Wastewater treatment, Victoria {AU}| | AusLCI, U
Unit process Australia v00.00.000
Domestic wastewater treatment in Melbourne as the main city in Victoria. Included processes: Energy inputs and Infrastructure materials for municipal wastewater treatment and greenhouse gas emissions and nutrient emission. Remark: Wastewater purified in a moderatly large municipal wastewater treatment plant. Direct emissions inlcuded in National Pollutant Inventory Reports have been included. Geography: Energy and emission data are specific to the region. Technology: Assume to mostly be three stage wastewater treatment (mechanical, biological, chemical) including sludge digestion (fermentation) according to the typical technology in Australia Version: 1.0 Record: Data entry by: Rahul Korattyile E-mail: info@lifecycles.com.au; Company: Lifecycles; Country: AU Generator: Data entry by: Rahul Korattyile E-mail: info@lifecycles.com.au; Company: Lifecycles; Country: AU
- Sector
- Waste Treatment
- Contributor
- —
- Last updated
- 01 Jul 2020
- Reference ID
e23ac84d-29ee-36e2-93be-73520a065cb9
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Documentation
- Quantitative reference
- Wastewater treatment, Victoria {AU}| | AusLCI, U
- Sampling procedure
- —
- Creation date
- 01 Jul 2020
- Is copyright protected
- No
- Is infrastructure process
- No
- Tags
- waste treatment
- Sources
-
Energy use in the provision and consumption of urban water /2012/Cook.S et al
National Greenhouse Gas Inventory/2019/Commonwealth of Australia
NPI data for year 2017/2019/Commonwealth of Australia
Technical inputs
| Flow | Amount | Unit | Comment |
|---|---|---|---|
| Aluminium sulfate, without water, in 4.33% aluminium solution state {GLO}| market for aluminium sulfate, without water, in 4.33% aluminium solution state | Cut-off, U | 0.0031512 | kg | direct wastewater treatment plant burden. Uncertainty calculated from wastewater composition and treatment model |
| Diesel, burned in building machine, <30 MW {AU}| | AusLCI, U | 0.21179887791864016 | MJ | — |
| Electricity, high voltage {AU}| electricity production, wind, >3MW turbine, onshore | Cut-off, U | 0.01323742986991501 | MJ | — |
| Electricity, high voltage {AU}| heat and power co-generation, biogas, gas engine | Cut-off, U | 0.6582111896283107 | MJ | — |
| Electricity, low voltage {AU-VIC}| market for electricity, low voltage | AusLCI, U | 1.4296424259508211 | MJ | — |
| Heat, district or industrial, natural gas {RoW}| heat production, natural gas, at industrial furnace >100kW | Cut-off, U | 0.15884915843898012 | MJ | — |
| Heat, liquefied petroleum gas, at industrial furnace >100kW/MJ/RER/adapted {AU}| | AusLCI, U | 0.05294971947966004 | MJ | — |
| Iron sulfate {RoW}| market for iron sulfate | Cut-off, U | 0.01166 | kg | direct wastewater treatment plant burden. Uncertainty calculated from wastewater composition and treatment model |
| Iron(II) chloride {GLO}| market for iron(II) chloride | Cut-off, U | 0.015944 | kg | direct wastewater treatment plant burden plus burden from sludge incineration. Uncertainty calculated from wastewater composition and treatment model |
| Operation, van, petrol less than 3,5t {AU}| | AusLCI, U | 0.019141323591897103 | km | [ The original product with unit "MJ" (Energy) was automatically replaced by SimaPro with the current product with unit "km" (Length) using conversion factor 0.241 km/MJ. ] |
| Sewer grid, 1E9l/year, 30 km {GLO}| market for sewer grid, 1E9l/year, 30 km | Cut-off, U | 0.000000218 | km | Based on econivent process |
| Wastewater treatment facility, capacity 1E9l/year {GLO}| market for wastewater treatment facility, capacity 1E9l/year | Cut-off, U | 0.00000000569 | Item(s) | Based on econivent process |
Elementary flow outputs
| Flow | Compartment | Sub-compartment | Amount | Unit | Comment |
|---|---|---|---|---|---|
| Ammonia, as N | Emissions to water | ocean | 0.004134861172935678 | kg | — |
| BOD5 (Biological Oxygen Demand) | Emissions to water | ocean | 6.080000000000005 | g | — |
| Boron | Emission to water | ocean | 0.00018718617849988872 | kg | — |
| COD (Chemical Oxygen Demand) | Emissions to water | ocean | 13.640000000000011 | g | — |
| Chlorine | Emissions to water | ocean | 0.00004813042510572001 | kg | — |
| Dinitrogen monoxide | Emission to air | high population density | 0.0010581713498775873 | kg | — |
| Fluoride | Emission to water | ocean | 0.001058053082572891 | kg | — |
| Methane, non-fossil | Emission to air | high population density | 0.03263054929890942 | kg | — |
| Nitrogen, total | Emissions to water | ocean | 0.013653407244602716 | kg | — |
| Phosphorus, total | Emissions to water | ocean | 0.005644506176274204 | kg | — |
| Suspended solids, unspecified | Emissions to water | ocean | 7.640000000000007 | g | — |
| Water | Emissions to water | ocean | 1.0 | t | — |
Other
| Flow | Amount | Unit | Comment |
|---|---|---|---|
| Wastewater treatment, Victoria {AU}| | AusLCI, U | 1.0 | m3 | — |
