CRE Flashcards

1
Q

Which of the following will give maximum gas conversion?

A

Semi-fluidised bed reactor.

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2
Q

__________ explains the mechanism of catalysis.

A

Activated complex theory

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3
Q

From among the following, choose one which is not an exothermic process.

A

Catalytic cracking

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4
Q

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

A

2

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5
Q

A catalyst

A

lowers the activation energy of reacting molecules.

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6
Q

What is the order of a chemical reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/450-191-1.png , 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

45475

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7
Q

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

A

fluidised bed reactor followed by a fixed

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8
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

16

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9
Q

The single parameter model proposed for describing non-ideal flow is the __________ model.

A

both (a) & (b)

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10
Q

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

A

more when they are connected in series.

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11
Q

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

A

1000

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12
Q

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

A

backmix reactor

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13
Q

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

A

The space velocity of 3 hr-1 means that one third reactor volume of feed at specified conditions are being fed into the reactor.

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14
Q

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

A

high pressure batch reactor.

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15
Q

6 gm 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

0.95

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16
Q

The rate constant of a chemical reaction decreases by decreasing the

A

temperature

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17
Q

Reaction rate equation for the reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/448-153-1.png . If S at is present in large excess, what is the order of this reaction?

A

one

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18
Q

Rate of a gaseous phase reaction is given by, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/460-311-1.png . The unit of rate constant is

A

(atm)-1.(hr)-1

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19
Q

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

A

S-curve

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20
Q

If the catalyst pore size is small in comparison with the mean free path, collisions with the pore wall controls the process’. The diffusivity under this condition is called ‘Knudsen diffusivity’, which is affected by the

A

temperature

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21
Q

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

A

Tubular flow reactor

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22
Q

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

A

exothermic

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23
Q

With decrease in temperature, the equilibrium conversion of a reversible endother-mic reaction

A

decreases

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24
Q

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

A

more energy

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25
Q

For a reaction of the type, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/458-286-1.png , the rate of reaction (- rx) is given by

A

K1CV - K2CX

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26
Q

In a consecutive reaction system https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/446-134-1.png when E1 is much greater than E2, the yield of B increases with the

A

increase of temperature.

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27
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

is at the highest allowable temperature throughout.

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28
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

9210°K

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29
Q

A batch reactor is suitable for

A

liquid phase reactions.

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30
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.

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31
Q

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

A

decrease in activation energy.

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32
Q

A catalyst loses its activity due to

A

all (a), (b) and (c).

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33
Q

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

any

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34
Q

Specific rate constant for a second order reaction

A

both (b) and (c).

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35
Q

For the irreversible elementary reactions in parallel viz https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/455-247-1.png , the rate of disappearance of ‘X’ is equal to

A

CA(K1+K2)

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36
Q

For an isothermal variable volume batch reactor, the following relation is applicable for a first order irreversible reaction.

A

CAo/(1+εAXA)(dXA/dt) = k

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37
Q

For a zero order chemical reaction, the

A

all (a), (b) and (c).

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38
Q

BET apparatus

A

none of these.

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39
Q

Radioactive decay follows __________ order kinetics.

A

first

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40
Q

The excess energy of reactants in a chemical reaction required to dissociate into products is termed as the __________ energy.

A

activation

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41
Q

For a solid catalysed chemical reaction, the effectiveness of solid catalyst depends upon the __________ adsorption.

A

chemical

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42
Q

Pick out the correct statement.

A

A catalyst lowers the activation energy of the reacting molecules.

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43
Q

The dimensions of rate constant for reaction 3A –> B are (l/gm mole)/min. Therefore the reaction order is

A

2

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44
Q

Pick out the correct statement

A

Reactions with high activation energies are very temperature sensitive.

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45
Q

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

2

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46
Q

Sulphuric acid is used as a catalyst in the

A

alkylation of hydrocarbons.

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47
Q

Fractional conversion __________ with increase in pressure for ammonia synthesis reaction i.e., N2 + 3H2 <->2NH3.

A

increases

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48
Q

Pick out the wrong statement.

A

Mixed reactor is always smaller than the plug flow reactor for all positive reaction orders for a particular duty.

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49
Q

The reason why a catalyst increases the rate of reaction is that, it

A

decreases the energy barrier for reaction.

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50
Q

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

conversion in both will be the same but concentrations will be different

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51
Q

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

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52
Q

In an ideal tubular-flow reactor

A

all (a), (b) and (c).

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53
Q

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 Arrhenious law is used. What will be this ratio, if transition state theory is used with the same value of E/R?

A

2.5

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54
Q

__________ is the controlling step in a highly temperature sensitive fluid-solid non-catalytic reaction.

A

Chemical reaction

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55
Q

An autothermal reactor is

A

completely self-supporting in its thermal energy requirements.

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56
Q

The rate constant of a first order reaction depends on the

A

temperature.

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57
Q

A reaction in which one of the products of reaction acts as a catalyst is called a/an __________ reaction.

A

autocatalytic

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58
Q

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

1

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59
Q

Which of the following will favour the reverse reaction in a chemical equilibrium reaction ?

A

Increasing the concentration of one or more of the products.

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60
Q

Conversion increases with increase in temperature in case of a an __________ reaction.

A

reversible endothermic

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61
Q

Effective diffusivity (DE) in a catalyst pellet is related to molecular diffusivity (DN) and Knudsen diffusivity (DK) as

A

1/DE = 1/DN + 1/DK

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62
Q

A photochemical reaction is __________ light.

A

initiated by

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63
Q

Pick out the wrong statement.

A

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

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64
Q

In a/an __________ reactor, there is exchange of heat with the surroundings with sizeable temperature variation.

A

non-adiabatic

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65
Q

Unreacted core model’ represents the reaction involving

A

roasting of sulphide ores.

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66
Q

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).

A

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/475-472-1.png

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67
Q

If a solid-gas non-catalytic reaction occurs at very high temperature, the rate controlling step is the __________ diffusion.

A

film

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68
Q

The units of frequency factor in Arhenious equation

A

are the same as those of the rate constant.

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69
Q

Which of the following is not a chemical step in a fluid solid catalytic reaction ?

A

None of these

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70
Q

For a series of reactions https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/473-457-1.png having k1 &laquo_space;k2, the reaction system can be approximated as

A

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/476-478-1u.png

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71
Q

At a given temperature, K1, K2 and K3 are equilibrium constants for the following reactions 1, 2, 3 respectively.
CH4(g) + H2O(g) CO(g) + 3H2(g),
CO(g) + H2O(g) CO2(g) + H2(g)
CH4(g) + 2H2O(g) CO2(g) + 4H2(g)
Then K1, K2 and K3 are related as:

A

K3 = K1.K2

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72
Q

In case of __________ reactions, the reaction rate does not decrease appreciably as the reaction proceeds.

A

auto catalytic

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73
Q

For nearly isothermal operation involving large reaction time in a liquid-phase reaction, the most suitable reactor is a __________ reactor.

A

stirred tank

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74
Q

What is the Thiele modulus of the solid catalysed first order reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/448-154-1.png , if the pore diffusion offers negligible resistance to reaction ?

