Chemical Reaction Engineering MCQs 2026

10 questions with detailed answers · 7 from past papers · 1 quiz batches available

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  1. Q1Past Paper · PPSC/FPSC/CSSeasy

    Elementary rate law r = k C_A^n implies

    1. Aequilibrium constant
    2. Bextent of reaction only
    3. Cheat transfer coefficient
    4. Dreaction order n with respect to A
    💡 Explanation:

    Power-law kinetics.

  2. Q2Past Paper · PPSC/FPSC/CSSeasy

    Arrhenius equation k = A exp(−E/RT) shows rate constant increases with

    1. Apressure only always
    2. Bcatalyst pore length only
    3. Ctemperature
    4. Dreactor diameter only
    💡 Explanation:

    Activation energy barrier.

  3. Q3Past Paper · PPSC/FPSC/CSSeasy

    CSTR characteristic is

    1. Aplug flow with no mixing
    2. Bno volume holdup
    3. Conly solid catalyst fixed bed without fluid
    4. Dwell-mixed contents with uniform composition
    💡 Explanation:

    Backmixing complete.

  4. Q4Past Paper · PPSC/FPSC/CSSeasy

    PFR model assumes

    1. Acomplete backmixing
    2. Bzero flow
    3. Cfluid elements move in series without mixing axially
    4. Donly batch operation
    💡 Explanation:

    Plug flow profile.

  5. Q5Past Paper · PPSC/FPSC/CSSmedium

    Space time τ in PFR is

    1. AF/V always called residence without volume
    2. Bonly catalyst weight
    3. Conly heat duty
    4. DV/F_total for volumetric basis
    💡 Explanation:

    τ = V/v̇.

  6. Q6hard

    Thiele modulus relates

    1. Aonly external film only
    2. Bonly pump head
    3. Conly distillation reflux
    4. Dreaction rate in pellet to diffusion rate inside pellet
    💡 Explanation:

    Effectiveness factor for porous catalyst.

  7. Q7hard

    Damköhler number compares

    1. Areaction rate to transport rate
    2. Bheat to work
    3. Cpressure to gravity
    4. Dmolecular weight to density only
    💡 Explanation:

    Da = reaction/residence or transport scale.

  8. Q8Past Paper · PPSC/FPSC/CSSeasy

    Half-life for first-order reaction t_1/2 equals

    1. A1/k
    2. Bk/2
    3. C0.693/k
    4. D2/k
    💡 Explanation:

    ln2/k.

  9. Q9Past Paper · PPSC/FPSC/CSShard

    Mixed flow reactor exit conversion for first-order liquid reaction is

    1. AX = kτ/(1+kτ)
    2. BX = 1 − exp(−kτ) for PFR
    3. CX = kτ always linear
    4. DX = 0 always
    💡 Explanation:

    CSTR first-order: C = C0/(1+kτ).

  10. Q10hard

    Langmuir-Hinshelwood mechanism applies to

    1. Aonly gas-phase chain reactions
    2. Bonly enzyme in solution without surface
    3. Conly distillation trays
    4. Dsurface reaction on catalyst with adsorption steps
    💡 Explanation:

    Heterogeneous catalytic rate form.