Option A: Batch
Option B: Slurry
Option C: Fluidised bed
Option D: Fixed bed
Correct Answer: Slurry ✔
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Option A: Biochemical
Option B: Photochemical
Option C: Catalytic
Option D: Autocatalytic
Correct Answer: Autocatalytic ✔
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Option A: Combustion of sulphur
Option B: Gasification of carbon
Option C: Thermal cracking of fuel oil
Option D: Steam reforming of naphtha
Correct Answer: Combustion of sulphur ✔
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Option A: For testing complicated mechanisms
Option B: When the data are scattered
Option C: When rate expressions are very simple
Option D: None of these
Correct Answer: For testing complicated mechanisms ✔
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Option A: Time
Option B: Length
Option C: Diameter
Option D: None of these
Correct Answer: Length ✔
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Option A: Non-catalytic homogeneous
Option B: Non-catalytic heterogeneous
Option C: Catalytic homogenous
Option D: Catalytic heterogeneous
Correct Answer: Catalytic homogenous ✔
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Option A: Equilibrium constant
Option B: Activation energy
Option C: Heat of formation of the product
Option D: Heat of reaction
Correct Answer: Activation energy ✔
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Option A: η and θ are always equal
Option B: η = θ, when the fluid density changes in the reactor
Option C: η = θ, for an isothermic tubular reactor in which the density of the process fluid is constant
Option D: η = θ, for a non-isothermal reactor
Correct Answer: η = θ, for an isothermic tubular reactor in which the density of the process fluid is constant ✔
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Option A: Batch
Option B: Plug-flow
Option C: Mixed
Option D: None of these
Correct Answer: Mixed ✔
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Option A: 1/(time)(concentration)n – 1
Option B: (Time)-1 (concentration)n – 1
Option C: (Time)n – 1 (concentration)
Option D: None of these
Correct Answer: A. 1/(time)(concentration)n – 1 ✔
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Option A: Normally tends to increase the reaction rate
Option B: Does not affect a catalysed reaction
Option C: Does not affect photo-chemical reaction rates
Option D: All A., B. and C.
Correct Answer: D. All A., B. and C. ✔
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Option A: Specific surface of a porous catalyst
Option B: Pore size distribution
Option C: Pore diameter
Option D: Porosity of the catalyst bed
Correct Answer: Specific surface of a porous catalyst ✔
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Option A: Pore diffusion
Option B: Gas film
Option C: Chemical reaction
Option D: None of these
Correct Answer: Pore diffusion ✔
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Option A: (i) exothermic (ii) endothermic
Option B: (i) exothermic (ii) exothermic
Option C: (i) endothermic (ii) endothermic
Option D: (i) endothermic (ii) exothermic
Correct Answer: (i) endothermic (ii) exothermic ✔
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Option A: 0.33
Option B: 0.5
Option C: 1
Option D: Data insufficient, can’t be predicted
Correct Answer: 1 ✔
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Option A: H2 + Cl2 ⇌ 2HCl
Option B: N2 + O2 ⇌ 2NO
Option C: N2O4 ⇌ 2 NO2
Option D: H2 + I2 ⇌ 2HI
Correct Answer: N2 + O2 ⇌ 2NO ✔
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Option A: High capacity
Option B: Presence of axial mixing
Option C: Presence of lateral mixing
Option D: Constant composition and temperature of reaction mixture
Correct Answer: Presence of lateral mixing ✔
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Option A: Reaction rate
Option B: Concentration
Option C: Both A. & B.
Option D: Neither A. nor B.
Correct Answer: D. Neither A. nor B. ✔
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Option A: Invertase
Option B: Maltase
Option C: Diastase
Option D: Zymase
Correct Answer: Zymase ✔
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Option A: Initial concentration of reactants
Option B: Time of reaction
Option C: Temperature of the system
Option D: Extent of reaction
Correct Answer: Temperature of the system ✔
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Option A: Non-isothermal gas reaction
Option B: Variable fluid density systems
Option C: Constant fluid density systems
Option D: Gas reactions with changing number of moles
Correct Answer: Constant fluid density systems ✔
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Option A: Increase of reaction time
Option B: Increase in initial concentration
Option C: Total pressure
Option D: Decrease in total pressure
Correct Answer: Increase of reaction time ✔
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Option A: Jacketed liquid phase CSTR
Option B: Jacketed steam heated multitubular reactor
Option C: Multitubular reactor with cooling
Option D: Multistage multitubular reactor with interstage cooling
Correct Answer: Jacketed liquid phase CSTR ✔
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Option A: 2/3
Option B: 5/8
Option C: 1/3
Option D: 3/8
Correct Answer: 5/8 ✔
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Option A: Temperature should be high in the beginning and decreased towards the end of the reaction
Option B: Very low temperature should be used throughout the reaction
Option C: Very high temperature should be used throughout the reaction
Option D: None of these
Correct Answer: Temperature should be high in the beginning and decreased towards the end of the reaction ✔
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Option A: Zero
Option B: First
Option C: Second
Option D: Third
Correct Answer: First ✔
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Option A: Decreases
Option B: Increases
Option C: Remain constant
Option D: Become infinite
Correct Answer: Increases ✔
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Option A: Lose a proton
Option B: Gain a proton
Option C: Gain an electron
Option D: None of these
Correct Answer: Gain a proton ✔
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Option A: Not feasible
Option B: Just feasible
Option C: Very much feasible
Option D: Unpredictable as ΔG is no measure of feasibility of a reaction
Correct Answer: Very much feasible ✔
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Option A: Homogeneous
Option B: Non-Homogeneous
Option C: Heterogeneous
Option D: Non-Heterogeneous
Correct Answer: Homogeneous ✔
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Option A: (1/η) exp (-t/η)
Option B: η exp (-t/η)
Option C: exp (-t/η)
Option D: (1/η) (-t/η)
Correct Answer: exp (-t/η) ✔
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Option A: Moles for med/(surface of catalyst) (time)
Option B: Moles formed/volume of reactor) (time)
Option C: Mole formed/volume of catalyst) (time)
Option D: None of these
Correct Answer: None of these ✔
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Option A: Zero order
Option B: Third order
Option C: Consecutive
Option D: None of these
Correct Answer: Zero order ✔
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Option A: Poor product quality control
Option B: High labour and handling cost
Option C: High shutdown time requirement for emptying, cleaning and refilling
Option D: All A., B. and C.
Correct Answer: D. All A., B. and C. ✔
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Option A: Lessens its selectivity
Option B: May be useful for suppressing undesirable side reactions
Option C: Is added in small quantity during the catalyst manufacture itself
Option D: All A., B. and C.
Correct Answer: D. All A., B. and C. ✔
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Option A: CaO is not dissociated
Option B: CO2 escapes continuously
Option C: Of high calcination temperature
Option D: CaO is more stable than CaCO3
Correct Answer: CO2 escapes continuously ✔
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Option A: Langmuir adsorption isotherm
Option B: Adsorption isobar
Option C: Freundlich adsorption isotherm
Option D: None of these
Correct Answer: Adsorption isobar ✔
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Option A: Porosity
Option B: Sensitivity
Option C: Surface area
Option D: None of these
Correct Answer: Sensitivity ✔
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Option A: Constant residence time
Option B: Variation in extent of reaction and properties of the reaction mixture with time
Option C: Variation in reactor volume
Option D: Very low conversion
Correct Answer: Variation in extent of reaction and properties of the reaction mixture with time ✔
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Option A: k. t = ln a/(a – x)
Option B: k. t = x/a (a – x)
Option C: k. t = ln (a – x)/a
Option D: k. t = ln a (a – x)/x
Correct Answer: A. k. t = ln a/(a – x) ✔
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Option A: CA0 = CB0
Option B: CA0 > CB0
Option C: CB0 > CA0
Option D: CB0 ≥ CB0
Correct Answer: CB0 ≥ CB0 ✔
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Option A: 1/2
Option B: 1/3
Option C: 1/4
Option D: 1/5
Correct Answer: 1/3 ✔
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Option A: Less than
Option B: Equal to
Option C: More than
Option D: Equal to or more than
Correct Answer: Equal to ✔
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Option A: Film diffusion
Option B: Diffusion through ash layer
Option C: Chemical reaction
Option D: Either A., B. or C.
