Scenario name: Gulde et al. 2017 - (00000)
Scenario description:
DOI: 10.1021/acs.est.7b03556
Scenario date: 2017
Scenario type: SLUDGE

The scenario contains the following Additional Information:
Name: Purpose of WWTP (purposeofwwtp)
Value: mixed WW (municipal & industrial)
Unit: 

Name: Type of compound addition (typeofaddition)
Value: spiking in solvent
Unit: 

Name: Type of Aeration (typeofaeration)
Value: shaking
Unit: 

Name: Oxygen uptake rate (OUR) (oxygenuptakerate)
Value: 21.7;14.8
Unit: mg L&#8315&#185 h&#8315&#185

Name: Ammonia uptake rate (AUR) (amionauptakerate)
Value: 6.4;4.2
Unit: mg L&#8315&#185 h&#8315&#185

Name: Acidity (acidity)
Value: 7.5 - 8.5;
Unit: pH

Name: Total suspended solids concentration (TSS) (tts)
Value: 2.5 - 2.2
Unit: g/L

Name: Solvent for compound addition (solventforcompoundsolution)
Value: MeOH
Unit: 

Name: Source of liquid matrix (sourceofliquidmatrix)
Value: liquid phase of the activated sludge sample
Unit: 

Name: Initial amount of sludge in bioreactor (originalsludgeamount)
Value: 100
Unit: mL

Name: Redox condition (redox)
Value: aerob
Unit: 

Name: Inoculum source (inoculumsource)
Value: activated sludge from nitrification basin
Unit: 

Name: Bioreactor (bioreactor)
Value: amber Schott bottles, 250.0
Unit: mL

Name: Final compound concentration (finalcompoundconcentration)
Value: 60
Unit: &#956g/L

Name: Sludge retention time (sludgeretentiontime)
Value: sludge age;25.0
Unit: d

Name: Biological treatment technology (biologicaltreatmenttechnology)
Value: nitrification & denitrification & biological phosphorus removal
Unit: 

Name: Location (location)
Value: WWTP Duebendorf, Switzerland
Unit: