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
Length of the streets, in km, are shown on the network. The minimum distance travelled by the sweeping machine for completing the job of sweeping all the streets is ________ km. (rounded off to nearest integer)
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).