A. None of these
B. N2 + O2 ? 2NO
C. 2HI ? H2 + I2
A. Butene
B. Acetylene
C. Butadiene
B. Removal of one of the products regularly
C. Increase in the concentration of one of the reactants
D. None of these
B. 90
C. 55
D. 45
A. Increases
B. Changes unpredictably
C. Remains unaltered
A. Equilibrium constant
B. Heat of reaction
D. Final products
A. 3
B. 0.5
C. 1
A. Aromatic
B. Olefin
D. Naphthene
B. A P.F. reactor in series
C. A P.F. reactor in parallel
D. More CSTRs in parallel
A. Tubular flow
C. Fixed bed
D. Batch
A. Three
C. Zero
D. Two
A. (i) increases (ii) increases
C. (i) increases (ii) decreases
D. (i) decreases (ii) decreases
A. 50
C. 5000
D. 250
B. Also be doubled
C. Become one fourth
D. Be halved
B. 70
D. 140
A. Surface reaction between absorbed A and absorbed B
B. Surface reaction between A in the gas phase and absorbed B
C. Absorption of A
A. Threshold
B. Thermal
D. Binding
B. K ? e-E/RT
C. K ? eE/RT
D. K ? ?T . e-E/RT
A. Ions
B. Masses
C. Atoms
A. Gasoline obtained has a very low octane number
B. Pressure & temperature is very high
C. Gasoline obtained has very high amount of gum forming compounds
A. Gas phase oxidation of SO2 in chamber process
B. None of these
C. Hydrogenation of oils
B. Plot of products concentration with time is a straight line through the origin
C. Products concentration increases linearly with time
D. Half life period is directly proportion to the initial concentration of the reactants
A. Intermediate
B. Fastest
C. Data insufficient; cant be predicted
A. Methane & ethane
B. High boiling naphthenes
D. High boiling olefins
A. Elimination of solvent drying facility
B. Higher nitration temperature
D. Lower solvent dilution ratio
A. Nickel
B. Alumina
C. Silica gel
B. Decay reactions
C. Pore diffusion
D. Form of surface attack by poison
A. 100000
C. 10000
D. 100
A. Low flash point
B. High breathing loss
C. Both A. and B.
B. i-paraffins
C. Olefins
A. 112
B. 256
C. 612
A. Sodium
B. Potassium
D. Calcium
B. Reversible exothermic
C. Irreversible exothermic
D. Irreversible endothermic
B. Desulphurisation
C. Steam reforming
B. 50
C. ?
A. Has altogether three streams either entering or leaving
C. Processes three reactants at different flow rates
D. Processes three reactants with same flow rate
A. Pulse
B. Step
D. Neither A. nor B.
A. Becomes infinite
C. Decreases
D. Remain same
A. Naphthenes
B. Cycloparaffins
A. 350-400
C. 150-250
D. 10-May
A. Electric immersion
C. None of these
D. Steam coil
A. -1
D. 1
A. -rA = (k . PA
B. #8211; k1PP)/(1 + KAPA + KPPP)
C. -rA = (k . PA . PB)/(1 + KAPB + KBPB . KPPP)
D. -rA = (k . PA . PB)/(1 + KAPA)
A. Physical
A. Petrol
C. Diesel
D. Kerosene
A. Gasoline
C. Naphtha
D. Diesel
B. 2
C. 2-Jan
D. 4
A. Any state
B. Liquid state only
C. Solid state only
B. Fluidised bed
C. Perforated plate
D. Packed bed
A. Smoking tendency of aromatics decreases with increase in its molecular weight
B. Smoking tendency of naphthenes decreases with its increasing molecular weight & also on
C. Smoking tendency of hydrocarbons increases in the order: paraffins ? isoparaffins ?
D. ition of double bond
E. hthenes ? aromatics
Showing 3101 to 3150 of 8709 mcqs