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Alkane → haloalkane: reaction and conditions?
Free-radical substitution; Cl₂ or Br₂ and UV light.
Haloalkane → alkane: reverse route?
Reduction (e.g. hydrogenolysis with H₂ and suitable catalyst); extension, not simply reverse UV substitution.
Alkene → alkane?
Hydrogenation: H₂, Ni catalyst, heat.
Alkane → alkene?
Cracking or catalytic dehydrogenation under suitable industrial conditions; not a simple reverse hydrogenation.
Alkene → haloalkane?
Hydrohalogenation: add HX (HCl, HBr); electrophilic addition.
Haloalkane → alkene?
Elimination: ethanolic KOH, heat/reflux.
Alkene → dihaloalkane?
Add Br₂ or Cl₂ across C=C; electrophilic addition.
Dihaloalkane → alkene?
Reductive dehalogenation, e.g. Zn; extension.
Alkene → alcohol?
Hydration: steam, H₃PO₄ catalyst, high temperature and pressure (ethene: ~300°C, 6–7 MPa).
Alcohol → alkene?
Dehydration/elimination: concentrated H₂SO₄ and heat (or heated Al₂O₃).
Haloalkane → alcohol?
Nucleophilic substitution: aqueous NaOH/KOH, heat.
Alcohol → haloalkane?
Substitution using HX or suitable halogenating reagent; e.g. ethanol + HBr → bromoethane + water.
Primary alcohol → aldehyde?
Oxidise using acidified K₂Cr₂O₇; warm and distil aldehyde as it forms.
Aldehyde → primary alcohol?
Reduction: NaBH₄ (commonly aqueous/alcoholic solvent).
Aldehyde → carboxylic acid?
Oxidise using acidified K₂Cr₂O₇; heat under reflux.
Carboxylic acid → aldehyde?
Not a straightforward reverse of oxidation; specialised partial reduction, extension.
Primary alcohol → carboxylic acid?
Oxidise using excess acidified K₂Cr₂O₇ and reflux.
Carboxylic acid → primary alcohol?
Reduction using LiAlH₄ followed by work-up; extension.
Secondary alcohol → ketone?
Oxidise using acidified K₂Cr₂O₇ and heat/reflux.
Ketone → secondary alcohol?
Reduction using NaBH₄.
Can tertiary alcohols be oxidised readily with acidified dichromate?
No: they lack a hydrogen on the carbon bearing OH; no straightforward oxidation under normal school conditions.
Carboxylic acid + alcohol → ester?
Esterification: concentrated H₂SO₄ catalyst, heat/reflux; produces ester + water.
Ester → carboxylic acid + alcohol?
Acid hydrolysis: dilute aqueous acid, heat/reflux; reversible.
Ester → carboxylate + alcohol?
Base hydrolysis/saponification: aqueous NaOH, heat/reflux; acidify carboxylate to obtain carboxylic acid.
Haloalkane → primary amine?
Nucleophilic substitution with excess ethanolic ammonia, heat (often sealed/under pressure).
Primary amine → haloalkane?
No standard simple reverse of ammonia substitution; do not assume same conditions backwards.
Carboxylic acid + amine → amide?
Amide formation requires suitable activation/dehydrating conditions or an acyl chloride; simply mixing usually first forms an ammonium carboxylate salt.
Acyl chloride + amine → amide?
Nucleophilic acyl substitution; typically room temperature, with base/excess amine to neutralise HCl.
Amide → carboxylic acid + amine/ammonium?
Hydrolysis: aqueous acid, heat/reflux; products depend on pH.
Amide → carboxylate + amine?
Base hydrolysis: aqueous NaOH, heat/reflux.
Alkene → addition polymer?
Addition polymerisation: C=C opens to form saturated backbone; conditions depend on monomer and catalyst/initiator.
Addition polymer → original alkene?
Not a standard simple reversible reaction; chemical recycling/depolymerisation needs specialised conditions.
Diol + dicarboxylic acid → polyester?
Condensation polymerisation; ester links form and small molecules (usually water) are eliminated.
Diamine + dicarboxylic acid → polyamide?
Condensation polymerisation under suitable heating/process conditions; amide links form and water is eliminated.
Polyester → monomers?
Hydrolysis of ester links using acid/base and heat; products depend on conditions.
Polyamide → monomers?
Hydrolysis of amide links using acid/base and heat; products depend on conditions.
Haber: equation?
N₂(g) + 3H₂(g) ⇌ 2NH₃(g); forward reaction exothermic.
Haber: typical temperature, pressure and catalyst?
~400–500°C, ~20 MPa, iron-based catalyst.
Why does high pressure favour ammonia?
4 mol gaseous reactants → 2 mol gaseous products; higher pressure shifts equilibrium right.
Why not use very low temperature for Haber?
Lower T favours exothermic forward equilibrium but slows reaction rate; compromise needed.
How is Haber overall conversion improved?
Cool/condense and remove NH₃; recycle unreacted N₂ and H₂.
Contact stage 1: equation?
S(s) + O₂(g) → SO₂(g); burn sulfur in air/oxygen.
Contact stage 2: equation and catalyst?
2SO₂(g) + O₂(g) ⇌ 2SO₃(g); exothermic, V₂O₅ catalyst.
Contact stage 2: temperature and pressure?
~450°C; typically near atmospheric or modest pressure. Check your course text for its inconsistent pressure figures.
Why does pressure favour SO₃?
3 mol gaseous reactants → 2 mol gaseous products; increasing pressure shifts equilibrium right.
Contact stage 3: why not add SO₃ straight to water?
Direct reaction forms difficult-to-control acid mist; absorb SO₃ in concentrated H₂SO₄ to make oleum first.
Contact: oleum equations?
SO₃ + H₂SO₄ → H₂S₂O₇; then H₂S₂O₇ + H₂O → 2H₂SO₄.
Fermentation: overall equation and conditions?
C₆H₁₂O₆ → 2C₂H₅OH + 2CO₂; yeast/zymase, anaerobic, warm conditions.
What is saccharification?
Enzymatic hydrolysis of polysaccharides such as starch into smaller soluble sugars; amylase is an example.
Why does fermentation stop and how is ethanol concentrated?
Accumulated ethanol inhibits yeast (textbook ~13%, variable); distillation increases ethanol concentration.
Ethene hydration: equation and conditions?
C₂H₄(g) + H₂O(g) ⇌ C₂H₅OH(g); H₃PO₄ catalyst, ~300°C, 6–7 MPa.
Hydration vs fermentation: key difference?
Hydration uses ethene/steam, high T/P and acid catalyst; fermentation uses sugar/yeast and anaerobic warm conditions.
Hydrogen fuel cell: anode half-equation (acidic PEM)?
H₂ → 2H⁺ + 2e⁻; oxidation at anode.
Hydrogen fuel cell: cathode half-equation (acidic PEM)?
O₂ + 4H⁺ + 4e⁻ → 2H₂O; reduction at cathode.
Hydrogen fuel cell: overall equation?
2H₂ + O₂ → 2H₂O; electrons travel through external circuit.
Catalyst effect on equilibrium yield?
Catalyst speeds both directions and attainment of equilibrium; does not change equilibrium constant or equilibrium yield.