U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Catalytic method and device for controlling VOC. CO and halogenated organic emissions

Patent 5451388 Issued on September 19, 1995. Estimated Expiration Date: Icon_subject January 21, 2014. 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

3767453

3785998

3920583

Method of decomposing halohydrocarbons
Patent #: 3972979
Issued on: 08/03/1976
Inventor: Kageyama

Method of decomposing chlorohydrocarbons
Patent #: 4053557
Issued on: 10/11/1977
Inventor: Kageyama

Decomposition of halogenated organic compounds
Patent #: 4059675
Issued on: 11/22/1977
Inventor: Yang ,   et al.

Decomposition of halogenated organic compounds
Patent #: 4059676
Issued on: 11/22/1977
Inventor: Yang ,   et al.

Decomposition of halogenated organic compounds
Patent #: 4059683
Issued on: 11/22/1977
Inventor: Lindberg ,   et al.

Catalytic process for reducing nitrogen oxides to nitrogen
Patent #: 4085193
Issued on: 04/18/1978
Inventor: Nakajima, et al.

Metal oxide having uniform pore sizes, the process for producing said metal oxide, and catalyst carrier comprising the said metal oxide
Patent #: 4622311
Issued on: 11/11/1986
Inventor: Wakui ,   et al.

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Inventors

Assignee

Application

No. 184312 filed on 01/21/1994

US Classes:

423/240R, Halogenous component422/171, Solid, extended surface, fluid contact type422/177, Including solid, extended surface, fluid contact reaction means; e.g., inert Raschig rings, particulate absorbent, particulate or monolithic catalyst, etc.422/190, Plural solid, extended surface, fluid contact reaction stages each containing; e.g., inert Raschig rings, particulate sorbent, particulate or monolithic catalyst, etc.422/193, Reaction stages located within single reaction chamber422/211, Including solid, extended surface, fluid contact reaction means; e.g., inert Raschig rings, particulate absorbent, particulate or monolithic catalyst, etc.423/245.3, By burning or catalytically combusting component423/247Utilizing solid sorbent, catalyst, or reactant

Examiners

Primary: Warden, Robert J.
Assistant: Thornton, Krisanne

Foreign Patent References

  • WO90/13352 WO. 11/13/1990

International Classes

B01D 050/00
B01D 053/00

Abstract

A method and device for treating a gas stream comprising at least one non-halogenated carbonaceous compound and optionally at least one halogenated organic compound. The gas stream, at 100° C. to 650° C. and in the presence of oxygen is contacted with a first catalyst in a first catalyst zone. The first catalyst comprises a first catalytic material deposited on a low acidity support material. In this zone, the non-halogenated compound is selectively reacted to form innocuous materials such as water and carbon monoxide. This can be followed by contacting the gas stream with a second catalyst in a second catalyst zone. The second catalyst comprises a second catalytic material deposited on a high acidity support material. In this zone, the halogenated organic compounds are reacted.

Other References

  • Journal of Applied Chemistry and Biotechnology, 1975, vol. 25, pp. 241-248, "Catalysed Destruction of Chlorinated Hydrocarbons", Bond & Sadeghi
  • Journal of Catalysis 130, 76-85 (1991), "Oxidative Catalysis of Chlorinated Hydrocarbons by Metal-Loaded Acid Catalysts", Chatterjee and Greene
  • Ind. Eng. Chem. Res. 1987, 26, 2165-2180, "Complete Catalytic Oxidation of Volatile Organics", J. J. Spivey
  • J. Chem. Soc., 1986, 82, 3667-3679, "Physicochemical Properties and Isomerization Activity of Chlorinated Pt/Al202 Catalysts", Melchor, et a
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