C60H135O50N5 = 60 × 12 + 135 × 1 + 50 × 16 + 5 × 14
= 720 + 135 + 800 + 70
= 1725 g/mol = 1.725 kg/mol
Step 2: Write and Balance the Composting Reaction
C60H135O50N5 + a O2 → b CO2 + c H2O + d NH3
Balancing:
Carbon: 60 → b = 60
d = 5
2c + 3(5) = 135 ⟶ c = 60
50 + 2a = 2(60) + 60 ⟶ a = 65
Balanced equation:
C60H135O50N5 + 65 O2 → 60 CO2 + 60 H2O + 5 NH3
Step 3: Calculate Theoretical Oxygen Requirement
O2 required per mole waste = 65 moles × 32 g/mol = 2080 g = 2.08 kg
O2 per kg waste = 2.08 kg / 1.725 kg ≈ 1.206 kg O2 / kg waste
Step 4: Convert Oxygen to Air Requirement
Air = O2 required / % O2 in air = 1.206 / 0.23 ≈ 5.243 kg air / kg waste
Step 5: Apply 100% Excess Air
Actual air = Theoretical air × 2 = 5.243 × 2 ≈ 10.486 kg air / kg waste
Final Answer
10.5 kg air per kg waste
Match List-I with List-II
| List-I (Type of Waste) | List-II (Classification) |
|---|---|
| (A) Type 0 Waste | (III) Garbage |
| (B) Type 1 Waste | (II) Rubbish |
| (C) Type 2 Waste | (I) Trash |
| (D) Type 3 Waste | (IV) Refuse |
A particle dispersoid has 1510 spherical particles of uniform density. An air purifier is proposed to be used to remove these particles. The diameter-specific number of particles in the dispersoid, along with the number removal efficiency of the proposed purifier is shown in the following table:
The overall mass removal efficiency of the proposed purifier is ________% (rounded off to one decimal place).