Correct Answer: Diffusion through ash layer ✔
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Option A: keff = k + kg
Option B: keff = (k+ kg)/2
Option C: keff = (kkg)1/2
Option D: 1/keff = 1/k + 1/kg
Correct Answer: 1/keff = 1/k + 1/kg ✔
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Option A: K1 . CX
Option B: (K1 + K2 + K3) CX
Option C: (K1 + K2) CX
Option D: (K2 + K3) CX
Correct Answer: (K1 + K2) CX ✔
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Option A: 15, 10, 5
Option B: 5, 10, 15
Option C: 10, 5, 15
Option D: 10, 15, 5
Correct Answer: 15, 10, 5 ✔
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Option A: 103.01
Option B: 10-0.67
Option C: 10-3.01
Option D: 100.67
Correct Answer: 100.67 ✔
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Option A: Reactor dispersion number (D/vL)
Option B: Reduced time (vt/V)
Option C: Thiele modulus L √(k/D1)
Option D: None of these
Correct Answer: None of these ✔
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Option A: XA Vs . η
Option B: XA Vs ln η
Option C: XA/(1 – XA)Vs η
Option D: XA(1 – XA)Vs η
Correct Answer: XA Vs . η ✔
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Option A: 0.4
Option B: 0.1
Option C: 0.2
Option D: None of these
Correct Answer: 0.4 ✔
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Option A: At the inlet
Option B: At the outlet
Option C: In the reactor
Option D: Averaged over the inlet and outlet
Correct Answer: At the outlet ✔
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Option A: tan hT/T
Option B: tan T/T
Option C: tan hT/tan T
Option D: None of these
Correct Answer: tan hT/T ✔
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Option A: Sunlight
Option B: Darkness
Option C: Solid catalysts
Option D: Monochromatic radiation only
Correct Answer: Sunlight ✔
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Option A: 0.875
Option B: 0.5
Option C: 0.425
Option D: Data insufficient to calculate
Correct Answer: 0.875 ✔
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Option A: Depends on the pressure only
Option B: Depends on the mechanism of reaction only
Option C: Depends on both pressure and mechanism of reaction
Option D: Is independent of the mechanism of reaction
Correct Answer: Is independent of the mechanism of reaction ✔
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Option A: Describes the extensive operating characteristics of a tubular flow reactor
Option B: Is the maximum feed rate per unit volume of reactor for a given conversion
Option C: Is a measure of the ease of the reaction
Option D: All A., B. and C.
Correct Answer: D. All A., B. and C. ✔
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Option A: Less than
Option B: Equal to
Option C: More than
Option D: Equal to or more than
Correct Answer: Equal to ✔
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Option A: Zero
Option B: First
Option C: Second
Option D: Fractional
Correct Answer: Zero ✔
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Option A: Single stirred tank (v = 5 litres)
Option B: Two stirred tank (each of 2.5 litres) in series
Option C: Stirred tank followed by tubular flow reactor (each of 2.5 litres)
Option D: Single tubular flow reactor (v = 5 litres)
Correct Answer: Single tubular flow reactor (v = 5 litres) ✔
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Option A: L √(K/D1)
Option B: 1/[L√(K/D1)]
Option C: 1
Option D: ∞
Correct Answer: 1/[L√(K/D1)] ✔
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Option A: Combustion of coal particles
Option B: Roasting of sulphide ores
Option C: Manufacture of carbon disulphide from elements
Option D: None of these
Correct Answer: Roasting of sulphide ores ✔
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Option A: 1.0 to 10-8
Option B: 1.1 to 102
Option C: 0.1 to 0.9
Option D: None of these
Correct Answer: 1.0 to 10-8 ✔
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Option A: k/2
Option B: ln k/2
Option C: ln 2/k
Option D: ln 0.5/k
Correct Answer: ln 2/k ✔
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Option A: More uniform operating conditions
Option B: Permits operation at the optimum temperature for a long reaction time
Option C: Higher overall selectivity for a first order consecutive reaction
Option D: All A., B. and C.
Correct Answer: D. All A., B. and C. ✔
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Option A: Plot of – rA Vs CA is a straight line with slope k
Option B: Plot of – rA Vs CA is a hyperbola
Option C: Rate of disappearance of reactant A is maximum, where CA = CB
Option D: Both B & C
Correct Answer: Both B & C ✔
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Option A: Plug flow
Option B: Dispersion
Option C: Mixed flow
Option D: Tank in series
Correct Answer: Dispersion ✔
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Option A: dXA/dt = k1 (1 – XA)2 (1 + 2XA)
Option B: dXA/dt = k1 (1 – XA) (1 + 0.5XA)
Option C: dXA/dt = k1 (1 – XA)
Option D: dXA/dt = k1 (1 – XA)/(1 + XA)
Correct Answer: C. dXA/dt = k1 (1 – XA) ✔
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Option A: 100
Option B: 150
Option C: 200
Option D: 225
Correct Answer: 100 ✔
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Option A: Be more in CSTR than in PFR
Option B: Be more in PFR than in CSTR
Option C: Be same in both cases
Option D: Depend on the temperature
Correct Answer: Be more in PFR than in CSTR ✔
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Option A: A Dirac delta function
Option B: A step function
Option C: A ramp function
Option D: None of the above
Correct Answer: None of the above ✔
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Option A: May be lateral mixing of fluid
Option B: Should not be any mixing along the flow path
Option C: Both A. and B.
