SF Prep
09 Chemistry Notes 🕒 Updated 2026-10-07
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Average and Instantaneous Rate of Reaction

Chemical Kinetics

1. Average and Instantaneous Rate of Reaction

Disappearance of Reactants :

  • For a reactant undergoing change: Reactant → Product.
  • The concentration decreases with time.
Average rate of disappearance = −(C2 − C1)t2 − t1 = −ΔCΔt
Instantaneous rate = −dCdt

Where C1, C2 are concentrations at times t1, t2.

Appearance of Products :

  • For a product formed: Reactant → Product.
  • The concentration increases with time.
Average rate of appearance = C2 − C1t2 − t1 = ΔCΔt
Instantaneous rate = dCdt

2. Rate Expression and Stoichiometry

  • For a general reaction aA + bB → cC + dD:
Rate = −1ad[A]dt = −1bd[B]dt = +1cd[C]dt = +1dd[D]dt

(+) indicates products and (−) indicates reactants.

3. Factors Affecting Rate of Reaction

1. Concentration :

  • Increasing reactant concentration increases the rate of reaction.
  • Reason: Number of reactant molecules per unit volume increases, leading to an increase in the number of effective collisions.

2. Temperature :

  • Increasing temperature increases the kinetic energy (K.E) of molecules.
  • More molecules acquire threshold energy, increasing effective collisions and thus the rate.

3. Temperature & Maxwell-Boltzmann Distribution :

  • For temperatures T3 > T2 > T1:
  • The Maxwell-Boltzmann distribution shows the fraction of molecules vs energy. The area under the curve to the right of the threshold energy (E0) increases as temperature increases, representing more molecules with sufficient energy for effective collisions.

4. Catalyst :

  • A positive catalyst provides an alternate pathway with lower activation energy (E'a).
  • E'a < Ea.

Energy profile (PE vs progress of reaction): the uncatalysed path has the higher peak (Ea); the catalysed path has a lower peak (E′a). Both are measured from the reactant level.

5. Surface Area :

  • Increasing surface area increases the rate. This is particularly relevant for solid reactants or solid catalysts.
  • Example: Fragmentation of a large solid reactant B into smaller particles increases available surface area for reaction with liquid A.

6. Presence of Light :

  • Sunlight (photons) can increase the rate of photochemical reactions.
  • H2 + Cl2 → 2HCl

4. Rate Law

  • The rate law relates the reaction rate to the concentration of reactants (and sometimes products).
  • For the reaction: A + 2B → Product
  • rate ∝ [A]x[B]y ⇒ rate = k[A]x[B]y
k = rate constant
x = order of reaction with respect to A
y = order of reaction with respect to B
x + y = overall order of reaction
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Rate Law for Elementary Reactions & Time calculations

5. Rate Law for Elementary Reactions

  • For a single-step reaction like 1A + 2B → Product:
rate = k [A]1 [B]2
  • Molecularity = number of reactant molecules involved in an elementary reaction.
  • For elementary reactions, Molecularity = Order.
  • In the example above, Molecularity = 1 + 2 = 3; Order = 1 + 2 = 3.

6. Rate Law for Net Chemical Reactions

  • For a net reaction A + 2B → Product, the rate law is given by:
rate = k [A]x [B]y
  • For net reactions, molecularity has no significance.
  • Order (x + y) must be determined experimentally.
  • Reaction mechanism example:
    • Step 1: B + B → B* (Intermediate/activated complex)
    • Step 2: B* + A → Product
  • Order w.r.t. A = x; Order w.r.t. B = y; Overall order = x + y.

7. Unit of Rate Constant

  • For a reaction A → Product, rate = -d[A]/dt = k[A]n (where n is the order).
  • Unit of k = (unit of rate) / (unit of conc)n.
Unit = (conc)1−n (time)−1
  • Specific cases:
Order (n)Unit of k
0mol L−1 time−1
1time−1
2mol−1 L time−1

8. Rate Laws for Complex Reactions (Mechanism)

  • For a multi-step reaction, the slowest step is the Rate Determining Step (RDS).
  • The rate law of the net reaction is determined by the RDS. If the RDS involves an intermediate, express the intermediate in terms of reactants using the equilibrium constant (Keq) of the preceding fast steps.

