR in series

A

A. backmix reactor

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11
Q

Pick out the wrong statement pertaining to space velocity of flow reactors.

A. The unit of space velocity is (time)-1
B. The space velocity of 3 hr-1 means that three reactor volumes of feed at specified conditions are being fed into the reactor every hour.
C. The space velocity of 3 hr-1 means that one third reactor volume of feed at specified conditions are being fed into the reactor.
D. none of these.

A

C. The space velocity of 3 hr-1 means that one third reactor volume

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12
Q

A reactor is generally termed as an autoclave, when it is a

A. high pressure batch reactor.
B. atmospheric pressure tank reactor.
C. high pressure tubular reactor.
D. atmospheric pressure CSTR

A

A. high pressure batch reactor
(PHB P18-57)

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13
Q

6 Kg of carbon is burnt with an amount of air containing 18 gm oxygen. The product contains 16.5 gms CO2 and 2.8 gms CO besides other constituents. What is the degree of conversion on the basis of disappearance of limiting reactant?

A. 100%
B. 95%
C. 75%
D. 20%

A

B. 95%

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14
Q

The rate constant of a chemical reaction decreases by decreasing the

A. pressure
B. concentration of reactants
C. temperature
D. duration of reaction

A

C. temperature

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15
Q

__________ is the response curve for a step input signal from a reactor.

A. S-curve
B. C-curve
C. I-curve
D. none of these

A

A. S-curve

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16
Q

Which of the following is the most suitable for very high pressure gas phase reaction?

A. Batch reactor
B. Tubular flow reactor
C. Stirred tank reactor
D. Fluidized bed reacto

A

B. Tubular flow reactor

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17
Q

The reaction between oxygen and organic material is a/an __________ reaction.

A. exothermic
B. endothermic
C. biochemical
D. photochemical

A

A. exothermic

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18
Q

With decrease in temperature, the equilibrium conversion of a reversible endothermic reaction

A. decreases
B. increases
C. remains unaffected
D. increases linearly with temperature

A

A. decreases

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19
Q

In an exothermic chemical reaction, the reactants compared to the products have

A. higher temperature
B. more energy
C. less energy
D. same energy.

A

B. more energy

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20
Q

A reversible liquid phase endothermic reaction is to be carried out in a plug flow reactor. For minimum reactor volume, it should be operated such that the temperature along the length

A. decreases.
B. increases.
C. is at the highest allowable temperature throughout.
D. first increases and then decrease

A

C. is at the highest allowable temperature throughout.

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21
Q

The rate constant of a chemical reaction increases by 100 times when the temperature is increased from 400 °K to 500 °K. Assuming transition state theory is valid, the value of E/R is

A. 8987°K
B. 9210°K
C. 8764°K
D. 8621°K

A

C. 9210°K
(9656.627°K by calculation)

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22
Q

A batch reactor is suitable for

A. achieving cent percent conversion of reactants into products.
B. large scale gaseous phase reactions.
C. liquid phase reactions.
D. obtaining uniform polymerization products in highly exothermic reactions.

A

C. liquid phase reactions.

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23
Q

For a heterogeneous catalytic reaction

A. free energy of activation is lowered in the presence of catalyst, which remains unchanged at the end of reaction.
B. a relatively small amount of catalyst can cause the conversion of large amount of reactants which does not mean that catalyst concentration is important.
C. the catalyst does not form an intermediate complex with the reactant.
D. the surface of the catalyst does not play an important role during reaction.

A

A. free energy of activation is lowered in the presence of catalyst, which remains unchanged at the end of reaction.

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24
Q

The increase in the rate of reaction with temperature is due to

A. increase in the number of effective collisions.
B. decrease in activation energy.
C. increase in the average kinetic energy of the reacting molecules.
D. none of these.

