English
عربى
Español
| Hangzhou AquaSust Water Technology Co., Ltd. Head ofice: #2808, Baiyue Center, Linping, Hangzhou, Zhejiang, China M:+86 152 6746 2807 Email: [email protected] website: www.nihaowater.com www.chinambbr.com www.aquasust.com www.aquasustfactory.com |
||||||||
| Paper Wastewater Operating Cost Calculator | ||||||||
| Blue block is the design datameter: be filled in Brown:calculate process data Red:last result for your process |
||||||||
| I.Basic data: | ||||||||
| Designed Water Quantity | 35000.00 | m³/d | ||||||
| Project | COD(mg/l) | BOD(mg/l) | ammonia nitrogen(mg/l) | SS(mg/l) | total phosphorus(mg/l) | |||
| nlet water quality | 1000.00 | 500.00 | 100.00 | 500.00 | 20.00 | |||
| Efluent water quality | 50.00 | 10.00 | 5.00 | 10.00 | ||||
| II.Calculations: | ||||||||
| 1. Calculation of labor costs | ||||||||
| Total number of people | 10.00 | people | payroll | 2000.00 | Yuan/month | Cost of tonnes of water | 0.019 | Yuan/Ton |
| 2. Calculation of electricity costs | ||||||||
| Running power | 1273.00 | KW | Unit electricity costs | 0.50 | Yuan/KW.h | Cost of tonnes of water | 0.436 | Yuan/Ton |
| 3. Pre-treatment chemicals cost | ||||||||
| PAC addition amount | 100.00 | ppm | unit cost | 1350.00 | Yuan/Ton | Cost of tonnes of water | 0.135 | Yuan/Ton |
| Amount of PAM added | 12.00 | ppm | unit cost | 15500.00 | Yuan/Ton | Cost of tonnes of water | 0.186 | Yuan/Ton |
| 4. Biochemical treatment chemicals | ||||||||
| Design Data | ||||||||
| Oxidation ditch influent BOD | 690.00 | mg/l | ammonia nitrogen | 1.00 | mg/l | total phosphorus | 1.000 | mg/l |
| Required carbon, nitrogen, and phosphorus ratio | 100.00 | 5.00 | 1.000 | |||||
| Actual amount of nutrients needed | nitrogen source | 33.50 | mg/l | quantity of phosphorus source | 5.900 | mg/ | ||
| When phosphorus source is(NH2)2HPO4 | Nitrogen content | 0.22 | phosphorus content | 0.24 | ||||
| (NH2)2HPO4 addition amount | 24.58 | mg/l | unit cost | 2300.00 | Yuan/Ton | Cost of tonnes of water | 0.057 | Yuan/Ton |
| When nitrogen source is CO(NH2)2 | Nitrogen content | 0.43 | ||||||
| CO(NH2)2 additionamount | 65.63 | mg/l | unit cost | 1660.00 | Yuan/Ton | Cost of tonnes of water | 0.109 | Yuan/Ton |
| When the phosphorus source is Na3PO4 | Purity | 0.98 | phosphorus content | 0.08 | ||||
| Amount of Na3PO4 added | 75.26 | mg/l | unit cost | 2990.00 | Yuan/Ton | Cost of tonnes of water | 0.225 | Yuan/Ton |
| Addition of CO(NH2)2 | 78.27 | mg/l | unit cost | 1660.00 | Yuan/Ton | Cost of tonnes of water | 0.130 | Yuan/Ton |
| 5. Cost of deep treatment chemicals | ||||||||
| PAC additive amount | 360.00 | mg/l | unit cost | 1350.00 | Yuan/Ton | Cost of tonnes of water | 0.486 | Yuan/Ton |
| Amount of PAM added | 2.00 | mg/l | unit cost | 15500.00 | Yuan/Ton | Cost of tonnes of water | 0.031 | Yuan/Ton |
| Addition of ferrous chemicals | 600.00 | mg/l | unit cost | 400.00 | Yuan/Ton | Cost of tonnes of water | 0.240 | Yuan/Ton |
| Additive amount of oxidizer | 400.00 | mg/l | unit cost | 1000.00 | Yuan/Ton | Cost of tonnes of water | 0.400 | Yuan/Ton |
