CN202983819U - Slice-shaped and block-shaped stearate breaking device - Google Patents
Slice-shaped and block-shaped stearate breaking device Download PDFInfo
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- CN202983819U CN202983819U CN 201220556888 CN201220556888U CN202983819U CN 202983819 U CN202983819 U CN 202983819U CN 201220556888 CN201220556888 CN 201220556888 CN 201220556888 U CN201220556888 U CN 201220556888U CN 202983819 U CN202983819 U CN 202983819U
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Abstract
The utility model discloses a slice-shaped and block-shaped stearate breaking device. A breaking process includes the steps of (1) receiving and storing semi-finished products, (2) conducting first-level breaking on the semi-finished products and removing dust after breaking, (3) collecting first-level breaking dust removal materials, and (4) conducting second-level breaking dust removal on first-level breaking dust removal, and collecting finished products. The breaking device comprises a micro negative pressure storage bin (1), a hammer type kibbler (2), a cyclone dust collector (4), a cloth dust collector (6), an intermediate storage bin (5), an airflow vortex kibbler (7), a cyclone dust collector (9), a pulse dust collector (11), a finished product storage bin (10) and an induced draft fan (12). The slice-shaped and block-shaped stearate breaking device has the advantages of being simple and reasonable in structure, petty in dust which is removed, environment-friendly, good in breaking effect and relatively high in breaking efficiency.
Description
Technical field
The utility model belongs to the stearate production field, relates in particular to a kind of flow process and equipment thereof that the semi-finished product of fusion method resin acid salt are pulverized.
Background technology
The zinc stearate production technology mainly contains double decomposition, water one-step method, fusion method at present.Fusion method is compared its characteristics with other techniques, does not consume water resource, does not produce technique waste water, comprehensive energy consumption is low, production technology is simple, the low advantage of production cost.Along with national energy-saving reduction of discharging and environmental requirement improve constantly, fusion method explained hereafter zinc stearate is more and more paid attention to.In reality was produced, the employing slicer was cut into sheet or lumps with the first products such as zinc stearate that the fusion method explained hereafter goes out, more cooling through the barrelling storage, then poured the feeding bin of air-flow vortex pulverizer into through elevator, pulverized processing.Its shortcoming is that the barrelling material is subject to external environment and contaminating impurity, and when falling bucket, dust is more, and operating environment is poor, and large sheet and lumps material easily stop up the pulverizer import, causes charging inhomogeneous, and the product cut size impact is larger, easily carries coarse granule in fine-powder secretly.
Summary of the invention
The purpose of this utility model is the shortcoming that overcomes prior art, and a kind of difficult obstruction is provided, and the operating environment dust is pulverized quality height and high a kind of sheet or lumps stearate circuit grinding and the equipment of efficient less.
For solving the problems of the technologies described above, concrete technical scheme of the present utility model is as follows:
A kind of sheet and lumps stearate disintegrating apparatus comprise a negative pressure stock bin, are provided with a beater disintegrating machine bottom negative pressure stock bin, both are connected by pipeline, and on this pipeline, changeover valve are set;
Described beater disintegrating machine outlet is connected with the cyclone dust collectors import by pipeline, also is provided with intermediate bunker below described cyclone dust collectors, is connected with the cyclone dust collectors dust hopper; The outlet of described cyclone dust collectors also is connected with a sack cleaner, and described sack cleaner dust mouth also is communicated with intermediate bunker;
Also be provided with an air-flow vortex pulverizer below intermediate bunker, be connected by pipeline with described intermediate bunker, and be provided with a rotary valve on this pipeline;
Described air-flow vortex pulverizer also is connected with another cyclone dust collectors import; Be provided with a finished product bin below described these cyclone dust collectors, described finished product bin is connected with the cyclone dust collectors dust hopper;
Described cyclone dust collectors exit also connects a pulse dust collector, and described pulse place deduster exit is connected with an air-introduced machine.
The utility model has the advantage of: (1) in whole work flow, the dust of generation is less, has greatly improved workman's production environment; the tail gas medium silt of discharging is less; protected environment (2) to adopt secondary to pulverize, the difficult pulverizer that stops up is pulverized quality simultaneously and efficient is high.
Description of drawings
Fig. 1 is the utility model apparatus structure schematic diagram.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is further described.
Be below a kind of embodiment of the present utility model.
