1 Aerobic Digestion, or, It s a Bug eat Bug World Brett Ward Municipal Technical Advisory Service The University of Tennessee
2 Aerobic Digestion Continuation of the Activated Sludge Process Super Extended Aeration No food is added Reduction of Volatile Solids through: Endogenous Respiration Bacterial Cells use their own protoplasm for energy Some cells die and become food for others
3 Biological Chemistry BOD, Bug Food, Organic Pollution Test of the organic strength of sewage Organic- from plants and animals Protein, carbohydrates, fats Fecal matter, food scrapes, paper, industrial waste of plant or animal origin. Normal Bacteriological Respiration BOD + BOD Bugs + O 2 = More BOD Bugs + CO 2 + H NH 3
4 Respiration / Oxidation Respiration We call it breathing Scientifically it is the release of energy The Bugs want the energy in the BOD Energy to live and grow The Bugs are teeny tiny chemical factories They split complex organic compounds into simple oxidized compounds.
5 Respiration / Oxidation Normal Bacteriological Respiration BOD + BOD Bugs + O 2 = More BOD Bugs + CO 2 + H NH 3 Glucose C 6 H 12 O 6 + BOD Bugs+ O 2 = More BOD Bugs + CO 2 + H 2 0 Protein C 3 H 7 O 2 N + BODBugs+ O 2 = More BOD Bugs + CO 2 + H NH 3
6 Sewage Treatment Sewage, BOD Carbs, Protein, Fats Add air and mix well Bugs grow And Grow And Grow
7 Waste excess Bugs to Digester With out wasting MLSS goes up, up, up and OUT! Waste today what grew today
8 Biological Chemistry Digesters receive no food or BOD Endogenous Respiration BOD Bugs +O 2 = Less BOD Bugs +CO 2 + H 2 O + NH 3 Bugs use stored energy Some die, and become food for others Reduction of Volatile Solids
9 Digestion Goals Thicken Waste Activated Sludge: Decanting Control Odors, Keep it aerobic Reduce Sludge Volume, Endogenous Resp. Meet Disposal Requirements Land Fill Land Application
10 Aerobic Advantages Low Construction Cost Easy to Operate High Quality Supernatant Safer process, no methane
11 Aerobic vs Anaerobic Supernatant Aerobic BOD 500 mg/l TSS mg/l TKN 170 mg/l T.Phos 98 mg/l Anaerobic BOD mg/l TSS mg/L Ammonia mg/L T. Phos mg/L
12 Aerobic Disadvantages High Aeration Costs, electricity Digested Sludge more difficult to dewater Process affected by temperature changes More Sludge produced for disposal
13 Aerobic Digester Design Various Sizes Various Aeration Diffused air Surface Mechanical Various Decant Fixed Valves Moving Arms Telescoping Valves Suspended Pumps
14 Operating Strategy WAS Biosolids Complete Mixed Batch, Fill and Draw Series, Parallel or combination Primary & WAS Primary Biosolids Secondary Digesters Biosolids
15 Digester Operations Operational Strategy Tools you have Basins Decant or supernatant equipment Aeration Personnel Destination Land Fill Land Application Other Facility
16 Digester Monitoring Daily to Weekly Dissolved Oxygen Settleometer ph, Alkalinity Nitrate 503 tests, Prior to use or disposal SOUR Temperature Fecal
17 Digester Monitoring
18 Supernatant Monitoring Monitor for affects on the water treatment system. Flow BOD Ammonia TSS Nitrate (NO 3 ) Phosphorus
19 Land Fill Special Waste Permit Division of Solid Waste Management No Free Water, AKA paint filter test No Toxic Lecheate, TCLP, Toxic Characteristics Lecheate Proceedure
20 Land Fill Primary Concerns Odor Control, too little O2, too much feed Sludge Oxygen Maintain Oxic environment Sacramento Manual, 1-2 mg/l DO What works for you 0.5 mg/l, can be more cost effective >2.0 mg/l» wastes electricity» can cause low ph» can contribute to foaming
21 Land Fill Dewatering Avoid excessive long aeration times Long times decrease floc and particle size Greater than 20 days, Capillary Suction Time (CST) greatly increases Lower CST means better dewatering.
22 Land Application 503 Requirements Metal accumulation Nitrogen management Pathogen Destruction Class A or B Vector Requirements 38% Red. of V.S. SOUR Bench top test Time and Temp.
23 Land Application Concerns Odors Pathogen Reduction Vector Attraction Red.
24 Land Application Class B Geometric Mean of seven samples is less than 2,000,000 cfu/g Requires Total Solids Test for Calculations Natural Die off in Digester Intestinal organisms Air Off cycles appear to assist in reduction.