A

< 0.5

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75
Q

B.E.T. method can be used to determine the __________ of a porous catalyst.

A

surface area

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76
Q

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/litre to 50 gm moles/litre is same as that required to reduce it from 2 gm moles/litre to 1 gm mole/litre in the same volume. Then the order of this reaction is

A

1

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77
Q

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

A

Time

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78
Q

For reactions in parallel viz A –>P (desired product) and A–>Q (unwanted product), if the order of the desired reaction is higher than that of the undesired reaction, a

A

both (a) and (b).

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79
Q

For a gaseous phase reaction, rate of reaction is equal to K. CA . CB. If the volume of the reactor is suddenly reduced to l/4th of its initial volume, then the rate of reaction compared to the original rate will be __________ times.

A

16

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80
Q

In a reversible chemical reaction having two reactants in equilibrium, if the concentration of the reactants are doubled, then the equilibrium constant will

A

remain the same

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81
Q

The equilibrium constant of a catalytic chemical reaction __________ due to the presence of a catalyst.

A

remains unaffected

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82
Q

The rate constant of a chemical reaction increases by increasing the

A

temperature

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83
Q

The catalytic activity of enzymes is due to their capacity to lower the __________ energy.

A

activation

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84
Q

A first order reaction requires two unequal sized CSTR. Which of the following gives higher yield ?

A

Either of the arrangement (a) or (b) will give the same yield.

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85
Q

Pick out the correct statement.

A

A lower temperature favours the reaction of lower activation energy.

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86
Q

The effect of increasing pressure on the gaseous equilibrium of the reaction 2X+3Y <–>3X+2Y indicates that

A

pressure has no effect.

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87
Q

If in the gaseous phase reaction, N2O4 <–> 2NO2, x is the part of N2O4 which dissociates, then the number of molecules at equilibrium will be

A

(1 + x)

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88
Q

A batch reactor is characterised by

A

variation in extent of reaction and properties of the reaction mixture with time.

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89
Q

When a catalyst increases the rate of forward reaction, the value of rate constant

A

increases

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90
Q

Rate determining step in a reaction consisting of a number of steps in series is the __________ step.

A

slowest

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91
Q

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 form 10 to 100°C.

A

512

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92
Q

A catalyst in a chemical reaction __________ free energy change in the reaction.

A

either (a) or (b); depends on the type of catalyst

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93
Q

Signal normally used to study non-ideal flow by stimulus response technique is __________ input.

A

both (a) & (b)

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94
Q

When all the limiting reactant is consumed in the reaction, the operational yield __________ the relative yield.

A

equals

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95
Q

The half life period of a first order reaction is

A

independent on initial concentration of the reactants.

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96
Q

The catalyst in a second order reversible reaction increases the rate of the forward reaction

A

and backward reaction equally.

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97
Q

Catalyst carriers

A

provide large surface area with a small amount of active material.

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98
Q

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

0.6

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99
Q

A high space velocity means that a given

A

both (a) and (b).

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100
Q

In flow reactors, the performance equations interrelate the rate of reaction to the

A

all (a), (b) and (c).

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101
Q

Space velocity

A

all (a), (b) and (c)

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102
Q

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 CAn, then what is the value of n for this reaction ?

A

1

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103
Q

A reaction which is catalysed by a base is catalysed by all substances which have a tendency to

A

gain a proton

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104
Q

For a homogeneous reaction of nth order, the dimension of the rate constant is given by

A

(concentration)^1 - n/(time)

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105
Q

The fractional volume change between no conversion and complete conversion, for the isothermal gas phase reaction, 2A–>R, is

A

-0.5

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106
Q

The reaction in which one of the products of reaction acts as a catalyst is called a/an __________ reaction.

A

autocatalytic

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107
Q

A typical example of an exothermic reversible reaction conducted at high pressure in industry is

A

dehydration of ethanol.

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108
Q

Study of chemical kinetics is the easiest in the case of __________ reactions.

A

irreversible

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109
Q

In autocatalytic reactions,

A

one of the products acts as a catalyst.

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110
Q

Semibatch reactor is preferred, when a/an

A

all (a), (b), and (c).

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111
Q

Exposure of a photographic plate to produce a latent image is an example of __________ reaction.

A

both (b) and (c)

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112
Q

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

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113
Q

Helium-mercury method is used for the measurement of the __________ of the catalyst.

A

both (b) & (c).

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114
Q

What is the order of a chemical reaction whose rate is deter-mined by the variation of one concentration term only?

A

first

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115
Q

Pick out the wrong statement.

A

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

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116
Q

The rate at which a chemical substance reacts is proportional to its

A

active mass

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117
Q

The exit age distribution of a fluid leaving a vessel (denoted by E) is used to study the extent of non-ideal flow in the vessel. The value of https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/467-387-1.png is

A

1

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118
Q

A plug-flow reactor is characterised by

A

presence of lateral mixing.

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119
Q

Three plug flow reactors (PFR’s) of 4, 5 & 6 m3 volumes are arranged in two branches as shown below in the figure. https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/468-389-1.png If the total feed rate is 300 tons/hr, then for the same conversion in each branch, the feed rate through branch II should be __________ tons/hr.

A

100

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120
Q

For a tubular reactor with space time ‘τ’ and residence time ‘θ’, the following statement holds good.

A

τ = θ , for an isothermic tubular reactor in which the density of the process fluid is constant.

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121
Q

Rate of an autocatalytic chemical reaction is a function of

A

all (a), (b) and (c).

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122
Q

Which of the following curves shows the effect of temperature on the extent of gas-solid adsorption at a given pressure?

A

Adsorption isobar

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123
Q

For an ideal mixed flow reactor (CSTR), the exit age distribution E(t) is given by

A

none of the above

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124
Q

Fluid flow in a real packed bed can be approximated as __________ model.

A

dispersion

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125
Q

For series reaction, the relative yield

A

both (a) and (c) hold good.

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126
Q

The ‘E’ curve for a non-ideal reactor defines the fraction of fluid having age between t and t + dt

A

at the outlet

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127
Q

To maximise the formation of R in the simultaneous reaction
A + B –> R , rR = 2CA^0.5.CB^2
A + B –> S , rS = 1.5 CA . CB
We should have

A

low CA, high CB

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128
Q

A reaction which is catalysed by an acid is also catalysed by any substance, which has a tendency to

A

lose a proton.

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129
Q

A stirred tank reactor compared to tubular-flow reactor provides

A

all (a), (b) and (c)

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130
Q

A chemical reaction, A –>3B, is conducted in a constant pressure vessel. Starting with pure A, the volume of the reaction mixture increases 3 times in 6 minutes. The fractional conversion is

A

1

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131
Q

A catalyst inhibitor

A

all(a), (b) and (c).

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132
Q

In chamber process of sulphuric acid manufacture in industry, the gas phase oxidation of SO2 to SO3 is accomplished by a __________ reaction.

A

catalytic homogenous

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133
Q

If the rate of a chemical reaction becomes slower at a given temperature, then the

A

free energy of activation is higher.