9. Zero Order Reaction

  • General form: A → Product
  • Rate law:
    rate = k[A]0 = k
  • Differential rate law:
    -d[A]dt = k
  • Integrated rate equation:
    [A]0 - [A]t = kt

[A]0 = initial concentration; [A]t = concentration remaining after time t.

10. Time calculations

  • Completion time (t100%): At t = t100%, [A]t = 0.
    t100% = [A]0k
  • Half-life time (t1/2): At t = t1/2, [A]t = [A]02.
    t1/2 = [A]02k
  • Three-quarter life (t75%): At t = t75%, [A]t = [A]04.
    t75% = 3[A]04k
  • Relation between t3/4 and t1/2:
    t3/4 = 32 t1/2

11. Examples of Zero Order Reactions

1. Photochemical Reactions :

  • H2(g) + Cl2(g) → 2HCl(g)
  • Br2(g) → 2Br(g)
  • Rate ∝ intensity of light (rate ∝ [intensity]1).

2. Surface Catalysed Reactions :

  • 2NH3(g) →Fe/W/Mo/Pt N2(g) + 3H2(g)
  • 2HI(g) →Au H2(g) + I2(g)
  • Note: Decomposition can only take place on the catalyst surface. Once the surface is completely covered, further increase in concentration has no effect on rate.

12. Graphical Representations

  • Graphs for rate = k[A]0:
    • Rate vs. time: Horizontal line.
    • Rate vs. [A]: Horizontal line.
    • t1/2 vs. [A]0: Linear line passing through origin (slope = 12k).
  • Graph for [A]0 - [A]t = kt:
    • ([A]0 - [A]t) vs. time: Straight line through origin (slope = k).
  • Graph for [A]t = [A]0 - kt:
    • [A]t vs. time: Downward sloping straight line (intercept on y-axis = [A]0, intercept on x-axis = [A]0k, slope = -k).

13. Half-life of Zero Order Reaction

  • For a general reaction: aA → Product with rate law rate = k[A]0:
[A]0 − [A]t = akt
t1/2 = [A]02ak

where a is the stoichiometric coefficient of the reactant.

  • Special Cases:
ReactionRate LawHalf-life (t1/2)
A → Productk[A]0[A]0 / 2k
2A → Productk[A]0[A]0 / 4k
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Half-life in Stoichiometric Reactions

14. Half-life in Stoichiometric Reactions

  • For a reaction: 2A + 3B → Product with rate = k [A]0 [B]0.
  • Assuming 1 L volume with initial moles a and b:
(t1/2)A = a4k ; (t1/2)B = b6k
  • If the half-lives are equal ((t1/2)A = (t1/2)B), then a4k = b6k ⇒ ab = 23.
  • Conclusion: Irrespective of the order, if the initial amounts of reactants are in their stoichiometric ratio, their half-lives are the same.

15. First Order Kinetics

  • i) Completion time (t100%): [A]t = 0.
t100% = ∞
  • Note: When given "after a long time", assume [A]t ≃ 0.
  • ii) Half-life time (t1/2 or t50%): [A]t = [A]02.
t1/2 = ln 2k = 0.693k
  • Note: Half-life for first order is independent of the initial amount of reactant.

16. Time for Completion of Reaction

  • For a first-order reaction: t = 2.303k log [A]0[A]t
  • t(99.9%) : [A]t = 0.1% [A]0 = [A]01000
    t(99.9%) = 2.303k log 1000 = 2.303 × 3k = 6.909k ≃ 10 0.693k
    t(99.9%) ≃ 10 t(1/2)
  • t(99%) : [A]t = [A]0100 ⇒ t(99%) = 203 t(50%)
  • t(90%) : [A]t = [A]010 ⇒ t(90%) = 103 t(50%)

Summary of Half-life Relationships :

