The theoretical aerobic oxidation of biomass (C5H7O2N) is
\[ \mathrm{C_5H_7O_2N + 5\,O_2 \rightarrow 5\,CO_2 + NH_3 + 2\,H_2O} \]
Given a first-order biochemical oxidation with $k=0.23\ \text{d}^{-1}$ at $20^{\circ}$C (base $e$) and neglecting the second-stage oxygen demand, find the ratio BOD5 at $20^{\circ}$C to TOC (round to two decimals).
Atomic weights: C=12, H=1, O=16, N=14 g/mol
Step 1: Ultimate first-stage oxygen demand per mole of biomass
From the stoichiometry, 1 mol C5H7O2N requires 5 mol O2.
Mass of O2 demanded (ultimate, first-stage): L0 = 5 × 32 = 160 g O2 per mol biomass.
Step 2: BOD over 5 days for first-order kinetics.
BODt = L0(1-e-kt) with k=0.23 d-1 and t=5 d.
kt=1.15 ⇒ e-1.15≈0.316 ⇒ 1-e-1.15≈0.684.
Thus, BOD5 = 160 × 0.684 ≈ 109.44 g O2 per mol biomass.
Step 3: Total organic carbon (TOC) per mole of biomass.
Moles of C in C5H7O2N = 5 ⇒ mass of organic carbon = 5×12 = 60 g C per mol.
Step 4: Ratio.
\[ \frac{\text{BOD}_5}{\text{TOC}}=\frac{109.44}{60}\approx 1.824 \ \Rightarrow\ \boxed{1.82}\ (\text{to two decimals}). \]
| Component of MSW | Treatment/separation technique |
| P - Ferrous metals | i - Incineration |
| Q - Aluminum and copper | ii - Rapid composting |
| R- Food waste | iii - Eddy current separator |
| S-Cardboard | iv - Magnetic separator |
| Point | Staff Readings Back side | Staff Readings Fore side | Remarks |
|---|---|---|---|
| P | -2.050 | - | 200.000 |
| Q | 1.050 | 0.95 | Change Point |
| R | - | -1.655 | - |