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

Bubble column and the use thereof

Patent 6375921 Issued on April 23, 2002. Estimated Expiration Date: Icon_subject May 23, 2020. 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

3073680

3752885

3853986

Sieve plates and distillation columns
Patent #: 4391675
Issued on: 07/05/1983
Inventor: Lynn ,   et al.

Liquid-phase catalyst-assembly for chemical process tower
Patent #: 5601797
Issued on: 02/11/1997
Inventor: Gentry

Process for the preparation of hydrogen peroxide Patent #: 5725837
Issued on: 03/10/1998
Inventor: Turunen

Inventors

Assignee

Application

No. 576178 filed on 05/23/2000

US Classes:

423/588, By oxidizing hydroquinone or anthraquinone261/114.1, Overflow baffles261/114.3, Jet plates422/189, And means providing discrete sequential reaction stages; e.g., train, 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.422/191, Superimposed reaction stages in single reaction chamber423/659MISCELLANEOUS PROCESS

Examiners

Primary: Langel, Wayne A.

Attorney, Agent or Firm

Foreign Patent References

  • 2 003 268 DE. 07/21/1971
  • 26 34 785 DE. 02/21/1978
  • 196 47 126 DE. 05/21/1997
  • 0 221 931 EP. 05/21/1987
  • 879539 GB. 10/21/1961

International Classes

C01B 015/023
F02M 029/04

Foreign Application Priority Data

1998-09-23 DE

Abstract

A bubble column can be operated using countercurrent flow including perforated trays. The space-time yield of gas-liquid reactions can be considerably increased if the perforated trays have a substantially uniform distribution of holes, if the cross-sectional area of the individual holes is 0.003 to 3 mm2, particularly 0.01 to 0.5 mm2, and if the open area of the trays is 3 to 20%, particularly 3 to 10%, and if the bubble column comprises passages for liquid between adjacent liquid zones.The bubble column can be used for carrying out gas-liquid reactions, such as oxidation reactions with air, with the gas and liquid preferably being passed in countercurrent flow through the column. Cocurrent flow may also be used.

Other References

  • Ullmann's Encyclopedia of Industrial Chemistry, 5th Ed. (1992), vol. B4, pp. 276-278, (no month)
  • Ullmann's Encyclopedia of Industrial Chemistry, 5th Ed. (1989), vol. A13, pp. 447-457. (no month
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