US3602439A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Pneumatic mill for extra-fine powder
Assignee: Nippon Pneumatic Manufacturing Co Ltd
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Filing: 1969-07-25
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Granted: 1971-08-31
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Expires: 1989-07-25
Abstract
Abstract A supersonic jet mill for producing extra fine and uniform powder from pregranulated material continuously, having a chamber to pulverize material by mutual collision and friction of granular material in a swirl of supersonic pneumatic fluid introduced through jet nozzles, another chamber to separate the pulverized fine powder from coarse powder in a swirl of pneumatic fluid, a cylinder to take out the fine powder without including material in process, and conduits to return the coarse powder to the pulverization chamber by way of the jet nozzles with auxiliary pulverizing effects.
Inventors
- 👤 Niro Nakayama
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 21:29
CPC Classifications
B; B02; B02C; B02C19/00; B02C19/06; B02C19/061
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
424 words
A pneumatic pulverizer to reduce pregranulated material into substantially fine and uniform powder continuously, comprising an annular chamber to swirl supersonic pneumatic fluid therein to pulverize pregranulated material, another annular chamber mounted on said annular pulverization chamber to swirl pneumatic fluid therein to separate pulverized fine powder from coarse powder, a cylinder extending downward from the center of said annular separation chamber through said annular pulverization chamber to deliver separated fine powder, nozzle means arranged around said annular pulverization chamber to jet supersonic pneumatic fluid into said pulverization chamber, conduit means arranged around said annular separation chamber to return coarse powder from said separation chamber to said pulverization chamber, means connected to said jet nozzle means to distribute pneumatic fluid to said jet nozzle means, means arranged around said pulverization chamber to feed pregranulated material into said pulverization chamber, means connected to said delivery cylinder to guide delivered fine powder out of said delivery cylinder, and means connected to said guide means to exhaust a gas from said guide means; said annular pulverization chamber being provided with an annular passage in the center thereof communicating with said annular separation chamber, said annular passage surrounding a portion intermediate the upper and lower ends of said delivery cylinder, said annular pulverization chamber being provided with a plurality of ports through an annular sidewall thereof to introduce supersonic pneumatic fluid therethrough, said ports in said pulverization chamber being spaced equally around the circumference of said annular pulverization chamber and directed in an eccentric relation to the center of said pulverization chamber to swirl supersonic pneumatic fluid satisfactorily therein, said separation chamber being provided with a plurality of ports through an annular sidewall thereof to withdraw pneumatic fluid therethrough, said ports in said separation chamber being spaced equally around the circumference of said separation chamber and directed in an eccentric relation to the center of said separation chamber to withdraw swirling fluid, said pulverization chamber provided with at least one radial port through an annular sidewall thereof to introduce pneumatic fluid therethrough, said delivery cylinder being provided with an annular flange extending from the upper end thereof into said separation chamber to shelter said annular passage sufficiently to keep separated fine powder from being mixed with material in process entering said separation chamber through said annular passage, said jet nozzle means being connected to said eccentric ports in said pulverization chamber, said return conduit means connected to said eccentric ports in said separation chamber, and said feed means being connected to said radial port in said pulverization chamber.