Parameters
| Name | Value | Formula | Description |
|---|---|---|---|
| NitrogenEff | 0.085162 | (Ninfluent*NReduction)/1000 | kg Ne |
| Lowesupplyperkl | 0.01323742986991501 | LowemTotal/WWatervol/1000 | MJ/kl |
| Ninfluent | 86.9 | — | (4,5,1,3,1,5) |
| N2Oemission | — | EFeffN2OFactor*NitrogenEff*N2Ofactor | kg N2O |
| PetrolFrac | 0.03 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| EI_other | 155241.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| BODreduction | 0.98 | — | (5,na,na,na,na,na) |
| TSSReduction | 0.98 | — | (5,5,5,5,5,5) |
| FuelSupperkl | 0.01323742986991501 | FuelTotal/WWatervol/1000 | MJ/kl |
| EFCO2eCodRemoval | — | — | Efw - Default methane emission factor for waste water 5.30 t CH4/ t |
| EnergyperKL | 2.6474859739830023 | (WastewaterEn)/WWatervol/1000 | MJ/kl |
| TotalA | 0.004134861172935678 | 1486234.5/WWatervol/1000000 | — |
| EI_wwaterpump | 172007.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| Pinfluent | 22.6 | — | (4,5,1,3,1,5) |
| NReduction | 0.98 | — | (5,5,5,5,5,5) |
| CH4 | 0.03263054929890942 | 11728724.64/WWatervol/1000000 | kg CO2e |
| CODtreated | 0.3 | — | MCFww (and MCFsl) - fraction of COD anaerobically treated |
| EI_waterpump | 381281.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| FuelTotal | 4758.061792442251 | FuelFrac*WastewaterEn | — |
| EthanolSupperkl | 0.02647485973983002 | EthanolTotal/WWatervol/1000 | MJ/kl |
| SplitOtherEnerg | 78212.35848845032 | EI_other*WWatervol/(WWatervol+Watervol) | — |
| DieselTotal | 76128.98867907602 | DieselFrac*WastewaterEn | — |
| WWatervol | 359.44 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| TSSinfluent | 382.0 | — | (4,5,1,3,1,5) |
| LPGSupperkl | 0.05294971947966004 | LPGTotal/WWatervol/1000 | MJ/kl |
| SelfGenFrac | 0.23 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| RenewFrac | 0.02 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| Selfsupplyperkl | 0.6582111896283107 | SelfGenTotal/WWatervol/1000 | MJ/kl |
| DieselSupperkl | 0.21179887791864016 | DieselTotal/WWatervol/1000 | MJ/kl |
| BODremovedinSludge | 0.29 | — | Fsl - Fraction of BOD in wastewater removed as sludge by plant |
| Watervol | 354.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| CODEmission | — | (1-BODremovedinSludge)*CODtreated*EFCH4CodRemoval | Wastewater emissions [COD*(1-Fsl)*MCFww*Efw] |
| NaturalGasFrac | 0.06 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| Renewsupplyperkl | 0.05294971947966004 | RenewTotal/WWatervol/1000 | MJ/kl |
| PReduction | 0.98 | — | (5,5,5,5,5,5) |
| SelfGenTotal | 236587.43000000002 | SelfGenFrac*(EI_wwaterpump+EI_wwatertreat+EI_other) | — |
| LPGTotal | 19032.247169769005 | LPGFrac*WastewaterEn | — |
| PetrolSupperkl | 0.07942457921949006 | PetrolTotal/WWatervol/1000 | MJ/kl |
| RenewTotal | 19032.247169769005 | RenewFrac*WastewaterEn | — |
| Gridtotal | 513870.6735837632 | GridFrac*WastewaterEn | — |
| N2O | 0.0010581713498775873 | 380349.11/WWatervol/1000000 | kg N2O |
| WastewaterEn | 951612.3584884503 | (EI_wwaterpump+EI_wwatertreat+SplitOtherEnerg) | — |
| EthanolFrac | 0.01 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| EFCH4CodRemoval | — | EFCO2eCodRemoval/23 | — |
| BODinfluent | 304.0 | — | (4,5,1,3,1,5) |
| TotalP | 0.005644506176274204 | 2028861.3/WWatervol/1000000 | — |
| Gridsupplyperkl | 1.4296424259508211 | GridTotal/WWatervol/1000 | MJ/Kl |
| Maginalsupply | 13.0 | — | (4,5,1,1,3,5), MJ per kl. Assumed energy from marginal water supply for this city based on desaliation. |
| LPGFrac | 0.02 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| TotalN | 0.013653407244602716 | 4907580.7/WWatervol/1000000 | — |
| PetrolTotal | 28548.370754653508 | Petrolfrac*WastewaterEn | — |
| GridFrac | 0.54 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| NatGasTotal | 57096.741509307016 | NaturalGasFrac*WastewaterEn | — |
| SludgeEmission | — | CODtreated*BODremovedinSludge*EFCH4CodRemoval | — |
| EI_wwatertreat | 701393.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| TotalC | 0.00004813042510572001 | 17300/WWatervol/1000000 | — |
| LowEmissFrac | 0.005 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| EthanolTotal | 9516.123584884503 | EthanolFrac*WastewaterEn | — |
| EFeffN2OFactor | — | — | (6,3,1,2) WASTEWATER TREATMENT AND DISCHARGE |
| EI_watertreat | 95185.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| DieselFrac | 0.08 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| N2Ofactor | 1.5714 | — | Conversion factor of kg N2O-N to kg N2O |
| TotalB | 0.00018718617849988872 | 67282.2/WWatervol/1000000 | — |
| NatgasSupperkl | 0.15884915843898012 | NatGasTotal/WWatervol/1000 | MJ/kl |
| LowEmTotal | 4758.061792442251 | LowEmissFrac*WastewaterEn | — |
| CODReduction | 0.98 | — | (5,5,5,5,5,5) |
| TotalF | 0.001058053082572891 | 380306.6/WWatervol/1000000 | — |
| CODinfluent | 682.0 | — | (4,5,1,3,1,5) |
| FuelFrac | 0.005 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |