| Stage | Cellular Location | Key Enzyme(s) that Produce Reduced Co‑enzymes | Reduced Co‑enzyme(s) Formed (per glucose) |
|---|---|---|---|
| Glycolysis (Embden‑Meyerhof pathway) | Cytosol | Glyceraldehyde‑3‑phosphate dehydrogenase | 2 NADH |
| Link reaction (pyruvate → acetyl‑CoA) | Mitochondrial matrix | Pyruvate dehydrogenase complex | 2 NADH |
| Krebs (citric acid) cycle | Mitochondrial matrix | Isocitrate dehydrogenase, α‑ketoglutarate dehydrogenase, succinate dehydrogenase | 6 NADH + 2 FADH2 |
| Oxidative phosphorylation (ETC & ATP synthase) | Inner mitochondrial membrane | Complex I–V, ubiquinone, cytochrome c | Energy from NADH/FADH2 used to make ATP |
The two co‑enzymes act as reversible electron carriers:
NAD+ + 2e⁻ + H⁺ ⇌ NADH (accepts two electrons and one proton)
FAD + 2e⁻ + 2H⁺ ⇌ FADH2 (accepts two electrons and two protons)
In glycolysis, the link reaction and the Krebs cycle these reductions store the energy of the electrons for transport to the inner mitochondrial membrane.
The ETC consists of four large protein complexes plus a fifth complex that synthesises ATP. Mobile carriers shuttle electrons between the complexes.
| Complex / Carrier | Source of Electrons | Primary Function | Protons Pumped (per pair of e⁻) |
|---|---|---|---|
| Complex I – NADH‑ubiquinone oxidoreductase | NADH (matrix) | Transfers electrons to ubiquinone (Q) → QH2 | 4 |
| Complex II – Succinate‑ubiquinone oxidoreductase | FADH2 (produced by succinate dehydrogenase) | Reduces Q to QH2 | 0 (no proton pumping) |
| Ubiquinone (Q) | Mobile lipid‑soluble carrier | Shuttles electrons from Complex I or II to Complex III | – |
| Complex III – Cytochrome bc1 complex | QH2 | Transfers electrons to cytochrome c; pumps protons | 4 |
| Cytochrome c | Mobile water‑soluble carrier | Carries electrons from Complex III to Complex IV | – |
| Complex IV – Cytochrome c oxidase | Cytochrome c (reduced) | Final electron acceptor: O2 + 4e⁻ + 4H⁺ → 2H2O; pumps protons | 2 |
| Complex V – ATP synthase | Uses the proton‑motive force | ADP + Pi + 4H⁺out → ATP + H₂O + 3H⁺in | – (synthesises ATP) |
Electrons travelling from NADH (Complex I) or FADH2 (Complex II) to O₂ release free energy that is used to pump protons from the matrix into the inter‑membrane space. The resulting electrochemical gradient (the proton‑motive force) drives Complex V, producing ATP from ADP and inorganic phosphate.
| Electron Donor | Complex of Entry | Total Protons Pumped (per pair of e⁻) | P/O Ratio* (ATP per donor) |
|---|---|---|---|
| NADH | Complex I | 4 (I) + 4 (III) + 2 (IV) = 10 | ≈ 2.5 ATP |
| FADH2 | Complex II | 0 (II) + 4 (III) + 2 (IV) = 6 | ≈ 1.5 ATP |
*The Cambridge syllabus expects the rounded figures 2.5 ATP per NADH and 1.5 ATP per FADH2.
Sample calculation – ATP from one molecule of glucose (aerobic)
When O₂ is unavailable the ETC cannot re‑oxidise NADH. Glycolysis would soon stop because NAD⁺ is depleted. Fermentation provides an alternative electron acceptor, regenerating NAD⁺ and allowing glycolysis to continue.
Pyruvate + NADH → Lactate + NAD⁺ (catalysed by lactate dehydrogenase). Net ATP from glycolysis = 2 ATP per glucose.
Pyruvate → Acetaldehyde + CO₂ (pyruvate decarboxylase);
Acetaldehyde + NADH → Ethanol + NAD⁺ (alcohol dehydrogenase). Net ATP = 2 ATP per glucose.
Because oxidative phosphorylation does not occur, the P/O contribution is zero, reducing the total ATP yield from ~30 ATP (aerobic) to only the 2 ATP obtained by substrate‑level phosphorylation.
RQ = CO₂ produced ÷ O₂ consumed. The value depends on the type of substrate oxidised because different substrates generate different numbers of NADH and FADH2.
| Substrate | Typical RQ | Reason (relative NADH/FADH2 production) |
|---|---|---|
| Glucose (C₆H₁₂O₆) | ≈ 1.0 | Complete oxidation yields equal moles of CO₂ and O₂ consumption (6 CO₂, 6 O₂). NADH dominates, giving a high O₂ demand. |
| Palmitate (C₁₆H₃₂O₂) | ≈ 0.7 | β‑oxidation produces relatively more FADH₂ than NADH, requiring less O₂ per CO₂ released. |
RQ calculation example – Glucose
Complete aerobic oxidation: C₆H₁₂O₆ + 6 O₂ → 6 CO₂ + 6 H₂O
RQ = 6 CO₂ ÷ 6 O₂ = 1.0
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