CN1559694A - Ultra micro air flow pulverizer set with inert gas shielded - Google Patents
Ultra micro air flow pulverizer set with inert gas shielded Download PDFInfo
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- CN1559694A CN1559694A CNA2004100142352A CN200410014235A CN1559694A CN 1559694 A CN1559694 A CN 1559694A CN A2004100142352 A CNA2004100142352 A CN A2004100142352A CN 200410014235 A CN200410014235 A CN 200410014235A CN 1559694 A CN1559694 A CN 1559694A
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- air flow
- gas
- communicated
- cyclone separator
- inert gas
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Abstract
A superfine airflow pulverizer system with inertial gas shielded for pulverizing the material to be oxidized easily is composed of airflow system and pulverizing system. Said airflow system consists of protective gas soorce, gas tank, compressor, fluidized-bed airflow pulverizer, cyclone separator, and dust capture. Said pulverizing system comprises sealed feeder, transition cabin, fluidized-bed airflow pulverzer, cyclone separator, and powder collector.
Description
Technical field
The present invention relates to a kind of materials crusher.
Background technology
The powder machine of comminuting matter is standard-sized sheet or semi-open type at present, and the material of some easy oxidation just can not be pulverized like this, also can influence powder quality when pulverizing unclassified stores.
Summary of the invention
In order to overcome above-mentioned defective, the invention provides for this reason and a kind ofly can pulverize the higher inert gas protection micro jet group of readily oxidizable substance material and powder quality.
The present invention for the technical scheme that solves its technical problem and adopt is: this inert gas protection micro jet group, form by air flow system and crushing system;
Air flow system mainly is made up of protection source of the gas, air accumulator, gas compressor, the protection source of the gas connects air accumulator, air accumulator connects gas compressor, the protective gas sealing that gas compressor comes out flows to fluidized bed air flow crusher, cyclone separator, dedusting trap successively, gets back to the inlet end of gas compressor at last;
Crushing system mainly is made up of fluidized bed air flow crusher, feeder, cyclone separator, dedusting trap, feeder is the star-like feeder of band sealing device, can guarantee that sealing is evenly reinforced, the feeder discharging opening is communicated with the former feed bin inlet of transition, transition raw material warehouse discharging mouth is communicated with the fluidized bed air flow crusher charging aperture, the fluidized bed air flow crusher discharging opening is communicated with the cyclone separator upper end, the cyclone separator lower end is communicated with finished product charging basket 12, the cyclone separator upper end is communicated with the dedusting trap, and dedusting trap lower end is communicated with finished product barrel 11.
Cyclone separator and dedusting trap lower end are communicated with transition finished product barrel 10,9 respectively, and transition finished product barrel 9,10 is communicated with finished product barrel 11,12 respectively.
Gas control valve is established in the gas compressor outlet side.
The current of electric of fluidized bed air flow crusher and star-like feeder current of electric are carried out interlocking, guarantee to grind constant material level in the body with this.
The inlet end of gas compressor is provided with fold cartridge, can prevent that micro-dust from entering gas compressor.
Be provided with the oxygen content supervising device again in the generator protection gas passage, further control powder quality.
The invention has the beneficial effects as follows: during comminuting matter, whole unit sealing also has the inert gas protection, can pulverize the material of some easy oxidations like this, and powder quality is higher.
Description of drawings
The present invention is described in further detail below in conjunction with the drawings and specific embodiments.
Fig. 1 is a connection diagram of the present invention.
The specific embodiment
Embodiment: referring to Fig. 1, a kind of inert gas protection micro jet group is made up of air flow system and crushing system, and drawn arrow is an airflow direction on the figure, and this device is totally-enclosed shape;
Air flow system mainly is made up of protection source of the gas 1, air accumulator 2, gas compressor 3, protection source of the gas 1 connects air accumulator 2, air accumulator 2 connects gas compressors 3, and the protective gas sealing that gas compressor 3 comes out flows to the inlet end that fluidized bed air flow crusher 4, cyclone separator 7, dedusting trap 8 are got back to gas compressor 3 at last successively;
Crushing system is mainly by fluidized bed air flow crusher 4, feeder 6, cyclone separator 7, dedusting trap 8 is formed, feeder 6 is the star-like feeder of band sealing device, can guarantee that sealing is evenly reinforced, feeder 6 discharging openings are communicated with former feed bin 5 inlets of transition, former feed bin 5 discharging openings of transition are communicated with fluidized bed air flow crusher 4 charging apertures, fluidized bed air flow crusher 4 discharging openings are communicated with cyclone separator 7 upper ends, cyclone separator 7 lower ends are communicated with finished product barrel 12 through transition finished product barrel 10, cyclone separator 7 upper ends are communicated with dedusting trap 8, and dedusting trap 8 lower ends are communicated with finished product barrel 11 through transition finished product barrel 9.