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134
Q

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

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135
Q

The rate of the reaction, X–> Y, quadruples when the concentration of ‘X’ is doubled. The rate expression for the reaction is, r = K Cx^n, the value of ‘n’ in this case will be

A

2

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136
Q

The value of steric factor ‘P’ in the equation k = PZe^E/RT usually ranges from

A

1.0 to 10^-8

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137
Q

For a zero order reaction, the concentration of product increases with the

A

increase of reaction time.

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138
Q

Pick out the wrong statement.

A

A batch reactor can not be used to study the kinetics of catalytic reaction.

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139
Q

Effectiveness factor of a catalyst pellet is a measure of the __________ resistance.

A

pore diffusion

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140
Q

The rate expression for a heterogenous catalytic reaction is given by, - rA = K.KA PA(1 + KA.PA + KR.PR), where K is surface reaction rate constant and KA and KR are absorption equilibrium constants of A and R respectively. If KR PR&raquo_space; (1 + KA PA), the apparent activation energy EA is equal to (given E is the activation energy for the reaction and ΔHR and ΔHA are the activation energies of adsorption of R and A)

A

E + ΔHA - ΔHR)

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141
Q

Given,
3H2 + CO = CH4 + H2O, KP = 101.84 and,
4H2 + CO2 = CH4 + 2H2O, KP = 101.17
the KP for the reaction CO + H2O = CO2 + H2 is

A

10^0.67

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142
Q

Differential method for analysing the kinetic data is used

A

for testing complicated mechanisms.

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143
Q

In case of the irreversible unimolecular type, first order reaction, the fractional conversion at any time for constant volume system as compared to variable volume system is

A

same

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144
Q

The reaction in which the rate equation corresponds to a stoichiometric equation, is called a/an __________ reaction.

A

elementary

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145
Q

A first order gaseous phase reaction is catalysed by a non-porous solid. The kinetic rate constant and the external mass transfer co-efficients are k and kg respectively. The effective rate constant (keff) is given by

A

1/keff = 1/k + 1/kg

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146
Q

Arrhenious equation represents graphically the variation between the __________ and temperature.

A

rate constant

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147
Q

__________ catalytic reaction is involved in the thermal cracking of gas oil.

A

Homogeneous

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148
Q

Variables affecting the rate of homogeneous reactions are

A

pressure, temperature and composition.

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149
Q

A chemical reaction occurs when the energy of the reacting molecules is __________ the activation energy of the reaction.

A

equal to or more than

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150
Q

Which of the following resistances is not involved in a gas phase catalytic (gas-solid) reaction?

A

Ash resistance.

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151
Q

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

one

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152
Q

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 50J/mole.K. The temperature rise after a conversion of 0.5 will be

A

10°C

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153
Q

If CA is the quantity of reactants initially present, the quantity left after ‘n’ half periods will be equal to

A

(1/2)^n.CA

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154
Q

A photochemical reaction is

A

initiated by light.

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155
Q

The rate controlling step for the heterogeneous irreversible catalytic reaction A(g) + B(g)–> C(g) is the surface reaction of absorbed A with absorbed B to give adsorbed C. The rate expression for this reaction can then be written as (where, KA, KB and KC are the equilibrium constants and is the rate constant of the rate controlling step.)

A

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/470-420-4.png

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156
Q

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.

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157
Q

A catalyst is said to be a negative catalyst, ifit

A

retards the rate of reaction.

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158
Q

For the non catalytic reaction of particles with surrounding fluid, the same needed to achive the same fractional conversion for particles of different unchanging sizes is proportional to the particle diameter, when the __________ is the controlling resistance.

A

chemical reaction

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159
Q

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 vapour: 97.5 k mole / hr and diethyl ether :2.5 kmole/hr. The reactions occuring can be represented by:
C2H5OH C2H4 + H2O
2C2H5OH C2H5 - O - C2H5 + H2O
The percent conversion of ethanol in the reactor is

A

100

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160
Q

The conversion for a second order, irreversible reaction (constant volume), https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/475-469-1.png , in batch mode is given by

A

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/475-469-3.png

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161
Q

Pick out the wrong statement.

A

When the reaction rate is independent of temperature, the reaction is said to be of zero order.

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162
Q

A backmix reactor

A

is same as ideal stirred tank reactor.

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163
Q

Rate of a chemical reaction is not influenced by the

A

number of molecules of reactants taking part in a reaction

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164
Q

Pick out the wrong statement:

A

The residence time for all the elements of fluid in case of a P.F.R. need not be same.

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165
Q

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

600

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166
Q

Which of the following is not a theory of homogeneous reaction?

A

None of these

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167
Q

A first order homogeneous reaction of the type X Y Z (consecutive reaction) is carried out in a CSTR. Which of the following curves respectively show the variation of the concentration of X, Y and Z with time? https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/446-129-1.png

A

III, II, I

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168
Q

In a semi-batch reactor,

A

velocity of reaction can be controlled.

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169
Q

Most important characteristics of gas-liquid reactors are the

A

both (a) and (b)

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170
Q

Which of the following is a controlling factor in very fast heterogeneous reaction?

A

Heat and mass transfer effects

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171
Q

Enzymes are destroyed, when the

A

temperature is very high,

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172
Q

For an autocatalytic reactor, the suitable reactor set up is

A

CSTR followed by P.F. reactor.

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173
Q

Ionic reactions occur in

A

solutions

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174
Q

Sometimes, batch process is preferred over continuous process, when the product

A

both (a) & (b).

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175
Q

In a chemical reaction https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/454-240-1.png , it is observed that the
(i) rate of formation of ‘P’ is doubled on doubling the concentration of ‘X’.
(ii) rate of formation of ‘P’ is quadrupled on doubling the concentration of ‘Y’.
(iii) doubling the concentration of ‘Z’ does not affect the rate of formation of ‘P’.
What is the order of the above chemical reaction?

A

Third order

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176
Q

The half life period of a first order reaction is given by (where, K = rate constant. )

A

0.693/K

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177
Q

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.

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178
Q

In the gaseous phase ammonia formation reaction (N2 + 3H2<–>2NH3), the value of the equilibrium constant depends on the

A

temperature.

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179
Q

Transition state theory relates the above quantities as

A

k ∝ T.e^E/RT

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180
Q

Photochemical reaction rate does not depend significantly on temperature, because

A

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

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181
Q

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: CA0= 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 m3/min (ρ and CP are same for the reactant and product streams). The amount of heat to be removed is

A

5/3 kW

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182
Q

According to the ‘law of mass action’, the rate of reaction is directly proportional to the

A

molar concentration of the reactants.

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183
Q

In a chemical reaction, __________ are conserved.

A

both(b) & (c)

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184
Q

For an ideal gas mixture undergoing a reversible gaseous phase chemical reaction, the equilibrium constant

A

increases with pressure.

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185
Q

In the reversible reaction of the type, A + B <–> AB, in general

A

the combination reaction will be exothermic, while the dissociation reaction will be endothermic.

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186
Q

A batch reactor is

A

suitable for liquid phase reactions involving small production rate.

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187
Q

For a first order reaction carried out in a plug flow reactor, the space time is

A

1/K ln Co/C

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188
Q

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

11

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189
Q

A chemical reaction is of zero order, when the reaction rate is (where, CA = concentration of reactant)

A

none of these.

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190
Q

Second order consecutive irreversible reactions https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/473-457-1.png were carried out in a constant volume isothermal batch reactor with different initial feed compositions. Reactor temperature was same in all the cases. In experiments where the ratio of concentration of B to that of A in the initial feed was less than 0.5, the concentration of B increased first, reached a maximum and then declined with time. However, for all experiments where this concentration ratio was 0.5 or above, concentration of B decreased monotonically with time right from the beginning. What is the ratio of the two rate constants (k1/k2)?

A

45295

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191
Q

Pick out the wrong statement.

A

Enzymes help in increasing the activation energy of the reaction.

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192
Q

There is no correspondence between stoichiometry and the rate equation in case of a/an __________ reaction.

A

non-elementary

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193
Q

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.

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194
Q

Which of the following is used for calcination of limestone and dolomite in industrial practice ?

A

Moving bed reactor

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195
Q

An imbalanced chemical reaction equation is against the law of

A

conservation of mass

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196
Q

For the chemical reaction P Q, it is found that the rate of reaction doubles as the concentration of ‘P’ is doubled. If the reaction rate is proportional to Cpn, then what is the value of ‘n’ for this chemical reaction ?

A

1

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197
Q

Which of the following is a characteristic of an ideal plug flow reactor ?

A

Flat velocity profile

198
Q

Velocity of a reaction depends upon the

A

all (a), (b) and (c).

199
Q

Threshold energy in a reaction is equal to the

A

sum of (a) & (b)

200
Q

An isothermal aqueous phase reversible reaction, P <–> R, is to be carried out in a mixed flow reactor. The reaction rate in k.mole/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

1.6

201
Q

Design of heterogeous catalytic reactor involves consideration of __________ steps.

A

both (a) & (b)

202
Q

A consecutive reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/446-133.png , is characterised by

A

maxima in the concentration of B.

203
Q

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

Litre/mole.second

204
Q

For a fluidised bed reactor, the most suitable/relevant model is a __________ model.

A

bubbling bed

205
Q

The rate at which a chemical substance reacts is proportional to its

A

active mass

206
Q

In a reaction, the threshold energy is equal to (where, A = activation energy N = normal energy of reactants)

A

A+N

207
Q

Thermodynamic equilibrium constant in a system is affected by

A

temperature

208
Q

The most suitable reactor for carrying out an auto-thermal reaction is a

A

CSTR

209
Q

Which of the following chemical reactions will be favoured by low pressure ?

A

N2O2 <–> 2NO2

210
Q

A catalyst in a chemical reaction

A

all (a), (b) and (c).

211
Q

Slurry reactors are characterised by the

A

both (a) and (b).

212
Q

Limiting reactant in a chemical reaction decides the

A

conversion

213
Q

Consider the ‘n’ th order irreversible liquid phase reaction A –> B. Which one of the following plots involving half life of the reaction (t1/2) and the initial reactant concentration (CA0) gives a straight line plot ?

A

CA0 Vs ln t1/2

214
Q

The rate of forward reaction, at chemical equilibrium is____the rate of backward reaction.

A

equal to

215
Q

Pick the WRONG design guideline for a reactor in which the reactions, A –>R (desired) and A –> S (undesired) are to take place. The ratio of the reaction rates is https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/478-493-1.png .

A

avoid recycle, when a > b.

216
Q

With increase in temperature, the equilibrium __________ rises in case of endothermic reaction.

A

conversion

217
Q

In case of a consecutive unimolecular type first order reaction https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/449-170-1.png , the concentration of component __________ increases continuously with time.

A

S

218
Q

Enzymes (a protein) are catalysts found in organisms. Its efficiency of catalysing a reaction is due to its capacity to lower the activation energy of the reaction. The enzyme ptyalin used for food digestion is present in

A

saliva

219
Q

Considering the endotheomic dissociation of CaCO3 in a closed vessel (CaCO3 <–>CaO + CO2), the pressure of CO2 increases, if

A

the temperature is increased.

220
Q

The exit age distribution of fluid leaving a vessel is used to know the

A

extent of non-ideal flow in the vessel.

221
Q

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

222
Q

In the converter of the contact process for the manufacture of H2SO4 the equilibrium conversion of SO2 __________ (A) __________ with increase in temperature and __________ (B) __________ with increase in the mole ratio of SO2 to air.

A

(A) decreases (B) increases

223
Q

For the irreversible elementary first order reaction in parallel viz. https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/455-248-1.png , a plot of Cy Vs. Cz will give a straight line having a slope of

A

K1/K2

224
Q

The time needed to achieve the same fractional conversion for particles of different sizes (d) when chemical reaction controls, is proportional to

A

d

225
Q

A balanced chemical reaction equation conforms to the law of

A

conservation of mass

226
Q

An exothermic reaction takes place in an adiabatic reactor. The product temperature __________ reactor feed temperature.

A

is always greater than

227
Q

Reverse reaction in a chemical equilibrium is favoured by the

A

increase in the concentration of oneof the products.

228
Q

The equilibrium constant for the reversible reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/449-174-1.png , is affected by the

A

pressure of the system.

229
Q

Sum of the powers of the concentration terms in the rate equation is called the __________ of the reaction.

A

overall order

230
Q

During manufacture of H2SO4, the oxidation of SO2 to SO3 by oxygen is an en-dothermic reaction. The yield of SO3 will be maximised, if the

A

temperature is reduced and pressure is increased.

231
Q

The role of a catalyst in a chemical reaction is to change the

A

activation energy

232
Q

Molecularity of a reaction

A

both (b) and (c).

233
Q

BET apparatus is used to determine the

A

specific surface of a porous catalyst.

234
Q

Carrier in a catalyst increases its

A

surface area

235
Q

When the reaction is dominated by in-traparticle diffusion, the apparent order of reaction (nD) as measured is related to the true order (n) as

A

nD = (n+1)/2

236
Q

When the reaction occurs in the diffusion controlled region, the apparent activation energy as measured is only __________ the true value.

A

half

237
Q

An isothermal irreversible reaction is being carried out in an ideal tubular flow reactor. The conversion in this case will __________ with decrease in space time.

A

decrease

238
Q

An elementary liquid phase decomposition reaction https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/476-479-1.png is to be carried out in a CSTR. The design equation is

A

kτ = XA/(1 - XA)

239
Q

Kinetics of a solid catalysed reaction can best be studied in a __________ reactor.

A

mixed

240
Q

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

A

k ∝ e^-E/RT

241
Q

The reactions of high molecularity are rare, because

A

of low probability of many body collisions.

242
Q

Which of the following is the most suitable for isothermal operation ?

A

Back-mix reactor

243
Q

For a first order chemical reaction, the rate constant

A

has unit of time-1.

244
Q

Which of the following is an autocatalytic reaction ?

A

Microbial fermentation reaction

245
Q

The performance of a cascade of CSTR’s can be improved by adding

A

more CSTR’s in series.

