Wastewater treatment, Australian Capital Territory {AU}| | AusLCI, U
Unit process Australia v00.00.000
Domestic wastewater treatment in Canberra as the main city is Australian Capital Territory. 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
53f8ffbd-04cd-3736-8972-c66e56e11bdd
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Documentation
- Quantitative reference
- Wastewater treatment, Australian Capital Territory {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 | 0.16593224316636512 | MJ | — |
| Electricity, high voltage {AU}| electricity production, wind, >3MW turbine, onshore | Cut-off, U | 0.0 | MJ | — |
| Electricity, high voltage {AU}| heat and power co-generation, biogas, gas engine | Cut-off, U | 0.0 | MJ | — |
| Electricity, low voltage {AU-NSW}| market for electricity, low voltage | AusLCI, U | 2.654915890661842 | MJ | — |
| Heat, district or industrial, natural gas {RoW}| heat production, natural gas, at industrial furnace >100kW | Cut-off, U | 0.06637289726654604 | MJ | — |
| Heat, liquefied petroleum gas, at industrial furnace >100kW/MJ/RER/adapted {AU}| | AusLCI, U | 0.01659322431663651 | 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 | 0.007997934120618796 | 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 | 0.00005624584717607973 | kg | — |
| BOD5 (Biological Oxygen Demand) | Emissions to water | ocean | 6.080000000000005 | g | — |
| COD (Chemical Oxygen Demand) | Emissions to water | ocean | 13.640000000000011 | g | — |
| Chlorine | Emissions to water | ocean | 0.00005053156146179402 | kg | — |
| Dinitrogen monoxide | Emission to air | high population density | 0.0008017787375415282 | kg | — |
| Fluoride | Emission to water | ocean | 0.0005033222591362127 | kg | — |
| Methane, non-fossil | Emission to air | high population density | 0.0364 | kg | — |
| Nitrogen, total | Emissions to water | ocean | 0.016981129568106313 | kg | — |
| Phosphorus, total | Emissions to water | ocean | 0.00006970099667774085 | 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, Australian Capital Territory {AU}| | AusLCI, U | 1.0 | m3 | — |
Parameters
| Name | Value | Formula | Description |
|---|---|---|---|
| NitrogenEff | 0.085162 | (Ninfluent*Nreduction)/1000 | kg Ne |
| EFCH4CodRemoval | — | EFCO2eCodRemoval/23 | — |
| Ninfluent | 86.9 | — | (4,5,1,3,1,5) |
| BODremovedinSludge | 0.29 | — | Fsl - Fraction of BOD in wastewater removed as sludge by plant |
| TotalN | 0.016981129568106313 | 511132/WWatervol/1000000 | — |
| PetrolTotal | 998.912103861518 | Petrolfrac*WastewaterEn | — |
| Gridsupplyperkl | 2.654915890661842 | GridTotal/WWatervol/1000 | MJ/Kl |
| Watervol | 45.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| FuelSupperkl | 0.2986780376994572 | FuelTotal/WWatervol/1000 | MJ/kl |
| Pinfluent | 22.6 | — | (4,5,1,3,1,5) |
| LPGTotal | 499.456051930759 | LPGFrac*WastewaterEn | — |
| Lowesupplyperkl | — | LowemTotal/WWatervol/1000 | MJ/kl |
| TSSReduction | 0.98 | — | (5,5,5,5,5,5) |
| EthanolTotal | 499.456051930759 | EthanolFrac*WastewaterEn | — |
| WWatervol | 30.1 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| SelfGenTotal | — | SelfGenFrac*(EI_wwaterpump+EI_wwatertreat+EI_other) | — |
| EI_wwatertreat | 78994.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| EFCO2eCodRemoval | — | — | Efw - Default methane emission factor for waste water 5.30 t CH4/ t |
