Wastewater treatment method for removing organic matter and nitrogen, carrier used thereof and method for manufacturing the carrier

• US 6,372,138 B1
• Filed: 09/27/2000
• Issued: 04/16/2002
• Est. Priority Date: 03/31/1998
• Status: Expired due to Term

• Current Assignee: Samsung Engineering Company Limited (Samsung Group)
• Original Assignee: Samsung Engineering Company Limited (Samsung Group)
• Inventors: Cho, Jae-hyun, Kim, Yong-hwan, Lee, Won-kwon, Lee, Yong-woo
• Primary Examiner(s): Upton, Christopher
• Application Number:
  US09/647,150
• Time in Patent Office: 566 Days
• Field of Search: 210/605, 210/615, 210/616, 210/621, 210/622, 210/626, 210/630, 210/150, 210/151, 210/903
• US Class Current: 210/605
• CPC Class Codes: C02F 3/30 Aerobic and anaerobic processes
• CPC Class Codes: C02F 3/302 Nitrification and denitrification treatment C02F3/308 takes precedence
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 210/903 Nitrogenous

Abstract

A wastewater treatment method for removing organic matter and nitrogen from wastewater. In the wastewater treatment method, an excessive amount of organic matter which prevents nitrifying bacteria from growing is removed in a leading aeration tank, and the conditions of the aeration tank are optimized using the nitrifying carrier to which a great amount of nitrifying bacteria can be attached for growth, such that the nitrifying bacteria can multiply therein. As a result, a large amount of wastewater can be treated within a short time, and it is possible to stably cope with a change in load of the organic matter of the wastewater. Thus, the wastewater treatment apparatus can be smaller, and an improvement in performance thereof can be expected. Also, the wastewater can be treated stably during the winter season when the activity of the nitrifying bacteria becomes low, so that the wastewater treatment method according to the present invention can be applied to most wastewater treatment plants, e.g., sewage treatment plants, excrement treatment plants, livestock and industrial wastewater treatment plants and the like.

Claims

1. A wastewater treatment method comprising the steps of:

(a) denitrifying wastewater flowing into an anoxic tank by reducing the nitrate nitrogen into gaseous nitrogen using denitrifying bacteria being resident in the anoxic tank, and organic matter of the wastewater flowing into the anoxic tank;

(b) making the carbon-to-nitrogen (C/N) ratio of the wastewater having undergone the step (a) suitable for a subsequent nitrification step after the wastewater flows into a first aeration tank by decomposing an excessive amount of organic matter using aerobic microorganisms attached to a carrier;

(c) changing ammonia nitrogen of the wastewater having undergone the step (b) into nitrate nitrogen after the wastewater flows into a second aeration tank by using nitrifying bacteria attached to a carrier;

(d) returning part of the wastewater having undergone the step (c) to the anoxic tank, while the remaining wastewater flows into a settling tank; and

(e) returning part of the sludge discharged from the settling tank to the anoxic tank, discarding the remaining sludge as surplus sludge, and obtaining a supernatant separated from the sludge settled in the settling tank as the treated water.

2. The method of claim 1, wherein the carrier used in the step (b) comprises:

a foamed polymer;

powdered active carbon attached to the foamed polymer; and

an adhesive for sticking the powdered active carbon to the foamed polymer.

3. The method of claim 2, wherein the foamed polymer is polyurethane, polystyrene or polyethylene, having a sponge foam or non-woven fabric structure.

4. The method of claim 2, wherein the adhesive is a mixture of acrylic resin and styrene/butadiene Latex (S/B Latex) in a weight ratio of 70:

30˜

90;

10.

5. The method of claim 2, wherein the powdered active carbon and the adhesive exist in a weight ratio of 40:

60˜

50;

50.

6. A method of claim 2, further comprising the step of preparing the carrier used in step (b) of claim 1, said carrier preparing step comprising the steps of:

(a) forming a slurry by mixing an adhesive solution and a powdered active carbon in a weight ratio of 90;

10˜

70;

30;

(b) coating the slurry on a foamed polymer, and evaporating solvent from the adhesive solution by heating the resulting product; and

(c) molding the resulting product of the step (b).

7. The method of claim 6, wherein heating of the step (b) is performed at 70˜

95°

C. for 2˜

3 hours.

