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

Method and a means for continuous, static mixing of thin layers

Patent 5507573 Issued on April 16, 1996. Estimated Expiration Date: Icon_subject November 19, 2013. 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

969978

1713260

1921059

2236551

Continuous flow static mixer for mixing powder and/or suspension materials with liquid materials
Patent #: 4191480
Issued on: 03/04/1980
Inventor: Hiorth

Process and apparatus for adding liquid components to pourable powdered or granular materials
Patent #: 4323314
Issued on: 04/06/1982
Inventor: Kaiser-Wirz

Apparatus for producing a gas solid two phase flow jet having a constant mass or volume flow rate and predetermined velocity
Patent #: 4573801
Issued on: 03/04/1986
Inventor: Leschonski ,   et al.

Premix injection system for asphalt compositions Patent #: 4662759
Issued on: 05/05/1987
Inventor: Leibee ,   et al.

Inventor

Application

No. 129113 filed on 11/19/1993

US Classes:

366/137.1, JET OR SPRAY IMPINGING FREE-FALLING STREAM239/417.3, Valving means for central fluid239/424, Flow means of one fluid surrounds the other at outlet366/178.1Concentric

Examiners

Primary: Cooley, Charles E.

Attorney, Agent or Firm

Foreign Patent References

  • 135398 DK. 04/13/1977
  • 1181952 FR. 06/13/2012
  • 2041230 DE. 06/13/1982
  • 140968 NO. 09/13/1979
  • 427328 SE. 03/13/1983

International Class

B01F 005/24

Foreign Application Priority Data

1991-04-05 NO

Abstract

A method and apparatus for controlling the volume or quantity of components being fed into a continuous, static mixing head are based upon the phenomenon of concentric, thin layers meeting with high velocities in a circular and free-flowing mixing zone (14). The regulating method can be adapted to various embodiments of mixing heads, and can be used for raw material combinations comprising powders, liquids, gas vapor or air, as well as mixing a small quantity into a large quantity. The thin layers are formed and controlled in conical, annular nozzles between fixed cone surfaces (12, 25, 27) and axially movable cone surfaces (11, 28, 29), where the movements are transferred from displacement members (15, 34) on the outside of the mixing head which regulate nozzle orifices and amounts or volumes. One situation regulates a mixing head where a downward directed powder layer in the mixing zone meets with obliquely downward directed liquid layers from the inside and the outside. In the mixing zone, mixing and discharge occurs instantaneously. A mixing process for cement related products uses three mixing heads connected in series, with different products after each respective steps. The mixing heads are compact. Capacities of up to 150 m3 /hour can be achieved with a mixing zone diameter smaller than 200 mm.

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