25 Land Application Class B, PSRP Aerobic Digestion MCRT, 40 days at 20 C 60 days at 15 C
26 Land Application Vector Attraction Reduction 38% Reduction of VS, Van Kleeck Equation Works best where there is Primary Sludge feed Bench Top Aerobic Digestion SOUR Test, don t thicken above 2% TS All are tests to document Sludge Stability Low BOD (food), Low energy, highly oxidized
27 Sludge Stabilization Requires Time and Air Low Temperature Slows the process High Temps speed the process TN Design Criteria Hydraulic detention time at 20 C should be days depending on type
28 Sludge Stabilization This may not be enough. Variables Feed Sludge, WAS, Primary, Combination We all have Winter Temperatures Design for 20 C guarantees failure in Winter Aeration equipment and location can warm your digester in the winter.
29 Aerobic Digester Tips Low Temperature Slows Pathogen Reduction Slows Volatile Solids Reduction High Temperature Speeds Pathogen Reduction Speeds Volatile Solid Reduction
30 Aerobic Digester Tips Low DO does not slow pathogen reduction does not slow volatile solids reduction High DO Will cause ph to decrease Will waste electricity
31 Digester ph Management Endogenous Respiration BOD Bugs +O 2 = Less BOD Bugs +CO 2 + H 2 O + NH 3 Ammonia is produced
32 Digester ph Management Where there is Ammonia, There is sure to be nitrification Elements of Nitrification Ammonia Present Old Sludge Age Adequate Oxygen Adequate Temperature Adequate Alkalinity
33 Digester ph Management NH 3 +NH 3Bugs + O 2 + Alk.= More NH 3 Bugs + NO 3 1 Part 4 Parts 7 Parts Nitrification is an expensive process If you aerate continuously for long times, alkalinity may drop and ph drop.
34 Digester ph Management If ph drops, If nitrates are present Turn the aeration Off and Denitrify!
35 Oxygen Usage Hierarchy Free Dissolved Oxygen Aerobic or Oxic Treatment Little or No free Oxygen, but NO 3 present Anoxic Treatment Sulfate, SO 4 is the next choice of the Bugs Anaerobic conditions are beginning. ODORS fm. H 2 S 12
36 Denitrification Normal Bacteriological Respiration BOD + BOD Bugs + O 2 = More BOD Bugs + CO 2 + H NH 3 1 Part 1.25 Parts BOD + BOD Bugs + O 2 = More BOD Bugs + CO 2 + H NH 3
37 Denitrification NH 3 +NH 3Bugs + O 2 + Alk.= More NH 3 Bugs + NO 3 BOD + BOD Bugs + NO 3 = More BOD Bugs + CO 2 + H N 2 + Alk Nitrogen gas 1 Part 0.3 Parts 3.5 Parts Denitrifying returns alkalinity to the basin and stops ph drop
38 Agronomic Loading Rates Nitrogen Fertilizer value of the Biosolids The lower the nitrate the more can be applied per acre.
39 Agronomic Loading Rates
40 Agronomic Loading Rates
41 Agronomic Loading Rates Nitrate Levels Digester #1, 5700 mg/l Digester #2, 22,000 mg/l Digester #2 Sludge requires 30% more land for application.
42 Actual Land Application Case Biosolids Nitrate mg/l Not enough land to apply at the present Agronomic Loading Rate Initiated Off- On aeration 8 hours ON, 16 hours OFF Biosolids Nitrate mg/l, % reduction Application rates up and no need for more land.
43 Benefits of Denitrification Prevent ph drops by recycling Alkalinity Save money by recycling Oxygen Apply Biosolids at higher rates Improved Dewatering characteristics Reduce sludge volume Select against filaments
44 Denitrification reduces the Aerobic Digester Disadvantages High Aeration Costs, electricity, Reduced Digested Sludge more difficult to dewater, Improved Process affected by temperature changes More Sludge produced for disposal, Improved
45 Digester Case Study Two Stage Aerated 24/7, odors, odors, odors First Stage, primary and WAS Stage Two Low ph, as low as 6.0 s.u. and under, What would you do?
46 On More Issue Foaming This looks like nocardiaform foam If it is a problem Microscopic Exam Surface chlorinate 1% Cl 2 liquid spray on the foam when the air is OFF More than once per day is better.
47 More Foam Light smelly foam Primary Sludge Feed Not filaments Microscopic Exam Small solids Paper fibers
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