Option D: Neither A. nor B.
Correct Answer: C. Both A. and B. ✔
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Option A: Temperature and pressure only
Option B: Temperature and composition only
Option C: Pressure and composition only
Option D: All temperature, pressure and composition
Correct Answer: All temperature, pressure and composition ✔
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Option A: Is always greater for plug-flow reactor than for the single CSTR of the same volume
Option B: Statement in A. is wrong
Option C: Decreases with increasing conversion
Option D: Both A. and C. hold good
Correct Answer: D. Both A. and C. hold good ✔
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Option A: One of the reactants acts as a catalyst
Option B: One of the products acts as a catalyst
Option C: Catalysts have very high selectivity
Option D: No catalyst is used
Correct Answer: One of the products acts as a catalyst ✔
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Option A: Pressure
Option B: Temperature
Option C: Concentration and catalyst
Option D: None of these
Correct Answer: Concentration and catalyst ✔
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Option A: Is same as heat of reaction at constant pressure
Option B: Is the minimum energy which the molecules must have before the reaction can take place
Option C: Varies as fifth power of the temperature
Option D: Both B. and C.
Correct Answer: Is the minimum energy which the molecules must have before the reaction can take place ✔
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If pore diffusion is the controlling step in a solid catalysed reaction, the catalyst__________?
Option A: Porosity is very important
Option B: Porosity is of less importance
Option C: Internal surface area is utilised efficiently
Option D: None of these
Correct Answer: Porosity is of less importance ✔
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Option A: Higher in P.F. reactor
Option B: Higher in CSTR
Option C: Same in both the reactors
Option D: Data insufficient; can’t be predicted
Correct Answer: Higher in P.F. reactor ✔
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Option A: Usually equal to the residence time
Option B: The reciprocal of the space velocity
Option C: A measure of its capacity
Option D: Both A. and B.
Correct Answer: D. Both A. and B. ✔
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Option A: Autocatalytic
Option B: Exothermic
Option C: Endothermic
Option D: Autothermal
Correct Answer: Autocatalytic ✔
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Option A: An experimentally determined quantity
Option B: Always equal to the total stoichiometric number of reactants
Option C: Never fractional
Option D: None of these
Correct Answer: An experimentally determined quantity ✔
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Option A: Increased temperature reduces the activation energy
Option B: Fraction of molecules having threshold energy increases
Option C: Collision frequency increases
Option D: Value of threshold energy decreases
Correct Answer: Fraction of molecules having threshold energy increases ✔
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Option A: The composition of reactants remains constant along a flow path
Option B: The conversion of the reactant varies from point to point along a flow path
Option C: There is no lateral mixing of fluid
Option D: There may be diffusion along the flow path
Correct Answer: The conversion of the reactant varies from point to point along a flow path ✔
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Option A: Initiates a chemical reaction and is a catalyst by itself
Option B: Alters the position of equilibrium in a reversible reaction
Option C: Increases the number of active centres by increasing the unevenness of catalyst surface and by
Option D: All A., B. and C.
Correct Answer: C. Increases the number of active centres by increasing the unevenness of catalyst surface and by
creating discontinuities in the crystals ✔
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Option A: 0.16
Option B: 0.144
Option C: 0.152
Option D: 0.136
Correct Answer: 0.144 ✔
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Option A: Slurry
Option B: Plug flow
Option C: Homogeneous catalytic
Option D: None of these
Correct Answer: Slurry ✔
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B.E.T. method of finding out surface area of a catalyst, uses the extension of __________ isotherm?
Option A: Langmuir
Option B: Freundlich
Option C: Tempkin
Option D: None of these
Correct Answer: Langmuir ✔
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Option A: First
Option B: Zero
Option C: Second
Option D: Third
Correct Answer: Second ✔
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Option A: Linearly with time
Option B: Exponentially with time
Option C: Very abruptly towards the end of the reaction
Option D: Logarithmically with time
Correct Answer: Exponentially with time ✔
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