Abstract:
Embodiments of an hydraulic opposed jet mill are disclosed which may be used to crush various minerals, including mica, or other materials to sub-micron size. At least one positive displacement pump forces an incompressible liquid, such as water, through a pair of opposed jets such that the two streams of water collide between the jets. A slurry of an incompressible liquid, such as water, and the mineral to be crushed is introduced into the jets at a point near the outlet end of the jets. The entrained mineral particles are forced out of the jets with great energy which causes multiple collisions and pulverization. In a second embodiment of the instant invention the slurry strikes an impingement plate rather than an opposed slurry stream.
Abstract:
An eductor-spike nozzle device includes (a) a first cylindrical member having a first wall including a cowl lip and defining a first hollow interior, and (b) a second cylindrical member mounted within the first hollow interior and having a second wall (i) externally defining an annular flow path with the first wall for flow of a first stream of fluid, and fluid compressing throat region with the cowl lip for creating a high velocity stream, and (ii) internally defining a second hollow interior for flow of a second stream of fluid so as to form the composite stream of high velocity fluid with the first stream of fluid, thereby increasing a probability of the composite stream receiving and entraining particles introduced into the composite stream.
Abstract:
A method and apparatus for treating fluids includes a vortex nozzle assembly having improved vortex nozzles. The overall system and system layout, which includes an elbow design, are improved as well as vortex system methods. The vortex nozzle assembly includes an access port and methods for measuring physical properties at the fluid flows. A frame assembly provides support for the vortex system.
Abstract:
In a method and apparatus for treating fluids, a pump delivers a fluid flow from a fluid source to a manifold. The manifold divides the fluid flow into first and second fluid flows, which are delivered from the manifold to a housing. The housing includes therein a first vortex nozzle positioned in opposed relationship to a second vortex nozzle. The first fluid flow enters the first vortex nozzle to create a first rotating fluid flow, and the second fluid flow enters the second vortex nozzle to create a second rotating fluid flow. The first and second vortex nozzles impinge the first and second rotating fluid flows in a collision chamber, thereby treating the fluid.
Abstract:
A mill offers superior milling efficiency by being provided with a partition to divide a milling chamber into a first guide path and a second guide path. Particles of a milling material that have been ground at a milling area in the milling chamber are guided into a particle classifier through the first guide path, and the ground particles of the milling material that were classified by the particle classifier as requiring further milling are guided back into the milling area through the second guide path.
Abstract:
An apparatus for grinding particulate material includes a grinding chamber. Fluid sources mounted on the peripheral wall of the grinding chamber generate a stream of fluid directed along the source axis of the fluid source towards the inside of the grinding chamber. Fluid flow guides associated with fluid sources have a first aperture. Guide members associated with fluid sources have a second aperture. Each guide member co-operates with the fluid stream of the associated fluid source and the associated fluid flow guide to draw fluid towards an upstream portion of the fluid stream and to direct fluid away from a downstream portion of the fluid stream. The fluid streams from the fluid sources overlap in an empty zone of the grinding chamber. The particulate material is introduced into the fluid streams, accelerated by the fluid streams and directed towards the empty zone. Thus particles from different streams collide in the empty zone.
Abstract:
The invention relates to a substantially dry fine product comprising fructose, glucose, a sugar alcohol or mixture containing them, prepared by grinding the fructose, glucose, sugar alcohol or mixture containing them substantially autogenously in a counterjet mill and classifying the ground product to a mean particle size of 5-25 .mu.m. The invention also relates to a process for preparing such a fine product and to the use of the product to prepare chocolate or icing, a fondant, hard candy, chewing-gum and a chocolate or truffle filling, and as seed crystals in the production of fructose or said sugar alcohols.
Abstract:
A mill for grinding powder material is disclosed having a cylindrical separation chamber into which the powder material is fed as a dispersion in a gas stream. Powdered material initially is supplied through two spaced powder inlets each located between a jet and a venturi throat assembly so that milling fluid introduces the powder material through the venturis and the venturis are mounted in opposition so that the gas streams carrying the powder impinge on one another to impart grinding. The impinged material passes to a third venturi to be entrained in a gas fed from a third jet nozzle and introduced through the venturi into the separation chamber. The mill is of particular use for milling pigmentary powders.
Abstract:
The present invention is concerned with a grinder housing of a pressure chamber grinder, which said grinder housing comprises a substantially cylindrical outer mantle (1), end walls (2, 3), at least two accelerating nozzles (4) passing radially through the outer mantle (1), between which said nozzles there is an obtuse angle, as well as a discharge opening (5) made into one of the end walls (3) for the ground product. The invention is characterized in that the grinder housing is provided with a substantially cylindrical partition wall (6), which is in itself known, centrally located, and which surrounds the grinding chamber (7) proper and is provided with an inlet opening (9) facing the orifice of each accelerating nozzle, preferably terminating at the plane of the inner face of the outer mantle (1), that the annular space surrounding the partition wall (6) is a gas removing chamber (8) to which an exhaust duct (10) passing through the outer mantle is connected for the removal of the excess quantity of working gas discharged out of the solids-working-gas jets of the accelerating nozzles (4) into the gas removing chamber (8).