  • t(1/2) = ln 2k = 0.693k (independent of [A]0)
  • t(75%) = 2 t(50%)
  • t(87.5%) = 3 t(50%)
  • t(90%) = 103 t(50%)
  • t(99%) = 203 t(50%)
  • t(99.9%) = 10 t(50%)

17. Graphical Representations

  • Rate = k[A] = k[A]0 e−kt
  • [A]t = [A]0 e−kt
  • kt = ln([A]0 / [A]t) ⇔ ln[A]t = ln[A]0 − kt
  • Plot of Rate vs Concentration: Straight line passing through origin, slope = k.
  • Plot of Rate vs Time: Exponential decay curve starting at y-intercept k[A]0.
  • Plot of [A]t vs Time: Exponential decay curve starting at y-intercept [A]0.
  • Plot of ln[A]t vs Time: Straight line with negative slope = −k.
  • Plot of ln([A]0 / [A]t) vs Time: Straight line passing through origin, slope = k.
  • Plot of t(1/2) vs [A]0: Horizontal line.

18. First Order Kinetics: Gas Phase Reactions

Case 1: A(g) → Products

  • For reaction A(g) → Products, where P0 is the initial pressure of A at t=0 and Pt is the pressure of A at time t:
k = 2.303t log10 P0Pt

Case 2: A(g) → 2B(g) + C(g)

  • Let P0 be the initial pressure of the system at t=0.
  • Let Pt be the total pressure of the system at time t.
TimeA2BC
t=0P000
t=tP0 − x2xx
  • Total pressure Pt = (P0 − x) + 2x + x = P0 + 2x.
  • Solving for x: x = Pt − P02.
  • Pressure of A at time t: PA = P0 − x = P0 − Pt − P02 = 3P0 − Pt2.
k = 2.303t log10 2P03P0 − Pt

19. General Property Method

  • If x is a property (e.g., pressure) common to both reactants and products, and we are provided with values x0 (t=0), x(t) (t=t), and x∞ (t=∞), then irrespective of the specific reaction:
k = 2.303t logx∞ − x0x∞ − x(t)
  • For two different times t1 and t2:
k = 2.303t2 − t1 logx∞ − x(t1)x∞ − x(t2)

20. Decomposition of H2O2

  • Reaction : H2O2 → H2O + 12 O2
  • Volume of KMnO4 consumed is proportional to the concentration of H2O2 remaining.
k = 2.303t log(V0Vt)

where V0 = volume of KMnO4 at t = 0, and Vt = volume of KMnO4 at time t.

21. Acid Catalyzed Hydrolysis of Ester

  • Reaction : CH3COOCH2CH3 + H2O →(H+) CH3COOH + CH3CH2OH
  • Pseudo first order rate constant (kapp) depends on [H+] and [H2O].
  • If concentration of H+ is higher, the reaction rate is faster (e.g., H2SO4 provides 2 H+ ions per molecule, while HCl provides 1).
k = 2.303t log(V∞ − V0V∞ − Vt)

where V0, Vt, and V∞ are volumes of NaOH/titrant used at t=0, t=t, and t=∞ respectively.

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Inversion of Cane Sugar & Parallel First Order Kinetics

22. Inversion of Cane Sugar

  • Reaction : C12H22O11 + H2O → C6H12O6 + C6H12O6 (Sucrose → Glucose + Fructose)
  • Optical rotation (measured by PPL) changes over time as the mixture transitions from Dextro(+) to Leavo(-).
  • r0 = optical rotation at t = 0
  • rt = optical rotation at t = t
  • r∞ = optical rotation at t = ∞
  • The rate follows pseudo first order kinetics : rate = kapp[sucrose].

23. Half-Life for nth Order Reaction

  • For a general reaction: A → Product
  • Rate law: −d[A]/dt = k[A]ⁿ
  • Integrating the rate law:
kt = 1n−1 [ 1[A]tn−1 − 1[A]0n−1 ]
  • For half-life (t1/2), the concentration of reactant [A]t = [A]0/2. Substituting this:
t1/2 = 2n−1 − 1(n−1)k[A]0n−1
  • General proportionality: t1/2 ∝ 1/[A]0n−1
  • For first-order (n=1), the half-life is constant: t1/2 = ln 2 / k ≈ 0.693 / k.

