CN100558466C - Dust-free overflowing environmental protection intelligent fluidized bed air current superfine reducing mechanism - Google Patents
Dust-free overflowing environmental protection intelligent fluidized bed air current superfine reducing mechanism Download PDFInfo
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- CN100558466C CN100558466C CNB2007100216966A CN200710021696A CN100558466C CN 100558466 C CN100558466 C CN 100558466C CN B2007100216966 A CNB2007100216966 A CN B2007100216966A CN 200710021696 A CN200710021696 A CN 200710021696A CN 100558466 C CN100558466 C CN 100558466C
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- cyclone separator
- feeding inlet
- discharging opening
- cloth filter
- pulsed jet
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Abstract
The invention discloses a kind of Dust-free overflowing environmental protection intelligent fluidized bed air current superfine reducing mechanism, mainly by first, second and third cyclone separator, first, second and third pulsed jet cloth filter, first, second and third air-introduced machine, first mixer communicate, pulverizer, first and second weigh bucket, the mixer of weighing, screw feeder, cross valve and suction tube form, each equipment room of whole device is tightly connected.This device is totally-enclosed negative-pressure operation, fed intake suspended hood, PLC control, touchscreen button, whole production line can realize adopting between three kinds of functions (promptly pulverizing again packing, hybrid packed and pack this three kinds of functions merely), each equipment be flexible coupling, no airborne dust, can effectively guarantee non-flour dust overflow in the course of work, be fit to processing poisonous material of human body such as pesticide industry.
Description
Technical field
The present invention relates to a kind of fluidized bed airflow ultramicro crushing apparatus.
Background technology
Crushing system is reinforced open not to be sealed, and no suspended hood, mechanical button control, function singleness, dust from flying, is harmful to health, and Toxic more injures health especially.
Summary of the invention
In order to overcome above-mentioned defective, the invention provides a kind of Dust-free overflowing environmental protection intelligent fluidized bed air current superfine reducing mechanism, non-flour dust overflow in the multiple function of this reducing mechanism tool and the course of work can not injure health.
The present invention for the technical scheme that solves its technical problem and adopt is: a kind of Dust-free overflowing environmental protection intelligent fluidized bed air current superfine reducing mechanism, the loading hopper lower discharge port successively by behind first rotary valve and the first-hand movable valve with first cyclone separator upper end feeding inlet, the loading hopper lower discharge port again simultaneously successively by behind first rotary valve and the 3rd manually-operated gate with second cyclone separator upper end feeding inlet, first cyclone separator upper end dust removing tube material overfall and the first pulsed jet cloth filter feeding inlet, the first pulsed jet cloth filter upside air outlet communicates with first air-introduced machine, the first pulsed jet cloth filter lower end material outlet successively by behind second rotary valve and the first-hand movable valve with first cyclone separator upper end feeding inlet, the first pulsed jet cloth filter lower end material outlet again simultaneously successively by behind second rotary valve and the 3rd manually-operated gate with second cyclone separator upper end feeding inlet, the loading hopper top is provided with reinforced suspended hood, and reinforced suspended hood outlet is passed through the 3rd manually-operated gate and second cyclone separator upper end feeding inlet simultaneously by first-hand movable valve and first cyclone separator upper end feeding inlet; The first cyclone separator lower end discharging opening and the first mixer feeding inlet, the first mixer discharging opening and the first barrel feeding inlet of weighing, first weigh barrel discharging opening and the pulverizer feeding inlet, the pulverizer discharging opening is by second-hand's movable valve and second cyclone separator upper end feeding inlet, second, the discharging opening while of three manually-operated gates and second cyclone separator upper end feeding inlet, the second cyclone separator lower end discharging opening and screw feeder feeding inlet, second cyclone separator upper end dust removing tube material overfall communicates with the second pulsed jet cloth filter lower end material inlet, the second pulsed jet cloth filter upside air outlet communicates with second air-introduced machine, the second pulsed jet cloth filter lower end material outlet and screw feeder feeding inlet, screw feeder one discharging opening and the mixer feeding inlet of weighing, another discharging opening of screw feeder and the ground bucket that connects material communicates, when the mixer material of weighing is full, material arrives ground bucket that connects material from another discharging opening of screw feeder, the mixer discharging opening of weighing communicates with the cross valve first material mouth by the 3rd rotary valve, the cross valve second material mouth is the first finished product material mouth, cross valve the 3rd material mouth connects the 4th manually-operated gate, cross valve the 4th material mouth and the 3rd cyclone separator upper end feeding inlet, one suction tube is communicated on the pipeline between the charging aperture of cross valve the 4th material mouth and the 3rd cyclone separator upper end by the 5th manually-operated gate, the 3rd cyclone separator lower end discharging opening and second weigh the bucket first feeding inlet, the 3rd cyclone separator upper end dust removing tube material overfall communicates with the 3rd pulsed jet cloth filter lower end material inlet, the 3rd pulsed jet cloth filter upside air outlet communicates with the 3rd air-introduced machine, the 3rd pulsed jet cloth filter lower end material outlet and second bucket second feeding inlet of weighing, the second barrel lower end discharging opening of weighing is the second finished product material mouth.
Beneficial effect of the present invention: this device is totally-enclosed negative-pressure operation, fed intake suspended hood, PLC control, touchscreen button, whole production line can realize adopting between three kinds of functions (promptly pulverizing again packing, hybrid packed and pack this three kinds of functions merely), each equipment be flexible coupling, no airborne dust, can effectively guarantee non-flour dust overflow in the course of work, be fit to processing poisonous material of human body such as pesticide industry.
Description of drawings
Fig. 1 is a schematic diagram of the present invention.
Arrow is an airflow direction among the figure, and material is driven by air-flow.
The specific embodiment
Embodiment: a kind of Dust-free overflowing environmental protection intelligent fluidized bed air current superfine reducing mechanism, loading hopper 10 lower discharge ports are successively by the first rotary valve M3 and first-hand movable valve 1 back and first cyclone separator, 21 upper end feeding inlet, the loading hopper lower discharge port is again simultaneously successively by the first rotary valve M3 and the 3rd manually-operated gate 3 backs and second cyclone separator, 22 upper end feeding inlet, first cyclone separator, 21 upper end dust removing tube material overfalls and first pulsed jet cloth filter, 31 feeding inlet, the first pulsed jet cloth filter upside air outlet communicates with first air-introduced machine 41, the first pulsed jet cloth filter lower end material outlet is successively by the second rotary valve M2 and first-hand movable valve 1 back and first cyclone separator, 21 upper end feeding inlet, first pulsed jet cloth filter, 31 lower end material outlets are again simultaneously successively by the second rotary valve M2 and the 3rd manually-operated gate 3 backs and second cyclone separator, 22 upper end feeding inlet, loading hopper top is provided with reinforced suspended hood 101, reinforced suspended hood outlet by first-hand movable valve 1 back and first cyclone separator upper end feeding inlet simultaneously by behind the 3rd manually-operated gate with second cyclone separator on feeding inlet; First cyclone separator, 21 lower end discharging openings and first mixer, 51 feeding inlet, the first mixer discharging opening and first weigh the bucket 61 feeding inlet, first weigh barrel discharging opening and pulverizer 7 feeding inlet, the pulverizer discharging opening is by second-hand's movable valve 2 and second cyclone separator, 22 upper end feeding inlet, second, the discharging opening while and second cyclone separator, the 22 upper end feeding inlet of three manually-operated gates, the second cyclone separator lower end discharging opening and screw feeder 71 feeding inlet, second cyclone separator, 22 upper end dust removing tube material overfalls communicate with second pulsed jet cloth filter, 32 lower end material inlets, the second pulsed jet cloth filter upside air outlet communicates with second air-introduced machine 42, the second pulsed jet cloth filter lower end material outlet and screw feeder 71 feeding inlet, screw feeder one discharging opening and mixer 8 feeding inlet of weighing, another discharging opening of screw feeder and the ground bucket that connects material communicates, when the mixer material of weighing is full, material arrives ground from another discharging opening of screw feeder and connects material that (the ground bucket that connects material plays the material effect that stores to bucket, after pulverizing end, again material is dropped into loading hopper by the first rotary valve M3, the 3rd manually-operated gate, second cyclone separator, second pulsed jet cloth filter, second air-introduced machine, screw feeder one discharging opening enters the mixer of weighing, and should guarantee the second rotary valve M2 this moment, first-hand movable valve, second-hand's movable valve is in closed condition); Mixer 8 discharging openings of weighing communicate by the 3rd rotary valve M12 and the cross valve first material mouth 91 (upward opening one), the cross valve second material mouth 92 is the first finished product material mouth (to of under shed), cross valve the 3rd material mouth 93 (one on the left side) connects the 4th manually-operated gate 4, and (thereby the 4th manually-operated gate 4 can be regulated intake and reaches the adjusting intake velocity, final control material loading speed), cross valve the 4th material mouth 94 (one on the right) and the 3rd cyclone separator 23 upper end feeding inlet, one suction tube 200 is communicated on the pipeline between cross valve the 4th material mouth 94 and the 3rd cyclone separator 23 upper end charging apertures by the 5th manually-operated gate 5, the 3rd cyclone separator lower end discharging opening and second weigh the bucket 62 first feeding inlet, the 3rd cyclone separator 23 upper end dust removing tube material overfalls communicate with the 3rd pulsed jet cloth filter 33 lower end material inlets, the 3rd pulsed jet cloth filter upside air outlet communicates with the 3rd air-introduced machine 43, the 3rd pulsed jet cloth filter 33 lower end material outlets and second bucket 62 second feeding inlet of weighing, the second barrel lower end discharging opening of weighing is the second finished product material mouth.
