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

System and process for hydrocyclone separation of particulate solids and at least one liquid phase from a multiphase liquid mixture

Patent 5350525 Issued on September 27, 1994. Estimated Expiration Date: Icon_subject September 11, 2012. 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

3723309

3764008

Separator
Patent #: 4519848
Issued on: 05/28/1985
Inventor: Underwood

Tangentially staged hydrocyclones
Patent #: 4711720
Issued on: 12/08/1987
Inventor: Young

Cyclone separator
Patent #: 4738779
Issued on: 04/19/1988
Inventor: Carroll ,   et al.

Low pressure hydrocyclone separator
Patent #: 4844817
Issued on: 07/04/1989
Inventor: Flanigan ,   et al.

Low pressure hydrocyclone separator
Patent #: 4900445
Issued on: 02/13/1990
Inventor: Flanigan, et al.

Separating liquids
Patent #: 4995989
Issued on: 02/26/1991
Inventor: Carroll, et al.

Oil and water separating system with hydrocyclone and floatation device
Patent #: 5021165
Issued on: 06/04/1991
Inventor: Kalnins

Cyclone separator Patent #: 5032275
Issued on: 07/16/1991
Inventor: Thew

Inventors

Assignee

Application

No. 943845 filed on 09/11/1992

US Classes:

210/744, Level sensing210/512.2, Multiple cyclone210/788, Introducing liquid tangentially210/805And recirculating liquid

Examiners

Primary: Drodge, Joseph W.

Attorney, Agent or Firm

Foreign Patent References

  • 1096238 SU 06/13/1984

International Classes

B01D 017/12
B01D 017/038

Abstract

This invention relates to a system for separating a multiphase liquid mixture into a plurality of streams. The invention has particular utility in the oil industry where particulate solids are produced with an oil/water mixture. Preferably, the mixture is first cyclonically separated to remove particulate solids from the oil and water. Then the mixture is delivered to a liquid/liquid hydrocyclone where a substantial portion of the oil is separated from the remaining mixture which now primarily comprises water. The pressure of the remaining mixture is elevated such as by a pump and is then subjected to a further cyclonic separation step to remove any remaining fine solids in the mixture.

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