24. First Order Kinetics: Optical Rotation

  • For reactions following first order kinetics measured by optical rotation (rt), the rate constant is given by:
k = 2.303t log(r₀ − r∞rt − r∞)

where r₀, rt, and r∞ are the optical rotations at time 0, t, and infinity, respectively.

  • This formula applies to the inversion of cane sugar and sucrose hydrolysis.

25. Reversible First Order Reaction

  • Consider the reversible reaction: A ⇌ B (with forward rate constant kf and backward rate constant kb).
Time[A][B]
t = 0a0
t = ta − xx
t = teqa − xeqxeq
  • Rate expression: d[B]dt = kf[A] − kb[B]
  • At equilibrium (t = teq): d[B]dt = 0   ⇒   kf[A] = kb[B]
  • kfkb = [B]eq[A]eq = xeqa − xeq    ⇒    xeq = kfkf + kb a
(kf + kb) = 2.303t logxeqxeq − x

26. Parallel First Order Kinetics

  • For the parallel decomposition of A: A → B (rate constant k1) and A → C (rate constant k2).
  • The total rate of disappearance of A is the sum of the rates of the two parallel paths:
-d[A]dt = (k1 + k2)[A]
[A]t = [A]0 e-(k1+k2)t
  • Overall rate constant: knet = k1 + k2
  • Overall half-life:
(t1/2)net = ln 2knet = ln 2k1 + k2

Concentration of products :

  • By integration of the rate expressions d[B]/dt = k1[A] and d[C]/dt = k2[A]:
[B]t = k1k1 + k2 [A]0 [1 - e-(k1+k2)t]
[C]t = k2k1 + k2 [A]0 [1 - e-(k1+k2)t]

27. Stoichiometric Branching (General Case)

  • For reaction: A → n1B (k1) and A → n2C (k2).
  • Rates: 1n1 d[B]dt = k1[A]  and  1n2 d[C]dt = k2[A].
  • The ratio of product concentrations at any time t is:
[B]t[C]t = n1k1n2k2
  • Percentage yield:
%[B] = n1k1n1k1 + n2k2 × 100%
%[C] = n2k2n1k1 + n2k2 × 100%

28. Parallel Reactions (Side Reactions)

Material Balance :

  • For a reactant A decomposing into products via multiple pathways:
    A →k₁ B
    A →k₂ C
  • If the reaction starts with only A, the stoichiometry dictates the distribution of products:
    [A]0 = [A]t + [B]tn1 + [C]tn2
  • Where n1 and n2 are the stoichiometric coefficients of B and C respectively.

Rate of Production Ratio :

  • For the parallel reactions:
    A →k₁ n1B
    A →k₂ n2C
  • The ratio of the rate of production of products B and C is given by:
    d[B]/dtd[C]/dt = n1k1[A]n2k2[A] = n1k1n2k2
  • This ratio is independent of time and independent of [A]t.

Product Composition :

  • For simultaneous 1st order reactions where A →k₁ B and A →k₂ C, the percentage of B formed is:
    % B (by mole) = 100 k1k1 + k2
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Sequential Reaction

29. Sequential Reaction

  • For the sequential reaction A →k1 B →k2 C:
-d[A]/dt = k1[A]
[A]t = [A]0 e−k1t
d[B]/dt = k1[A] − k2[B]

30. Concentration of B and C at time t

  • Concentration of B at time t:
[B]t = k1[A]0k2 − k1 [e−k1t − e−k2t]
  • Concentration of C at time t:
[C]t = [A]0k2 − k1 [k2(1 − e−k1t) − k1(1 − e−k2t)]

31. Maximum Concentration of B

  • Time at which [B]t is maximum (tmax):
tmax = 1k1 − k2 ln k1k2
  • Value of maximum concentration [B]max:
[B]max = [A]0 (k2/k1)k2k1 − k2