A

B. decrease in activation energy.
(PHB P7-6)

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25
A catalyst loses its activity due to A. loss in surface area of the active component. B. agglomeration of metal particles caused by thermal sintering of the solid surface. C. covering of the catalytic active sites by a foreign substance. D. all (a), (b) and (c).
D. all (a), (b) and (c).
26
'N' plug flow reactors in series with a total volume 'V' gives the same conversion as a single plug flow reactor of volume 'V' for __________ order reactions. A. first B. second C. third D. any
D. any
27
For a zero order chemical reaction, the A. half life period is directly proportion to the initial concentration of the reactants. B. plot of products concentration with time is a straight line through the origin. C. products concentration increases linearly with time. D. all (a), (b) and (c).
D. all (a), (b) and (c).
28
BET apparatus A. measures the catalyst surface area directly. B. operates at very high pressure. C. is made entirely of stainless steel. D. none of these.
D. none of these.
29
Radioactive decay follows __________ order kinetics. A. first B. second C. third D. zero.
A. first
30
The excess energy of reactants in a chemical reaction required to dissociate into products is termed as the __________ energy. A. activation B. potential C. binding D. threshold
A. activation
31
Pick out the correct statement. A. In catalytic reactions, the catalyst reacts with the reactants. B. A catalyst initiates a chemical reaction. C. A catalyst lowers the activation energy of the reacting molecules. D. A catalyst cannot be recovered chemically unchanged at the end of the chemical reaction.
C. A catalyst lowers the activation energy of the reacting molecules.
32
The dimensions of rate constant for reaction 3A → B are (l/gm mole)/min. Therefore the reaction order is A. 0 B. 1 C. 2 D. 3
C. 2
33
Pick out the correct statement A. Reactions with high activation energies are very temperature sensitive. B. Chemical equilibrium is a static state. C. A photochemical reaction is catalyzed by light. D. A chemical reaction occurs when the energy of the reacting molecule is less than the activation energy of the reaction.
A. Reactions with high activation energies are very temperature sensitive.
34
If the time required to complete a definite fraction of reaction varies inversely as the concentration of the reactants, then the order of reaction is A. 0 B. 1 C. 2 D. 3
C. 2
35
Sulphuric acid is used as a catalyst in the A. hydrogenation of oils. B. gas phase oxidation of SO2 in chamber process. C. alkylation of hydrocarbons. D. none of these.
C. alkylation of hydrocarbons.
36
Fractional conversion __________ with increase in pressure for ammonia synthesis reaction i.e., N2 + 3H2  2NH3. A. increases B. decreases C. remains unchanged D. unpredictable from the data
A. increases
37
Pick out the wrong statement. A. The vessel dispersion number (D/UL) for plug flow and mixed flow approaches zero and infinity respectively. B. Space time in a flow reactor is a measure of its capacity and is equal to the residence time when the density of reaction mixture is constant. C. Mixed reactor is always smaller than the plug flow reactor for all positive reaction orders for a particular duty. D. In an ideal tubular flow reactor, mixing takes place in radial direction and there is no mixing in longitudinal direction.
C. Mixed reactor is always smaller than the plug flow reactor for all positive reaction orders for a particular duty.
38
The reason why a catalyst increases the rate of reaction is that, it A. decreases the energy barrier for reaction. B. increases the activation energy. C. decreases the molecular collision diameter. D. none of these.
A. decreases the energy barrier for reaction.
39
A first order irreversible reaction, A → B is carried out separately in a constant volume as well as in a variable volume reactor for a particular period. It signifies that __________ in the two reactors. A. both conversion as well as concentration are same B. conversion in both will be the same but concentrations will be different C. both the conversion as well as concentrations will be different D. none of these.
B. conversion in both will be the same but concentrations will be different
40
The excess energy of reactants in a chemical reaction required to dissociate into products is termed as the __________ energy. A. activation B. potential C. binding D. threshhold
A. activation
41
When the density of the reaction mixture is constant in a chemical reaction, the ratio of the mean residence time to space time is A. > 1 B. < 1 C. 1 D. 0
C. 1
42
In an ideal tubular-flow reactor A. there is no mixing in longitudinal direction. B. mixing takes place in radial direction. C. there is a uniform velocity across the radius. D. all (a), (b) and (c).
D. all (a), (b) and (c).
43
At a given value of E/R (ratio of activation energy and gas constant), the ratio of the rate constants at 500°K and 400°K is 2, if Arrhenius law is used. What will be this ratio, if transition state theory is used with the same value of E/R? A. 1.6 B. 2 C. 2.24 D. 2.5
D. 2.5 (by calculation: 1.6)
44
__________ is the controlling step in a highly temperature sensitive fluid-solid non-catalytic reaction. A. Gas film diffusion B. Ash diffusion C. Chemical reaction D. none of these
C. Chemical reaction
45
An autothermal reactor is A. most suitable for a second order reaction. B. most suitable for a reversible reaction. C. completely self-supporting in its thermal energy requirements. D. isothermal in nature.
C. completely self-supporting in its thermal energy requirements.
46
The rate constant of a first order reaction depends on the A. concentration of the reactant. B. temperature. C. concentration of the product. D. time.
B. temperature.
47
A reaction in which one of the products of reaction acts as a catalyst is called a/an __________ reaction. A. catalytic B. autocatalytic C. photochemical D. none of these
B. autocatalytic
48
The ratio of volume of mixed reactor to the volume of P.F.R. (for identical flow rate, feed composition and conversion) for zero order reaction is A. ∞ B. 0 C. 1 D. > 1
C. 1
49
Which of the following will favor the reverse reaction in a chemical equilibrium reaction? A. Increasing the concentration of one of the reactants. B. Increasing the concentration of one or more of the products. C. Removal of at least one of the products at regular interval. D. None of these.
B. Increasing the concentration of one or more of the products.
50
Conversion increases with increase in temperature in case of a an __________ reaction. A. autocatalytic B. irreversible C. reversible endothermic D. reversible exothermic
C. reversible endothermic
51
A photochemical reaction is __________ light. A. initiated by B. accompanied with emission of C. catalyzed by D. used to convert heat energy into
A. initiated by
52
Pick out the wrong statement. 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.
C. In a continuous flow reactor, uniform concentration cannot be maintained throughout the vessel even in a well agitated system.
53
In a/an __________ reactor, there is exchange of heat with the surroundings with sizeable temperature variation. A. adiabatic B. isothermal C. non-adiabatic D. none of these.