Native system is a negative-pressure operation, usually rotary valve need be set on the discharging opening pipeline of each function apparatus, adopts between the charging aperture of each adjacent functional apparatus, the discharging opening in addition to be flexible coupling.
The course of work of the present invention is as follows:
One, pulverize packing (the 4th manually-operated gate is often opened) again:
At this moment, first and second manual valve-opening and the 3rd, five manually-operated gates are closed;
Start power supply, first, two, three air-introduced machines are successively worked according to program, raw material drop into loading hopper by lower discharge port through the first rotary valve M3, first-hand movable valve 1, send into first cyclone separator upper end charging aperture by pipeline by air-flow, the few material of a part sucks the back by loading hopper top suspended hood and enters first cyclone separator upper end charging aperture by first-hand movable valve, and the few material of another part enters the first pulsed jet cloth filter charging aperture again through the first pulsed jet cloth filter discharging opening by the first cyclone separator dust removing tube material overfall, enter first cyclone separator upper end charging aperture by first-hand movable valve behind the second rotary valve M2, realization moves in circles to reach raw material is sent into the stirring of first mixer successively like this.After the stirring, material enters the first barrel charging aperture of weighing according to program from the first mixer discharging opening automatically, enter the pulverizer charging aperture and pulverize from the first barrel discharging opening of weighing again, after the pulverizing, material enters second cyclone separator upper end charging aperture from the pulverizer discharging opening, the small part material is got back to the second pulsed jet cloth filter lower end material inlet from second cyclone separator upper end dust removing tube material overfall, material is again from the second cyclone separator lower end discharging opening, after the second pulsed jet cloth filter lower end material outlet enters screw feeder 71 charging apertures, material enters the mixer charging aperture of weighing from the screw feeder discharging opening again, when the mixer material of weighing is full, material is charging basket outside another discharging opening of screw feeder arrives, this can set in addition, be the easy technological means that realizes of same domain technical staff, this example is not describing in detail, last material is successively through the mixer discharging opening of weighing, cross valve second discharging opening finished product packing that comes out, or material is successively through the mixer discharging opening of weighing, cross valve the 4th discharging opening strength is sent into the 3rd cyclone separator upper end charging aperture, after the small part material is got back to the 3rd pulsed jet cloth filter lower end material inlet from the 3rd cyclone separator upper end dust removing tube material overfall, material enters the second barrel charging aperture of weighing from the 3rd cyclone separator lower end discharging opening and the 3rd pulsed jet cloth filter lower end material outlet again, comes out to carry out finished product packing by the 4th rotary valve M16 from the second barrel discharging opening of weighing at last.
