A. A ferment or an enzyme
B. Haemoglobin
C. Fungi
D. None of these
Related Mcqs:
- Photo-chemical reactions occur in presence of ___________________?
A. Sunlight
B. Darkness
C. Solid catalysts
D. Monochromatic radiation only - Fractional conversion _____________ with increase in pressure for ammonia synthesis reaction i.e., N2 + 3H2 ⇌ 2NH3?
A. Increases
B. Decreases
C. Remains unchanged
D. Unpredictable from the data - The ratio of moles of a reactant converted into the desired product to that converted into unwanted product is called_________________?
A. Operational yield
B. Relative yield
C. Selectivity
D. None of these - The equilibrium constant of a catalytic chemical reaction _______________ due to the presence of?
a catalyst.
A. Increases
B. Decreases
C. Remain unaffected
D. Unpredictable from the data - For a packed bed reactor; the presence of a long tail in the residence time distribution curve is an indication of ?
A. Ideal plug flow
B. Bypass
C. Dead zone
D. Channelling - The molecularity and the order of reaction respectively, for the hydrolysis of methyl acetate in presence of acids are_______________?
A. 2 & 1
B. 11 & 2
C. 2 & 2
D. 1 & 1 - On application of pressure to the equilibrium system, ice ⇌ water; which of the following phenomenon will occur ?
A. Water will evaporate
B. Equilibrium will not be attained
C. More ice will be formed
D. More water will be formed - 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. 0.16
B. 0.144
C. 0.152
D. 0.136 - Ionic reactions occur in____________________?
A. Solid state only
B. Liquid state only
C. Solutions
D. Any state - Which of the following is the most suitable for isothermal operation?
A. Batch reactor
B. Back-mix reactor
C. Plug-flow reactor
D. Fixed bed reactor