Govt. Exams
Entrance Exams
For second-order reaction with CA0 = CB0: 1/CA - 1/CA0 = kt. At 50% conversion, CA = 0.5. So (1/0.5 - 1/1) = 0.5×t gives t = 2 minutes
Equilibrium conversion is thermodynamically determined and independent of reactor type
Adiabatic reactor: no heat removal; exothermic reaction raises temperature, increasing k and hence rate
K_m represents substrate concentration [S] at which reaction velocity = V_max/2
Da = kτ = (reaction rate constant × residence time), dimensionless number indicating reaction extent
For 2nd order: 1/[A] = 1/[A]₀ + kt; 1/1 = 1/2 + k(5); k = 0.1 L/(mol·min)
Catalyst doesn't change ΔG or equilibrium position; it only lowers Eₐ. ΔG determines feasibility, not rate
Selectivity = rate of desired product formation/rate of undesired product formation
For CSTR: X = kτ/(1+kτ). Increasing τ increases conversion for first-order reactions
PFR with heat removal maintains optimal temperature profile and continuous removal of products, favoring forward reaction equilibrium