L4- Anaerobic Treatment Flashcards
Anaerobic Digestion (AD) and traits
Convert organic substances into gas via anaerobic m/o
Traits: high treatment times, low biomass production, high biogas production, high volumetric loads, low content in pathogen m/o
Aerobic Digestions traits
Aerobic m/o, oxygen supply, high growth rates, low treatment times, high biomass production, low gas production, high content in pathogen m/o
Advantages and disadvantages of AD
Adv: Energy producer, low sludge formation, less space/smaller reactors
Dis: long treatment times, sensitivity to toxic chemicals, potential for odour production, corrosiveness of digester gas, high cost to construct, effluent cannot be directly discharged readily
Differences in aerobic to anaerobic processes
Sankey diagram- AD: more effluent, less sludge, more gases, CH4 instead of H2O
AD Stages Overview (3 stages)
1st stage: hydrolysis - low reaction rate;
Biomass -> glucose + H2
2nd stage: acetogenesis - high growth rate;
Glucose -> Acetic acid + other acids
3rd stage: Methanogenesis - low growth rate;
Acetic acid-> methane/biogas
Factors affecting AD process
-Temperature: affects reaction rate and bacteria composition
-pH: bacterial reactions stop below pH=6.5
-Type/quantity of organic load
-Stirring/mixing: contact m/o with organic load
-Alkalinity, presence of nutrients & toxic substances
Typical AD Digester traits
Cylindrical tank
Diameter of 6-35m
Height 14m
Types of AD reactor
Anaerobic lagoon;
UASB- upflow anaerobic sludge blanket
EGSB- expanded granular sludge blanket
ANF- anaerobic filter
ANMBR- anaerobic membrane process
Residence time (tow c) equation, when its equal to hydraulic residence time and effect of increase in tow
t = V/Q
tow c = tow (hydraulic residence time) when no recycling
Increase tow- decrease volatile acids concentration & increase biogas production
Define variables of the Recycling ratio
tow- hydraulic residence time
Tow c- residence time of m/o
MR - sludge concentration in recycling stream
M - sludge concentration in digester
Define variables of sludge concentration in digester, M
E- degradation of volatile solids
XVSS- concentration of volatile solids (VSS)
XTSS- concentration of total solids (TSS)
Define variables of total production of methane, VCH4
VCH4- volume of produced methane (m3/d)
E- conversion factor of organic load during AD (0.6-0.9)
Q- volumetric flow (m3/d)
S0- COD influent (mg/L)
Px- produce biomass (kg/d)
Define variables of produced biomass, Px
Y- efficiency factor
E- conversion factor of organic load during anaerobic digestion (0.6-0.9)
Q- volumetric flow (m3/d)
S0- initial organic load (mg/L)
kd- endogenous respiration factor (1/d)
tow c- residence time of m/o (d)
Methane production
Volume produce CH4: 0.35m3 CH4/kg BOD
(1 mol CH4 -> 22.4 dm3)
Define variables of Energy requirements (q1) for waste water heating
q1- required heat for wastewater heating (J/d)
Q- volumetric flow (kg/d)
Cp- specific heat of wastewater (4200 J/kg C)
Delta T- temperature difference between reactant liquid and influent (deg C)