CRE section 4 Flashcards

(50 cards)

1
Q

not involved in a gas phase catalytic rxn

A

ash resistance

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2
Q

if the time required to change the concentration of reactant to its original value is independent of the initial concentration, the order is

A

one

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3
Q

a batch adiabatic reqctor at an initual temp of 373 is being used for the rxn A -> B. the temp rise after a conversion of 0.5 will be

A

10°C

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4
Q

if CA is the quantity of reactants initially present, the quantity left after n half period will be equal to

A

(1/2)^n.CA

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5
Q

a photochemical rxn is

A

initiated by light

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6
Q

the rate controlling step for the heterogeneous irreversible catalytic rxn is the surface rxn absorbed A with absorbed B to give absorbed C. the rate expression for this rxn can be written as (pic)

A

(pic)

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7
Q

optimum performance of 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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8
Q

a catalyst is said to be a negative catalyst if it

A

retards the rate of rxn

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9
Q

for the non catalytic rxn of particles with surrounding fluid, the same needed to achieve the same fractional conversion for particles of different unchanging sizes is proportional to the particle diameter, when the ___ is the controlling resistance

A

chemical rxn

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10
Q

pure ethanol vapor is fed to a reactor packed with alumina catalyst at the rate of 100kmole / hr. the percent conversion of ethanol in the reactor is

A

100

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11
Q

the conversion for a second order irreversible rxn in batch mode is given by (pic)

A

pic

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12
Q

wrong statement (when the rxn rate)

A

when the rxn rate is independent of temperature, then order rxn is said to be of zero order

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13
Q

a backmix reactor

A

is same as ideal stirred tank reactor

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14
Q

rate of chemicla rxn is not influenced by the

A

number of molecules of reactant taking part in a rxn

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15
Q

wrong statement (residence time)

A

residence time for all the elements of fluid in case of PFR need not be same

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16
Q

the rxn AB is conducted in an adiabatic pfr. if the exit conversion is 20% then the exit temperature is

A

600

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17
Q

which is not a theory of homogeneous rxn

A

none if these

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18
Q

a first order homogeneous rxn of the type XYZ is carried out in a CSTR, which of the following curves respectively show the variation of the conc xyz with time

A

iii, ii, i

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19
Q

in a semi- batch reactor

A

velocity of rxn can be controlled

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20
Q

most important characteristics of gas-liquid reactors are the

A

both a and b

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21
Q

controlling factor in very fast heterogeneous rxn

A

heat and mass transfer effects

22
Q

enzymes are destroyed when the

A

temperature is very high

23
Q

for an autocatalytic reactor, the suitable reactor setup is

A

cstr followed by pfr

24
Q

ionic rxn occur in

25
batch process is preferred over continuous process when the product
both a and b
26
in a chemical rxn (pic) i. rate if formation of P is doubled ii. rate of formation of P is quadrupled iii. doubling the conc of Z order of rxn
third order
27
half life period of a first order rxn is given by
0.693/K
28
half life period of a chemical rxn is
the time required to reduce the conc to half its initial value
29
in the gaseous phase ammonia formation rxn, the value if rquilibrium constant depends on
temperature
30
transition state theory relates the above quantities as
k (infinity) T.e^E/RT
31
photochemical rxn rate does not depend significantly on temperature
energy of reacting molecules exceeds the activation energy by absorption of light
32
A cstr is to designed in which exothermic liquid phase forst order rxn is taking place. reactor has jacket in which coolant is flowing. amount of heat to be removed is
5/3 kW
33
according to law of mass action, rate if rxn is directly proportional to the
molar conc of the reactants
34
in a chemical rxn, ____ conserved
both b and c mass and atoms
35
for an ideal gas mixture undergoing a reversible gaseous phase chemical rxn, the equilibrium constant is
increases with pressure
36
in the reversible rxn of the type A + B <--> AB, in general,
the combination rxn will be exothermic, while the dissociation rxn will be endothermic
37
a batch reactor is
suitable for liquid phase rxns involving small production rate
38
for a first order rxn carried out in a pfr, the space time is
1/K ln Co/C
39
for an isothermal second krder aqueous rxn, the ratio of the tine required for 90% conversion to the time required for 45% conversion is
11
40
a chemical rxn is of zero order, when the rxn rate is
none of these
41
second order consecutive irreversi rxn were carried out in a constant volume isothermal batch reactor with different inital feed compositions. what is the ratio of two rate constant
1/4
42
wrong statement (enzymes)
enzymes help in increasing the activation energy of the rxn
43
there is no correspondence between stoichiometry and the rate equation in case of
non-elementary rxn
44
a spherical porous catalyst particle of radius R is subjected to reactant A which reacts to form B by a zero order surface rxn AB. the effectiveness factor of the catalyst is reported as 7/8. which of the following is true
inner catalyst core of radius R/8 does not participate in rxn
45
which of the following is used for the calcinationif limestone and dolomite
moving bed reactor
46
an imbalanced chemical rxn equation is against the law of
conservation of mass
47
for the chemical rxn PQ found that the rate of rxn doubles as the concentration of P doubled. what is the value of n for the rxn
1
48
characteristics of an ideal plug flow reactor
flat velocity profile
49
velocity of a rxn depends upon the
all abc
50
threshold energy in a rxn is equal to the
sum of a and b activation energy and normal energy