EP0211117A3 - Method and apparatus for providing finely divided powder - Google Patents
Method and apparatus for providing finely divided powder Download PDFInfo
- Publication number
- EP0211117A3 EP0211117A3 EP85305506A EP85305506A EP0211117A3 EP 0211117 A3 EP0211117 A3 EP 0211117A3 EP 85305506 A EP85305506 A EP 85305506A EP 85305506 A EP85305506 A EP 85305506A EP 0211117 A3 EP0211117 A3 EP 0211117A3
- Authority
- EP
- European Patent Office
- Prior art keywords
- classifier
- feedstock
- pulverizer
- gas
- pressure
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 238000000034 method Methods 0.000 title abstract 3
- 239000000843 powder Substances 0.000 title 1
- 239000002245 particle Substances 0.000 abstract 3
- 239000007787 solid Substances 0.000 abstract 2
- 239000000463 material Substances 0.000 abstract 1
- 238000005549 size reduction Methods 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
- B02C19/06—Jet mills
- B02C19/065—Jet mills of the opposed-jet type
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Combined Means For Separation Of Solids (AREA)
- Disintegrating Or Milling (AREA)
Abstract
A no-moving parts pulverizer (19) and classifier
system (15) reduces materials to one hundred fifty microns
to less than ten microns using superheated steam or
any gas capable of being compressed and expanded thru
machined orifices. The resultant size reduction
depends upon the classifier gas rate and pressure,
the pulverizer gas rate and its pressure. These
combinations control and regulate miximum particle
size, average particle size and the mix of gas and
solids in process.
The feedstock enters the classifier chamber (15)
by auger (12) or similar manner as long as the feeder
maintains a positive seal. The classifier chamber (15)
separates the feedstock by size and particles of a
predetermined size exit (32) the system in a specific
ratio of gas and solids. The feedstock larger than
specified exit the base of the classifier (15), split into
two equal streams (20A, 20B) and accelerate thru the
pulverizer (19). The reduced feedstock exits (13) the
pulverizer (19), mixes with incocming feedstock (10) and again
enters the classifier (15).
The system is controlled using pressure,
temperature, feedrate or any combination of the
three. Other control methods can be used if any one
of the three are part of the control circuit.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/510,089 US4538764A (en) | 1983-06-30 | 1983-06-30 | Method and apparatus for providing finely divided powder |
| EP85305506A EP0211117A3 (en) | 1985-08-02 | 1985-08-02 | Method and apparatus for providing finely divided powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP85305506A EP0211117A3 (en) | 1985-08-02 | 1985-08-02 | Method and apparatus for providing finely divided powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0211117A2 EP0211117A2 (en) | 1987-02-25 |
| EP0211117A3 true EP0211117A3 (en) | 1988-02-03 |
Family
ID=8194308
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP85305506A Withdrawn EP0211117A3 (en) | 1983-06-30 | 1985-08-02 | Method and apparatus for providing finely divided powder |
Country Status (1)
| Country | Link |
|---|---|
| EP (1) | EP0211117A3 (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3943733C2 (en) * | 1989-05-12 | 1999-01-21 | Canon Kk | Air separator classifying powders |
| DE4431534B4 (en) * | 1994-02-10 | 2006-12-28 | Nied, Roland, Dr. Ing. | Machine for acting on comminuted and classifiable raw material, as well as method for operating the machine |
| DE102006017472A1 (en) | 2006-04-13 | 2007-10-18 | Nied, Roland, Dr. Ing. | Method for producing finest particles by means of a jet mill |
| DE102006023193A1 (en) | 2006-05-17 | 2007-11-22 | Nied, Roland, Dr.-Ing. | Method for producing finest particles by means of a jet mill |
| TW200940619A (en) | 2007-10-09 | 2009-10-01 | Cbp Carbon Ind Inc | Elastomer composition with reclaimed filler materials |
| US8394189B2 (en) | 2007-11-07 | 2013-03-12 | John H. Fader | Asphalt composition using pyrolysed carbonaceous material |
| RU2403097C1 (en) * | 2009-06-09 | 2010-11-10 | Закрытое акционерное общество "НИИЦемент" | Method of dry enrichment of metal and non-metal minerals and counterflow jet mill (versions) |
| CN117816325B (en) * | 2024-01-26 | 2024-07-02 | 青岛新天和碳材料有限公司 | High-energy jet mill for natural graphite |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2624516A (en) * | 1949-01-04 | 1953-01-06 | Blaw Knox Co | Fluid impact pulverizer and separator |
| US2636688A (en) * | 1948-02-20 | 1953-04-28 | Inst Gas Technology | Method for treating coal and the like |
| US3186648A (en) * | 1963-05-27 | 1965-06-01 | Grace W R & Co | Fluid energy mill |
| US3885931A (en) * | 1972-06-12 | 1975-05-27 | Donaldson Co Inc | Vortex forming apparatus and method |
| US4019688A (en) * | 1975-06-02 | 1977-04-26 | Viktor Ivanovich Akunov | Device for treating loose materials |
| US4538764A (en) * | 1983-06-30 | 1985-09-03 | Dunbar Richard M | Method and apparatus for providing finely divided powder |
-
1985
- 1985-08-02 EP EP85305506A patent/EP0211117A3/en not_active Withdrawn
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2636688A (en) * | 1948-02-20 | 1953-04-28 | Inst Gas Technology | Method for treating coal and the like |
| US2624516A (en) * | 1949-01-04 | 1953-01-06 | Blaw Knox Co | Fluid impact pulverizer and separator |
| US3186648A (en) * | 1963-05-27 | 1965-06-01 | Grace W R & Co | Fluid energy mill |
| US3885931A (en) * | 1972-06-12 | 1975-05-27 | Donaldson Co Inc | Vortex forming apparatus and method |
| US4019688A (en) * | 1975-06-02 | 1977-04-26 | Viktor Ivanovich Akunov | Device for treating loose materials |
| US4538764A (en) * | 1983-06-30 | 1985-09-03 | Dunbar Richard M | Method and apparatus for providing finely divided powder |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0211117A2 (en) | 1987-02-25 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| AK | Designated contracting states |
Kind code of ref document: A2 Designated state(s): AT BE CH DE FR GB IT LI LU NL SE |
|
| PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
| AK | Designated contracting states |
Kind code of ref document: A3 Designated state(s): AT BE CH DE FR GB IT LI LU NL SE |
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| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
| 18D | Application deemed to be withdrawn |
Effective date: 19880804 |
|
| RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: DUNBAR, RICHARD M |