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Aerobic biological dehalogenation reactor

Patent 5057221 Issued on October 15, 1991. Estimated Expiration Date: Icon_subject December 19, 2008. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

Microbial degradation of DDT
Patent #: 3979283
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Method for producing microbial cells and use thereof to produce oxidation products
Patent #: 4266034
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Issued on: 04/06/1982
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Inventor: Jhaveri ,   et al.

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Microbiological oxidations
Patent #: 4455373
Issued on: 06/19/1984
Inventor: Higgins

Microbiological oxidation process
Patent #: 4473643
Issued on: 09/25/1984
Inventor: Higgins

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Inventors

Assignee

Application

No. 287477 filed on 12/19/1988

US Classes:

210/610, Including adding ancillary growth medium for microorganism210/617, In bed form210/631, And additional treating agent other than mere mechanical manipulation (e.g., chemical, sorption, etc.)210/747, Including geographic feature (e.g., drainage ditch, septic, pond)210/908, Organic435/250, Having five or less carbon atoms435/267Treating animal or plant material or micro-organism

Examiners

Primary: Wyse, Thomas G.

Attorney, Agent or Firm

Foreign Patent References

  • 1148488 CA. 06/13/1983
  • 3208977A1 DE. 09/13/1983
  • 239197A1 DE. 09/13/1986

International Class

C02F 003/34

Abstract

Methylotrophic and heterotrophic microorganisms are supported on a rigid substrate bed. Oxygen, such as from air, and a low-molecular-weight alkane, such as methane, flow through the bed. Organic compounds in contaminated water processing through the bed are biodegraded by the microorganisms. The bed may be formed of manufactured particlate material, such as of activated carbon. These bed-forming materials may be preloaded with organic carbon materials to provide a nutrient source for the microogranisms. The biological reactor may continuously treat effluent from, for example, an industrial plant, in either a batch or continuous process. A water solids removal subsystem may be positioned upstream of the biological reactor to remove organic carbon compounds and various solids from the contaminated water prior to treatment. Optional bed cleaning mechanisms may also be included in the biological reactor. A methane gas source for the biological reactor may comprise a methanogenic microorganism-containing second reactor which uses liquid from the first biological reactor as a carbon and energy source.

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