Bioreactor for treating sewage and sewage treatment system comprising the same

Patent metadata

Field	Value
Publication number	US-10494282-B2
Application number	US-201815953390-A
Country	US
Kind code	B2
Filing date	Apr 13, 2018
Priority date	Apr 18, 2017
Publication date	Dec 3, 2019
Grant date	Dec 3, 2019

Abstract

Disclosed is a bioreactor for treating sewage comprising an aerobic tank including a mixing cell for receiving sewage to be supplied from an inlet and mixing the sewage with activated sludge and an aerobic reactor tank in which the activated sludge adsorbs organic substance existing in the sewage; a backwashing cartridge filter for removing floc resulting from growth of the activated sludge adsorbing the organic substance; and an anaerobic tank for carrying out a denitrification process for denitrifying treated water flowed through the backwashing cartridge filter using anaerobic ammonium oxidation (anammox) bacteria wherein the backwashing cartridge filter allows the sewage discharged from the aerobic tank to pass through the cartridge filter and separates the floc and the treated water using difference in size between the floc contained in the sewage and pores in the cartridge filter, and wherein foreign matter adsorbed on the cartridge filter is easily removed by means of washing water to be injected into the cartridge filter.

First claim

What is claimed is:

1. A bioreactor for treating sewage comprising:
an aerobic tank including a mixing cell for receiving sewage to be supplied from an inlet and mixing the sewage with activated sludge and an aerobic reactor tank in which the activated sludge adsorbs organic substance existing in the sewage;
a backwashing cartridge filter for removing floc resulting from growth of the activated sludge adsorbing the organic substance; and
an anaerobic tank for carrying out a denitrification process for denitrifying treated water flowed through the backwashing cartridge filter using anaerobic ammonium oxidation (anammox) bacteria,
wherein the backwashing cartridge filter allows the sewage discharged from the aerobic tank to pass through the cartridge filter and separates the floc and the treated water using difference in size between the floc contained in the sewage and pores in the cartridge filter, and wherein foreign matter adsorbed on the cartridge filter is easily removed by means of washing water injected into the cartridge filter, and
wherein the backwashing cartridge filter comprises:
a cartridge filter housing;
a cartridge filter fixedly installed inside the cartridge filter housing to separate the floc and the treated water;
a transfer port arranged at an upper or lower end of the cartridge filter to allow the treated water flowed through the cartridge filter to be discharged therethrough; and
an inlet arranged at an upper or lower end of the cartridge filter to allow the washing water for removing the floc not having been passed through the cartridge filter to be introduced therethrough.

2. The bioreactor according to claim 1 , wherein the cartridge filter comprises a large number of pores having a diameter at 30 to 300 μm.

3. The bioreactor according to claim 1 , wherein the backwashing cartridge filter further comprises a sludge supply piping for transferring the separated floc to the aerobic tank.

4. The bioreactor according to claim 1 , wherein the activated sludge comprises one selected from the group consisting of ammonia-oxidizing archaea (AOA), ammonia-oxidizing bacteria (AOB) and nitrite-oxidizing bacteria (NOB).

5. The bioreactor according to claim 1 , wherein the aerobic reactor tank further comprises an air injection unit for injecting air.

6. A sewage treatment system comprising:
a primary sedimentation tank for sedimenting sewage containing sludge to separate the sewage into raw sludge and settled sewage water;
a bioreactor according to claim 1 for allowing organic substance in the settled sewage water separated in the primary sedimentation tank to be adsorbed on activated sludge such that the organic substance is separated out of the settled sewage water and carrying out a denitrification process;
a secondary sedimentation tank for sedimenting surplus sludge in the settled sewage water, on which the organic substance has adsorbed in an aerobic tank of the bioreactor;
a dehydration tank for dehydrating the raw sludge recovered by being sedimented in the primary sedimentation tank and the surplus sludge recovered by being sedimented in the secondary sedimentation tank;
a digestion tank for anaerobically digesting the raw sludge and the surplus sludge dehydrated in the dehydration tank to produce biogas; and
a sequential batch reactor (SBR) reaction tank for removing nitrogen by allowing supernatant containing ammonium generated in the digestion tank to react with anaerobic ammonium oxidation (anammox) bacteria.