Claim 2
Dependent Claim
424 words
A pneumatic pulverizer to reduce pregranulated material into substantially fine and uniform powder continuously, comprising an annular chamber to swirl supersonic pneumatic fluid therein to pulverize pregranulated material, another annular chamber mounted on said annular pulverization chamber to swirl pneumatic fluid therein to separate pulverized fine powder from coarse powder, a cylinder extending downward from the center of said annular separation chamber through said annular pulverization chamber to deliver separated fine powder, nozzle means arranged around said annular pulverization chamber to jet supersonic pneumatic fluid into said pulverization chamber, conduit means arranged around said annular separation chamber to return coarse powder from said separation chamber to said pulverization chamber, means connected to said jet nozzle means to distribute pneumatic fluid to said jet nozzle means, means arranged around said pulverization chamber to feed pregranulated material into said pulverization chamber, means connected to said delivery cylinder to guide delivered fine powder out of said delivery cylinder, and means connected to said guide means to exhaust a gas from said guide means; said annular pulverization chamber being provided with an annular passage in the center thereof communicating with said annular separation chamber, said annular passage surrounding a portion intermediate the upper and lower ends of said delivery cylinder, said annular pulverization chamber being provided with a plurality of ports through an annular sidewall thereof to introduce supersonic pneumatic fluid therethrough, said ports in said pulverization chamber being spaced equally around the circumference of said annular pulverization chamber and directed in an eccentric relation to the center of said pulverization chamber to swirl supersonic pneumatic fluid satisfactorily therein, said separation chamber being provided with a plurality of ports through an annular sidewall thereof to withdraw pneumatic fluid therethrough, said ports in said separation chamber being spaced equally around the circumference of said separation chamber and directed in an eccentric relation to the center of said separation chamber to withdraw swirling fluid, said pulverization chamber provided with at least one radial port through an annular sidewall thereof to introduce pneumatic fluid therethrough, said delivery cylinder being provided with an annular flange extending from the upper end thereof into said separation chamber to shelter said annular passage sufficiently to keep separated fine powder from being mixed with material in process entering said separation chamber through said annular passage, said jet nozzle means being connected to said eccentric ports in said pulverization chamber, said return conduit means connected to said eccentric ports in said separation chamber, and said feed means being connected to said radial port in said pulverization chamber.
Claim 3
Dependent Claim
115 words
A pnuematic pulverizer in accordance with claim 1 wherein said jet nozzle means comprises a plurality of nozzles, each of which has a throat intermediate both ends thereof, the inner diameter of said jet nozzle being a minimum at said throat and gradually increasing toward both ends thereof, the graduation of the inner diameter of said jet nozzle being such that pneumatic fluid is changed from subsonic to supersonic speed, causing a shock wave immediately after it passes said throat as it flows through said jet nozzle from one to the other end thereof, the pressure within said jet nozzle being a minimum intermediate said throat and a critical point where the shock wave occurs.
Claim 4
Dependent Claim
42 words
A pneumatic pulverizer in accordance with claim 2 wherein said return conduit means comprises a plurality of pipes connected respectively to said jet nozzles to return coarse powder from said separation chamber to said pulverization chamber by way of said jet nozzles.
Claim 5
Dependent Claim
62 words
A pneumatic pulverizer in accordance with claim 3 wherein each of said jet nozzles is provided with a radial port intermediate said throat and said critical point where the shock wave occurs, said radial port being connected to said return pipe to facilitate the return flow and to pulverize coarse powder in the shock wave before returning in to said pulverization chamber.
Claim 6
Dependent Claim
22 words
A pneumatic pulverizer in accordance with claim 4 wherein said distribution means comprises an annular manifold connected to an outside pneumatic source.
Claim 7
Dependent Claim
46 words
A pneumatic pulverizer in accordance with claim 5 wherein said feed means comprises inlet means connected to an outside material source, another inlet means connected to an outside pneumatic source, and nozzle means connected to both of said inlet means to feed material by pneumatic fluid.
Claim 8
Dependent Claim
16 words
A pneumatic pulverizer in accordance with claim 6 wherein said guide means comprises a conical drum.
Claim 9
Dependent Claim
33 words
A pneumatic pulverizer in accordance with claim 7 wherein said exhaust means comprises a cylindrical stack extending upward from the center of said conical drum through said delivery cylinder and said separation chamber.
References Cited (Backward Citations)
No citation records indexed.
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1974-08-30 | 1975-03-01 | 1975-08-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1978-08-30 | 1979-03-01 | 1979-08-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1982-08-30 | 1983-03-01 | 1983-08-31 | $7700.00 | Window Closed / Lapsed |