Comminution of pulverulent material by fluid energy
AssigneeMicroFuels, Inc.
InventorDavid W. Taylor
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AssigneeMicroFuels, Inc.
InventorDavid W. Taylor
Estimating the term…
A fluid energy grinding mill having a hollow vessel providing a central cylindrical core zone and a peripheral annular zone both disposed beyond a grinding zone at one end of the vessel. Carrier medium is injected into the grinding zone to generate a vertically-flowing vortex in the core zone. At the other end of the vessel, a first portion of the flow from the vortex is recirculated in a counter flow through an annular peripheral zone surrounding the core zone to interface with injected carrier medium in a grinding zone. A second portion is discharged through a central opening in the other end of the vessel. Particulate material is fed into the recirculating flow so that it may be comminuted in the grinding zone. In the vortex, the particulate material is classified by centrifugal action and the coarse particles are recirculated. The particles ground to the desired mass are discharged with the second portion of the carrier medium which is not recirculated. Several forms of regulation are disclosed for regulating the upwardly-flowing vortex and the portion of the flow which is recirculated. Guide means and deflectors are disclosed to assist in directing the particulate material to follow the desired path.
A fluid energy mill for grinding pulverulent material comprising a vessel having a closed bottom providing a grinding zone at one end, outlet means at the other end, and a generally cylindrical core zone having an axis disposed generally centrally within said vessel between said grinding zone and said outlet means, and an annular peripheral zone surrounding said generally cylindrical core zone, a plurality of circumferentially-spaced ejector nozzles for injecting fluid carrier medium into said grinding zone in a direction between a radius to said central zone axis and a direction perpendicular to said radius, all of said nozzles being disposed in said grinding zone to inject a primary flow of fluid carrier medium into said vessel through said grinding zone, said nozzles cooperating with said closed bottom and said outlet means so as to generate an axially-flowing vortex within said central zone, said vessel having transverse wall means at the other end spaced from said grinding zone to intercept the axially-flowing vortex and deflect at least a first portion of the medium therein outwardly into the peripheral zone, the fluid medium being deflected into said peripheral zone flowing oppositely as a secondary flow and being introduced into said primary flow issuing from said nozzles to thereby effect a recirculation of the fluid carrier medium within said vessel, and feed means to introduce pulverulent material into said circulating flow of fluid carrier medium, so that the material is introduced into said primary flow for fluid energy grinding thereof, said outlet means at the remote end of said vortex operable to withdraw a second portion of said fluid medium and with it a fraction of the pulverulent material which has been reduced in mass below a predetermined limit in said grinding zone.
A method of comminuting a pulverulent material having particles with varying means comprising the steps of supplying a primary flow of fluid medium to a vessel, generating an axially-flowing vortex of said fluid medium in a core zone within said vessel, deflecting a first portion of the axially-flowing medium outwardly at the remote end of said core zone into a peripheral zone surrounding said core zone, directing said first portion in a counter flow through in said peripheral zone and introducing it into said primary flow to effect recirculation of said fluid medium, discharging a second portion of said flow through an outlet at the remote end of said core zone and introducing pulverulent material into said recirculating flow, said comminuting being effected by supplying said fluid medium in a plurality of jets projected inwardly of said vessel from adjacent its circumference, said jets having divergent spray angles providing a high-velocity issuing flow and decreasing flow velocities at increasing distances from said issuing flow, said jets being spaced apart a distance to provide varying flow velocities intermediate the issuing flows of said jets, the pulverulent material being entrained in said jets and thereby being subjected to varying accelerations dependent upon the flow velocity of the medium entraining the material and the mass of the particles entrained, the varying acceleration effecting impacts between said particles.
Dependencies are inferred from the claim text.