7. The sewage treatment system according to claim 6 , wherein the bioreactor is configured to allow the organic substance in the sewage water to be adsorbed on the activated sludge and comprises a backwashing cartridge filter for separating floc resulting from growth of the activated sludge adsorbing the organic substance.

8. The sewage treatment system according to claim 7 , wherein the backwashing cartridge filter comprises:
a cartridge filter housing;
a cartridge filter fixedly installed inside the cartridge filter housing to separate the floc and the treated water;
a transfer port arranged at an upper or lower end of the cartridge filter to allow the treated water having been passed through the cartridge filter to be discharged therethrough; and
an inlet arranged at a lower or upper end of the cartridge filter to allow the washing water for removing the floc not having been passed through the cartridge filter to be introduced therethrough.

9. The sewage treatment system according to claim 8 , wherein the cartridge filter comprises a large number of pores having a diameter of 30 to 300 μm.

10. The sewage treatment system according to claim 6 , wherein the activated sludge comprises one selected from the group consisting of ammonia-oxidizing archaea (AOA), ammonia-oxidizing bacteria (AOB) and nitrite-oxidizing bacteria (NOB).

11. The sewage treatment system according to claim 6 , wherein the bioreactor further comprises an air injection unit for injecting air to allow the organic substance in the sewage water to be adsorbed on the activated sludge.

12. The sewage treatment system according to claim 6 , wherein the anaerobic ammonium oxidation (anammox) bacteria is Planctomycetes (Brocadia, Kuenenia, Anammoxoglobus, Jettenia and Scalindua including heterotrophic bacteria).

13. The sewage treatment system according to claim 6 , wherein the SBR reaction tank is connected to a treated water reservoir, and the treated water reservoir comprises a backwashing cartridge filter for selectively separating the activated sludge.

14. The sewage treatment system according to claim 6 , further comprising a biogas collector for collecting the biogas generated in the digestion tank.

15. A method of treating sewage comprising:
primarily sedimenting sewage containing sludge to separate the sewage into raw sludge and settled sewage water;
allowing organic substance in the settled sewage water separated in the primarily sedimenting sewage to be adsorbed on activated sludge such that the organic substance is separated out of the settled sewage water and carrying out a denitrification process;
secondarily sedimenting surplus sludge in the settled sewage water, on which the organic substance has been adsorbed, to separate the surplus sludge from treated sewage water;
recovering and discharging the treated sewage water from which the surplus sludge has been layer-separated by being sedimented in the secondarily sedimenting surplus sludge;
dehydrating the raw sludge recovered by being sedimented in the primarily sedimenting sewage and the surplus sludge recovered by being sedimented in the secondarily sedimenting surplus sludge;
anaerobically digesting the raw sludge and the surplus sludge dehydrated to produce biogas; and
removing nitrogen by allowing supernatant containing ammonium to react with anaerobic ammonium oxidation (anammox) bacteria.

16. The method according to claim 15 , wherein the allowing organic substance is configured to allow the organic substance in the settled sewage water to be adsorbed on the activated sludge such that floc resulting from growth of the activated sludge adsorbing the organic substance is separated and wherein a backwashing cartridge filter is utilized in order to separate the floc.

17. The method according to claim 15 , wherein the activated sludge comprises one selected from the group consisting of ammonia-oxidizing archaea (AOA), ammonia-oxidizing bacteria (AOB) and nitrite-oxidizing bacteria (NOB).

18. The method according to claim 15 , wherein the anaerobic ammonium oxidation (anamm

Assignees

• Doosan Heavy Ind & Construction Co Ltd
• Doosan Heavy Ind Constr Co Ltd

Inventors

• Cho Hwan Chul
• Kim Seong Ju
• Jin Yang Oh
• Lee Chul Woo

Classifications

• C02F2101/38

  containing nitrogen · CPC title

• C02F2201/006

  Cartridges · CPC title

• C02F2101/16

  Nitrogen compounds, e.g. ammonia · CPC title

• C02F3/302

  Nitrification and denitrification treatment (C02F3/308 takes precedence) · CPC title

• C02F2001/007

  Processes including a sedimentation step · CPC title