C. non-adiabatic
54
'Unreacted core model' represents the reaction involving A. combustion of coal particles. B. roasting of sulphide ores. C. manufacture of carbon disulphide from elements. D. none of these.
B. roasting of sulphide ores.
55
If a solid-gas non-catalytic reaction occurs at very high temperature, the rate controlling step is the __________ diffusion. A. film B. ash layer C. pore D. none of these
A. film
56
The units of frequency factor in Arrhenius equation A. are the same as those of the rate constant. B. depend on the order of the reaction. C. depend on temperature, pressure etc. of the reaction. D. are cycles per unit time.
A. are the same as those of the rate constant.
57
Which of the following is not a chemical step in a fluid solid catalytic reaction? A. Surface chemical reaction B. Adsorption C. Desorption D. None of these
D. None of these
58
In case of __________ reactions, the reaction rate does not decrease appreciably as the reaction proceeds. A. catalytic B. parallel C. series D. auto catalytic
D. auto catalytic
59
For nearly isothermal operation involving large reaction time in a liquid-phase reaction, the most suitable reactor is a __________ reactor. A. stirred tank B. tubular flow C. batch D. fixed bed
A. stirred tank
60
B.E.T. method can be used to determine the __________ of a porous catalyst. A. solid density B. pore volume C. surface area D. all (a), (b) and (c)
C. surface area
61
Rate constant for a first order reaction does not depend upon reaction time, extent of reaction and the initial concentration of reactants; but it is a function of reaction temperature. In a chemical reaction, the time required to reduce the concentration of reactant from 100 gm moles/liter to 50 gm moles/liter is same as that required to reduce it from 2 gm moles/liter to 1 gm mole liter in the same volume. Then the order of this reaction is A. 0 B. 1 C. 2 D. 3
B. 1
62
Which of the following is an independent variable for a batch tank reactor with uniform concentration and temperature? A. Time B. Useful volume of the tank C. Diameter of the reactor D. None of these
A. Time
63
For a gaseous phase reaction, rate of reaction is equal to K CA CB. If the volume of the reactor is suddenly reduced to 1/4th of its initial volume, then the rate of reaction compared to the original rate will be __________ times. A. 8 B. 16 C. 1/8 D. 1/16
B. 16
64
In a reversible chemical reaction having two reactants in equilibrium, if the concentration of the reactants is doubled, then the equilibrium constant will A. remain the same B. be halved C. also be doubled D. become one fourth
A. remain the same
65
The equilibrium constant of a catalytic chemical reaction __________ due to the presence of a catalyst. A. increases B. decreases C. remains unaffected D. unpredictable from the data
C. remains unaffected
66
The rate constant of a chemical reaction increases by increasing the A. temperature B. pressure C. reactant's concentration D. none of these
A. temperature
67
The catalytic activity of enzymes is due to their capacity to lower the __________ energy. A. activation B. potential C. kinetic D. none of these
A. activation
68
Pick out the correct statement. A. A lower temperature favors the reaction of lower activation energy. B. The dispersion number for a reactor/vessel is uL/D. C. The rate controlling step in a reaction involving many steps is the fastest step. D. Pore volume and porosity of a catalyst is measured by Brunaver-Emmet-Teller (BET) technique.
A. A lower temperature favors the reaction of lower activation energy.
69
A batch reactor is characterized by A. constant residence time. B. variation in extent of reaction and properties of the reaction mixture with time. C. variation in reactor volume. D. very low conversion.
B. variation in extent of reaction and properties of the reaction mixture with time.
70
When a catalyst increases the rate of forward reaction, the value of rate constant A. increases B. decreases C. remain same D. becomes infinite
A. increases
71
Rate determining step in a reaction consisting of a number of steps in series is the __________ step. A. fastest B. slowest C. intermediate D. data insufficient; can't be predicte
B. slowest
72
The rate of a chemical reaction is almost doubled for every 10°C rise in temperature. The rate will increase __________ times, if the temperature rises from 10 to 100°C. A. 256 B. 512 C. 112 D. 612
B. 512
73
When all the limiting reactant is consumed in the reaction, the operational yield __________ the relative yield. A. is greater than B. is smaller than C. equals D. can be either greater or smaller than (depends on the type of reaction)
C. equals
74
The half life period of a first order reaction is A. always the same irrespective of the reaction. B. dependent on initial concentration of the reactants. C .proportional to the initial concentration of reactants. D .half the specific rate constant.
B. dependent on initial concentration of the reactants.
75
Catalyst carriers A. have very high selectivity. B. increase the activity of a catalyst. C. provide large surface area with a small amount of active material. D. inhibit catalyst poisoning.
C. provide large surface area with a small amount of active material.
76
For the liquid phase zero order irreversible reaction A → B, the conversion of A in a CSTR is found to be 0.3 at a space velocity of 0.1min-1 . What will be the conversion for a PFR with a space velocity of 0.2 min-1? Assume that all the other operating conditions are the same for CSTR and PFR. A. 0.15 B. 0.30 C. 0.60 D. 0.90
C. 0.60
77
In flow reactors, the performance equations interrelate the rate of reaction to the A. feed rate. B. reactor volume, C. extent of reaction. D. all (a), (b) and (c).
D. all (a), (b) and (c).
78
Space velocity A. describes the extensive operating characteristics of a tubular flow reactor. B. is the maximum feed rate pre unit volume of reactor for a given conversion. C. is a measure of the ease of the reaction. D. all (a), (b) and (c)
D. all (a), (b) and (c)
79
The rate of the chemical reaction A → B doubles as the concentration of A i.e.., CA is doubled. If rate of reaction is proportional to CA, then what is the value of n for this reaction? A. 0.5 B. 1 C. 0 D. 2
B. 1
80
A reaction which is caalyzed by a base is catalyzed by all substances which have a tendency to A. lose a proton B. gain a proton C. gain an electron D. none of these
C. gain an electron
81
For a homogeneous reaction of nth order, the dimension of the rate constant is given by A. 1/(time)n B. (concentration)1-n/(time) C. (concentration)n-1/(time) D. none of these
B. (concentration)1-n/(time)
82
The fractional volume change between no conversion and complete conversion, for the isothermal gas phase reaction, 2A → R, is A. 0.5 B. -0.5 C. 1 D. 1.5
B. -0.5
83
The reaction in which one of the products of reaction acts as a catalyst is called a/an __________ reaction. A. biochemical B. photochemical C. catalytic D. autocatalytic
D. autocatalytic
84
A typical example of an exothermic reversible reaction conducted at high pressure in industry is A. dehydration of ethanol. B. methanol synthesis. C. reformation of methane. D. polymerization of ethylene.
A. dehydration of ethanol.
85