8. The method of claim 1, wherein said carrier used in the step (c) comprises a polyvinyl alcohol foam carrier or a cellulose fiber carrier.

9. The method of claim 8, wherein the cellulose fiber is obtained from cotton, wood pulp, ramie, hemp, jute or flax.

10. The method of claim 8, further comprising the step of preparing the cellulose carrier by the steps of:

(a) molding a cellulose fiber into a planar shape;

(b) infiltrating the planar cellulose fiber with a foaming composition containing polyvinyl alcohol, a cross-linking agent and a foaming agent;

(c) foaming the resulting product of the step (b) by dehydrating;

(d) infiltrating the resulting product of the step (c) with a reinforcing composition containing polyvinyl alcohol and a cross-linking agent; and

(e) drying the resulting product of the step (d) taken out of the composition.

11. The method of claim 10, wherein the foaming composition comprises 0.5˜

5 wt % of polyvinyl alcohol, 0.2˜

5 wt % of cross-linking agent, 0.1˜

1 wt % of foaming agent, and solvent as the remainder.

12. The method of claim 11, wherein the cross-linking agent is melamine urea resin or polyamide polyamine epichlorhydrine (PPE).

13. The method of claim 10, wherein the reinforcing composition comprises 1˜

5 wt % of polyvinyl alcohol, 0.1˜

5 wt % of cross-linking agent, and solvent as the remainder.

14. The method of claim 13, wherein the cross-linking agent is melamine urea resin or polyamide polyamine epichlorhydrine (PPE).

15. The method of claim 10, wherein dehydration of the step (c) is performed such that the water content of the planar cellulose fiber before foaming is maintained at 20˜

50% based on the weight of the planar cellulose fiber.

16. The method of claim 10, wherein foaming in the step (c) is performed at 120˜

150°

C. such that the volume of pores per unit gram of the foamed cellulose carrier on the dry basis is in the range of 0.3˜

4.5cm³.

17. A wastewater treatment method comprising the steps of:

(a) denitrifying wastewater flowing into an anoxic tank by reducing the nitrate nitrogen into gaseous nitrogen using denitrifying bacteria being resident in the anoxic tank, and organic matter of the wastewater flowing into the anoxic tank;

(b) making the carbon-to-nitrogen (C/N) ratio of the wastewater having undergone the step (a) suitable for a subsequent nitrification step after the wastewater flows into a first aeration tank by decomposing an excessive amount of organic matter using aerobic microorganisms attached to a carrier;

(c) changing ammonia nitrogen of the wastewater having undergone the step (b) into nitrate nitrogen after the wastewater flows into a second aeration tank by using nitrifying bacteria attached to a carrier if the load of ammonia nitrogen of the wastewater to be treated exceeds a predetermined level;

(d) returning part of the wastewater having undergone at least step (b) to the anoxic tank, while the remaining wastewater flows into a settling tank; and

(e) returning part of the sludge discharged from the settling tank to the anoxic tank, discarding the remaining sludge as surplus sludge, and obtaining a supernatant separated from the sludge settled in the settling tank as the treated water.

18. A wastewater treatment method comprising the steps of:

(a) denitrifying wastewater flowing into an anoxic tank by reducing the nitrate nitrogen into gaseous nitrogen using denitrifying bacteria being resident in the anoxic tank, and organic matter of the wastewater flowing into the anoxic tank;

(b) making the carbon-to-nitrogen (C/N) ratio of the wastewater having undergone the step (a) suitable for a subsequent nitrification step after the wastewater flows into a first aeration tank by decomposing an excessive amount of organic matter using aerobic microorganisms attached to a carrier if the load by the organic matter of the wastewater to be treated exceeds a predetermined level;

(c) changing ammonia nitrogen of the wastewater having undergone at least step (a) into nitrate nitrogen after the wastewater flows into a second aeration tank by using nitrifying bacteria attached to a carrier;

(d) returning part of the wastewater having undergone the step (c) to the anoxic tank, while the remaining wastewater flows into a settling tank; and

(e) returning part of the sludge discharged from the settling tank to the anoxic tank, discarding the remaining sludge as surplus sludge, and obtaining a supernatant separated from the sludge settled in the settling tank as the treated water.