32. Concentration vs Time Graph (A → B → C)

  • The graph shows [A] decaying from [A]0, [B] increasing from 0 to a peak and then decreasing, and [C] starting from 0 and plateauing.
  • A vertical dashed line at tmax aligns with the peak of curve [B].
time → conc tmax [A]₀

33. Steady State Approximation

  • For a consecutive reaction scheme: A →k1 B →k2 C
  • If the rate of formation of intermediate B is assumed to be zero (Steady State Approximation), the concentration of B is:
[B] = k1k2 [A]

34. Consecutive Reactions: A → k1 B → k2 C

  • Case: k1 >> k2
  • Concentration profiles:
[A]t = [A]0e−k1t
[B]t = [A]0e−k2t
[C]t = [A]0(1 − e−k2t)
  • [A]t decays exponentially from [A]0 to zero.
  • [B]t starts at zero, rises to a peak, and then decays towards zero.
  • [C]t starts at zero and rises to approach [A]0.

35. Sequential Reaction : Case 2 (k2 >> k1)

  • Reaction : A →k1 B →k2 C
  • [A]t = [A]0 e-k1t
  • [B]t ≃ 0
  • [C]t = [A]0 - [A]0 e-k1t = [A]0 (1 - e-k1t)
  • Graph description: [A]t curve decreases from [A]0. [C]t curve starts at 0 and increases to [A]0 asymptotically. [B]t curve remains near the x-axis.

36. Second & Third Order Reactions

Second Order (n=2) :

  • kt = 1(2-1) [ 1[A]t2-1 - 1[A]02-1 ] = 1[A]t - 1[A]0
  • For t1/2, [A]t = [A]0/2 ⇒ t1/2 = 1k[A]0

Third Order (n=3) :

  • kt = 1(3-1) [ 1[A]t3-1 - 1[A]03-1 ] = 12 [ 1[A]t2 - 1[A]02 ]
  • For t1/2, [A]t = [A]0/2 ⇒ t1/2 = 32k[A]02
Zero order: t1/2 = [A]02k ; First order: t1/2 = ln 2k

37. Graphical Representation

  • n=2: Rate = k[conc]2 (Linear graph, y=rate, x=[conc]2, slope=k)
  • n=3: Rate = k[conc]3 (Linear graph, y=rate, x=[conc]3, slope=k)
  • n=2: t1/2 = 1k[A]0 (Linear graph, y=t1/2, x=1/[A]0, slope=1/k)
  • n=3: Linear graph, y=t1/2, x=1/[A]02, slope=3/2k
  • n=2: 1[A]t = kt + 1[A]0 (Linear graph, y=1/[A]t, x=time, slope=k, intercept=1/[A]0)
  • n=3: 1[A]t2 = 2kt + 1[A]02 (Linear graph, y=1/[A]t2, x=time, slope=2k, intercept=1/[A]02)

38. Temperature Dependence

  • Temperature coefficient (T.C) = kT+10°kT ≃ 2-3
knew = kold (T.C)ΔT/10

39. Collision Theory

  • Product is formed due to collisions among reactant molecules.
  • Every collision does not lead to product formation; only effective collisions result in products.
  • Effective collisions require:
    • (a) Sufficient energy
    • (b) Proper orientation
  • To form products, reactant molecules must overcome two barriers:
    • Energy barrier
    • Orientation barrier
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Arrhenius Equation & Net Activation Energy

40. Arrhenius Equation

  • The Arrhenius equation describes the dependence of the rate constant on temperature:
k = A · e−Ea/RT

where k = rate constant, T = absolute temperature (K), A = frequency factor (unit of A = unit of k), Ea = activation energy.

  • A represents the effective collisions per unit volume per unit time.
  • e−Ea/RT represents the fraction of molecules having energy more than or equal to the threshold energy.

41. Temperature Dependence of Rate Constant

  • As temperature (T) changes, the rate constant (k) varies:
  • If T → 0, then k → 0.
  • If T → ∞, then k → A.
T k A

42. Linear Forms of Arrhenius Equation

lnk = lnA − EaR(1/T)
logk = logA − Ea2.303R(1/T)

43. Calculation of Activation Energy

  • Activation energy can be calculated using the graphical method by plotting the linear forms of the Arrhenius equation:
  • Plot of lnk vs 1/T: A straight line with slope = −Ea/R.
  • Plot of logk vs 1/T: A straight line with slope = −Ea/(2.303R).

