Patent References 969978 1713260 1921059 2236551 Continuous flow static mixer for mixing powder and/or suspension materials with liquid materials Process and apparatus for adding liquid components to pourable powdered or granular materials Apparatus for producing a gas solid two phase flow jet having a constant mass or volume flow rate and predetermined velocity Premix injection system for asphalt compositions Patent #: 4662759 InventorApplicationNo. 129113 filed on 11/19/1993US 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 outlet366/178.1ConcentricExaminersPrimary: Cooley, Charles E.Attorney, Agent or FirmForeign Patent References
International ClassB01F 005/24Foreign Application Priority Data1991-04-05 NOAbstractA 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.Field of SearchMethodsWITH TEST, SIGNAL, OR INDICATOR MEANS STATIONARY DEFLECTOR (DIVIDING AND RECOMBINING TYPE) IN FLOW-THROUGH MIXING CHAMBER Angularly related flat surfaces STATIONARY MIXING CHAMBER METHOD JET OR SPRAY IMPINGING FREE-FALLING STREAM Concentric Concentric flow paths Valving means for central fluid Flow means of one fluid surrounds the other at outlet Moved by rotatable flow conducting terminal member part | |