| PReduction | 0.98 | — | (5,5,5,5,5,5) |
| BODinfluent | 304.0 | — | (4,5,1,3,1,5) |
| EthanolSupperkl | 0.01659322431663651 | EthanolTotal/WWatervol/1000 | MJ/kl |
| PetrolSupperkl | 0.03318644863327302 | PetrolTotal/WWatervol/1000 | MJ/kl |
| TotalF | 0.0005033222591362127 | 15150/WWatervol/1000000 | 1 |
| EI_wwaterpump | 3133.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| EI_other | 44322.0 | — | (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] |
| GridFrac | 0.8 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| SludgeEmission | — | CODtreated*BODremovedinSludge*EFCH4CodRemoval | — |
| DieselTotal | 4994.56051930759 | DieselFrac*WastewaterEn | — |
| NatgasSupperkl | 0.06637289726654604 | NatGasTotal/WWatervol/1000 | MJ/kl |
| SelfGenFrac | — | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| Selfsupplyperkl | — | SelfGenTotal/WWatervol/1000 | MJ/kl |
| EI_watertreat | 27096.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| N2Ofactor | 1.5714 | — | Conversion factor of kg N2O-N to kg N2O |
| TotalA | 0.00005624584717607973 | 1693/WWatervol/1000000 | — |
| SplitOtherEnerg | 17764.210386151797 | EI_other*WWatervol/(WWatervol+Watervol) | — |
| NatGasTotal | 1997.824207723036 | NaturalGasFrac*WastewaterEn | — |
| NaturalGasFrac | 0.02 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| EnergyperKL | 3.318644863327302 | (WastewaterEn)/WWatervol/1000 | MJ/kl |
| DieselFrac | 0.05 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| Maginalsupply | 13.0 | — | (4,5,1,1,3,5), MJ per kl. Assumed energy from marginal water supply for this city based on desaliation. |
| LowEmissFrac | — | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| N2Oemission | 0.0008017787375415282 | 24133.54/WWatervol/1000000 | kg N2O |
| NReduction | 0.98 | — | (5,5,5,5,5,5) |
| LPGSupperkl | 0.01659322431663651 | LPGTotal/WWatervol/1000 | MJ/kl |
| LPGFrac | 0.005 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| DieselSupperkl | 0.16593224316636512 | DieselTotal/WWatervol/1000 | MJ/kl |
| CH4emission | 0.0364 | 0.0364 | kg CH4 - From NSW number as no value listed in ACT |
| EthanolFrac | 0.005 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| CODReduction | 0.98 | — | (5,5,5,5,5,5) |
| LowEmTotal | — | LowEmissFrac*WastewaterEn | — |
| FuelFrac | 0.09 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| FuelTotal | 8990.208934753662 | FuelFrac*WastewaterEn | — |
| Renewsupplyperkl | 0.06637289726654604 | RenewTotal/WWatervol/1000 | MJ/kl |
| PetrolFrac | 0.01 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| RenewTotal | 1997.824207723036 | RenewFrac*WastewaterEn | — |
| TotalC | 0.00005053156146179402 | 1521/WWatervol/1000000 | — |
| EFeffN2OFactor | — | — | (6,3,1,2) WASTEWATER TREATMENT AND DISCHARGE |
| CODtreated | 0.3 | — | MCFww (and MCFsl) - fraction of COD anaerobically treated |
| WastewaterEn | 99891.2103861518 | (EI_wwaterpump+EI_wwatertreat+SplitOtherEnerg) | — |
| CODinfluent | 682.0 | — | (4,5,1,3,1,5) |
| EI_waterpump | 53121.0 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012) |
| TotalP | 0.00006970099667774085 | 2098/WWatervol/1000000 | — |
| Gridtotal | 79912.96830892144 | GridFrac*WastewaterEn | — |
| BODreduction | 0.98 | — | (5,na,na,na,na,na) |
| RenewFrac | 0.02 | — | (2,1,1,1,1,5) GJ, Cook, S. Hall. M. and Gregory, A. (2012)-based on derived energy |
| TSSinfluent | 382.0 | — | (4,5,1,3,1,5) |