Study of chemical kinetics is the easiest in the case of __________ reactions. A. irreversible B. reversible C. surface D. autolysis
A. irreversible
86
In autocatalytic reactions, A. one of the reactants acts as a catalyst. B. one of the products acts as a catalyst. C. catalysts have very high selectivity. D. no catalyst is use
B. one of the products acts as a catalyst.
87
Semi-batch reactor is preferred, when a/an A. a highly exothermic reaction is to be controlled. B. undesirable side reaction (at high concentration of one of the reactants) is to be avoided. C. a gas is to be reacted with liquid (e.g. hydrogenation of fat). D. all (a), (b), and (c).
D. all (a), (b), and (c).
88
For identical flow rate, feed composition and for elementary first order reactions, 'N' equal sized mixed reactors in series with a total volume 'V' gives the same conversion as a single plug flow reactor of volume 'V' for constant density systems. This is true, when the value of 'N' is A. 1 B. >1 C. ∞ D. ≥1
C. ∞
89
What is the order of a chemical reaction whose rate is deter-mined by the variation of one concentration term only? A. zero B. first C. second D. third
B. first
90
Pick out the wrong statement. A. Visible radiation provides the necessary activation energy in photochemical reactions. B. The order and molecularity of a complex reaction may not be the same. C. For a second order reaction, the slope of the graph/plot between rate and (concentration) is equal to the rate constant (k). D. Molecularity of the reaction is always a whole number greater than zero.
B. The order and molecularity of a complex reaction may not be the same.
91
The rate at which a chemical substance reacts is proportional to its A. active mass B. equivalent weight C. molecular weight D. none of these
A. active mass
92
A plug-flow reactor is characterized by A. high capacity. B. presence of axial mixing. C. presence of lateral mixing. D. constant composition and temperature of reaction mixture.
C. presence of lateral mixing.
93
For a tubular reactor with space time 'τ' and residence time 'θ', the following statement holds good. A. τ and θ are always equal. B. τ = θ, when the fluid density changes in the reactor. C. τ = θ, for an isothermic tubular reactor in which the density of the process fluid is constant. D. τ = θ, for a non-isothermal reactor.
C. τ = θ, for an isothermic tubular reactor in which the density of the process fluid is constant.
94
Rate of an autocatalytic chemical reaction is a function of A. temperature only. B. pressure only. C. composition only. D. all (a), (b) and (c).
D. all (a), (b) and (c).
95
Which of the following curves shows the effect of temperature on the extent of gas-solid adsorption at a given pressure? A. Langmuir adsorption isotherm B. Adsorption isobar C. Freundlich adsorption isotherm D. None of these
B. Adsorption isobar
96
Fluid flow in a real packed bed can be approximated as __________ model. A. plug flow B. dispersion C. mixed flow D. tank in series
B. dispersion
97
A reaction which is catalyzed by an acid is also catalyzed by any substance, which has a tendency to A. lose a proton. B. gain a proton. C. lose an electron D. none of these.
A. lose a proton.
98
A stirred tank reactor compared to tubular-flow reactor provides A. more uniform operating conditions. B. permits operation at the optimum temperature for a long reaction time. C. higher overall selectivity for a first order consecutive reaction. D. all (a), (b) and (c)
D. all (a), (b) and (c)
99
In chamber process of sulphuric acid manufacture in industry, the gas phase oxidation of SO2 to SO3 is accomplished by a __________ reaction. A. non-catalytic homogeneous B. non-catalytic heterogeneous C. catalytic homogenous D. catalytic heterogeneous
C. catalytic homogenous
100
If the rate of a chemical reaction becomes slower at a given temperature, then the A. initial concentration of the reactants remains constant. B. free energy of activation is lower. C. entropy changes. D. free energy of activation is higher.
D. free energy of activation is higher.
101
The conversion XA and residence time data are collected for zero order liquid phase reaction in a stirred tank reactor. Which of the following will be a straight line ? A. XA Vs τ B. XA Vs ln τ C. XA/(1 - XA) Vs τ D. XA(1 - XA) Vs τ
A. XA Vs τ
102
The rate of the reaction, X → Y, quadruples when the concentration of 'X' is doubled. The rate expression for the reaction is, r = K Cxn, the value of 'n' in this case will be A. 0 B. 1 C. 2 D. 3
C. 2
103
The value of steric factor 'P' in the equation k = PZeE/RT usually ranges from A. 1.0 to 10-8 B. 1.1 to 102 C. 0.1 to 0.9 D. none of these
A. 1.0 to 10-8
104
For a zero order reaction, the concentration of product increases with the A. increase of reaction time. B. increase in initial concentration. C. total pressure. D. decrease in total pressure.
A. increase of reaction time.
105
Pick out the wrong statement. A. 'Hold back' is defined as the fraction of material that stays longer than the mean residence time. B. Study of non-ideal flow reactor is done experimentally by stimulus-response technique. C. For studying a chemical reaction, it is desirable to monitor the reactants during initial stages and the products during the final stages of reaction. D. A batch reactor cannot be used to study the kinetics of catalytic reaction.
D. A batch reactor cannot be used to study the kinetics of catalytic reaction.
106
Effectiveness factor of a catalyst pellet is a measure of the __________ resistance. A. pore diffusion B. gas film C. chemical reaction D. none of these
B. gas film
107
Given, 3H2 + CO = CH4 + H2O, Kp = 101.84 4H2 + CO2 = CH4 + 2H2O, Kp = 101.17 The Kp for the reaction CO + H2O = CO2 + H2 is A. 103.01 B. 10-0.67 C. 10-3.01 D. 100.67
D. 100.67
108
Differential method for analyzing the kinetic data is used A. for testing complicated mechanisms. B. when the data are scattered. C. when rate expressions are very simple. D. none of these.
A. for testing complicated mechanisms.
109
The reaction in which the rate equation corresponds to a stoichiometric equation is called a/an __________ reaction. A. elementary B. non-elementary C. parallel D. autokinetic
A. elementary
110
The reaction A → B is conducted in an isothermal batch reactor. If the conversion of A increases linearly with holding time, then the order of the reaction is A. 0 B. 1 C. 1.5 D. 2
A. 0
111
Arrhenius equation represents graphically the variation between the __________ and temperature. A. rate of reaction B. frequency factor C. rate constant D. activation energy
C. rate constant
112
__________ catalytic reaction is involved in the thermal cracking of gas oil. A. Homogeneous B. Non- Homogeneous C. Heterogeneous D. Non-Heterogeneous
A. Homogeneous
113
Variables affecting the rate of homogeneous reactions are A. pressure and temperature only. B. temperature and composition only. C. pressure and composition only. D. pressure, temperature and composition.
D. pressure, temperature and composition.
114
A chemical reaction occurs when the energy of the reacting molecules is __________ the activation energy of the reaction. A. less than B. equal to C. more than D. equal to or more than
D. equal to or more than
115
Which of the following resistances is not involved in a gas phase catalytic (gas-solid) reaction? A. Ash resistance. B. Gas film and pore surface diffusion resistances for reactants. C. Surface phenomenon resistance. D. Gas film and pore surface diffusion resistances for products.
A. Ash resistance.
116
If the time required to change the concentration of reactant to half its original value is independent of the initial concentration, the order of reaction is A. zero B. one C. two D. three
B. one
117
A batch adiabatic reactor at an initial temperature of 373°K is being used for the reaction, A → B. Assume the heat of reaction is - 1kJ/mole at 373°K and heat capacity of both A and B to be constant and equal to 50 J/mole-K. The temperature rise after a conversion of 0.5 will be A. 5°C B. 10°C C. 20°C D. 100°C
B. 10°C
118
A photochemical reaction is A. accompanied with emission of light. B. catalyzed by light. C. initiated by light. D. all (a), (b) & (c).
C. initiated by light.
119
The optimum performance for reactors operating in parallel is obtained when the feed stream is distributed in such a way, that the A. space time for each parallel line is same B. space time for parallel lines is different. C. larger reactors have more space time compared to smaller ones. D. none of these.
A. space time for each parallel line is same
120
Pure ethanol vapor is fed to a reactor packed with alumina catalyst, at the rate of 100 kmole / hr. The reactor products comprise: ethylene: 95 kmole / hr, water vapor: 97.5 k mole / hr and diethyl ether: 2.5 kmole/hr. The reactions occurring can be represented by: C2H5OH → C2H4 + H2O 2C2H5OH → C2H5 - O - C2H5 + H2O The percent conversion of ethanol in the reactor is A. 100 B. 97.5 C. 95 D. 2.5
A. 100
121
A backmix reactor A. is same as plug-flow reactor. B. is same as ideal stirred tank reactor. C. employs mixing in axial direction only. D. is most suitable for gas phase reaction.
B. is same as ideal stirred tank reactor.
122
Rate of a chemical reaction is not influenced by the A. catalyst B. temperature C. reactants concentration D. number of molecules of reactants taking part in a reaction
D. number of molecules of reactants taking part in a reaction
123
Pick out the wrong statement: A. Chemical reactions with high activation energy are very temperature sensitive. B. A flat velocity profile exists in a plug flow reactor. C. The residence time for all the elements of fluid in case of a P.F.R. need not be same. D. Half life of a reaction increases with increased initial concentration for reaction orders more than one.
124
The reaction A → B is conducted in an adiabatic plug flow reactor (PFR). Pure A at a concentration of 2 kmol/m3 is fed to the reactor at the rate of 0.01 m3 /s and at a temperature of 500 K. If the exit conversion is 20%, then the exit temperature (in k)is (Data: Heat of reaction at 298 K = - 50000 kJ/ kmole of A reacted Heat capacities CPA = CPB = 100kJ/kmole. K (may be assumed to be independent of temperature) A. 400 B. 500 C. 600 D. 1000
C. 600
125
In a semi-batch reactor, A. mixing takes place in axial direction only. B. velocity of reaction can be controlled. C. condition similar to plug flow reactor exists. D. residence time is constant.
B. velocity of reaction can be controlled.
126
Which of the following is a controlling factor in very fast heterogeneous reaction? A. Heat and mass transfer effects B. Pressure C. Temperature D. Composition of reactant
A. Heat and mass transfer effects
127
Enzymes are destroyed, when the A. temperature is very high, B. reactant's concentration is very high. C. reactant's concentration is very low. D. reaction rate is independent of the reactant's concentration.
A. temperature is very high,
128
For an autocatalytic reactor, the suitable reactor set up is A. P.F. reactors in series. B. CSTR in series. C. CSTR followed by P.F. reactor. D. P.F. reactor followed by CSTR.
C. CSTR followed by P.F. reactor.
129
Ionic reactions occur in A. solid state only B. liquid state only C. solutions D. any state
C. solutions
130
Half life period of a chemical reaction is A. the time required to reduce the concentration of the reacting substance to half its initial value. B. half of the space time of a reaction. C. half of the residence time of a reaction. D. none of these
A. the time required to reduce the concentration of the reacting substance to half its initial value.
131
In the gaseous phase ammonia formation reaction (N2 + 3H2 → 2NH3), the value of the equilibrium constant depends on the A. total pressure of the system. B. volume of the reactor. C. temperature. D. initial concentration of N2 and H2.
C. temperature.
132
Photochemical reaction rate does not depend significantly on temperature, because 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.
C. the energy of reacting molecules exceeds the activation energy by absorption of light.
133
A CSTR is to be designed in which an exothermic liquid phase first order reaction of the type, A → R, is taking place. The reactor is to be provided with a jacket in which coolant is flowing. Following data is given: Cao = 5 kmole/m3; XA = 0.5; Feed temperature = reactor temperature = 40°C. Rate constant at 40°C = 1 min-1; (ΔH) = - 40kJ/mole; ρ = 1000kg/m3 CP = 4 J/gm-°C; q = 10-3 m2/min (ρ and CP are same for the reactant and product streams). The amount of heat to be removed is A. 2/3 kW B. 1kW C. 5/3 kW D. 4kW
C. 5/3 kW
134
According to the 'law of mass action', the rate of reaction is directly proportional to the A. equilibrium constant. B. volume of the reaction vessel. C. nature of the reactants. D. molar concentration of the reactants.
D. molar concentration of the reactants.
135
For an ideal gas mixture undergoing a reversible gaseous phase chemical reaction, the equilibrium constant A. is independent of pressure. B. increases with pressure. C. decreases with pressure. D. increases /decreases with pressure depending on the stoichiometric coefficients of the reaction.
B. increases with pressure.
136
A batch reactor is A. suitable for gas-phase reactions on commercial scale. B. suitable for liquid phase reactions involving small production rate. C. least expensive to operate for a given rate. D. most suitable for very large production rate.
B. suitable for liquid phase reactions involving small production rate.
137
For an isothermal second order aqueous phase reaction, A → B, the ratio of the time required for 90% conversion to the time required for 45% conversion is A. 2 B. 4 C. 11 D. 22
C. 11
138
There is no correspondence between stoichiometry and the rate equation in case of a/an __________ reaction. A. elementary B. multiple C. autocatalytic D. non-elementary
D. non-elementary
139
A spherical porous catalyst particle of radius R is subjected to reactant A which reacts to form B by a zero order surface reaction A → B. Film mass transfer resistance is negligible and pore diffusion of A is rate controlling. The effectiveness factor of the catalyst is reported as 7/8. Which of the following statement is true? A. Inner catalyst core of radius R/8 does not participate in reaction. B. Inner catalyst core of radius R/2 does not participate in reaction. C .Inner catalyst core of radius 7R/8 does not participate in reaction. D. Effectiveness factor for a zero order reaction cannot be 7/8 as it must always be 1.
A. Inner catalyst core of radius R/8 does not participate in reaction.
140
Which of the following is used for calcination of limestone and dolomite in industrial practice? A. Fluidized bed reactor B. Moving bed reactor C. Fixed bed reactor D. None of these
B. Moving bed reactor
141
An imbalanced chemical reaction equation is against the law of A. multiple proportion B. conservation of mass C. constant proportion D. none of these
B. conservation of mass
142
Which of the following is a characteristic of an ideal plug flow reactor? A. Axial dispersion B. Flat velocity profile C. Uniform mixing D. None of these
B. Flat velocity profile
143
An isothermal aqueous phase reversible reaction, P ⇔ R, is to be carried out in a mixed flow reactor. The reaction rate in kmole/m3-h is given by, r = 0.5CP - 0.125CR. A stream containing only P enters the reactor. The residence time required (in hours) for 40% conversion of P is A. 0.80 B. 1.33 C. 1.60 D. 2.67
C. 1.60
144
145
What is the unit of the rate constant in a chemical reaction in which 10% of the reactant decomposes in one hour, 20% in two hours, 30% in three hours and so on? A. Liter/mole-second B. Moles/liter-second C. Liter/mole D. Liter/second
A. Liter/mole-second
146
For a fluidized bed reactor, the most suitable/relevant model is a __________ model. A. tank in series B. bubbling bed C. plug flow D. none of these
B. bubbling bed
147
The rate at which a chemical substance reacts is proportional to its A. active mass B. molecular weight C. equivalent weight D. atomic weight
A. active mass
148
The most suitable reactor for carrying out an auto-thermal reaction is a A. batch reactor B. CSTR C. semi-batch reactor D. plug-flow reactor
B. CSTR
149
Limiting reactant in a chemical reaction decides the A. rate constant B. conversion C. reaction speed D. equilibrium constant
B. conversion
150
In case of a consecutive unimolecular type first order reaction , the concentration of component __________ increases continuously with time. A. S B. R C. A D. none of these
A. S
151
The exit age distribution of fluid leaving a vessel is used to know the A. activation energies of a reaction. B. reaction mechanism. C. extent of non-ideal flow in the vessel. D. none of these.
C. extent of non-ideal flow in the vessel.
152
From Arhenius law, a plot of loge K versus 1/T gives a straight line with a slope of (-E/R). The unit of E/R is A. k cal B. k cal/°K C. °K D. k cal. °K
C. °K
153
Reverse reaction in a chemical equilibrium is favoured by the A. removal of one of the products regularly. B. increase in the concentration of one of the products. C. increase in the concentration of one of the reactants. D. none of these.
B. increase in the concentration of one of the products.
154
Sum of the powers of the concentration terms in the rate equation is called the __________ of the reaction. A. order B. overall order C. molecularity D. none of these
B. overall order
155
During manufacture of H2SO2, the oxidation of SO2 to SO3 by oxygen is an endothermic reaction. The yield of SO3 will be maximised, if the A. temperature is increased. B. pressure is reduced. C. temperature is increased and pressure is reduced. D. temperature is reduced pressure is increased.
D. temperature is reduced pressure is increased.
156
BET apparatus is used to determine the A. specific surface of a porous catalyst. B. pore size distribution. C. pore diameter. D. porosity of the catalyst bed.
A. specific surface of a porous catalyst.
157
When the reaction occurs in the diffusion controlled region, the apparent activation energy as measured is only __________ the true value. A. twice B. half C. equal D. none of thes
B. half
158
Kinetics of a solid catalysed reaction can best be studied in a __________ reactor. A. batch B. plug-flow C. mixed D. none of these
C. mixed
159
The reactions of high molecularity are rare, because A. of very large activation energy of many bodies. B. of low probability of many body collisions. C. many body collisions are not favoured energetically. D. of requirement of very large concentration for such reactions.
B. of low probability of many body collisions.
160
Which of the following is the most suitable for isothermal operation ? A. Batch reactor B. Back-mix reactor C. Plug-flow reactor D. Fixed bed reactor
B. Back-mix reactor
161
For a first order chemical reaction, the rate constant A. changes on changing the concentration units. B. is not a function of the unit of time. C. has unit of time-1 D. none of these
C. has unit of time-1
162
Which of the following is an autocatalytic reaction ? A. Photochemical reactions B. Microbial fermentation reaction C. Enzyme fermentation reaction D. Ammonia synthesis reaction
B. Microbial fermentation reaction
163
Oil is hydrogenated using nickel catalyst in a __________ reactor. a. batch b. slurry c. fluidised bed d. fixed bed
b. slurry
164
The performance equations for constant density systems are identical for a. P.F.R. and backmix reactor. b. P.F.R. and batch reactor. c. P.F.R, batch reactor and backmix reactor. d. batch reactor and backmix reactor.
b. P.F.R. and batch reactor.
165
Reaction rate of a first order reaction, which is half completed in 23 minutes will be a. 0.03 sec-1 b. 0.03 min-1 c. 0.03 hr-1 d. 0.05 min-1
b. 0.03 min-1
166
Which of the following is the optimum operating condition for an exothermic reversible reaction taking place in a plug-flow reactor? a. Temperature should be high in the beginning and decreased towards the end of the reaction. b. Very low temperature should be used throughout the reaction. c. Very high temperature should be used throughout the reaction. d. none of these.
a. Temperature should be high in the beginning and decreased towards the end of the reaction.
167
Promoter is added to the catalyst to improve its a. porosity b. sensitivity c. surface area d none of these
b. sensitivity
168
An irreversible first order reaction is being carried out in a CSTR and PFR of same volume. The liquid flow rates are same. The relative conversion will a. be more in CSTR than in PFR. b. be more in PFR than in CSTR. c. be same in both cases. d. depend on the temperature.
b. be more in PFR than in CSTR.
169
When a high liquid hold up is required in a reactor for gas liquid reaction, use __________ column. a. packed b. spray c. tray d. bubble
d. bubble
170
For a tubular flow reactor with uniform concentration and temperature, the independent variable is a. time b. length c. diameter d. none of these
b. length
171
The reactions with low activation energy are a. always spontaneous b. slow c. fast d. non-spontaneous
c. fast
172
Which of the following is not endothermic in nature ? a. Combustion of sulphur. b. Gasification of carbon. c. Thermal cracking of fuel oil. d. Steam reforming of naphtha.
a. Combustion of sulphur.
173
The space time is equivalent to the holding time in a steady state mixed reactor for a. non-isothermal gas reaction. b. variable fluid density systems. c. constant fluid density systems. d. gas reactions with changing no. of moles.
c. constant fluid density systems.
174
The dispersion number of perfect mixed flow is a. 0 b. > 150 c. ∞ d. < 2100
c. ∞
175
