Scenario name: Helbling et al., 2012 (IND1) - (00000) Scenario description: DOI: 10.1021/es3019012 Scenario date: no date Scenario type: SLUDGE The scenario contains the following Additional Information: Name: Bioreactor (bioreactor) Value: amber glass Schott bottles (loosely capped), 100.0 Unit: mL Name: Biological treatment technology (biologicaltreatmenttechnology) Value: nitrification & denitrification Unit: Name: Type of Aeration (typeofaeration) Value: shaking Unit: Name: Type of compound addition (typeofaddition) Value: plating Unit: Name: Initial amount of sludge in bioreactor (originalsludgeamount) Value: 70 Unit: mL Name: Solvent for compound addition (solventforcompoundsolution) Value: MeOH Unit: Name: Sludge retention time (sludgeretentiontime) Value: sludge retention time;9.5 Unit: d Name: Purpose of WWTP (purposeofwwtp) Value: mixed WW (municipal & industrial) Unit: Name: Nitrogen Content (nitrogencontent) Value: NH₄-N;23.0; Unit: mg/L Name: Oxygen Demand (oxygendemand) Value: Biological Oxygen Demand (BOD5);500.0; Unit: mg/L Name: Redox condition (redox) Value: aerob Unit: Name: Total suspended solids concentration (TSS) (tts) Value: 6.8 - 6.8 Unit: g/L Name: Phosphorus Content (phosphoruscontent) Value: 3.0; Unit: mg/L Name: Temperature (temperature) Value: 20.0;20.0 Unit: °C Name: Final compound concentration (finalcompoundconcentration) Value: 100 Unit: μg/L Name: Inoculum source (inoculumsource) Value: activated sludge from biological aeration basin Unit: Name: Source of liquid matrix (sourceofliquidmatrix) Value: none (sludge only) Unit: Name: Acidity (acidity) Value: 7.0; Unit: pH Name: Location (location) Value: Switzerland (IND1) Unit: