The aeration system is a crucial component in water treatment processes, used to introduce air or oxygen into the water body to support the growth of beneficial microorganisms and facilitate the degradation of pollutants. The aeration process provides oxygen to meet the microbial oxygen demand, enabling efficient breakdown of organic matter. The Aeration Volume Calculator Is A Highly Valuable Tool That Aids Engineers And Water Treatment Professionals In Determining The Required Aeration Volume. This calculator takes into account factors such as water volume, pollutant concentrations, desired oxygen transfer efficiency, and the type of aeration equipment used. Accurate aeration volume calculations help optimize the design of aeration systems, leading to improved water treatment efficiency while reducing energy consumption and operational costs. Such calculators play a vital role in water treatment engineering, contributing significantly to environmental preservation and the provision of clean water resources.
The Following Is Juntai For You To Sort Out The Correct Way To Calculate The Amount Of Aeration:
- Blue Block Is The Design Datameter : Be Filled In
- Brown: Calculate Process Data
- Red : Last Result For Your Process
1. Aerobic Tank Volume Calculation
1.Aerobic Tank Volume Calculation | ||
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Calculation Formula | ||
Design parameters: | ||
Qmax | 150 | Daily sewage design flow, m3/d |
So | 400 | Sewage untreated for five days - (BOD5 concentration), mg/l |
Se | 20 | Five days after treatment - (BOD5 concentration), mg/l |
BODSS | 0.12 | Sludge load, kg-BOD/kg·MLSS/day |
MLSS | 4000 | Sludge concentration, mg/l |
Result | 118.75 | M3 |
2. Denitrification Cabinet Volume Calculation
2.Denitrification Cabinet Volume Calculation |
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Calculation Formula | ||
Design parameters: | ||
NIKN | 250 | Concentration of ammonia nitrogen in treated effluent, mg/l |
NETN | 30 | Concentration of ammonia nitrogen in treated effluent, mg/l |
MDNL | 0.5 | Sludge denitrification load, kg-NH3-N/kg·MLSS/day |
MLSS | 3000 | Sludge concentration, mg/l |
Result | 22 | M3 |
3. Aeration Calculation
3.Aeration Calculation | ||
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Calculation Formula | ||
Design parameters: | ||
Ro2- | 172.35 | Design sewage oxygen demand, kgO2/d |
So- | 400 | Five-day biochemical oxygen demand of influent water, mg/L |
Se- | 20 | Five-day biochemical oxygen demand of effluent, mg/L |
△Xv- | 11.08 | Amount of microorganisms discharged from the oxidation tank to the system, kg/d |
Nk | 275 | Total Kjeldahl nitrogen in influent, mg/L |
Nke- | 45 | Total Kjeldahl nitrogen in effluent, mg/L |
Nt- | 275 | Total nitrogen in influent, mg/L |
Noe- | 21 | Amount of nitrate nitrogen in effluent, mg/L |
a- | 1.47 | Carbon equivalent, when the carbonaceous material is measured in terms of five-day biochemical oxygen demand, take 1.47 |
b- | 4.57 | Constant, oxygen demand for oxidizing each kilogram of ammonia nitrogen, kgO2/kgN, take 4.57. |
c- | 1.42 | Constant, oxygen content of bacterial cells, taken as 1.42 |
d- | 0.08 | Constant, sludge auto-oxidation rate, taken as 0.08 |
N'- | 2.8 | Average concentration of volatile suspended solids in the mixture (g vss/L) at 70% of the sludge volume |
θ- | 30 | Sludge age, 30d |
Result |
172.3518987 |
kgO2/d |
4. Absolute Pressure Calculation
4.Absolute Pressure Calculation | ||
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Calculation Formula | ||
Design parameters: | ||
Pb- | 133040 | Absolute pressure at which the aeration device is located, Pa |
H- | 4.3 | Aeration diffuser gas port at the water depth, m (water depth minus the aeration disc installation height, according to the depth of the tank accounting) |
P- | 90900 | Atmospheric pressure, Pa (actual atmospheric pressure at location) |
Result | 133040 | Pa |
5.Calculation Of Oxygen Content In Per Cent
5.Calculation Of Oxygen Content In Per Cent | |||
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Calculation Formula | |||
Design parameters: | |||
Ot- | 16.62% | Percentage of oxygen in the gas escaping from the aeration basin, dimensionless | |
EA- | 25% | Transfer coefficient of diffusion device, % oxygen utilisation (value selected with reference to technical parameters provided by SSI manufacturer) |
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Result | 0.166226913 |
6. Calculation Of Average Dissolved Value
6. Calculation Of Average Dissolved Value | ||
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Calculation Formula | ||
Design parameters: | ||
Csm | 8.82 | T℃、Average dissolved value of clear water from the depth of the water under which the actual aeration device is located to the surface of the pool, mg/1TC, |
Csw | 8.38 | T℃、Saturated dissolved oxygen on the surface of clear water at actual calculated pressure, mg/1(CS(20)=9.17mg/L,CS(25)=8.38mg/L) |
T- | 25 | ℃ |
Result | 8.818924806 | mg/L |
7. Calculation Of Oxygen Demand Correction Factor
7. Calculation Of Oxygen Demand Correction Factor | ||
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Calculation Formula | ||
Design parameters: | ||
KO- | 1.715 | Oxygen demand correction factor |
Co- | 2 | Remaining dissolved oxygen concentration of mixed liquid, mg/L |
Cs | 9.17 | Saturated dissolved oxygen mass concentration in clear water under standard condition, mg/L |
α- | 0.8 | Transfer efficiency resistance coefficient, the influence of the nature of wastewater on dissolved oxygen, correction factor K1a |
Raw domestic sewagea value of about 0.4~0.5 | ||
Industrial wastewatera value varies greatly 0.8~0.85 | ||
The effect of salts in wastewater on dissolved oxygen, saturated oxygen resistance factor | ||
β- | 0.9 | β value is generally between 0.9~0.97 |
Result | 1.71 |
8. (Calculated On 24h Basis) Aeration Basin Air Supply Volume Aeration Basin Air Supply Volume Calculation
8. (Calculated On 24h Basis) Aeration Basin Air Supply Volume Aeration Basin Air Supply Volume Calculation | ||
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Calculation Formula | ||
Design parameters: | ||
Ro | 295.52 | kgO2/d |
Gs | 12.31 | kgO2/h Aeration basin gas supply (24h) |
Gs | 175.91 | m3/h |
Gs- | 2.93 | m3/min |
Calculation Formula | ||
Design parameters: | ||
Gs max | 3.66 | m3/min |
Gs max | 219.88 | m3/h |
9. Air Pressure Required For Aeration P (Relative Pressure)
9. Air Pressure Required For Aeration P (Relative Pressure) | ||
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Calculation Formula | P=h1+h2+h3+h4+△h | |
Design parameters: | ||
h1+h2 | 0.2 | m(Duct length and local resistance) |
h3 | 4.3 | m(Aeration head submergence depth) |
h4 | 0.3 | m(Aerator resistance) |
△h | 0.5 | m(Have a high head of water) |
P | 5.3 | m(Total air pressure0.53kg/m2) |