An irreversible aqueous phase reaction, A + B → P, is carried out in an adiabatic mixed flow reactor. A feed containing 4kmole/m3 of each A and B enters the reactor at 8 m2/hr. If the temperature of the exit stream is never to exceed 390 K, what is the maximum inlet feed temperature allowed? Data: Heat of reaction = - 50 kJ/mole Density of the reacting mixture = 1000 kg/m3 Specific heat of reacting mixture = 2 kJ/kg-K The above data can be assumed to be independent of temperature and composition. a. 190 b. 290 c. 390 d. 490
b. 290
176
Half life period of a first order irreversible reaction A → B is a. k/2 b. ln k/2 c. ln 2/k d. ln 0.5/k
c. ln 2/k
177
Half life period of decomposition of a liquid 'A' by irreversible first order reaction is 12 minutes. The time required for 75% conversion of 'A' is __________ minutes. a.18 b. 24 c. 6 d. 12
b. 24
178
With increase in the space time of an irreversible isothermal reaction being carried out in a P.F. reactor, the conversion will a. increase b. decrease c. remain same d. data in insufficient; can't be predicted
a. increase
179
If ΔG (free energy change) for a chemical reaction is very large and negative, then the reaction is a. not feasible. b. just feasible. c. very much feasible. d. unpredictable as ΔG is no measure of feasibility of a reaction.
c. very much feasible.
180
In a zero order reaction, reactants concentration does not change with time and the a. time for half change is half the time taken for completion of the reaction. b. time for half change is independent of the initial concentration. c. time for completion of the reaction is independent of the initial concentration. d. reaction rate is trebled when the initial concentration is trebled.
a. time for half change is half the time taken for completion of the reaction.
181
The minimum energy required to allow a chemical reaction to proceed is termed as the 'threshold energy '. Chemical reaction with low activation energy are a. always irreversible. b. insensitive to temperature changes. c. mostly irreversible d. highly temperature sensitivr
b. insensitive to temperature changes.
182
If Thiele modulus is __________ , then the pore diffusion resistance in a catalyst may be considered as negligible. a. 0 b. ∞ c. < 0.5 d. 0.5
c. < 0.5
183
Catalytic action in a catalytic chemical reaction follows from the ability of catalyst to change the a. activation energy b. equilibrium constant c. heat of reaction d. none of these
a. activation energy
184
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.
b. whole surface of the catalyst is essentially uniform and the adsorbed molecule has no effect on the rate of adsorption per site.
185
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.
c. proteinous in nature.
186
An endothermic aqueous phase first order irreversible reaction is carried out in an adiabatic plug flow reactor. The rate of reaction a. is maximum at the inlet of the reactor. b. goes through a maximum along the length of the reactor. c. goes through a minimum along the length of the reactor. d. is maximum at the exit of the reactor.
a. is maximum at the inlet of the reactor.
187
For an ideal plug flow reactor, the value of Peclet number is a. 0 b. ∞ c. 1 d. 10
a. 0
188
An endothermic second order reaction is carried out in an adiabatic plug flow reactor. The rate of heat generation i a. maximum at the inlet of the reactor. b. maximum at the exit of the reactor. c. maximum at the centre of the reactor. d. constant throughout the reactor.
189
Equilibrium of a chemical reaction as viewed by kinetics is a __________ state. a. dynamic steady b. static steady c. dynamic unsteady d. none of these
a. dynamic steady
190
The conversion in a mixed reactor/accomplishing a reaction A → 3R is 50% when gaseous reactant 'A' is introduced at the rate of 1 litre/second and the leaving flow rate is 2 litres/second. The holding time for this operation is __________ second. a. 0.5 b. 1 c. 2 d. 3
a. 0.5
191
The size of plug flow reactor (PFR) for all positive reaction orders and for any given duty, is __________ that of mixed reactor. a. greater than b. equal to c. smaller than d. unpredictable from the data
c. smaller than
192
A space time of 3 hours for a flow reactor means that a. the time required to process one reactor volume of feed (measured at specified conditions) is 3 hours. b. three reactor volumes of feed can be processed every hour. c. it takes three hours to dump the entire volume of the reactor with feed. d. conversion is cent per cent after three hours.
a. the time required to process one reactor volume of feed (measured at specified conditions) is 3 hours.
193
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
c. 3
194
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.
a. is same as that in the reactor.
195
The energy balance equation over a tubular reactor under transient conditions is a. an ordinary non-linear differential equation. b. an algebraic differential equation. c. a linear partial differential equation. d. a non-linear partial differential equation.
c. a linear partial differential equation.
196
Maximum equilibrium conversion for endothermic reaction is obtained at the __________ temperature. a. highest possible b. lowest possible c. intermediate d. room
a. highest possible
197
198
For a first order chemical reaction in a porous catalyst, the Thiele modulus is 10. The effectiveness factor is approximately equal to a. 1 b. 0.5 c. 0.1 d. 0
c. 0.1
199
In solid catalysed reactions the diffusional effects are more likely to affect the overall rate of reaction for a. fast reactions in catalyst of small pore diameter. b. fast reaction in catalyst of large pore diameter. c. slow reactions in catalyst of small pore diameter. d. slow reactions in catalyst of large pore diameter.
c. slow reactions in catalyst of small pore diameter.
200
Helium-mercury method can be used to determine the __________ of the catalyst particle. a. pore volume b. solid density c. porosity d. all (a), (b), & (c).
d. all (a), (b), & (c).
201
In a semi-batch reactor a. velocity of reaction can be controlled. b. maximum conversion can be controlled. c. both the reactants flow counter-currently. d. residence time is constant.
a. velocity of reaction can be controlled.
202
A trickle bed reactor is the one, which a. has altogether three streams either entering or leaving. b. processes three reactants at different flow rates. c. processes three reactants with same flow rate. d. employs all the three phases (i.e.. .solid, liquid and gas).
d. employs all the three phases (i.e.. .solid, liquid and gas).
203
What is the order of a chemical reaction in which doubling the initial concentration of the reactants doubles the half lifetime of the reaction? a. 0 b. 1 c. 2 d. 3
a. 0
204
In a/an __________ vessel, the fluid enters and leaves following plug flow. a. open b. closed c. open-closed d. close-opened
b. closed
205
Shift conversion reaction a. converts N2 and H2 into NH3. b. converts CO to CO2 with steam. c. is non-catalytic. d. is highly exothermic.
b. converts CO to CO2 with steam.
206
Which one is the rate controlling step in a solid-gas non-catalytic reaction occurring at very high temperature? a. Pore diffusion b. Film diffusion c. Ash layer diffusion d. Chemical reaction
b. Film diffusion
207
The ratio of moles of a reactant converted into the desired product to that converted into unwanted product is called a. operational yield b. relative yield c. selectivity d. none of these