246
Q

A multiple reaction may be classified as a __________ reaction.

A

all (a), (b) and (c)

247
Q

Holding time for flow reactors is __________ the space time, for constant fluid density

A

equal to

248
Q

Pick out the wrong statement.

A

In general, the rate of a reaction becomes triple for every 10°C rise in temperature.

249
Q

Arhenious equation shows the variation of __________ with temperature.

A

rate constant

250
Q

When a catalyst increases the rate of chemical reaction, the rate constant

A

increases

251
Q

In which of the following reactions, the equilibrium will shift to the right, if the total pressure is increased?

A

N2 + O2 <–> 2NO

252
Q

The catalyst in a first order chemical reaction changes the

A

activation energy

253
Q

Oil is hydrogenated using nickel catalyst in a __________ reactor.

A

slurry

254
Q

The performance equations for constant density systems are identical for

A

P.F.R. and batch reactor.

255
Q

Reaction rate of a first order reaction, which is half completed in 23 minutes will be

A

0.03 min-1

256
Q

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.

257
Q

The half life period ‘t’ of a zero order reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/449-168-1.png , is equal to

A

CA0/2K

258
Q

The point selectivity of the product ‘Y’ in the reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/458-295-1.png is equal to

A

K1/K2

259
Q

In case of calcination of limestone, CaCO3 CaO + CO2, the addition of more of CaO will result in __________ in the concentration of CO2.

A

no change

260
Q

The rate of a homogeneous reaction is a function of

A

all temperature, pressure and composition.

261
Q

In the fluid catalytic cracker (FCC), the cracking reaction is __________ (A) and the regeneration is___(B) __________

A

(A) endothermic (B) exothermic

262
Q

Pick out the correct statement.

A

A catalyst does not change AH of the reaction.

263
Q

Promoter is added to the catalyst to improve its

A

sensitivity

264
Q

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 PFR than in CSTR.

265
Q

When a high liquid hold up is required in a reactor for gas liquid reaction, use __________ coloumn.

A

bubble

266
Q

In an exothermic reaction, the energy of the reacting substances as compared to that of products is

A

more

267
Q

For a tubular flow reactor with uniform concentration and temperature, the independent variable is

A

length

268
Q

Pick out the wrong statement.

A

For a first order consecutive reaction, a tubular flow reactor as compared to a stirred tank reactor provides higher overall selectivity.

269
Q

The first order gas phase reaction https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/475-470-1.png is conducted isothermally in batch mode. The rate of change of conversion with time is given by

A

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/475-470-4.png

270
Q

The extent of a reaction is

A

all of the above.

271
Q

Higher free energy of activation of a chemical reaction (at a given temperature) implies

A

slower rate of reaction.

272
Q

Calcination reaction of limestone (CaCO3 –> CaO + CO2) goes to completion in the rotary kiln, because

A

CO2 escapes continuously.

273
Q

The reactions with low activation energy are

A

fast

274
Q

Molecularity of an elementary reaction, P + Q –> R + S is

A

4

275
Q

Which of the following is not endothermic in nature ?

A

Combustion of sulphur.

276
Q

The rate of an autocatalytic reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/467-388-1.png , is given by -rA = k . CA . CB. In this case, the

A

both ‘b’ & ‘c’

277
Q

The space time is equivalent to the holding time in a steady state mixed reactor for

A

constant fluid density systems.

278
Q

The dispersion number of perfect mixed flow is

A

279
Q

For the reaction https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/454-239-1.png , the rate of formation of Z is 0.2 gm mole/litre.hr. what is the rate of disappearance of X in gm mole/litre. hr ?

A

0.4

280
Q

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 8m3 /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 = 1000kg/m3
Specific heat of reacting mixture = 2kJ/kg.K
The above data can be assumed to be independent of temperature and composition.

A

290

281
Q

For a heterogenous catalytic reaction, A + B –> C, with equimole feed of A and B, the initial rate - rA0 is invariant with total pressure. The rate controlling step is

A

desorption of C.

282
Q

Half life period of a first order irreversible reaction A B is

A

ln 2/k

283
Q

Pick out the wrong statement.

A

Hydrolysis of ester in presence of alkali or acid is a zero order reaction.

284
Q

Which of the following is not a dimension-less group used in catalysis ? (where, D = dispersion co-efficient, cm2 /sec.D1 = diffusion co-efficient; cm2/sec L = length of the reactor, cm t = time, sec, v = volumetric flow rate, cm3/sec . V = volume, cm3.)

A

None of these

285
Q

Pick out the wrong statement

A

The mechanism for the decomposition of CH3CHO into CH4 and CO in presence of I2 is:
CH3CHO +I2 –> CH3I + HI + CO; slow
CH3I + HI –> CH4 + I2; fast
Then the rate of disappearance of CH3CHO is equal to K.CCH3I.CHI and acts as a catalyst.

286
Q

The energy of activation of a chemical reaction

A

is the minimum energy which the molecules must have before the reaction can take place.

287
Q

Chemical kinetics can predict the __________ of a chemical reaction.

A

rate

288
Q

Which of the following fixes the volume of a batch reactor for a particular conversion and production rate?

A

Density of mixture

289
Q

Volume change for unimolecular type first order reaction https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/449-172-1.png , increases __________ with time.

A

exponentially

290
Q

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

24

291
Q

Decomposition rate of a liquid ‘X’ which decomposes as per the reaction https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/456-270-1.png is given by

A

(K1 + K2)CX

292
Q

With increase in the space time of an irreversible isothermal reaction being carried out in a P.F. reactor, the conversion will

A

increase

293
Q

A catalyst promoter

A

improves the activity of a catalyst.

294
Q

In case of a P.F.R., there

A

both (a) and (b).

295
Q

For the non-catalytic reaction of particles with surrounding fluid, the time needed to achieve the same fractional conversion for particles of different but unchanging sizes is proportional to the square of particle diameter, when the __________ is the controlling resistance.

A

diffusion through ash layer

296
Q

If ΔG (free energy change) for a chemical reaction is very large and negative, then the reaction is

A

very much feasible.

297
Q

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.

298
Q

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

insensitive to temperature changes.

299
Q

If Thiele modulus is __________ , then the pore diffusion resistance in a catalyst may be considered as negligible.

A

< 0.5

300
Q

From collison theory, the reaction rate constant is proportional to

A

T^rn.exp(-E/RT)

301
Q

For a mixed flow reactor operating at steady state, the rate of reaction is given by

A

FAo/V . XA

302
Q

Catalytic action in a catalytic chemical reaction follows from the ability of catalyst to change the

A

activation energy

303
Q

In Langmuir treatment of adsorption,

A

whole surface of the catalyst is essentially uniform and the adsorbed molecule has no effect on the rate of adsorption per site.

304
Q

Organic catalysts differ from the inorganic catalyst in the sense that the former is

A

proteinous in nature.

305
Q

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.

306
Q

Pick out the wrong statement.

A

A catalyst increases the potential energy barrier over which the reactants must pass to form products.

