A. 2
B. 3
D. 1
A. A ferment or an enzyme
C. Haemoglobin
D. None of these
B. Second
C. Zero
D. Third
A. High aromatics content
C. Low paraffins content
D. Low smoke point
A. Only
B. To a greater extent than that of the backward reaction
C. And decreases that of backward reaction
A. Increases the activation energy
B. Decreases the molecular collision diameter
C. None of these
A. Oxidation & polymerisation of unsaturated
C. Alkylation of unsaturated
D. Higher aromatic content
A. 70
B. 35
C. 0.03
A. Suitable for gas-phase reactions on commercial scale
B. Least expensive to operate for a given rate
D. Most suitable for very large production rate
A. K ? ?T . e-E/RT
B. K ? eE/RT
C. K ? T . e-E/RT
A. Fixed bed reactor
C. Batch reactor
D. Plug-flow reactor
B. > 1
C. < 1
D. 0
A. Reaction can be accomplished with small reactor
B. Conversion can be obtained with a high feed rate
B. Polymerisation
C. Isomerisation
D. Cracking
A. Temperature is increased and pressure is reduced
C. Pressure is reduced
D. Temperature is increased
A. Increases
B. Remain unaffected
C. Increases linearly with temperature
A. None of these
B. Double
D. Triple
A. Sulphur
B. Nitrogen
A. Atomic weight
C. Molecular weight
D. Equivalent weight
A. (CA/2)n
C. (CA)1/2n
D. (CA/2)1/n
B. Reactants concentration is very high
C. Reaction rate is independent of the reactants concentration
D. Reactants concentration is very low
A. k cal. K
B. k cal/K
C. k cal
A. Fuel oil
C. Naphtha
D. Diesel
A. k ? e-E/RT
C. k ? ?T
D. k ? T1.5
A. Maximum at the exit of the reactor
B. Maximum at the centre of the reactor
D. Constant throughout the reactor
A. Isomerisation of paraffins
C. Dehydrogenation of Naphthene
D. Dehydrocyclization of higher paraffins
A. Diameter of the reactor
C. Useful volume of the tank
A. Is independent of temperature
B. Varies with temperature
C. Depends on the nature of the reactants
B. Decreases
D. Neither A. nor B.
A. Is not a function of the unit of time
C. Changes on changing the concentration units
A. 1.6
C. 2
D. 2.24
A. Chemical reaction
B. Pore diffusion
C. Ash layer diffusion
A. Either A. or B., depends on the type of reaction
C. Decrease
D. Increase
A. Condition similar to plug flow reactor exists
C. Residence time is constant
D. Mixing takes place in axial direction only
A. 32
B. 3-Jan
B. Forward reaction is favoured
C. Backward reaction is favoured
B. Inhibit catalyst poisoning
C. Increase the activity of a catalyst
D. Have very high selectivity
A. 2 & 2
B. 11 & 2
D. 1 & 1
A. Kinetics of the reaction
B. Temperature of the system
C. Presence or absence of inerts
B. None of these
C. Removal of at least one of the products at regular interval
D. Increasing the concentration of one of the reactants
A. High exothermicity
C. Maxima in the concentration of A
D. Maxima in the concentration of C
A. Penetration number
C. Melting point
D. Specific gravity
A. ln CA0 Vs ln t1/2
C. ln CA0 Vs t1/2
D. CA0 Vs t1/2
A. 18
C. 28
D. 35
A. Twice
D. Equal
B. Ammonia synthesis reaction
C. Enzyme fermentation reaction
D. Photochemical reactions
C. Same as that of activation energy
D. Dimensionless
A. First increases and then decreases
C. Increases
D. Decreases
B. Reversible exothermic
C. Autocatalytic
D. Irreversible
B. At high P and high T
C. At high P and low T
D. At low P and high T
Showing 3201 to 3250 of 8709 mcqs