Biological treatment of waste water

• US 4,443,337 A
• Filed: 02/25/1982
• Issued: 04/17/1984
• Est. Priority Date: 03/31/1978
• Status: Expired due to Term

• Current Assignee: Toray Industries Incorporated
• Original Assignee: Toray Industries Incorporated
• Inventors: Otani, Mitsunobu, Hirose, Michio, Senda, Teruo
• Primary Examiner(s): Wyse, Thomas G.
• Application Number:
  US06/352,203
• Time in Patent Office: 782 Days
• Field of Search: 210/602, 210/609, 210/615-618, 210/625, 210/614
• US Class Current: 210/602
• CPC Class Codes: C02F 3/04 using trickle filters
• CPC Class Codes: C02F 3/121 Multistep treatment
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

A method for biologically purifiying waste water which produces substantially no excess waste sludge is provided. In this method, a waste water containing biodegradable substances is treated in a biological fixed film type reactor and aqueous water sludge discharged from the reactor is aerobically digested after being separated from the biologically treated waste water. The digested aqueous sludge is returned to the reactor or the upstream thereof. This method can be advantageously combined with any installed activated sludge type water purification process, to thereby substantially eliminate the production of excess waste sludge from the water purification system.

Claims

1. A method for biologically purifying waste water containing biodegradable substances comprising the steps of:

a. contacting the waste water with microorganisms in a biological fixed film type reactor under conditions sufficient to degrade the biodegradable substances and to produce a sludge which contains a mixture of bacteria, protozoa, and large organisms;

b. separating and concentrating the sludge from the biologically treated waste water discharged from the reactor of step (a) in the presence of sufficient oxygen to maintain life in the protozoa and large organisms of the sludge by using a static inclined screen separator;

c. aerobically digesting the sludge discharged from the separator of step (b) in the presence of sufficient oxygen to maintain life in the protozoa and large organisms of the sludge by using a digester; and

d. returning substantially all of the digested sludge containing live protozoa and live organisms to the reactor of step (a) or to a line upstream thereof, whereby substantially all of the sludge is recycled.

2. The method defined in claim 1, wherein the digestion step is performed for a period of 5 to 60 days.

3. The method defined in claim 2, wherein the period is 10 to 30 days.

9. A method for biologically purifying waste water as defined in claim 1 or 4, wherein said inclined screen separator has a wedge wire screen composed of a plurality of parallel spaced rows of wedge wires each having a V cross sectional shape.

10. The method defined in claim 1 or 4, wherein said biological film type reactor comprises a vessel having an inlet for influent and an outlet for effluent and is provided with a support within the vessel onto which microorganisms are attached.

11. The method defined in claim 1 or 4, wherein said biological film type reactor comprises:

i. a vessel having an inlet and an outlet for the waste water and having means for holding the waste water;

ii. a support comprising a plurality of perforated plates or sheets or net-like materials substantially vertically mounted within the vessel substantially parallel and spaced from each other, and

iii. an aeration device mounted under the support for continuously and uniformly supplying air to the waste water present in the vessel.

12. The method defined in claim 1 or 4, wherein said concentrated sludge is transported to said aerobic digestion step on a belt conveyor.

13. The method defined in claim 1 or 4, wherein said concentrated sludge is transported to said aerobic digestion step by gravity.

14. The method defined in claim 1 or 4, wherein said concentrated sludge is transported continuously to said aerobic digestion step.

15. The method defined in claim 1 or 4, wherein said concentrated sludge is transported semi-continuously to said aerobic digestion step.

16. The method defined in claim 1 or 4, wherein said concentrated sludge is transported to said aerobic digestion step within a period of four hours.

17. The method defined in claim 1 or 4, wherein said concentrated sludge is transported to said aerobic digestion step within one hour.

18. The method defined in claim 1 or 4, wherein aerobically digested sludge is returned to the biological film reactor from the aerobic digester and is absorbed onto or into the surfaces of biological fixed films and converted therein to fresh biological films, with digestion by microbiological food chains.

19. The method defined in claim 1 or 4, wherein poisonous substances accumulated in the aerobic digestion step, which substances would inhibit the digestion reaction, are washed off or degraded by bacteria in the course of the recycling step.

20. The method defined in claim 1 or 4, wherein microbiological food chains are formed in the recycling system.

21. The method defined in claim 1 or 4, wherein the amount of water treated, per unit of area of the separating element utilized in step (b), is about 10-10,000m³ /m² /day.

22. The method defined in claim 21, wherein said amount is about 100-500m³ /m² /day.

4. A method for biologically purifying waste water containing biodegradable substances comprising the steps of:

a. dividing a stream of the waste water into two portions;

b. contacting a portion of the waste water with suspended microorganisms in water in an activated sludge type reactor under conditions sufficient to degrade the biodegradable substances to produce a sludge;

c. simultaneously and separately treating another portion of the waste water by contact with microorganisms in a biological fixed film type reactor under conditions sufficient to degrade the biodegradable substances and to produce a sludge which contains a mixture of bacteria, protozoa, and large organisms;

d. separating and concentrating the sludge from the biologically treated waste water discharged from the reactor of step (c) in the presence of sufficient oxygen to maintain life in the protozoa and large organisms of the sludge by using a static inclined screen separator;

e. aerobically digesting a mixture of sludges discharged from the reactor of step (b) and the separator of step (d) in the presence of sufficient oxygen to maintain life in the protozoa and large organisms of the sludge by using a digester; and

f. returning substantially all of the digested sludge containing live protozoa and live organisms to the reactor of step (b), to the reactor of step (c) or to a line upstream thereof, whereby substantially all of the sludge is recycled.

5. The method defined in claim 4, wherein the digestion step is performed for a period of 3 to 30 days.

6. The method defined in claim 5, wherein the period is 5 to 20 days.

7. The method defined in claim 4, wherein a mixing ratio of the sludge discharged from step (b) to that discharged from step (d) is within the range of from 98:

2 to 50;

50 in terms of the dry weight of the sludge.

8. The method defined in claim 7, wherein the mixing ratio is 95:

5 to 70;

30.