Method for conditioning and dewatering thermophilic aerobically digested biosolids

• US 6,685,834 B1
• Filed: 12/20/1999
• Issued: 02/03/2004
• Est. Priority Date: 12/20/1999
• Status: Expired due to Fees

• Current Assignee: Kruger Incorporated
• Original Assignee: Kruger Incorporated
• Inventors: Novak, John T., Murthy, Sudhir N., Hong, Sun-Nan, Holbrook, R. David
• Primary Examiner(s): Barry, Chester T.
• Application Number:
  US09/467,814
• Time in Patent Office: 1,506 Days
• Field of Search: 210/609, 210/612, 210/613, 210/620-623, 210/723, 210/727, 210/732, 210/733, 210/631
• US Class Current: 210/613
• CPC Class Codes: C02F 11/02 Biological treatment
• CPC Class Codes: C02F 11/148 Combined use of inorganic and organic substances, being added in the same treatment step
• CPC Class Codes: C02F 2301/106 Thermophilic treatment
• CPC Class Codes: Y02W 10/20 Sludge processing

Abstract

A Method of treating sludge prior to dewatering by mixing with the sludge a cationic metal in the form of an iron or aluminum slat along with a cationic polymer. The addition of the iron or aluminum salt substantially reduces the amount of polymer required for acceptable dewatering, thusly significantly reducing the cost of the dewatering process. The method is enhanced by subjecting the prior digested sludge to mesophilic aeration prior to the cationic metal salt and polymer being added.

Claims

1. A method for digesting, conditioning and dewatering sludge comprising:

a. directing sludge to an autothermal thermophilic aerobic digester (ATAD) and subjecting the sludge to an ATAD digestion process;

b. directing the ATAD digested sludge to a mesophilic aerator and subjecting the digested sludge to mesophilic aeration;

c. after the ATAD sludge has been subjected to mesophilic aeration, mixing with the sludge a metal salt selected from the group consisting of ferric chloride, ferrous chloride, and alum;

d. mixing a cationic polymer with the sludge and wherein the metal salt along with the cationic polymer forms conditioned sludge; and

e. directing the conditioned sludge to a dewatering station and dewatering the sludge.

2. The method of claim 1 including the step of nitrfying ammonia nitrogen present in the sludge in the mesophilic aerator.

3. The method of claim 1 wherein the ATAD digestion process produces a digested sludge having concentrations of COD, protein, and polysaccharides, and wherein adding the metal salt to the ATAD digested sludge tends to reduce the concentration of COD, protein and polysaccharides within solution.

4. The method of claim 1 including subjecting the sludge to a temperature of approximately 50°

-70°

C. during the ATAD digestion process.

5. The method of claim 4 including subjecting the ATAD sludge to a temperature of 20°

-40°

C. during mesophilic aeration.

6. A method for digesting, conditioning and dewaterlng sludge comprising:

a) subjecting the sludge to autothermal thermophilic aerobic digestion (ATAD) and in the process producing concentrations of COD Including protein and polysaccharides;

b) directing the ATAD sludge to a mesophilic aerator and subjecting the ATAD digested sludge to mesophilic aeration;

c) treating the ATAD digested sludge and COD by mixing a metal salt with the ATAD sludge wherein the metal salt is based on iron or aluminum and wherein the metal salt effectively drives quantities of COD from solution and thereby decreases the polymer demand for acceptable dewatering of the sludge, and wherein the metal salt is mixed with the sludge after the sludge has been subjected to mesophilic aeration;

d) mixing at least one cationic polymer with the digested sludge to promote flocculation and dewatering;

e) directing the conditioned sludge to a dewatering station and dewatering sludge; and

f) wherein the aeration is achieved through a mesophilic aerator and the ATAD digested sludge is aerated therein for a period of approximately 10-15 days at a temperature of approximately 20-40°

C.

7. The method of claim 6 including the step of aerating the ATAD digested sludge.

8. The method of claim 7 wherein the metal salt is mixed with the sludge after the sludge has been aerated.

9. The method of claim 7 wherein the aeration is achieved through a mesophilic aerator and the ATAD digested sludge is aerated therein for a period of approximately 10-15 days at a temperature of approximately 20-40°

C.

10. The method of claim 6 wherein the metal salt is selected from the group consisting of ferric chloride, ferrous chloride and alum.

11. The method of claim 10 wherein the metal salt is mixed with the sludge at the rate of approximately 0.02-0.20 lb of iron or iron equivalent per pound of dry solids.

12. The method of claim 11 wherein the polymer is mixed with the sludge at the rate of approximately 15-25 lbs per dry ton of solids.

13. The method of claim 6 including subjecting the sludge to a temperature of 50°

-70°

C. during the ATAD digestive process.