208
The response curve for a step input signal from a reactor is called C-curve. The variance of C-curve in a 'tanks in series model' comprising of 'm' tanks is equal to a. m b. 1/m c. m d. m2
b. 1/m
209
The eddy diffusivity for a liquid in plug flow must be a. 1 b. 0 c. ∞ d. between 0 and 1
b. 0
210
For the same residence time, which one will give the maximum conversion? a. Single stirred tank (v = 5 litres). b. Two stirred tank (each of 2.5 litres) in series. c. Stirred tank followed by tubular flow reactor (each of 2.5 litres). d. Single tubular flow reactor (v = 5 litres).
d. Single tubular flow reactor (v = 5 litres).
211
The rate constant of a reaction depends on the a. Initial concentration of reactants. b. Time of reaction. c. Temperature of the system. d. Extent of reaction
c. Temperature of the system.
212
For the reversible reaction A 2B, if the equilibrium constant K is 0.05 mole litre; starting from initially 2 moles of A and zero moles of B, how many moles will be formed at equilibrium? a. 0.253 b. 0.338 c. 0.152 d. 0.637
b. 0.338
213
For identical flow rate and feed composition, X plug flow reactors (PER) in series with a total volume V gives the same conversion as single a. CSTR of volume b. PFR of volume V c. CSTR of volume V/X d. PFR of volume V/X
b. PFR of volume V
214
Time required for 50% decomposition of a liquid in an isothermal batch reactor following first order kinetics is 2 minutes. The time required for 75% decomposition will be about __________ minutes. a. 3 b. 4 c. 6 d. 8
b. 4
215
For a __________ order reaction, the units of rate constant and rate of reaction are the same. a. Zero b. First c. Second d. Fractional
a. Zero
216
Vegetable oils are hydrogenated in a __________ reactor. a. slurry b. plug flow c. homogeneous catalytic d. none of these
a. slurry
217
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
b. 1/3
218
The rate of reaction does not decrease appreciably as the reaction proceeds in case of __________ reactions. a. autocatalytic b. exothermic c. endothermic d. autothermal
a. autocatalytic
219
The heat of reaction a. depends on the pressure only. b. depends on the mechanism of reaction only. c. depends on both pressure and mechanism of reaction. d. Is independent of the mechanism of reaction.
d. Is independent of the mechanism of reaction.
220
Which of the following does not produce a change in the value of rate constant of a reaction ? a. Pressure b. Temperature c. Concentration and catalyst d. None of these.
c. Concentration and catalyst
221
With increase in temperature, the equilibrium conversion of a reversible exothermic reaction a. decreases b. increase c. remains unaffected d. decreases linearily with temperature
a. decreases
222
Photo-chemical reactions occur in presence of a. sunlight. b. darkness, c. solid catalysts. d. monochromatic radiation only.
a. sunlight.
223
Knudsen diffusion is directly proportional to a. T b. √T c. 1/T d. T2
b. √T
224
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
c. decreases
225
A pulse tracer is introduced in an ideal CSTR (with a mean residence time (t) at time, t = 0. The time taken for the exit concentration of the tracer to reach half of its initial value will be a. 2τ b. 0.5τ c. τ/0.693 d. 0.693τ
a. 2τ
226
On application of pressure to the equilibrium system, ice water ; which of the following phenomenon will occur? a. Water will evaporate b. Equilibrium will not be attained c. More ice will be formed d. More water will be formed.
d. More water will be formed.
227
Participation of __________ is involved in the occurrence of a chemical reaction. a. protons b. neutrons c. electrons d. none of these
c. electrons
228
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
d. 3
229
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
a. higher in P.F. reactor
230
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
b. ideal tubular-flow reactor
231
Autocatalytic reactions are best carried out in a a. CSTR b. CSTR in series c. plug flow reactor d. recycle reactor
d. recycle reactor
232
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/Cao at the outlet of the reactor is a. 2/3 b. 5/8 c. 1/3 d. 3/8
b. 5/8
233
A first order reaction is to be treated in a series of two mixed reactors. The total volume of the two reactors is minimum, when the reactors are a. Equal in size. b. of different sizes. c. of such size that the ratio of their volumes is < 5. d. none of these.
a. Equal in size.
234
The equilibrium constant K of a chemical reaction depends on a. temperature only. b. pressure only. c. temperature and pressure. d. ratio of reactants.
a. temperature only.
235
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.
b. fraction of molecules having threshold energy increases.
236
The synthesis of proteins and metabolism in biological objects occur in the presence of biocatalyst called a. a ferment or an enzyme b. haemoglobin c. fungi d. none of these
c. fungi
237
In case of a __________ reactor, the composition in the reactor and at the exit of the reactor is the same. a. semi-batch b. tubular c. batch d. back-mix
d. back-mix
238
Exothermic reactions are best carried out in a. a CSTR. b. CSTR in series. c. a plug flow reactor followed by CSTR. d. CSTR followed by a plug flow reactor.
d. CSTR followed by a plug flow reactor.
239
Reactions with high activation energy are a. very temperature sensitive b. temperature insensitive c. always irreversible d. always reversible
a. very temperature sensitive
240
A space velocity of 5 hr-1 means that a. five reactor volumes of feed (at specified conditions) are being fed into the reactor per hour. b. after every 5 hours, reactor is being filled with the feed. c. cent per cent conversion can be achieved in at least 5 hours. d. a fixed conversion of a given batch of feed takes 5 hours.
a. five reactor volumes of feed (at specified conditions) are being fed into the reactor per hour.
241
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
c. independent of
242
A gaseous reactant is introduced in a mixed reactor of 3 litres volume at the rate of 1 litre/second. The space time is __________ seconds. a. 1 b. 3 c. 1/3 d. 32
b. 3
243
Fluidized 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.
a. uniformity of temperature
244
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.
a. when the density of the reaction mixture is constant.
245
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
d. 16
246
The conversion for a first order liquid phase reaction. A B in a CSTR is 50%. If another CSTR of the same volume is connected in series, then the % conversion at the exit of the second reactor will be a. 60 b. 75 c. 90 d. 100
b. 75
247
What is the dispersion number for a CSTR?. a. 0 b. 1 c. < 1 d. ∞
d. ∞
248
Rate of a chemical reaction is independent of the concentration of the reactants for a __________ reaction. a. zero order b. third order c. consecutive d. none of these
a. zero order
249
Bulk diffusion in catalyst pore __________ with increase in pressure. a. increases b. decreases c. remains unchanged d. increases exponentially
a. increases
250
A second order reaction of the form A + B → C is called a pseudo-first order reaction, when a. Cao = Cbo b. Cao > Cbo c. Cbo > Cao d. Cbo ≥ Cbo
d. Cbo ≥ Cbo