IP Library Granted Patent US 10,280,099
Granted Patent B2
US 10,280,099 · App. 15/313,698 · Granted May 7, 2019

Method for biological purification of waste water

Inventors: Gjermund Sørensen (Stange, NO); Sondre Eikås (Hamar, NO); Torgeir Saltnes (Eidsvoll, NO)
Assignee: Hias How2O AS
C02F3/308C02F3/08C02F2101/105Y02W10/15
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Quick Facts
Patent No.
US 10,280,099
App. No.
15/313,698
Granted
May 7, 2019
Kind
B2
Abstract

A circulating moving bed biofilm method for biological purification of waste water in a continuous process includes receiving a pretreated waste water inlet stream in an anaerobic zone of a reactor wherein micro-organism culture exist on free flowing biofilm carriers, letting the waste water stream with the biofilm carriers into an aerobic zone aerating the waste water stream and carriers received from the anaerobic zone, at an end of the aerobic zone, transferring the biofilm carriers to the anaerobic zone without transfer of water, and discharging the water through an outlet to a sludge separation process.

Claims (19)

1. A circulating moving bed biofilm method for biological purification of waste water in a continuous process comprising:

receiving a pretreated waste water inlet stream in an anaerobic zone of a reactor wherein micro-organism culture exist on free flowing biofilm carriers,

letting the waste water stream with the biofilm carriers into an aerobic zone aerating the waste water stream and carriers received from the anaerobic zone,

at an end of the aerobic zone transferring the biofilm carriers to the anaerobic zone without transfer of water, and

discharging the water through an outlet to a sludge separation process,

wherein an amount of phosphate in the outlet stream is less than 0.5 mg/l.

2. The method according to claim 1 comprising an anoxic zone between the anaerobic and aerobic zone.

3. The method according to claim 1 comprising mechanical transfer of the biofilm carriers between zones/chambers.

4. The method according to claim 2 wherein a part of an outlet stream from the outlet is re-introduced into the anoxic zone.

5. The method according to claim 1 wherein the filling ratio of carrier media is between 1% and 100% of the wet volume of the reactor.

6. The method according to claim 1 wherein the outlet stream proceeds to a separation step for collection of sludge for further treatment, and discharge of purified water to a recipient.

7. The method according to claim 1 , wherein an amount of phosphate in the outlet stream is less than 0.2 mg/l.

8. The method according to claim 1 wherein the filling ratio of carrier media is between 30% to 75% of the wet volume of the reactor.

9. A circulating moving bed biofilm reactor for continuous biological purification of waste water comprising:

an inlet to an anaerobic zone, optionally an anoxic zone, followed by an aerobic zone;

one or more devices for transfer of biofilm carriers from the aerobic zone to the anaerobic zone without water; and

an outlet.

10. The reactor according to claim 9 , wherein the one or more transport devices for transfer of biofilm carriers allow water to drain off.

11. The reactor according to claim 9 , wherein the one or more transport devices are selected from the group consisting of: elevators, transport screws and belt conveyers.

Assignments (2)
CHANGE OF NAME Recorded Mar 11, 2019
From: HIAS MILJØPARTNER AS
To: HIAS HOW2O AS
Reel/Frame 048567/0518 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 23, 2016
From: SØRENSEN, GJERMUND; EIKÅS, SONDRE; SALTNES, TORGEIR
To: HIAS MILJØPARTNER AS
Reel/Frame 040410/0551 →
Priority Claims (1)
NO 20140660 · May 28, 2014 · national
Continuity (1)
Related Publication 20170158534A1 · Jun 8, 2017
Cited By (1)
US 12,291,473