U.S. patents available from 1976 to present.
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Catalyst for purifying fumigation exhaust gases and a method of purifying fumigation exhaust gases

Patent 6051198 Issued on April 18, 2000. Estimated Expiration Date: Icon_subject July 7, 2017. 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

Production of shaped catalysts or carriers comprising titanium oxides
Patent #: 4113660
Issued on: 09/12/1978
Inventor: Abe ,   et al.

Catalyst for purifying exhaust and waste gases
Patent #: 4221768
Issued on: 09/09/1980
Inventor: Inoue ,   et al.

Process for hydrocracking heavy hydrocarbon oils and catalyst therefor
Patent #: 4440631
Issued on: 04/03/1984
Inventor: Togari ,   et al.

Treatment equipment of exhaust gas containing organic halogen compounds
Patent #: 5238656
Issued on: 08/24/1993
Inventor: Tajima, et al.

Catalytic incineration of organic compounds
Patent #: 5283041
Issued on: 02/01/1994
Inventor: Nguyen, et al.

Catalytic method and device for controlling VOC. CO and halogenated organic emissions
Patent #: 5451388
Issued on: 09/19/1995
Inventor: Chen, et al.

Catalytic system for the reduction of nitrogen oxides Patent #: 5552129
Issued on: 09/03/1996
Inventor: Farnos, et al.

Inventors

Assignee

Application

No. 860464 filed on 07/07/1997

US Classes:

423/240SSolid removal agent

Examiners

Primary: Griffin, Steven P.
Assistant: Hendrickson, Stuart L.

Attorney, Agent or Firm

Foreign Patent References

  • 0 415 145 A1 EP. 03/11/1991
  • 0 544 282 A1 EP. 06/11/1993
  • 5-23598 JP. 02/11/1993
  • 6-165915 JP. 06/11/1994
  • 7-299329 JP. 11/11/1995
  • 7-318036 JP. 12/11/1995
  • 8-24572 JP. 01/11/1996
  • WO 90/13352 WO. 11/11/1990

International Class

C01B 007/00

Foreign Application Priority Data

1995-01-05 JP

Abstract

A catalyst of the present invention is adapted for purifying fumigation exhaust gases, and comprises, as a catalyst component A, a metal oxide containing at least one, or a composite oxide containing two or more metals selected from the group consisting of Ti, Si and Zr; and, as a catalyst component B, an oxide containing at least one selected from the group consisting of V, Cu, W and Cr; and has an average micropore diameter in the range of 0.010 to 0.070 μm, a total micropore volume in the range of 0.30 to 0.60 ml/g, and a specific surface area in the range of 50 to 200 m2 /g. The use of this catalyst makes it possible to economically and efficiently purify fumigation exhaust gas.

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