307
Q

An endothermic second order reaction is carried out in an adiabatic plug flow reactor. The rate of heat generation is

A

maximum at the inlet of the reactor.

308
Q

Equilibrium of a chemical reaction as viewed by kinetics is a __________ state.

A

dynamic steady

309
Q

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

310
Q

The size of plug flow reactor (PFR) for all positive reaction orders and for any given duty, is __________ that of mixed reactor.

A

smaller than

311
Q

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.

312
Q

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

3

313
Q

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.

314
Q

In a continuous flow stirred tank reactor, the composition of the exit stream

A

is same as that in the reactor.

315
Q

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

no change

316
Q

The energy balance equation over a tubular reactor under transient conditions is

A

a linear partial differential equation.

317
Q

Which of the following factors control the deactivation of a porous catalyst pellet ?

A

All (a), (b) and (c).

318
Q

For the reaction, A + B –>2B + C,

A

rA = -rB

319
Q

Transition state theory gives the rate constant as

A

K α T . e^-E/RT

320
Q

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

PFR followed by a CSTR

321
Q

Pick out the wrong statement.

A

Activation energy for a reaction is obtained from the intercept of the Ar-rhenious plot.

322
Q

In a reversible reaction, a catalyst increases the rate of forward reaction

A

and the backward reaction equally.

323
Q

Maximum equilibrium conversion for endothermic reaction is obtained at the __________ temperature.

A

highest possible

324
Q

When an exothermic reversible reaction is conducted adiabatically, the rate of reaction

A

continuously decreases.

325
Q

For a first order chemical reaction in a porous catalyst, the Thiele modulus is 10. The effectiveness factor is approximately equal to

A

0.1

326
Q

The rate equation for the reaction represented by https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/455-245-1.png , is given by - rx = K1 . Cx/(1 + K2 Cx). At high value of Cx (i.e.., K2Cx > > 1), the order of the reaction and the rate constant are respectively

A

zero order & K1/K2

327
Q

In solid catalysed reactions the diffusional effects are more likely to affect the overall rate of reaction for

A

fast reaction in catalyst of large pore diameter.

328
Q

Helium-mercury method can be used to determine the __________ of the catalyst particle.

A

all (a), (b), & (c).

329
Q

For the chemical reaction X –> Y, it is observed that, on doubling the concentration of ‘X’, the reaction rate quadruples. If the reaction rate is proportional to Cxn, then what is the value of ‘n’ ?

A

4

330
Q

Chemical reaction rate of a component depends upon the

A

all (a), (b) and (c).

331
Q

In a semi-batch reactor

A

velocity of reaction can be controlled.

332
Q

A trickle bed reactor is the one, which

A

employs all the three phases (i.e.. .solid, liquid and gas).

333
Q

The excess energy of the reactants required to dissociate into products is known as the __________ energy.

A

activation

334
Q

In a/an __________ vessel, the fluid enters and leaves following plug flow.

A

closed

335
Q

Shift conversion reaction

A

converts CO to CO2 with steam.

336
Q

The importance of diffusion in a catalyst are increased by

A

all (a), (b) and (c).

337
Q

A back mix reactor is

A

same as ideal stirred tank reactor.

338
Q

Which one is the rate controlling step in a solid-gas non-catalytic reaction occurring at very high temperature?

A

Film diffusion

339
Q

The rate of the heterogenous catalytic reaction A(g) + B(g) –>C(g) is given by -rA = k.KA.pA.PB/(1 + KA.PA + Kc.pc), where KA and Kc are the adsorption equilibrium constants. The rate controlling step for this reaction is

A

surface reaction between absorbed A and B in the gas phase.

340
Q

For a __________ order chemical reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/449-168-1.png , the half life period is independent of the initial concentration of the reactant A.

A

first

341
Q

The ratio of moles of a reactant converted into the desired product to that converted into unwanted product is called

A

selectivity

342
Q

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

1/m

343
Q

For multiple reactions, the flow pattern within the vessel affects the

A

both (a) and (b)

344
Q

The rate expression for the gaseous phase reaction, CO + 2H2 –> CH3OH, is given by, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/477-488-1.png . Which of the following is not possible ?

A

α = 1, β = 1, γ =1

345
Q

For the same residence time, which one will give the maximum conversion ?

A

Single tubular flow reactor (v = 5 litres).

346
Q

__________ gas is normally employed in B.E.T.method of finding out the surface area of catalyst.

A

N2

347
Q

The exit age distribution curve E(t) for an ideal CSTR with the average residence time, τ, is given by

A

[(e^-t/τ)/T]

348
Q

The rate constant of a reaction depends on the

A

temperature of the system.

349
Q

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

0.338

350
Q

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

PFR of volume V

351
Q

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

4

352
Q

For a __________ order reaction, the units of rate constant and rate of reaction are the same.

A

zero

353
Q

In case of staged packed bed reactors carrying out exothermic reaction, use

A

all (a), (b) and (c).

354
Q

Vegetable oils are hydrogenated in a __________ reactor.

A

slurry

355
Q

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

45294

356
Q

The rate of reaction does not decrease appreciably as the reaction proceeds in case of __________ reactions.

A

autocatalytic

357
Q

For all positive reaction orders for a particular duty,

A

mixed reactor is always larger than the plug-flow reactor.

358
Q

The heat of reaction

A

is independent of the mechanism of reaction.

359
Q

Which of the following does not produce a change in the value of rate constant of a reaction ?

A

Concentration and catalyst

360
Q

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

A

decreases

361
Q

In a CSTR __________ varies with time.

A

neither (a) nor (b)

362
Q

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

45325

363
Q

As the chemical reaction proceeds, the rate of reaction

A

decreases.

364
Q

Pick out the wrong statement.

A

A catalyst initiates a reaction.

365
Q

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

same as

366
Q

Photo-chemical reactions occur in presence of

A

sunlight.

367
Q

n’ number of plug flow reactors (P.F.R) in series with a total volume ‘V’ gives the same conversion as one P.F.R. of volume

A

V

368
Q

Knudsen diffusion is directly proportional to

A

sqrt(T)

369
Q

Fractional conversion __________ for an exothermic reversible chemical reaction, when the temperature is maximum.

A

decreases

370
Q

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

A

both (a) and (b)

371
Q

A pulse tracer is introduced in an ideal CSTR (with a mean residence time ι) at time, t = 0. The time taken for the exit concentration of the tracer to reach half of its initial value will be

A

372
Q

On application of pressure to the equilibrium system, ice <–> water ; which of the following phenomenon will occur ?

A

More water will be formed.

373
Q

Participation of __________ is involved in the occurrence of a chemical reaction.

A

electrons

374
Q

Promoter.

A

increases the number of active centres by increasing the unevenness of catalyst surface and by creating discontinuities in the crystals.

375
Q

The rate constant of a reaction is a function of the

A

temperature of the system.

376
Q

Mean residence time is equal to the space time, when

A

all (a), (b) and (c).