Gas control valve is established in gas compressor 3 outlet sides;
The current of electric of fluidized bed air flow crusher 4 and star-like feeder 6 current of electric are carried out interlocking, guarantee to grind constant material level in the body with this;
The inlet end of gas compressor 3 is provided with fold cartridge, can prevent that micro-dust from entering gas compressor 3;
Be provided with oxygen content supervising device (this is mature technology, here no longer explanation) in the generator protection gas passage again, further control powder quality.
The course of work of the present invention is: startup power supply, gas compressor 3 work, system's running, raw material enters the former feed bin 5 of transition from feeder 6, enter fluidized bed air flow crusher 4 again and pulverize, then enter cyclone separator 7, cyclone separator 7 lower ends promptly go out finished product, arrive finished product barrel 12 through transition finished product barrel 10, some crushing rear material enters dedusting trap 8 through cyclone separator 7 upper ends, and dedusting trap 8 lower ends promptly go out finished product, arrive finished product barrel 11 through transition finished product barrel 9.
Air-flow workflow of the present invention to process is: from the protection source of the gas 1 to air accumulator 2 again to gas compressor 3; the protective gas sealing of coming out from gas compressor 3 flows to fluidized bed air flow crusher 4, cyclone separator 7, dedusting trap 8 successively; get back to the inlet end of gas compressor 3 at last from dedusting trap 8, form recycling.
Claims (6)
1. an inert gas protection micro jet group is characterized in that: be made up of air flow system and crushing system;
Air flow system mainly is made up of protection source of the gas (1), air accumulator (2), gas compressor (3), protection source of the gas (1) connects air accumulator (2), air accumulator (2) connects gas compressor (3), the protective gas sealing that gas compressor (3) comes out flows to fluidized bed air flow crusher (4), cyclone separator (7), dedusting trap (8) successively, gets back to the inlet end of gas compressor (3) at last;
Crushing system is mainly by fluidized bed air flow crusher (4), feeder (6), cyclone separator (7), dedusting trap (8) is formed, feeder (6) is the star-like feeder of band sealing device, can guarantee that sealing is evenly reinforced, feeder (6) discharging opening is communicated with the former feed bin of transition (5) inlet, the former feed bin of transition (5) discharging opening is communicated with fluidized bed air flow crusher (4) charging aperture, fluidized bed air flow crusher (4) discharging opening is communicated with cyclone separator (7) upper end, cyclone separator (7) lower end is communicated with finished product barrel (12), cyclone separator (7) upper end is communicated with dedusting trap (8), and dedusting trap (8) lower end is communicated with finished product barrel (11).
2. inert gas protection micro jet group according to claim 1; it is characterized in that: cyclone separator (7) and dedusting trap (8) lower end are communicated with transition finished product barrel (10,9) respectively, and transition finished product barrel (9,10) is communicated with finished product barrel (11,12) respectively.
3. inert gas protection micro jet group according to claim 1, it is characterized in that: gas control valve is established in gas compressor (3) outlet side.
4. inert gas protection micro jet group according to claim 1, it is characterized in that: the current of electric of fluidized bed air flow crusher (4) and star-like feeder (6) current of electric are carried out interlocking, guarantee to grind constant material level in the body with this.
5. inert gas protection micro jet group according to claim 1, it is characterized in that: the inlet end of gas compressor (3) is provided with fold cartridge, can prevent that micro-dust from entering gas compressor (3).
