Alkanes: properties, reactions, mechanisms

Alkanes – Properties, Production, Reactions & Mechanisms (Cambridge AS & A‑Level Chemistry 9701)

1. General Features

  • Alkanes are the simplest saturated hydrocarbons. General formula: CnH2n+2 (n ≥ 1).
  • All C–C and C–H bonds are single σ‑bonds; the carbon atoms are sp³ hybridised.
  • Consequences:
    • Non‑polar molecules – only London dispersion forces act between them.
    • Relatively low reactivity compared with alkenes, alkynes and aromatics.
    • Colourless gases or liquids at 25 °C; major components of natural gas and petroleum.

2. Production of Alkanes

2.1 Catalytic Hydrogenation of Alkenes

Alkenes are converted into the corresponding alkanes by adding H₂ across the C=C bond.

C2H4 + H2 \xrightarrow[\Delta]{\text{Pt, Ni, Pd}} C2H6

Typical conditions: 150–300 °C, 1–5 atm H₂, metal catalyst (Pt, Ni **or** Pd). The reaction is exothermic and proceeds via adsorption of H₂ on the metal surface followed by syn‑addition to the double bond.

2.2 Cracking of Long‑Chain Alkanes

Cracking deliberately breaks C–C bonds in heavy n‑alkanes to give shorter‑chain alkanes (and alkenes). Two industrial variants are used.

Type Typical Temperature Pressure Catalyst / Conditions Typical Products
Thermal cracking ≥ 500 °C (often 600–800 °C) Atmospheric (≈ 1 atm) No catalyst; rapid heating in a furnace Mixture of alkanes + alkenes (e.g., C₁₀H₂₂ → C₆H₁₄ + C₄H₈)
Catalytic cracking ≈ 450 °C (400–500 °C) 1–3 atm (often under slight excess H₂) Solid acid catalysts – zeolites (e.g., H‑ZSM‑5, H‑β), silica‑alumina, or AlCl₃‑based systems Predominantly alkanes (e.g., C₈H₁₈ → 2 C₄H₁₀) and valuable light alkenes (ethylene, propene)

Both routes are exploited to produce LPG (propane, butane) and to generate feed‑stock alkenes for polymer manufacture.

3. Physical & Structural Properties

3.1 General Trends

  • Inter‑molecular forces: Only London dispersion forces → low boiling points for small alkanes.
  • Boiling point, melting point & density increase steadily with molecular size (more electrons → stronger dispersion forces).
  • Solubility: Insoluble in water; soluble in non‑polar organic solvents (benzene, ether, carbon tetrachloride).
  • Isomerism: Only structural (chain) isomerism. No geometric or optical isomerism because every carbon is tetra‑substituted with single bonds.

3.2 Representative Physical Data

Alkane Formula Molar Mass (g mol⁻¹) Boiling Point (°C) State at 25 °C
MethaneCH₄16.04-161.5Gas
EthaneC₂H₆30.07-88.6Gas
PropaneC₃H₈44.10-42.1Gas
ButaneC₄H₁₀58.12-0.5Gas (n‑butane) / Liquid (i‑butane)
HexaneC₆H₁₄86.1868.7Liquid
OctaneC₈H₁₈114.23125.6Liquid
DecaneC₁₀H₂₂142.29174.0Liquid

4. Main Reactions of Alkanes

4.1 Combustion

  1. Complete combustion (excess O₂)

    CnH2n+2 + \left(n+\tfrac12\right) O₂ \rightarrow n CO₂ + (n+1) H₂O \quad \Delta H < 0

    Produces carbon dioxide, water and a large amount of heat – the basis of fuel‑energy applications.

  2. Incomplete combustion (limited O₂)

    CnH2n+2 + \tfrac{3n+1}{2} O₂ \rightarrow n CO + (n+1) H₂O \; (+\; \text{soot})

    Gives toxic carbon monoxide and carbon (soot), both hazardous.

4.2 Free‑Radical Halogenation (Substitution)

General equation (X = Cl or Br):

CnH2n+2 + X₂ \xrightarrow{hu} CnH2n+1X + HX

The reaction proceeds by a radical chain mechanism (see Section 5). Chlorination is fast and non‑selective; bromination is slower and more selective.

4.3 Industrial Cracking (Re‑visited)

  • Deliberate production of LPG (propane, butane) and light alkenes (ethylene, propene).
  • Thermal cracking favours formation of alkenes; catalytic cracking, because of acid sites, gives a higher proportion of saturated products.

4.4 Catalytic Reforming

Heavy n‑alkanes are converted into branched alkanes and cycloalkanes using platinum‑group metal catalysts (Pt, Pt‑Re, Pt‑Os) at 500 °C and 1–2 atm H₂. The process raises the octane rating of gasoline and supplies cycloalkanes for petrochemical synthesis.

5. Mechanism of Free‑Radical Halogenation

5.1 Chain‑Reaction Overview

  1. Initiation – homolytic cleavage of X₂ under UV light.
  2. Propagation – alternating hydrogen abstraction and radical substitution.
  3. Termination – combination of two radicals, removing them from the chain.

5.2 Detailed Steps

5.2.1 Initiation

X₂ \xrightarrow{hu} 2\,X^\bullet

5.2.2 Propagation
  1. Hydrogen abstraction
    CnH2n+2 + X^\bullet \rightarrow CnH2n+1^\bullet + HX
  2. Radical substitution
    CnH2n+1^\bullet + X₂ \rightarrow CnH2n+1X + X^\bullet
5.2.3 Termination

Any two radicals may combine:

X^\bullet + X^\bullet \rightarrow X₂

CnH2n+1^\bullet + X^\bullet \rightarrow CnH2n+1X

CnH2n+1^\bullet + CmH2m+1^\bullet \rightarrow Cn+mH2(n+m)+2

5.3 Selectivity – Influence of Radical Stability

Relative stability of carbon‑centred radicals governs the rate of hydrogen abstraction:

tert‑> sec‑> prim‑> methyl

Consequences:

  • Hydrogen atoms on tertiary carbons are abstracted fastest; primary hydrogens are the slowest.
  • Product distribution mirrors radical stability. Example – chlorination of isobutane (2‑methylpropane) gives predominantly tert‑butyl chloride because the tertiary radical is most stable.
  • For bromination, the higher activation energy accentuates this selectivity, often giving > 90 % of the most substituted product.

5.4 Energy Profile (illustrative)

Energy diagram showing initiation, two propagation steps and termination; relative radical stabilities indicated.
Typical energy profile for a free‑radical halogenation. The first propagation step (hydrogen abstraction) is endothermic; the second (radical substitution) is exothermic, giving an overall exothermic chain.

6. Summary of Key Points

  • Alkanes are saturated, non‑polar hydrocarbons with formula CnH2n+2.
  • Physical properties (boiling point, density, solubility) depend solely on molecular size and dispersion forces.
  • Industrial production:
    • Hydrogenation of alkenes (catalysts: Pt, Ni **or** Pd; 150–300 °C, 1–5 atm H₂).
    • Thermal cracking (≥ 500 °C, no catalyst) and catalytic cracking (≈ 450 °C, solid acid catalysts such as zeolites).
  • Key reactions:
    • Complete and incomplete combustion – source of energy and a safety hazard.
    • Free‑radical halogenation – radical chain mechanism; product ratios predicted from radical stability.
    • Cracking – industrial source of LPG and light alkenes.
    • Catalytic reforming – improves octane rating and provides cycloalkanes.
  • Understanding the radical chain (initiation → propagation → termination) enables accurate prediction of both the rate and the selectivity of halogenation reactions.

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