44. Pressure Relation for First Order Gaseous Reaction

  • Reaction: A(g) → nB(g)
  • At t = 0: PA = P0, PB = 0, Ptotal = P0
  • At time t: PA = P0e−kt, PB = n(P0 − P0e−kt)
  • Total Pressure (Ptotal) = PA + PB
Ptotal = P0e−kt + nP0(1 − e−kt) = P0[e−kt + n − ne−kt] = P0[n + (1 − n)e−kt]

45. Catalyst Effect

  • A catalyst provides an alternative path for a reaction, lowering the activation energy (Ea → Ea').
  • Effect on Potential Energy : Ea decreases, rate of reaction increases.
  • Enthalpy Change : ΔH = (Ea)f − (Ea)b = (Ea')f − (Ea')b (remains unchanged).
  • Effect on Rate Constant (k) :
    • k = A e−Ea/RT (uncatalyzed)
    • kcat = A e−Ea'/RT (catalyzed)
logkcatk = Ea − Ea'2.303 R T

46. Net Activation Energy

  • For a multi-step complex reaction with net rate constant knet:
knet = k1 k22k3 ⇒ Enet = E1 + 2E2 − E3
  • For knet = k12 k31/2k23, the net activation energy is Enet = 2E1 + 12E3 − 3E2.

47. Reaction Mechanism & Catalysis

  • Reaction profile: The slow step determines the magnitude of the activation energy hill.
  • A → B (slow, endothermic) followed by fast steps indicates a high initial activation energy.
  • Catalyst effects:
    • Lowers Ea for both forward and backward reactions.
    • Does not alter the Gibbs energy change (ΔG) or enthalpy change (ΔH) of the reaction.
    • Does not make a non-spontaneous reaction spontaneous.

48. Energy Profile and Catalysis

  • In a two-step reaction mechanism, the activation energy of the forward reaction is E1 + E2 (measured from the reactant level to the highest peak). If the product lies above the reactant, the product is less stable (endothermic).
  • Catalyst: A positive catalyst provides an alternative path for the reaction with lower activation energy, thus lowering the peak of the energy profile diagram.

49. Activation Energy Calculation

  • Arrhenius equation for two temperatures: ln(k₂k₁) = EaR (T₂ − T₁T₁T₂).

50. Nuclear Forces

  • Postulated to be attractive forces between proton-neutron, neutron-neutron, and proton-proton within the nucleus.
  • 1021 times stronger than electrostatic forces.
  • Operate over a short range.
  • They do not follow the inverse square law.

51. Binding Energy (B.E.)

  • The energy released that stabilizes the nucleus by binding nucleons together.
E = Δmc2
E = Δm × 931.5 MeV (where Δm is in amu)

If Δm is in grams, E is in MeV per g-atom.

52. Stability of Nucleus

  • B.E. per nucleon = 28.144 = 7.03 MeV.
  • Conclusion: Higher binding energy per nucleon indicates greater nuclear stability.
  • Higher mass defect (Δm) corresponds to higher Energy (E).
Packing fraction = Actual isotopic mass − Mass numberMass number
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Neutron-Proton (n/p) Ratio & Calculations of Emissions

53. Neutron-Proton (n/p) Ratio

  • For atomic number < 20, the stable ratio is n/p = 1.
  • Examples: ₁H1 (n/p = 0); ₁H3 (n/p = 2).
  • The n/p ratio increases from 1.0 to 1.5 as atomic number increases.
  • Elements with n/p > 1.5 (atomic number ≥ 84) are radioactive, undergo spontaneous disintegration, and lie outside the belt of stability.

Graph: A plot of "Number of neutrons" vs "Number of protons" shows a stable region curve where the n/p ratio deviates from the n=p line as Z increases.

