2. THE GROUP MEMBERS ARE,
TESSY S ALEX (UR12CE115)
ANJALI KUMARI (UR12CE013)
SURENDAR N (UR12CE111)
SUJITH ALEN S (UR12CE110)
JAESON ANTONY A (UR12CE046)
4. UNIT – IV Sewage Disposal and Sludge Management
Methods of sewage disposal, sewage farming
Sewage sickness and its preventive measures
Final products in Sludge Digester : stages
Factors affecting sludge digestion and control
Design of sludge digestion tank
Sludge thickening
Sludge conditioning and dewatering
Final disposal of digested sludge
Bioremediation: constructed wetlands, stabilization pond
Self purification and oxygen sag curve
7. Pre treatment
• Screening-for removal of objects
Eg: wood logs ,cloths, chappals
etc….
• Grit Chamber
For removing high density inorganic
particles by discrete settling
principle
Eg: Removal of sand, silt etc….
• Primary settling tank
For removal of low density organic
solids
8. Post treatment
• Secondary settling tank-for biomass
settling.
• Sludge from primary and secondary
settling tanks is sent to sludge
treatment unit.
17. [ ODOURLESS , DISPOSABLE IN NATURE WITHOUT POLLUTING OR
HARMING ]
SLUDGE IS STABILISED BY
DECOMPOSING THE ORGANIC
MATTER UNDER CONTROLLED
ANAEROBIC CONDITION.
[The decomposition of organic and inorganic matter in the
absence of molecular oxygen.]
20. THE MAIN TOPICS TO BE DISCUSSED IN THIS
PRESENTATION ARE,
(A) FINAL PRODUCTS IN SLUDGE
DIGESTER.
(B) STAGES IN SLUDGE DIGESTION
PROCESS.
&
(C) FACTORS AFFECTING SLUDGE
DIGESTION AND THEIR CONTROL.
25. 1. DIGESTED SLUDGE
• HUMUS LIKE SOLID MATTER.
• TARY BLACK IN COLOR.
• REDUCED MOISTURE CONTENT.
• QUALITY IS MUCH BETTER THAN UNDIGESTED
SLUDGE.
• FREE OF PATHOGENIC BACTERIA.
26. 2 . SUPERNATANT LIQUOR
• LIQUIFIED AND FINELY DIVIDED SOLID
MATTER.
• HIGH BOD (3000 ppm).
38. • HIGHLY OFFENSIVE ODOUR ARE EVOLVED FOR
3MONTHS.
• PH INCREASES TO ABOUT 6.8. HOW?
• DECOMPOSED SLUDGE ENTRAPS THE GASES
OF DECOMPOSITION. IT BECOMES FOAMY
AND RISES TO THE SURFACE TO FORM SCUM.
• BOD REMAIN HIGH.
39. 3. ALKALINE
FERMENTATION
• FINAL STAGE OF SLUDGE DIGESTION.
• PROTIENS
+
ORGANIC ACIDS
(ATTACKED BY
ANAEROBIC BACTERIA CALLED
METHANE FORMERS / STRICT ANAEROBER)
AMMONIA + ORGANIC ACIDS + GASES
HIGH RESISTANT MATERIALS
40. • THE LIQUID SEPARATES OUT FROM SOLIDS TO
FORM DIGESTED SLUDGE.
• THE SLUDGE IS GRANULAR AND STABLE .
• DOES NOT GIVE OFFENSIVE SMELL.
• IT HAS MUSTY EARTHY ODOUR.
• DIGESTED SLUDGE IS COLLECTED AT THE BOTTOM
OF THE DIGESTION TANK AND IS CALLED RIPENED
SLUDGE.
41. • IT IS ALKALINE IN NATURE.
• PH ≥ 7
• METHANE (60 % – 75%), 𝐶𝑂2 (30%), 𝑁2
• THIS STAGE EXTENTS TO A PERIOD OF 1 MONTH.
• BOD IS REDUCED.
42. CONCLUSION OF STAGES IN THE SLUDGE DIGESTION PROCESS
(NATURALLY)
• 4
1
2
MONTHS ARE REQUIRED FOR THE COMPLETE
PROCESS OF SLUDGE DIGESTION TO TAKE PLACE
UNDER NATURAL , UNCONTROLLED CONDITION AT
ABOUT 210
𝐶.
• DIGESTION DEPENDS ON MANY FACTORS LIKE
TEMPERATURE .