377
Q

If ‘n’ is the order of reaction, then unit of rate constant is

A

1/(time)(concentration)^n - 1

378
Q

Batch process is preferred over continuous process, when the

A

all (a), (b) & (c)

379
Q

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

3

380
Q

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

381
Q

For any reaction, we may write conversion as a function of

A

all (a), (b) & (c)

382
Q

The use of space time is preferred over the mean residence time in the design of a/an

A

ideal tubular-flow reactor

383
Q

Autocatalytic reactions are best carried out in a

A

recycle reactor

384
Q

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

45420

385
Q

A batch reactor suffers from following disadvantage.

A

All (a), (b)and(c).

386
Q

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.

387
Q

A second order liquid phase reaction, A –>B, is carried out in a mixed flow reactor operated in semi batch mode (no exit stream). The reactant A at concentration CAF is fed to the reactor at a volumetric flow rate of F. The volume of the reacting mixture is V and the density of the liquid mixture is constant. The mass balance for A is

A

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/479-499-4.png

388
Q

Half life period of a chemical reaction is proportional to CA0-1 , if the reaction is of __________ order.

A

second

389
Q

The irreversible reaction, X –> Y, is the special case of the reversible reaction, X <–>Y, in which the

A

all (a), (b) and (c).

390
Q

The equilibrium constant K of a chemical reaction depends on

A

temperature only.

391
Q

The reaction rate almost gets doubled for 10°C rise in temperature. This is due to the fact that the

A

fraction of molecules having threshold energy increases.

392
Q

Which of the following is not a unit of reaction rate ?

A

None of these

393
Q

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

There is no dynamic equilibrium between successive layer.

394
Q

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

395
Q

The following half life data are available for the irreversible liquid phase reaction A products.
https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/470-419-1.png The overall order of reaction is

A

1.5

396
Q

A non-catalytic chemical reaction of the type https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/457-279-1.png is called a __________ reaction.

A

series-parallel

397
Q

The unit of frequency factor in Arhenious equation is

A

same as that of rate constant.

398
Q

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

399
Q

Reaction of benzene with chlorine gas to produce tri-chlorobenzene exemplifies a/an __________ reaction.

A

consecutive

400
Q

For the gaseous reaction 2A –> B, where the feed consists of 50 mole % A and 50 mole % inerts, the expansion factor is

A

-0.25

401
Q

The molecularity and the order of reaction respectively, for the hydrolysis of methyl acetate in presence of acids are

A

2 & 1

402
Q

The irreversible reaction is a special case of reversible reaction, if the

A

reactant concentration at equilibrium condition is zero.

403
Q

A pollutant P degrades according to first order kinetics. An aqueous stream containing P at 2 kmole/m3 and volumetric flow rate 1m3 /h requires a mixed flow reactor of volume V to bring down the pollutant level to 0.5 kmole/m3 . The inlet concentration of the pollutant is now doubled and the volumetric flow rate is tripled. If the pollutant level is to be brought down to the same level of 0.5 kmole/m3 , the volume of the mixed flow reactor should be increased by a factor of

A

7

404
Q

For the liquid phase parallel reactions:
R, rR = K1.CA2; E1 = 80 KJ/mole
S, rs= K1.CA ; E2 = 120 KJ/mole
The desired product is R. A higher selectivity of R will be achieved, if the reaction is conducted at

A

high temperature in a PFR.

405
Q

In an ideal mixed reactor (at steady state), the

A

all (a), (b) and (c).

406
Q

The knowledge of initial concentration and rate constant is necessary to determine the half life time of a reaction of __________ order.

A

second

407
Q

Which of the following factors control the design of a fluid-solid reactor ?

A

All (a), (b) and (c).

408
Q

A Catalyst

A

shortens the time to reach the equilibrium.

409
Q

The reaction rate constants at two different temperature T1 and T2 are related by

A

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/470-421-2.png

410
Q

The synthesis of proteins and metabolism in biological objects occur in the presence of biocatalyst called

A

fungi

411
Q

Pick out the wrong statement.

A

The intercept of the Arrhenious plot is called the ‘activation energy’.

412
Q

Kinetics of a catalytic reaction can be best studied on a/an __________ reactor.

A

either (a), (b) and (c).

413
Q

In case of a __________ reactor, the composition in the reactor and at the exit of the reactor is the same.

A

back-mix

414
Q

Exothermic reactions are best carried out in

A

CSTR followed by a plug flow reactor.

415
Q

What is the order of chemical reaction https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/449-166-1.png , 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

2

416
Q

Reactions with high activation energy are

A

very temperature sensitive

417
Q

If n = overall order of a chemical reaction. a = initial concentration of reactant. t = time required to complete a definite fraction of the reaction. Then pick out the correct relationship.

A

t ∝ 1/a^n-1

418
Q

In case of a/an __________ chemical reaction, conversion increases with the rise in temperature.

A

reversible endothermic

419
Q

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.

420
Q

With increase in initial concentration, the fractional conversion of a first order reaction in a given time

A

remains constant

421
Q

The rate of reaction of a/an __________ reaction is not affected by temperature rise.

A

photochemical

422
Q

With an increase in pressure in gaseous phase chemical reactions, the fractional conversion __________ when the number of moles decreases.

A

increases

423
Q

Half-life period for a first order reaction is __________ the initial concentration of the reactant.

A

independent of

424
Q

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

A

deposited

425
Q

The order of the chemical reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/448-163-1.png , whose rate equation is given as -rA= KCA2. CB is

A

3

426
Q

The decomposition of A into B is represented by the exothermic reaction, A <–> 2B. To achieve maximum decomposition, it is desirable to carry out the reaction.

A

at low P and low T.

427
Q

The catalytic converter for conversion of SO2 to SO3 by contact process should have a feed with SO2 content between

A

7-10%

428
Q

If the pore diffusion controls in a catalytic reaction, the apparent activation energy Ea is equal to

A

ED/2

429
Q

With increase in K2/K1 in case of a unimolecular type elementary reactions https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/449-170-1.png , the fractional yield of ‘R’ in mixed reactor (for a given conversion of ‘A’)

A

decreases

430
Q

Collision theory gives the rate constant for bimolecular reaction as

A

K α e^-E/RT

431
Q

Find a mechanism that is consistent with the rate equation and reaction given below:
2A + B –> A2B, ( - rA) = k.CA.CB

A

A + A <–> AA;AA + B –> A2B

432
Q

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

3

433
Q

The temperature dependence of reaction rate constant (K) by Arhenius law is given by

A

K α e^-E/RT

434
Q

For a __________ order chemical reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/449-169-1.png , the fractional conversion of reactant ‘A’ is proportional to time.

A

zero

435
Q

Velocity of a chemical reaction

A

none of these.

436
Q

Backmixing is most predominant in

A

a single CSTR.

437
Q

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

438
Q

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

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/478-497-2.png

439
Q

Fluidised bed reactor is characterised by

A

uniformity of temperature.

440
Q

In which of the following gaseous phase reversible reactions, the product yield can not be increased by the application of high pressure ?

A

N2 + O2 <–> 2NO

441
Q

Space time equals the mean residence time

A

when the density of the reaction mixture is constant.