54. Disintegration and β-emission

  • Nature of disintegration depends on the n/p ratio.
  • If n/p is high, β-emission occurs to reduce the ratio (n decreases, p increases):
₀n1 → ₁H1 + −1e0
  • Examples:
    • ₆C14 → ₇N14 + −1e0 (n/p ratio changes from 1.3 to 1)
    • ₁₁Na24 → ₁₂Mg24 + −1e0 (n/p ratio changes from 13/11 to 1)

55. Alpha Emission

  • Emission of alpha particle (42He) is a form of natural radioactivity.
  • Effect on nucleus: Atomic number decreases by 2; Mass number decreases by 4.
  • Example: 23892U → 23490Th + 42He
  • Alpha particle = 42He++. It captures electrons from the atmosphere to convert into Helium gas.
  • Soddy-Fajan displacement rule: After alpha emission, the element shifts two places to the left in the periodic table (not applicable for f-block elements).

56. Positron & K-Electron Capture

  • Positron emission (artificial): 0+1e. The n/p ratio increases.
  • Examples:
    • 116C → 115B + 0+1e
    • 137N → 136C + 0+1e
  • K-electron capture (artificial): An electron from the K-shell is captured by the nucleus.
  • Example: 19479Au + 0-1e → 19478Pt

57. Beta Emission

  • Beta particle (0-1e) emission involves the process: 10n → 11H + 0-1e.
  • Effect on nucleus: No change in mass number; Atomic number increases by 1.
  • Example: 4019K → 4020Ca + 0-1e
  • Beta decay results in isobaric elements. The element shifts 1 unit to the right in the periodic table (not valid for f-block elements).

58. Calculations of Emissions

  • Number of alpha-particles emitted = change in mass number4.
  • Alpha-decay produces isodiapheres (nuclides with the same difference between neutron and proton numbers).
  • Example: 22688Ra → 22286Rn + 42He. (For both: n − p = 138 − 88 = 50 and 136 − 86 = 50).
  • Successive decay: Emission of 1 alpha and 2 beta particles in succession produces an isotope of the parent element.
23592U → α → 23190Th → 2β → 23192U (Isotope)

59. γ-Emission

  • It is electromagnetic radiation; charge-less and mass-less.
  • No change in atomic number, mass number, or position in the periodic table.
  • Only a change in the energy state of the nucleus is observed.
92U235 (Higher energy) → 92U235 (Lower energy) + γ

60. Radioactivity

  • Defined as the spontaneous disintegration of nuclei of certain elements by the ejection of α- or β-particles.
  • Rate is characteristic for each particular active isotope.
  • Radioactive changes are spontaneous and are not controlled by temperature, pressure, or the nature of chemical combination.
  • Heavy elements from Bismuth (At. No. 83) through Uranium possess radioactive properties.

61. Radioactive Decay Kinetics

  • Radioactive decay follows first-order kinetics:
−d[A]dt = k[A] ; At = A0·e−kt
t1/2 = 0.693k
  • Disintegration rate (Activity) is given by:
−dNdt = λN = Activity
  • Integrating −dN/dt = λN gives:
Nt = N0·e−λt

where λ = decay constant, Nt = no. of active nuclei left after time t.

  • Similarly for activity:
At = A0·e−λt

where At = activity after time t.

Page 8
Comparison of α, β and γ Rays & Quick Formula Revision

62. Comparison of α, β and γ Rays

Propertyα-Particleβ-Particleγ-Ray
Charge & Mass+2 charge, 4 mass−1 charge, 0 mass0 charge, 0 mass
Nature2He4 (He++)−1e0 (electron)0γ0
Magnetic FieldDeflected to cathodeDeflected to anodeNot deflected

γ-Rays are electromagnetic rays with very short wavelength (approx. 0.05 Å).

