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

Apparatus and method for mixing components with a venturi arrangement

Patent 6796704 Issued on September 28, 2004. Estimated Expiration Date: Icon_subject June 6, 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

1982479

3298669

3542342

3741533

Mixing method
Patent #: 3994480
Issued on: 11/30/1976
Inventor: Fothergill ,   et al.

Eductor-mixer system
Patent #: 4186772
Issued on: 02/05/1980
Inventor: Handleman

Multi-stage centrifugal mixer
Patent #: 4345841
Issued on: 08/24/1982
Inventor: Day

Method and apparatus for wetting powder
Patent #: 4390284
Issued on: 06/28/1983
Inventor: Hyde ,   et al.

Mixing nozzle
Patent #: 4407456
Issued on: 10/04/1983
Inventor: Daniel, deceased ,   et al.

Spray jet polymer powder wetter
Patent #: 4531673
Issued on: 07/30/1985
Inventor: Holland ,   et al.

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Inventor

Application

No. 09588210 filed on 06/06/2000

US Classes:

366/163.2, By venturi or jet pump type device366/165.2, Including deflector in chamber (deflector may be part of chamber wall)366/178.1Concentric

Examiners

Primary: Cooley, Charles E.

Attorney, Agent or Firm

Foreign Patent References

  • 50312 EP 04/01/1982

International Class

B01F 1502

Abstract

An eductor mixing device (10) has a main body or housing (28) of a generally cylindrical shape and an inner tube (42) for one component to be mixed with a liquid is mounted in main body (28) with a vortex chamber (56) formed in an annulus between the main body (28) and the inlet flow tube (42). Pressurized liquid enters the vortex chamber through a generally rectangular entrance opening (36) along an arcuate surface (42) which smoothly merges with the cylindrical surface (30) of the main body or housing (28). A liquid in a swirling motion moves in a descending helical path about inner tube (42) and passes through a gap G between coaxial frusto-conical surfaces (55) and (68) of the converging inner nozzle (52) of the inner tube (42) and an outer coaxial liquid nozzle (60) of diffuser ring (58) . A high velocity is created by the swirling liquid for exerting a suction or negative pressure at the lower end of inner nozzle (52) to draw the component to be mixed, such as a particulate material, into the swirling liquid stream where the swirling liquid and particulate material form a strong vortex to create a slurry in a minimal travel distance after passing inner converging nozzle (52) of particulate inner tube (42).

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