Two, hybrid packed (the 4th manually-operated gate is often opened):
At this moment, first and second, five manually-operated gates are closed and the 3rd manual valve-opening, pulverizer does not move;
Start power supply, second, three air-introduced machines are successively worked according to program, raw material drops into loading hopper and passes through first rotary valve by lower discharge port respectively, the 3rd manually-operated gate, pipeline enters second cyclone separator upper end charging aperture, after few part airborne dust material converges with the lower discharge port of loading hopper after loading hopper top suspended hood sucks by the road, enter second cyclone separator upper end charging aperture through the 3rd manually-operated gate again, the small part material is got back to the second pulsed jet cloth filter lower end material inlet from second cyclone separator upper end dust removing tube material overfall again, material is again from the second cyclone separator lower end discharging opening, the second pulsed jet cloth filter lower end material outlet enters the screw feeder charging aperture, material enters the mixer charging aperture of weighing from the screw feeder discharging opening again, last material is successively through the mixer discharging opening of weighing, cross valve second discharging opening finished product packing that comes out, or material is successively through the mixer discharging opening of weighing, cross valve the 4th discharging opening strength is sent into the 3rd cyclone separator upper end charging aperture, after the small part material is got back to the 3rd pulsed jet cloth filter lower end material inlet from the 3rd cyclone separator upper end dust removing tube material overfall, material enters the second barrel charging aperture of weighing from the 3rd cyclone separator lower end discharging opening and the 3rd pulsed jet cloth filter lower end material outlet again, comes out to carry out finished product packing by the 4th rotary valve M16 from the second barrel discharging opening of weighing at last.
Three, simple packing:
The 4th manually-operated gate is closed and the 5th manual valve-opening, and first and second air-introduced machine and pulverizer are closed, and the 3rd air-introduced machine is opened;
Start power supply, the 3rd air-introduced machine work, material is sucked by powder absorbing pipe and enters the 3rd cyclone separator upper end charging aperture, after the small part material is got back to the 3rd pulsed jet cloth filter lower end material inlet from the 3rd cyclone separator upper end dust removing tube material overfall, material enters the second barrel charging aperture of weighing from the 3rd cyclone separator lower end discharging opening and the 3rd pulsed jet cloth filter lower end material outlet again, come out to carry out finished product packing from the second barrel discharging opening of weighing at last by the 4th rotary valve M16.
The present invention is totally closed operation not to be had dust and overflows, and is suitable for processing noxious material, as agricultural chemicals etc.
Claims (1)
1. Dust-free overflowing environmental protection intelligent fluidized bed air current superfine reducing mechanism, it is characterized in that: the loading hopper lower discharge port successively by behind first rotary valve and the first-hand movable valve with first cyclone separator upper end feeding inlet, the loading hopper lower discharge port again simultaneously successively by behind first rotary valve and the 3rd manually-operated gate with second cyclone separator upper end feeding inlet, first cyclone separator upper end dust removing tube material overfall and the first pulsed jet cloth filter feeding inlet, the first pulsed jet cloth filter upside air outlet communicates with first air-introduced machine, the first pulsed jet cloth filter lower end material outlet successively by behind second rotary valve and the first-hand movable valve with first cyclone separator upper end feeding inlet, the first pulsed jet cloth filter lower end material outlet again simultaneously successively by behind second rotary valve and the 3rd manually-operated gate with second cyclone separator upper end feeding inlet, the loading hopper top is provided with reinforced suspended hood, and reinforced suspended hood outlet is passed through the 3rd manually-operated gate and second cyclone separator upper end feeding inlet simultaneously by first-hand movable valve and first cyclone separator upper end feeding inlet; The first cyclone separator lower end discharging opening and the first mixer feeding inlet, the first mixer discharging opening and the first barrel feeding inlet of weighing, first weigh barrel discharging opening and the pulverizer feeding inlet, the pulverizer discharging opening is by second-hand's movable valve and second cyclone separator upper end feeding inlet, second, the discharging opening while of three manually-operated gates and second cyclone separator upper end feeding inlet, the