12.7 Process Control Mathematics: Loading, Efficiency, Removal & Solids
Key Takeaways
- Removal efficiency equals (influent minus effluent) divided by influent, times 100, and is applied to BOD, TSS, and any other parameter measured on both sides of a process.
- Organic loading rate equals pounds of BOD per day divided by the treatment volume, expressed per 1,000 cubic feet for fixed film or per acre-foot for lagoons.
- Solids loading rate on a secondary clarifier uses the combined influent and return activated sludge flow times the MLSS concentration times 8.34, divided by the clarifier surface area.
- Percent volatile solids reduction in digestion uses the Van Kleeck relationship, which corrects for the fact that only volatile matter is destroyed while fixed solids remain.
- Sludge pumping mass equals gallons pumped times 8.34 times percent solids expressed as a decimal, times specific gravity when it differs meaningfully from 1.0.
12.7 Process Control Mathematics: Loading, Efficiency, Removal & Solids
Every North Carolina needs-to-know document lists mathematics as a required subject, and the examinations provide a state formula sheet. Knowing which formula applies — and what each variable means — is the actual skill being tested.
1. Removal efficiency
Example. Influent BOD 240 mg/L, effluent BOD 12 mg/L:
(240 − 12) ÷ 240 × 100 = 95.0 percent removal
The same relationship works on mass (pounds per day), which is what you use when flows differ between the two sampling points. North Carolina secondary treatment permits typically require a minimum 85 percent removal of BOD and TSS in addition to the concentration limits.
2. Loading rates
| Rate | Formula | Typical units |
|---|---|---|
| Hydraulic loading | Flow ÷ surface area | gpd/ft² |
| Organic loading (fixed film) | lb BOD/day ÷ media volume | lb BOD/day per 1,000 ft³ |
| Organic loading (lagoon) | lb BOD/day ÷ surface area | lb BOD/day per acre |
| Solids loading (clarifier) | lb solids/day ÷ surface area | lb/day/ft² |
| Weir overflow rate | Flow ÷ weir length | gpd/linear ft |
| Filtration rate | Flow ÷ filter area | gpm/ft² |
| Backwash rate | Backwash flow ÷ filter area | gpm/ft² |
Worked example — solids loading rate on a secondary clarifier. A 65-foot diameter clarifier receives 2.4 MGD of plant flow plus 1.2 MGD of RAS, with MLSS at 3,100 mg/L.
- Area = 0.785 × 65² = 0.785 × 4,225 = 3,316.6 ft²
- Solids applied = (2.4 + 1.2) MGD × 3,100 mg/L × 8.34 = 3.6 × 3,100 × 8.34 = 93,074 lb/day
- SLR = 93,074 ÷ 3,316.6 = 28.1 lb/day/ft²
That sits at the upper end of the usual 20 to 30 lb/day/ft² design range — a number worth watching if the sludge blanket is rising.
3. Sludge mass and volume
Example. 12,000 gallons of primary sludge at 4.5 percent solids (specific gravity taken as 1.02):
12,000 × 8.34 × 0.045 × 1.02 = 4,593 lb of dry solids
Volume change with thickening uses the inverse relationship between concentration and volume:
Thickening 30,000 gallons of 1.0 percent WAS to 5.0 percent gives 30,000 × (1.0 ÷ 5.0) = 6,000 gallons — an 80 percent volume reduction.
4. Volatile solids reduction (the Van Kleeck formula)
Because digestion destroys volatile matter but leaves fixed solids behind, a simple before-and-after comparison of volatile percentages understates the destruction. The standard correction is:
where V is the volatile fraction expressed as a decimal.
Example. Feed sludge is 72 percent volatile (0.72); digested sludge is 52 percent volatile (0.52):
- Numerator: 0.72 − 0.52 = 0.20
- Denominator: 0.72 − (0.72 × 0.52) = 0.72 − 0.3744 = 0.3456
- %VSR = 0.20 ÷ 0.3456 × 100 = 57.9 percent
That comfortably exceeds the 38 percent minimum used for the volatile solids reduction option under the federal vector attraction reduction requirements.
5. Blending, dilution, and chemical strength
The blending (mixture) equation:
Example. 4,000 gallons of 12.5 percent hypochlorite is blended with 1,000 gallons of water:
(4,000 × 12.5) + (1,000 × 0) = 5,000 × C → 50,000 = 5,000C → C = 10.0 percent
Chemical usage tracking. Pounds of chemical used per day divided by pounds of a target parameter removed per day gives a chemical efficiency figure that is far more useful for budgeting and troubleshooting than raw consumption. A rising alum-per-pound-of-turbidity figure means the water changed or the feed system is losing accuracy.
6. Detention time and hydraulic checks
Use it to sanity-check process problems: if a clarifier's detention time has fallen from 2.4 hours to 1.1 hours because the plant is passing wet weather flow, the solids carryover is hydraulic, not biological, and no amount of wasting adjustment will fix it.
7. Working an exam math problem
- Write down what is asked, with units.
- List the given values, converting to the units the formula expects — MGD, mg/L, feet, and gallons are the usual offenders.
- Select the formula from the state formula sheet, and confirm the variables mean what you think.
- Solve stepwise, carrying units through the arithmetic.
- Sanity-check the answer: is an F/M of 12 plausible? Is a detention time of 0.02 hours plausible? A wrong unit conversion almost always produces an answer that is off by a factor of 10, 8.34, 1,440, or 7.48 — learn to recognize those fingerprints.
[!NOTE] Common conversions worth memorizing: 8.34 lb/gal; 7.48 gal/ft³; 62.4 lb/ft³; 1,440 min/day; 694.4 gpm per MGD; 1.547 cfs per MGD; 43,560 ft² per acre; 325,851 gallons per acre-foot; 2.31 ft of head per psi; 0.433 psi per foot of head.
A digester feed sludge is 70 percent volatile solids and the digested sludge is 48 percent volatile solids. Using the Van Kleeck relationship, what is the percent volatile solids reduction?
A 60-foot diameter secondary clarifier receives 1.8 MGD of plant flow plus 0.9 MGD of RAS, with MLSS at 2,900 mg/L. What is the solids loading rate?
An operator blends 3,000 gallons of 12.5 percent sodium hypochlorite with 2,000 gallons of water. What is the strength of the blended solution?