ANNEX entrada FQ desengreix Flow 1000 1000 1000 m3dia 1 TSS 1400 1700 gTSSm 3 SSV 75 75 75 BOD 4205 423 685 gO2m 3 Soluble BOD 1529 154 249 gO2m COD 5720 576 932 gO2m Soluble COD 3445 ID: 825891
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ANNEX1. Paràmetres de l’aigua d&#
ANNEX1. Paràmetres de l’aigua d’entrada al reactor biològic SBR entrada F/Q desengreix Flow 1000 1000 1000 m3·dia-1 TSS 1400 1700 gTSS.m-3 %SSV 75 75 75 % BOD 4205 423 685 gO2.m-3 Soluble BOD 1529 154 249 gO2.m COD 5720 576 932 gO2.m Soluble COD 3445 561 gO2.m TKN 320 320 320 gN.m-3 TKN soluble 224 224 224 gN.m Amonia 200 200 200 gN.m phosphorus 50 50 50 2. Alternativa 2Aigua d’entrada sense tractament Oper(/yr) Maint(/yr) Mat(/yr) Chem(/yr) Energy(/yr) $927,000 $92,900 $47,800 $32,400 $0 $269,000 User Input DataDescriptionValueUnitsProcess DesignCarbon, Nitrogen And Phosphorus RemovalAeration Bubble SizeCourse BubbleDesign BasisSpecify Design SRTDesign SRTEffluent Soluble BODg/m3Effluent NitrogengN/m3Effluent Total PhosphorusgP/m3Biomass Yield0.5Maximum Heterotrophic Specific Growth Rate umaxhet201/dHeterotrophic Decay Rate0.241/dMaximum Autotrophic Specific Growth Rate umax200.
51/dANNEXExcavation Depth1.3Required A
51/dANNEXExcavation Depth1.3Required Air Flow iffused Aeration1180N m3/min/1000 m3Number Of Mixers Per SBROverride Database CostsFALSEStandard 2 scfm Fine Bubble DiffuserStandard 12 scfm Coarse Bubble DiffuserStandard 550 scfm Swing Arm Diffuser$7,9705 hp Vertical Turbine Mixer$8,860Standard 3000 gpm Pump and Driver Unit$37,900Fine Bubble DiffuseryearsCoarse Bubble DiffuseryearsSwing Arm DiffuseryearsTurbine MixeryearsPumpyearsStructuralyearsDesign Output DataDescriptionValueUnitsequencing Batch ReactorCarbon, Nitrogen and Phosphorus Removal DesignDesign SRT for design at winter temperatureAerated cycle timeUnaerated cycle timeSuggested anoxic cycle time1.2Suggested anaerobic cycle time0.75Settle and decant time1.5Total cycle time7.5Total exchange volume required1000Total volume of SBRSVolume of one SBRHydraulic retention timeF/M ratio0.208kg BOD/kg MLSS/dCalculated SS60800g/m3Calculated VSS43600g/m3lculated VSS:TSS ratio0.717mg VSS/mg SSAmount of sludge generated3800kg/dNitrogen requirement for biomass growthg/m3Phosphorus requirement for biomass growth
g/m3Oxygen requirement to meet average d
g/m3Oxygen requirement to meet average demand4250kg/dAir flow required to meet average demand44100N m3/hrOperation labor required4450pershrs/yrMaintenance labor required2800pershrs/yrElectrical energy required3340000kWh/yrVolume of earthwork requiredVolume of slab concrete requiredVolume of wall concreterequiredHandrail lengthNumber of diffusers per train1080Number of swing arm headers per trainConstruction and equipment cost$595,000ANNEXO&M material and supply cost$30,100$/yrEnergy cost$268,000$/yrAmortization cost$52,600$/yrSBR PumpingAverage daily pumping rate7500m3/dTotal pumping capacity7500m3/dDesign capacity per pump3750m3/dNumber of pumpsNumber of batteriesFirm pumping capacity7500m3/dOperation labor requiredpershrs/yrMaintenance labor requiredpershours/yrElectrical energy required8840kWh/yrVolume of earthwork required54.2Area of pump building22.2Construction and equipment cost$332,000O&M material and supply cost$2,320$/yrEnergy cost$1,410$/yrater Quality DatParameterInfluentEffluentSludgeUnitsMaximum flow1000m3/dMinimum flow1000m3/dAverage flow1
000m3/dSuspended solids43008000g/m3% vol