| Amount of sulfuric acid added | 0.00 | mg/l | unit cost | 800.00 | Yuan/Ton | Cost of tonnes of water | 0.000 | Yuan/Ton |
| NaOH additive | 0.00 | mg/l | unit cost | 1850.00 | Yuan/Ton | Cost of tonnes of water | 0.000 | Yuan/Ton |
| 6. Sludge dewatering chemicals | ||||||||
| Ⅰ. Calculationof sludge volume of primary sedimentation tank | ||||||||
| Calculation formua | W1=Q×(SS removal)-1000÷1000(SS removal mainly refers to the diference between the SS inand ou of the primary sedimertation tank) | |||||||
| Primary dust influent SS | 1000.00 | mg/ | First Dust Out of Water SS | 500.00 | mg/l | sludge quantity | 17.500 | tons/day |
| Ⅱ. Calculation of biochemical sludge volume | ||||||||
| Calculation formua | W2=Q×(BOD removal)×0.3+1000÷1000(BOD removal mainly refers to the diference between the BOD into the oxidation ditch and the BOD out of the secondary sedimentation tank) |
|||||||
| Biochemical tank influent BOD | 1000.00 | mg/ | Secondary Settling Tank Effluent BOD | 500.00 | mg/l | sludge quantity | 5.250 | tons/day |
| Ⅲ.The amount of air flotation slag calculation | ||||||||
| Calculation formua | flotation=△COD*Q*0.6+△SS*Q+PAC*Q*0.46+PAM*Q | |||||||
| nlet water for air flotation COD | 0.00 | mg/ | Air Floatation Efluent COD | 0.00 | mg/l | |||
| Air floatation feed water SS | 0.00 | mg/l | Air foatationefluent SS | 0.00 | mg/l | |||
| Addition of PAC | 0.00 | mg/l | Addition of PAM | 0.00 | mg/l | sludge quantity | 0.000 | tons/day |
| Ⅳ.Calculation of chemical sludge volume | ||||||||
| Calculation | Chemical sludge volume=Q÷10000×(4000~7000) | Sludge volume | 17.500 | tons/day | ||||
| When Fenton | Chemical sludge volume=Q÷10000×6000 | Sludge volume | 21.000 | tons/day | ||||
| When it is catalytic oxidation | Chemical sludge volume=Q÷10000×6000×(0.3~0.4) | Sludge Volume | 6.300 | tons/day | ||||
| Ⅴ.Total amount of sludge | Total sludge volume | 67.550 | tons/day | |||||
| PAC addition amount | 10.00 | kg/per tonof sludge | unit cost | 1350.00 | tons/day | Cost per ton of water | 0.026 | tons/day |
| Amount of PAM added | 3.00 | kg/per ton of sludge | unit cost | 1350.00 | tons/day | Cost of ton of water | 0.008 | tons/day |
| 7.Water charges | ||||||||
| Total PAC | 16.10 | tons/day | Configuration Concentration | 10.00 | % | Water consumption | 161.000 | tons/day |
| Total amount of PAM | 0.49 | tons/day | Configuration Concentration | 0.10 | % | Water consumption | 493.000 | tons/day |
| Total amount of oxidizer | 14.00 | tons/day | Configuration Concentration | 30.00 | % | Water consumption | 46.667 | tons/day |
| (NH2)2HPO4 addition amount | 0.86 | tons/day | Configuration Concentration | 50.00 | % | Water Consumption | 1.721 | tons/day |
| Amount of Na3PO4 added | 2.63 | tons/day | Configuration Concentration | 50.00 | % | Water Consumption | 5.268 | tons/day |
| Amount of urea added when the phosphorus source is(NH2)2HPO4 |
230 | tons/day | Configuration Concentration | 50.00 | % | Water Consumption | 4.594 | tons/day |