• IF THE FACTORS AFFECTING SLUDGE DIGESTION ARE
CONTROLLED , QUICKER AND EFFECTIVE DIGESTION
CAN BE DONE.
44. THE IMPORTANT FACTORS
AFFECTING SLUDGE
DIGESTION ARE ,
1 . TEMPERATURE
2 . PH VALUE
3 . SEEDING WITH DIGESTED SLUDGE AND
4 . MIXING AND STIRRING OF THE RAW SLUDGE
WITH DIGESTED SLUDGE.
45. THE MINOR FACTORS
ARE,
• QUALITY OF WATER SUPPLIED.
• PRESENCE OF –
COPPER,
FLUORIDES,
RADIO ACTIVE SUBSTANCES.
47. 1. TEMPERATURE
• HIGHER THE TEMPERATURE , HIGHER IS THE
RATE OF DIGESTION .
• THE 2 DISTINCT TEMPERATURE ZONES ARE,
- (a) ZONE OF THERMOPHILIC DIGESTION.
- (b) ZONE OF MESOPHILIC DIGESTION.
48. (a) ZONE OF THERMOPHILIC
DIGESTION
• THERMOPHILIC ORGANISMS MEAN HEAT LOVING
ORGANISMS.
• 400
𝐶 - 600
𝐶
• OPTIMUM THERMOPHILIC TEMPERATURE = 540
𝐶
• DIGESTION PERIOD – 10 TO 15 DAYS
• IT IS NOT PREFFERED BECAUSE OF ODOUR AND
OPERATIONAL DIFFICULTIES.
49. (b) ZONE OF MESOPHILIC
DIGESTION
• 250
𝐶 − 400
𝐶
• OPTIMUM MESOPHILIC TEMPERATURE = 290
𝐶
• DIGESTION PERIOD – 30 DAYS
• EXTERNAL HEATING DEVICES IS FIXED IN DIGESTION
TANK TO CONTROL TEMPERATURE.
51. 2. PH VALUE
• VOLATILE ACIDS METHANE FORMERS METHANE GAS
• IF METHANE FORMERS WERE NOT PRESENT IN THE SLUDGE
DIGESTER ,PH VALUE WILL GO BELOW 5 . IT WILL INCREASE THE
ACIDITY, AND THUS SUPPRESS FURTHER BACTERIAL ACTION.
• IN INITIAL STAGE (ACID FERMENTATION/ACID PRODUCTION
STAGE) PH VALUE OF 6.5 HAVE TO BE MAINTAINED.
• SO THAT IN FINAL STAGE (ALKALINE FERMENTATION
STAGE) PH VALUE OF 7.2 – 7.4 WILL BE MAINTAINED.
52. • ACIDITY INCREASES DUE TO
- OVERDOSING OF RAW SLUDGE .
- OVERWITHDRAWAL OF DIGESTED SLUDGE.
• REMEDY
- ADD HYDRATED LIME (2.3- 4.5 𝐾𝐺
1000 𝑃𝐸𝑅𝑆𝑂𝑁) IN RAW SLUDGE.
• FOR THE MAINTENANCE OF OPTIMUM VALUE OF PH
- WEIGHT OF RAW SLUDGE TO BE ADDED SHOULD BE 2 - 3%
WEIGHT OF DIGESTED SLUDGE WHICH IS REMOVING FROM
THE SLUDGE DIGESTER.
53. SEEDING WITH THE
SLUDGE DIGESTER
WHAT IS SEEDING ?
*A SLUDGE DIGESTION TANK .
*WHEN FIRST PUT IN OPERATION –
*DIGESTED SLUDGE FROM OLD SLUDGE DIGESTER
IS KEPT IN IT FOR SOME DAYS .
55. • WITHOUT SEEDING , IT MAY TAKE A FEW
MONTHS TO GET A TANK TO OPERATE
PROPERLY.
• PROPER SEEDING CAN GIVE GOOD RESULTS
QUICKLY.
56. MIXING AND STIRRING OF
THE RAW SLUDGE WITH
THE DIGESTED SLUDGE
• RAW SLUDGE + DIGESTED SLUDGE
(MIX WELL)
HOMOGENEOUS MIXTURE
*HELPS IN DECOMPOSITION OF ORGANIC MATTER
QUICKLY.
*MIXING IS DONE IN SLUDGE DIGESTOR USING
AGITATOR / OTHER DEVICES.
57. *THIS REDUCES SCUM AND INCREASES THE
PRODUCTION OF GAS.
*EXCESSIVE STIRRING WILL KILL USEFUL
BACTERIAS.