000m3/dSuspended solids43008000g/m3% volatile solids71.771.7BOD379011.8g/m3Soluble BOD1380g/m3530041.98620g/m3Soluble COD3300g/m3TKN0.9321.53gN/m3Soluble TKN0.930.93gN/m3Ammonia0.930.93gN/m3Nitrite0.00.00.0gN/m3Nitrate0.035.435.4gN/m3Total phosphorusgP/m36.86.86.8Cationsg/m3Anionsg/m3Settleable solids0.00.0mL/LOil and grease0.00.0g/m3Summer temperaturedeg CWinter temperaturedeg CANNEXAlternativa3Aigua d’entrada ambtractamentfísicoquímic Construction Oper(/yr) Maint(/yr) Mat(/yr) Chem(/yr) Energy(/yr) $685,000 $54,500 $24,600 $20,100 $0 $84,700 User Input DataDescriptionValueUnitsProcess DesignCarbon, Nitrogen And Phosphorus RemovalAeration Bubble SizeCourse BubbleDesign BasisSpecify Design SRTesign SRTEffluent Soluble BODg/m3Effluent NitrogengN/m3Effluent Total PhosphorusgP/m3Biomass Yield0.5Maximum Heterotrophic Specific Growth Rate umaxhet201/dHeterotrophic Decay Rate0.241/dMaximum Autotrophic Specific Growth Rate umax200.51/dAutotrophic Decay Rate ba200.041/dAerated PeriodUnaerated PeriodSettle And Decant Time1.5Exch
ange Volume/CycleNumber Of SBRsAlpha Fac
ange Volume/CycleNumber Of SBRsAlpha Factor For Oxygen Transfer In Wastewater0.7Beta Factor For Oxygen Saturation In Wastewater0.95Minimum Air FlowN m3/min/1000 m3Standard Oxygen Transfer EfficiencyUnderflow Concentration0.8Decant Suspended Solidsg/m3Override DesignFALSELength To Width RatioTank DepthPipe Gallery Wid6.12Excavation Depth1.3Required Air Flow Diffused AerationN m3/min/1000 m3Number Of Mixers Per SBROverride Database CostsFALSEStandard 2 scfm Fine Bubble DiffuserStandard 12 scfm Coarse Bubble DiffuserStandard 550 scfm Swing Arm Diffuser$7,9705 hp Vertical Turbine Mixer$8,860Standard 3000 gpm Pump and Driver Unit$37,900Fine Bubble DiffuseryearsCoarse Bubble DiffuseryearsSwing Arm DiffuseryearsTurbine MixeryearsPumpyearsStructuralyearsANNEXDesign Output DataDescriptionValueUnitsSequencing Batch ReactorCarbon, Nitrogen and Phosphorus Removal DesignDesign SRT for design at winter temperatureAerated cycle timeUnaerated cycle timeSuggested anoxic cycle time2.6Suggested anaerobic cycle time40.6Settle and decant time1.5Total cycle time7.5Total excha
nge volume required1000Total volume of S
nge volume required1000Total volume of SBRSVolume of one SBRHydraulic retention timeF/M ratio0.0998kg BOD/kg MLSS/dCalculated SS14600g/m3Calculated VSS8990g/m3Calculated VSS:TSS ratio0.616mg VSS/mg SSAmount of sludge generatedkg/dNitrogen requirement for biomass growth28.1g/m3Phosphorus requirement for biomass growth5.61g/m3Oxygen requirement to meet average demand1320kg/dAir flow required to meet average demand13700N m3/hrOperation labor required2470pershrs/yrMaintenance labor required1380pershrs/yrElectrical energy required1040000kWh/yrVolume of earthwork requiredVolume of slab concrete requiredVolume of wall concrete requiredHandrail lengthNumber of diffusers per trainNumber of swing arm headers per trainConstruction and equipment cost$353,000O&M material and supply cost$17,800$/yrergy cost$83,300$/yrAmortization cost$31,000$/yrSBR PumpingAverage daily pumping rate7500m3/dTotal pumping capacity7500m3/dDesign capacity per pump3750m3/dNumber of pumpsNumber of batteriesFirm pumping capacity7500m3/dOperationlabor requiredpershrs/yrMaintenance labor required
pershours/yrElectrical energy required88
pershours/yrElectrical energy required8840kWh/yrVolume of earthwork required54.2Area of pump building22.2Construction and equipment cost$332,000ANNEXO&M material and supply cost2,320$/yrEnergy cost$1,410$/yrWater Quality DataParameterInfluentEffluentSludgeUnitsMaximum flow1000m3/dMinimum flow1000m3/dAverage flow1000m3/dSuspended solids14008000g/m3% volatile solids61.661.6BOD10.7g/m3Soluble BODg/m3COD38.17410g/m3Soluble CODg/m3TKN0.9311.18gN/m3Soluble TKN0.930.93gN/m3Ammonia0.930.93gN/m3Nitrite0.00.00.0gN/m3Nitrate0.0gN/m3Total phosphorusgP/m36.86.86.8Cationsg/m3Anionsg/m3Settleable solids0.00.0mL/LOil and grease0.00.0g/m3Summer temperaturedeg CWinter temperaturedeg ClternativaAigua d’entrada amb tractament de desengreix Construction Oper(/yr) Maint(/yr) Mat(/yr) Chem(/yr) Energy(/yr) $707,000 $58,100 $26,600 $21,300 $0 $97,500 User Input DataDescriptionValueUnitsProcess DesignCarbon, Nitrogen And Phosphorus RemovalAeration Bubble SizeCourse BubbleDesign BasisSpecify Design SRTDesign SRTEffluent Soluble BODg/m3Effluent Nitr