442
Q

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

16

443
Q

Rate constant ‘k’ and absolute temperature ‘T’ are related by collision theory (for bimolecular) as

A

k ∝ sqrt(T)

444
Q

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

75

445
Q

What is the dispersion number for a CSTR?

A

446
Q

Rate of a chemical reaction is independent of the concentration of the reactants for a __________ reaction.

A

zero order

447
Q

With increase in temperature, the rate constant obeying Arhenious equation

A

increases.

448
Q

Bulk diffusion in catalyst pore __________ with increase in pressure.

A

decreases

449
Q

Pick out the correct statement.

A

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

450
Q

The concentration of A in a first order reaction, A –> B, decreases

A

exponentially with time.

451
Q

The equilibrium constant of chemical reaction __________ in the presence of catalyst.

A

remains unaffected

452
Q

The order of a chemical reaction is

A

an experimentally determined quantity.

453
Q

A chemical reaction occurs, when the energy of the reacting molecules is __________ the activation energy of reaction.

A

equal to or more than

454
Q

In the hydrodealkylation of toluene to benzene, the following reactions occur:
C7H8 + H2 –> C6H6 + CH4
2C6H6 <–> C12H10 + H2
Toluene 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

A

0.144

455
Q

Catalyst is a substance, which __________ chemical reaction.

A

can either increase or decrease the speed of a

456
Q

The residence time distribution of an ideal CSTR is

A

exp (-t/τ)

457
Q

A rise in temperature

A

all (a), (b) and (c).

458
Q

The enzyme which can catalyse the conversion of glucose to ethyl alcohol is

A

zymase

459
Q

For reaction, P + 2 –>3R, molar rate of consumption of P is

A

half of that of Q.

460
Q

If pore diffusion is the controlling step in a solid catalysed reaction, the catalyst

A

porosity is of less importance.

461
Q

The conversion of a reactant, undergoing a first order reaction, at a time equal to three times the half life of the reaction is

A

0.875

462
Q

In case of unimolecular type elementary reaction, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/449-176-1.png , plug flow reactor as compared to mixed reactor is

A

more

463
Q

What is the value of ‘n’ if the reaction rate of the chemical reaction A –> B, is proportional to CAn and it is found that the reaction rate triples, when the concentration of ‘A’ is increased 9 times ?

A

45293

464
Q

The first order series reaction https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/473-457-1.png is conducted in a batch reactor. The initial concentrations of A, B and C (CA0, CB0, CC0 respectively) are all non-zero. The variation of CB with reaction time will not show a maximum, if

A

k2 CB0 > k1 CA0

465
Q

A second order reaction of the form A + B –> C is called a pseudo-first order reaction, when

A

CB0 ≥ CB0

466
Q

Pick out the wrong statement.

A

According to the penetration theory, the mass transfer co-efficient decreases, if the exposure time of an eddy to the solute decreases.

467
Q

Effectiveness factor (E) of a catalyst pellet is defined as https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/458-294-1.png , Effectiveness factor for a first order reaction is given by (where, T = Thiele modulus)

A

tan hT/T

468
Q

Inversion of cane sugar is an example of

A

bimolecular reaction with first order.

469
Q

Pick out the correct statement.

A

Pressure changes do not change the equilibrium concentrations.

470
Q

In which of the following gaseous phase reactions, the equilibrium of the reaction remains unaffacted by pressure changes ?

A

N2 + O2 <–> 2NO

471
Q

The mean conversion in the exit stream, for a second order, liquid phase reaction in a non-ideal flow reactor is given by

A

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/475-471-1.png

472
Q

Integral method for analysing the kinetic data is used

A

both (a) and (b).

473
Q

Concentration of the limiting reactant (with initial concentration of a moles/litre) after time t is (a-x). Then ‘t’ for a first order reaction is given by

A

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/437-12-1.png

474
Q

The rate of a gas phase reaction is given by K . CA . CB. If the volume of the reaction vessel is reduced to l/4th of its initial volume, then the reaction rate compared to the original rate will be __________ times.

A

16

475
Q

Rate of a chemical reaction is not affected by the

A

number of molecules of reactants taking part in the reaction.

476
Q

Overall rate of reaction in a heterogenous catalytic reaction depends upon the mass and energy transfer from the fluid to solid surface and its rate of reaction is usually __________ the concentration of catalyst, if it does not entail a chain mechanism.

A

proportional to

477
Q

__________ resistance is not involved in the combustion of a carbon particle.

A

Ash

478
Q

In an ideal P.F.R. at steady state conditions

A

the conversion of the reactant varies from point to point along a flow path.

479
Q

B.E.T. method of finding out surface area of a catalyst, uses the extension of __________ isotherm.

A

Langmuir

480
Q

In a chemical reaction, repesented by, https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/454-241-1.png , it is observed that the
(i) rate of reaction increases by a factor of 4 on doubling the concentration of the reactant.
(ii) rate of reaction increases by a factor of 9 on trebling the concentration of the reactant.
Then the rate of the reaction is proportional to(where, CA = contentration of the reactant)

A

CA^2

481
Q

Which of the following holds good for an elementary reaction,https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/455-249-1.png ?

A

Three times the rate of disappearance of ‘X’ is equal to the rate of appearance of ‘Z’.

482
Q

An example of autothermal reactor operation is

A

ethylene oxidation

483
Q

For a packed bed reactor; the presence of a long tail in the residence time distribution curve is an indication of

A

dead zone

484
Q

Space time in flow reactor is

A

both (a) and (b).

485
Q

For a first order isothermal chemical reaction in a porous catalyst, the effectiveness factor is 0.3. The effectiveness factor will increase if the

A

catalyst size is reduced or the catalyst diffusivity is increased.

486
Q

Cold shot cooling is only practical when the feed temperature is __________ than the reaction temperature.

A

much lower

487
Q

The following gas phase reaction is taking place in a plug flow reactor. https:/ /www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/478-498-1.png

A stoichiometric mixture of A and B at 300 K is fed to the reactor. At 1 m along the length of the reactor, the temperature is 360 K. The pressure drop is negligible and an ideal gas behaviour can be assumed. Identify the correct expression relating the concentration of A at the inlet (CA0), concentration of A at 1m (CA) and the corresponding conversion of A (X).

A

https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/479-498-3.png

488
Q

The preferred reacting system for oxidation of o-xylene to phthalic anhydride is

A

jacketted liquid phase CSTR.

489
Q

The effectiveness factor for large value of Thiele modulus (L.sqrt(K/D1)) of a solid catalysed first order reaction is equal to (where, L = length of the reactor, cm, D1 = diffusion co-efficient, cm2/second)

A

1/L(sqrt(K/D1))

490
Q

A first order reaction A B occurs in an isothermal porous catalyst pellet of spherical shape. If the concentration of A at the centre of the pellet is much less than at the external surface, the process is limited by

A

diffusion within the pellet.

491
Q

Following isothermal kinetic data are obtained in a basket type of mixed flow reactor for a porous catalyst. Determine the role of pore diffusion and external mass transfer processes. https://www.indiabix.com/_files/images/chemical-engineering/chemical-reaction-engineering/477-486-1.png

A

Strong pore diffusion control and mass transfer not controlling.