Methods and apparatus for biological treatment of waste waters

• US 20050115880A1
• Filed: 05/17/2004
• Published: 06/02/2005
• Est. Priority Date: 02/23/2001
• Status: Active Grant

• Current Assignee: Vost Environmental Technologies, Inc.
• Original Assignee: VAI Ltd.
• Inventors: Pollock, David C.
• Granted Patent: US 7,018,530 B2
• Time in Patent Office: Days
• US Class Current: 210/194
• CPC Class Codes: C02F 1/24 by flotation C02F1/465 takes precedence
• CPC Class Codes: C02F 1/32 with ultraviolet light
• CPC Class Codes: C02F 11/185 by pasteurisation
• CPC Class Codes: C02F 2301/106 Thermophilic treatment
• CPC Class Codes: C02F 3/02 Aerobic processes
• CPC Class Codes: C02F 3/1268 Membrane bioreactor systems
• CPC Class Codes: C02F 3/226 "Deep shaft" processes
• CPC Class Codes: C02F 3/301 Aerobic and anaerobic treatment in the same reactor
• CPC Class Codes: C02F 3/308 Biological phosphorus removal
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10T 29/49826 Assembling or joining

Abstract

In a vertical shaft bioreactor, improved devices and methods are provided for enhanced secondary and/or tertiary treatment of wastewater, including residential, municipal and industrial wastewater. The devices and methods of the invention are useful for enhanced secondary wastewater treatment, including BOD and TSS removal. Tertiary treatment can alternately or additionally be achieved in the bioreactor with nitrification of ammonia, with nitrification and denitrification, and with nitrification, denitrification, and chemical phosphorus removal. A vertical shaft bioreactor is also provided which achieves thermophilic aerobic digestion and pasteurization of sewage sludges, optionally to produce class A biosolids.

Claims

1-31. -31. (canceled)

32. A long vertical shaft bio-reactor for the purification of waste waters containing biodegradable organic matter comprising:

at least one primary downflow channel extending downward to a depth of approximately 70-90% of a total depth of the bio-reactor;

at least one primary upflow channel in fluid connection with said primary downflow channel defining a mixing zone located below a lower port of the primary downflow channel, said primary upflow channel partitioned by at least one partition, valve, or baffle into at least first and second superior upflow channels fluidly connected with said primary upflow channel;

said first superior upflow channel in fluid connection with said primary downflow channel through a first head tank, said first head tank fitted with a degassing plate to direct flow from said first superior upflow channel laterally to effectuate degassing;

a waste water influent channel fluidly connected with said first superior upflow channel;

a first fluid flow regulator operable to regulate fluid flow between said waste water influent channel and said first superior upflow channel;

said second superior upflow channel in fluid connection with a second head tank, said second head tank fitted with a degassing plate to direct flow from said second superior upflow channel laterally to effectuate degassing;

a recirculation channel fluidly connected with said second superior upflow channel;

a second fluid flow regulator operable to regulate fluid flow between said recirculation channel and said second superior upflow channel; and

,

a gas distribution port for distributing an oxygen-containing gas into said primary upflow channel to generate air-lift within said primary upflow channel, wherein said first superior upflow channel and said first head tank partially define a first treatment zone and said second superior upflow channel and said second head tank partially define a second treatment zone.

33. The long vertical shaft bio-reactor of claim 32, wherein said first and second treatment zones are structurally segregated to prevent substantial liquid transfer between said first and second treatment zones.

34. The long vertical shaft bio-reactor of claim 32, wherein said first and second treatment zones are structurally segregated by a self-batching air lock that functions to substantially prevent fluid transfer between said first and second treatment zones to minimize heat loss in the bio-reactor.

35. The long vertical shaft bio-reactor of claim 32, wherein said first treatment zone surrounds or is positioned adjacent to said second treatment zone.

36. The long vertical shaft bio-reactor of claim 32, wherein said first treatment zone further comprises said primary downflow channel and said primary upflow channel.

37. The long vertical shaft bio-reactor of claim 32, wherein said second treatment zone is surrounded by a second sealed outer wall to minimize heat loss from the bio-reactor to surrounding geological materials.

38. The long vertical shaft bio-reactor of claim 32, wherein each of said first and second treatment zones comprise independent aeration means.

39. The long vertical shaft bio-reactor of claim 32, wherein each of said first and second treatment zones comprise an upper circulating zone and a lower pseudo plug flow zone.

40. The long vertical shaft bio-reactor of claim 32, wherein deoxygenation in said first treatment zone can be achieved without mechanical mixers.

41. The long vertical shaft bio-reactor of claim 32, wherein denitrification in said first treatment zone can be achieved without mechanical mixers.

42-74. -74. (canceled)