| Amount of urea added when the phosphorus source is Na3PO4 |
2.74 | tons/day | Configuration Concentration | 50.00 | % | Water Consumption | 5.479 | tons/day |
| Total water volume (whenphosphorus source is(NH2)2HPO4) |
36.38 | tons/day | Price of tons of water | 3.67 | Yuan/per ton of water | Cost of tons of water | 0.004 | Yuan/ton of water |
| Total water volume (whenphosphorus source is Na3PO4) |
36.83 | tons/day | Price of tons of water | 3.67 | Yuan/per ton of water | Cost of tonof water | 0.004 | Yuan/ton of water |
| 8.Anaerobic treatment chemicals | ||||||||
| Design Data | ||||||||
| Anaerobic influent BOD | 5000.00 | mg/l | Ammonia Nitrogen | 50.00 | mg/l | Total Phosphorus | 1.000 | mg/l |
| Required Carbon,Nitrogenand Phosphorus Ratio |
300.00 | 5.00 | 1.000 | |||||
| Actual amount of nutrients needed | Nitrogen source | 33.33 | mg/l | Phosphorus Source Volume | 15.667 | mgl | ||
| When the phosphorus source is(NH2)2HPO4 | Nitrogen content | 0.22 | phosphorus content | 0.24 | ||||
| ( NH2)2HPO4 additive quantity | 65.28 | mg/l | unit cost | 2300.00 | Yuan/Ton | Cost per ton of water | 0.150 | Yuanton of water |
| Whenthe nitrogen source is CO(NH2)2 | Nitrogen content | 0.43 | ||||||
| CO(NH2)2 additive quantity | 44.33 | mg/l | unit cost | 1660.00 | YuanTon | Ton of water cost | 0.074 | Yuan/ton of water |
| When the phosphorus source is Na3PO4 | Purity | 0.98 | phosphorus content | 0.08 | ||||
| Na3PO4 additive quantity | 199.83 | mg/l | unit cost | 2990.00 | Yuan/Ton | Ton of water cost | 0.597 | Yuan/ton of water |
| CO(NH2)2 additive quantity | 77.88 | mg/l | unit cost | 1660.00 | YuanTon | Ton of water cost | 0.129 | Yuan/ton ofwater |
| Backwash air volume strength | ||||||||
| Water flushing strength | ||||||||
| Indicators of water consumption per ton | Daily consumption | Cost(Yuan/tonne of water) | ||||
| 1abor cost | 10.00 | human | 666.67 | Yuan | 0.019 | |
| Electricity consumption | 0.87 | kwh | 30552.00 | kwh | 0.436 | |
| Consumption of pre- treatment chemicals |
PAC | 0.10 | kg | 3500.00 | kg | 0.135 |
| PAM | 0.01 | kg | 420.00 | kg | 0.186 | |
| Anaerobic nutrient salt consumption |
(NH2)2HPO4 | 0.07 | kg | 2284.72 | kg | 0.150 |
| CO(NH₂)₂ | 0.04 | kg | 1551.47 | kg | 0.074 | |
| Na3P04 | 0.20 | kg | 6994.05 | kg | 0.597 | |
| CO(NH₂)2 | 0.08 | kg | 2725.86 | kg | 0.129 | |
| Oxidation ditch nutrient salt consumption |
(NH2)2HPO4 | 0.02 | kg | 860.42 | kg | 0.057 |
| CO(NH₂)2 | 0.07 | kg | 2297.22 | kg | 0.109 | |
| Na3PO4 | 0.08 | kg | 2633.93 | kg | 0.225 | |
| CO(NH₂)2 | 0.08 | kg | 2739.49 | kg | 0.130 | |
| Deep treatment drug consumption |
PAC | 0.36 | kg | 12600.00 | kg | 0.486 |
| PAM | 0.00 | kg | 70.00 | kg | 0.031 | |
| hydrogen peroxide(H202) | 0.40 | kg | 14000.00 | kg | 0.400 | |
| Ferrous salts | 0.60 | kg | 21000.00 | kg | 0.240 | |
| Sludge Dewatering PAM Consuption | 3-5 | kg/ton dry sludge | 3.00 | kg | 0.008 | |
| Sludge dewatering PAC consumption | 10-15 | kg/ton dry sludge | 10.00 | kg | 0.026 | |
| Total | 3.438 | |||||