6. inert gas protection micro jet group according to claim 1 is characterized in that: be provided with the oxygen content supervising device again in the generator protection gas passage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100142352A CN1295020C (en) | 2004-03-05 | 2004-03-05 | Ultra micro air flow pulverizer set with inert gas shielded |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100142352A CN1295020C (en) | 2004-03-05 | 2004-03-05 | Ultra micro air flow pulverizer set with inert gas shielded |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1559694A true CN1559694A (en) | 2005-01-05 |
| CN1295020C CN1295020C (en) | 2007-01-17 |
Family
ID=34440273
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100142352A Expired - Fee Related CN1295020C (en) | 2004-03-05 | 2004-03-05 | Ultra micro air flow pulverizer set with inert gas shielded |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1295020C (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102613325A (en) * | 2012-04-13 | 2012-08-01 | 浙江德清奥萃生物科技有限公司 | Processing device for superfine tea powder |
| CN102698848A (en) * | 2012-05-16 | 2012-10-03 | 李莉 | Fluidized bed airflow grinding system |
| CN103492080A (en) * | 2011-03-21 | 2014-01-01 | 罗兰·尼德 | Operating method for a jet mill plant and jet mill plant |
| CN105536960A (en) * | 2015-11-27 | 2016-05-04 | 金堆城钼业股份有限公司 | Preparation system and preparation method of low-oxygen ultrafine molybdenum disulfide |
| CN106311440A (en) * | 2016-08-30 | 2017-01-11 | 周易 | Airflow crushing unit |
| CN106964458A (en) * | 2017-03-31 | 2017-07-21 | 浙江工业大学 | A kind of powder is crushed and conveying explosive-proof protector system |
| CN107051691A (en) * | 2017-04-10 | 2017-08-18 | 太仓金溪粉碎设备有限公司 | A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system |
| CN108452917A (en) * | 2018-03-26 | 2018-08-28 | 四川中科贝特纳米科技有限公司 | Closed cycle airflow comminution system |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4190005A (en) * | 1978-12-15 | 1980-02-26 | COMCO - Dravo Corporation | Process for pulverizing coal using combination gas in fluid energy pulverizers |
| CN2147900Y (en) * | 1993-05-15 | 1993-12-01 | 王宝芬 | Supersonic airstream superfine milling classer |
| CN2182384Y (en) * | 1994-01-08 | 1994-11-09 | 中国石油天然气管道勘察设计院 | Pneumatic rotary flue blower |
| CN2260662Y (en) * | 1996-05-21 | 1997-08-27 | 哈尔滨多元超细粉体工程有限责任公司 | Counter-jetting type super micro air-flow disintegrating grader |
| US5915635A (en) * | 1996-09-13 | 1999-06-29 | Gowan Milling Company, L.L.C. | Jet milling of agrichemical feedstocks |
| CN2452615Y (en) * | 2000-11-13 | 2001-10-10 | 昆山市超微粉碎机厂 | Super fine powder making machine set for traditional Chinese herb medicines |
| CN2668259Y (en) * | 2003-11-25 | 2005-01-05 | 昆山密友实业有限公司 | Inert gas shielded super micro airflow disintegrator set |
-
2004
- 2004-03-05 CN CNB2004100142352A patent/CN1295020C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103492080A (en) * | 2011-03-21 | 2014-01-01 | 罗兰·尼德 | Operating method for a jet mill plant and jet mill plant |
| CN102613325A (en) * | 2012-04-13 | 2012-08-01 | 浙江德清奥萃生物科技有限公司 | Processing device for superfine tea powder |
| CN102698848A (en) * | 2012-05-16 | 2012-10-03 | 李莉 | Fluidized bed airflow grinding system |
| CN105536960A (en) * | 2015-11-27 | 2016-05-04 | 金堆城钼业股份有限公司 | Preparation system and preparation method of low-oxygen ultrafine molybdenum disulfide |
| CN105536960B (en) * | 2015-11-27 | 2018-09-07 | 金堆城钼业股份有限公司 | A kind of preparation system and preparation method thereof of the ultra-fine molybdenum disulfide of hypoxemia |
| CN106311440A (en) * | 2016-08-30 | 2017-01-11 | 周易 | Airflow crushing unit |
| CN106311440B (en) * | 2016-08-30 | 2019-04-12 | 周易 | A kind of air-flow crushing unit |
| CN106964458A (en) * | 2017-03-31 | 2017-07-21 | 浙江工业大学 | A kind of powder is crushed and conveying explosive-proof protector system |
| CN107051691A (en) * | 2017-04-10 | 2017-08-18 | 太仓金溪粉碎设备有限公司 | A kind of intelligently realizing explosion-proof air-flow crushing and hierarchy system |
| CN108452917A (en) * | 2018-03-26 | 2018-08-28 | 四川中科贝特纳米科技有限公司 | Closed cycle airflow comminution system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1295020C (en) | 2007-01-17 |
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| C06 | Publication | ||
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| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: CLOSE FRIEND GROUP CO., LTD. Free format text: FORMER NAME: KUNSHAN MIYOU INDUSTRY CO.,LTD. |
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| CP01 | Change in the name or title of a patent holder |
Address after: No. 16, South hope road, Yushan Town, Kunshan City, Jiangsu Patentee after: Miyou Group Co.,Ltd. Address before: No. 16, South hope road, Yushan Town, Kunshan City, Jiangsu Patentee before: Kunshan MIyou Industrial Co., Ltd. |
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| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Kunshan Miyou Smash Equipment Co.,Ltd. Assignor: Kunshan MIyou Industrial Co., Ltd. Contract fulfillment period: 2008.12.25 to 2013.12.24 Contract record no.: 2009320001427 Denomination of invention: Ultra micro air flow pulverizer set with inert gas shielded Granted publication date: 20070117 License type: Exclusive license Record date: 20090807 |
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| LIC | Patent licence contract for exploitation submitted for record |
Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2008.12.25 TO 2013.12.24; CHANGE OF CONTRACT Name of requester: KUNSHAN MIYOU SMASH EQUIPMENT CO., LTD. Effective date: 20090807 |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070117 Termination date: 20190305 |
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| CF01 | Termination of patent right due to non-payment of annual fee |