63. Properties of α, β, and γ Rays

Propertyα-rayβ-rayγ-ray
Velocity2.36 to 2.83 × 107 m/s2 × 107 to 2.83 × 108 m/s3 × 108 m/s
Ionizing powerVery high (100× β)Low (100× γ)Very low
ZnS plate effectLuminescenceVery littleVery little
Penetrating powerLow (stopped by air)100× α10× β
Kinetic energyHighVery lessZero

64. Units of Radioactivity

  • Curie (c): 1 c = 3.7 × 1010 dps.
  • Rutherford (rd): 1 rd = 106 dps.
  • Becquerel (Bq): 1 Bq = 1 dps (SI unit).
1 c = 103 mc = 106 μc
1 Bq = 1 μrd
106 Bq = 1 rd
3.7 × 1010 Bq = 1 c

Conversion Relations :

1 c = 3.7 × 104 rd
1 mc = 37 rd
1 μc = 37 mrd

65. Radioactive Disintegration Series

SeriesStartingFinalParticles
αβ
4n (Thorium)90Th23282Pb20864
4n+1 (Neptunium)94Pu241 (via 93Np237)83Bi20985
4n+2 (Uranium)92U23882Pb20686
4n+3 (Actinium)92U235 (via 89Ac227)82Pb20774

66. Quick Formula Revision

QuantityFormula
Rate (aA + bB → cC + dD)−(1/a) d[A]/dt = −(1/b) d[B]/dt = (1/c) d[C]/dt = (1/d) d[D]/dt
Rate lawrate = k[A]x[B]y ; order = x + y ; unit of k = (mol L−1)1−n time−1
Zero order[A]0 − [A]t = kt ; t1/2 = [A]0/2k ; t100% = [A]0/k
First orderkt = 2.303 log([A]0/[A]t) ; [A]t = [A]0e−kt ; t1/2 = 0.693/k
First order time ratiost75% = 2t1/2 ; t87.5% = 3t1/2 ; t99.9% ≈ 10t1/2
Second order1/[A]t − 1/[A]0 = kt ; t1/2 = 1/(k[A]0)
nth order half-lifet1/2 = (2n−1 − 1)/[(n − 1)k[A]0n−1] ; t1/2 ∝ [A]01−n
Property method (first order)k = (2.303/t) log[(x∞ − x0)/(x∞ − xt)]
A(g) → 2B(g) + C(g)k = (2.303/t) log[2P0/(3P0 − Pt)]
Parallel reactionsknet = k1 + k2 ; [B]/[C] = k1/k2 ; %B = 100k1/(k1 + k2)
Consecutive A → B → Ctmax = ln(k1/k2)/(k1 − k2) ; [B]max = [A]0(k2/k1)k2/(k1−k2)
Temperature coefficientk2/k1 = (T.C.)ΔT/10
Arrhenius equationk = Ae−Ea/RT ; log(k2/k1) = (Ea/2.303R)(1/T1 − 1/T2)
Catalystlog(kcat/k) = (Ea − E′a)/2.303RT
Radioactive decayNt = N0e−λt ; activity = λN ; t1/2 = 0.693/λ
Number of α and βα = ΔA/4 ; β = 2α − ΔZ

Key Points :

  • Order is found experimentally and can be zero, fractional or negative; molecularity applies only to elementary steps and is a whole number (1, 2 or 3).
  • For a complex reaction, the rate law comes from the slowest step; intermediates are replaced using the equilibrium constant of the preceding fast step.
  • Zero order: [A] vs t is a straight line; first order: ln[A] vs t is a straight line and t1/2 does not depend on [A]0.
  • If reactants are taken in stoichiometric ratio, all of them have the same half-life.
  • Pseudo first order: one reactant (e.g., water in ester hydrolysis or sucrose inversion) is in large excess, so its concentration stays constant.
  • A catalyst lowers Ea for both forward and backward reactions; it does not change ΔH, ΔG or the equilibrium constant.
  • Slope of ln k vs 1/T = −Ea/R; a steeper line means higher activation energy and greater sensitivity to temperature.
  • Effective collisions need enough energy (≥ threshold energy) and proper orientation.
  • Radioactive decay is first order and is not affected by temperature, pressure or chemical combination.
  • α-emission: Z − 2, A − 4; β-emission: Z + 1, A same; positron emission or K-capture: Z − 1, A same; γ-emission: no change.