second cyclone separator lower end discharging opening and screw feeder feeding inlet, second cyclone separator upper end dust removing tube material overfall communicates with the second pulsed jet cloth filter lower end material inlet, the second pulsed jet cloth filter upside air outlet communicates with second air-introduced machine, the second pulsed jet cloth filter lower end material outlet and screw feeder feeding inlet, screw feeder one discharging opening and the mixer feeding inlet of weighing, another discharging opening of screw feeder and the ground bucket that connects material communicates, when the mixer material of weighing is full, material arrives ground bucket that connects material from another discharging opening of screw feeder, the mixer discharging opening of weighing communicates with the cross valve first material mouth by the 3rd rotary valve, the cross valve second material mouth is the first finished product material mouth, cross valve the 3rd material mouth connects the 4th manually-operated gate, cross valve the 4th material mouth and the 3rd cyclone separator upper end feeding inlet, one suction tube is communicated on the pipeline between the charging aperture of cross valve the 4th material mouth and the 3rd cyclone separator upper end by the 5th manually-operated gate, the 3rd cyclone separator lower end discharging opening and second weigh the bucket first feeding inlet, the 3rd cyclone separator upper end dust removing tube material overfall communicates with the 3rd pulsed jet cloth filter lower end material inlet, the 3rd pulsed jet cloth filter upside air outlet communicates with the 3rd air-introduced machine, the 3rd pulsed jet cloth filter lower end material outlet and second bucket second feeding inlet of weighing, the second barrel lower end discharging opening of weighing is the second finished product material mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100216966A CN100558466C (en) | 2007-04-23 | 2007-04-23 | Dust-free overflowing environmental protection intelligent fluidized bed air current superfine reducing mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100216966A CN100558466C (en) | 2007-04-23 | 2007-04-23 | Dust-free overflowing environmental protection intelligent fluidized bed air current superfine reducing mechanism |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101293218A CN101293218A (en) | 2008-10-29 |
| CN100558466C true CN100558466C (en) | 2009-11-11 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2007100216966A Expired - Fee Related CN100558466C (en) | 2007-04-23 | 2007-04-23 | Dust-free overflowing environmental protection intelligent fluidized bed air current superfine reducing mechanism |
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| CN (1) | CN100558466C (en) |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101879392A (en) * | 2009-05-07 | 2010-11-10 | 中冶天工上海十三冶建设有限公司 | Decompression dust remover for stirring system |
| CN102505198B (en) * | 2011-11-03 | 2014-10-15 | 宁波大发化纤有限公司 | Particle twisting semiautomatic mixed feeding system for waste terylene textiles |
| CN102489376B (en) * | 2011-11-28 | 2013-12-04 | 河南省康星药业股份有限公司 | Rod mill powder-sieve linkage system |
| CN102489378B (en) * | 2011-11-28 | 2013-09-25 | 河南省康星药业股份有限公司 | wood powder and powder sieve linkage system |
| CN102489377B (en) * | 2011-11-28 | 2013-12-04 | 河南省康星药业股份有限公司 | Superfine powder sieve linkage system |
| CN102407186B (en) * | 2011-11-28 | 2013-08-21 | 河南省康星药业股份有限公司 | Chinese medicine ultrafine powder screening linkage system |
| CN103202292B (en) * | 2012-01-16 | 2015-05-06 | 昆山市密友装备制造有限责任公司 | Automatic continuous cleaning product line for pesticide solid preparation |
| CN103662126A (en) * | 2013-06-07 | 2014-03-26 | 山东舜合胶业有限公司 | Automatic intelligent packaging machine for producing rubber powder on basis of waste tires |
| CN103657816B (en) * | 2013-12-31 | 2015-06-03 | 昆明特康科技有限公司 | Airflow grinding equipment and wall breaking method with same for pollen pini |
| CN103963184A (en) * | 2014-04-25 | 2014-08-06 | 江苏赛宝龙石化有限公司 | Polystyrene recycling and pelletization device |
| CN104588190B (en) * | 2014-12-23 | 2017-04-05 | 玉溪加宝生物能源有限公司 | A kind of crushing system |
| CN109604038A (en) * | 2019-01-09 | 2019-04-12 | 四川极速动力超微粉体设备制造有限公司 | A kind of dedusting dust guard and ultra-fine grinding process equipment |
| CN110142941A (en) * | 2019-05-23 | 2019-08-20 | 杭州红其线缆材料有限公司 | A kind of dustless plastic pellet production line |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20060071104A1 (en) * | 2004-09-29 | 2006-04-06 | Montag Roger A | Granular material grinder and method of use |
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2007
- 2007-04-23 CN CNB2007100216966A patent/CN100558466C/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20060071104A1 (en) * | 2004-09-29 | 2006-04-06 | Montag Roger A | Granular material grinder and method of use |
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| CN101293218A (en) | 2008-10-29 |
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Granted publication date: 20091111 Termination date: 20190423 |