ogengN/m3Effluent Total PhosphorusgP/m3B
ogengN/m3Effluent Total PhosphorusgP/m3Biomass Yield0.5Maximum Heterotrophic Specific Growth Rate umaxhet201/dHeterotrophic Decay Rate0.241/dMaximum Autotrophic Specific Growth Rate umax200.51/dAutotrophic Decay Rate ba200.041/dAerated PeriodUnaerated PeriodANNEXSettle And Decant Time1.5Exchange Volume/CycleNumber Of SBRsAlpha Factor For Oxygen Transfer In Wastewater0.7Beta Factor For Oxygen Saturation In Wastewater0.95Minimum Air FlowN m3/min/1000 m3Standard Oxygen Transfer EfficiencyUnderflow Concentration0.8Decant Suspended Solidsg/m3Override DesignFALSELength To Width RatioTank DepthPipe Gallery Width6.12Excavation Depth1.3Required Air Flow Diffused AerationN m3/min/1000 m3Number Of Mixers Per SBROverride Database CostsFALSEStandard 2 scfm Fine Bubble DiffuserStandard 12 scfm Coarse Bubble DiffuserStandard 550 scfm Swing Arm Diffuser$7,9705 hp Vertical Turbine Mixer$8,860Standard 3000 gpm Pump and Driver Unit$37,900Fine Bubble DiffuseryearsCoarse Bubble DiffuseryearsSwing Arm DiffuseryearsTurbine MixeryearsPumpyearsStructuralyearsDesign Output DataDe
scriptionValueUnitsSequencing Batch Reac
scriptionValueUnitsSequencing Batch ReactorCarbon, Nitrogen and Phosphorus Removal DesignDesign SRT for design at winter temperatureAerated cycle timeUnaerated cycle timeSuggested anoxic cycle time2.6Suggested anaerobic cycle time40.6Settle and decant time1.5Total cycle time7.5Total exchange volume required1000Total volume of SBRSVolume of one SBRHydraulic retention timeF/M ratio0.123kg BOD/kg MLSS/dCalculated SS18700g/m3Calculated VSS11900g/m3Calculated VSS:TSS ratio0.635mg VSS/mg SSAmount of sludge generated1170kg/dNitrogen requirement for biomass growth45.7g/m3ANNEXPhosphorus requirement for biomass growth9.15g/m3Oxygen requirement to meet average demand1530kg/dAir flow required to meet average demand15800N m3/hrOperation labor required2650pershrs/yrMaintenance labor required1510pershrs/yrElectrical energy required1200000kWh/yrVolume of earthwork requiredVolume of slab concrete requiredVolume of wall concrete requiredHandrail lengthNumber of diffusers per trainNumber of swing arm headers per trainConstruction and equipment cost$375,000O&M material and
supply cost$18,900$/yrEnergy cost$96,10
supply cost$18,900$/yrEnergy cost$96,100$/yrAmortization cost$32,900$/yrSBR PumpingAverage daily pumping rate7500m3/dTotal pumping capacity7500m3/dDesign capacity per pump3750m3/dNumber of pumpsNumber of batteriesFirm pumping capacity7500m3/dOperation labor requiredpershrs/yrMaintenance labor requiredpershours/yrElectrical energy required8840kWh/yrVolume of earthwork required54.2Area of pump building22.2Construction and equipment cost$332,000O&M material and supply cost$2,320$/yrEnergy cost$1,410$/yrWater Quality DataParameterInfluentEffluentSludgeUnitsMaximum flow1000m3/dMinimum flow1000m3/dAverage flow1000m3/dSuspended solids17008000g/m3% volatile solids63.663.6BOD10.9g/m3Soluble BODg/m3COD38.87640g/m3Soluble CODg/m3TKN0.9311.24gN/m3Soluble TKN0.930.93gN/m3Ammonia0.930.93gN/m3Nitrite0.00.00.0gN/m3Nitrate0.0gN/m3Total phosphorusgP/m36.86.86.8ANNEXCationsg/m3Anionsg/m3Settleable solids0.00.0mL/LOil and grease0.00.0g/m3Summer temperaturedeg CWinter temperaturedeg CEsquema del tractament biològic SBR simulat pel Software CAPDETWORKS 115 ANNE