Stearate semi-finished product reducing mechanism of the present utility model comprises a little negative pressure stock bin 1 as shown in Figure 1, is provided with a beater disintegrating machine 2 in negative pressure stock bin 1 bottom, both is connected by pipeline 3, and on this pipeline, changeover valve 3a is set; The 2 machines outlets of described hammer type crushing are connected with the first cyclone dust collectors 4 imports by pipeline, and described the first cyclone dust collectors 4 belows also are provided with intermediate bunker 5, are connected with the first cyclone dust collectors 4 dust hoppers; 4 outlets of described cyclone dust collectors also are connected with a sack cleaner 6, and described sack cleaner 6 dust mouths also are communicated with intermediate bunker 5; Also be provided with an air-flow vortex pulverizer 7 below intermediate bunker 5, be connected by pipeline 8 with described intermediate bunker 5, and be provided with a rotary valve 8a on this pipeline; Described air-flow vortex pulverizer 7 also is connected with another the second cyclone dust collectors 9 imports; Described this second cyclone dust collectors 9 belows are provided with a finished product bin 10, and described finished product bin 10 is connected with the second cyclone dust collectors 9 dust hoppers; Described the second cyclone dust collectors 9 exits also connect a pulse dust collector 11, and described pulse place deduster 11 exits are connected with an air-introduced machine 12.
The zinc stearate semi-finished product of fusion method zinc stearate lumps or sheet enter little negative pressure stock bin interior 1, control by the rotary valve 3a opening degree of regulating on pipeline the zinc stearate amount that enters in beater disintegrating machine 2, zinc stearate is carried out one-level to be pulverized, particle after pulverizing or powdery are because the air-flow of pulverizer 2 enters in the first follow-up cyclone dust collectors 4, heavier material is collected through cyclone dust collectors and is entered intermediate bunker 5, and lighter material is collected through sack cleaner 6 and also entered intermediate bunker 5; Air-flow overflows through sack cleaner 6 outlets, and the air-flow that discharge this moment only contains less powder impurity, can the environment in the production operation flow process not impacted.Material in intermediate bunker 5 enters air-flow vortex pulverizer 7 again and again pulverizes, and most of finished product is collected through the second cyclone dust collectors 9 and entered finished product bin 19, and a small amount of trickle grit is clipped in air-flow catches 11 through the pulse deduster, collects to obtain the less product of particle diameter; Air-flow after purification is drawn by air-introduced machine 12 and is entered atmosphere.
The utility model charging is even, and crush efficiency is high.Can effectively improve environment, improve pulverizer efficient, tool has a broad prospect of the use.
Claims (1)
1. a sheet and lumps stearate disintegrating apparatus, it is characterized in that: comprise a negative pressure stock bin (1), be provided with a beater disintegrating machine (2) bottom negative pressure stock bin (1), both be connected by pipeline (3), and changeover valve (3a) is set on this pipeline; Described beater disintegrating machine (2) outlet is connected with the first cyclone dust collectors (4) import by pipeline, also is provided with intermediate bunker (5) below described the first cyclone dust collectors (4), is connected with cyclone dust collectors (4) dust hopper; Described the first cyclone dust collectors (4) outlets also is connected with a sack cleaner (6), and described sack cleaner (6) dust mouth also is communicated with intermediate bunker (5); Also be provided with an air-flow vortex pulverizer (7) below intermediate bunker (5), be connected by pipeline (8) with described intermediate bunker (5), and be provided with a rotary valve (8a) on this pipeline; Described air-flow vortex pulverizer (7) also is connected with another the second cyclone dust collectors (9) import; Be provided with a finished product bin (10) below described these second cyclone dust collectors (9), described finished product bin (10) is connected with the second cyclone dust collectors (9) dust hopper; Described the second cyclone dust collectors (9) exit also connects a pulse dust collector (11), and described pulse place deduster (11) exit is connected with an air-introduced machine (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220556888 CN202983819U (en) | 2012-10-29 | 2012-10-29 | Slice-shaped and block-shaped stearate breaking device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220556888 CN202983819U (en) | 2012-10-29 | 2012-10-29 | Slice-shaped and block-shaped stearate breaking device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202983819U true CN202983819U (en) | 2013-06-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220556888 Expired - Fee Related CN202983819U (en) | 2012-10-29 | 2012-10-29 | Slice-shaped and block-shaped stearate breaking device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202983819U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105149070A (en) * | 2015-09-15 | 2015-12-16 | 山东东源新材料科技有限公司 | Pneumatic transmitting and fine grinding system for producing vanadium-free rare earth based titanium-tungsten powder |
| CN105833977A (en) * | 2016-05-04 | 2016-08-10 | 枣庄市金山机械有限公司 | Planar sand making system |
| CN107497575A (en) * | 2017-08-02 | 2017-12-22 | 广东省长大公路工程有限公司 | A kind of aggregate production line |
| CN109527628A (en) * | 2018-12-12 | 2019-03-29 | 宜昌天工智能机械股份有限公司 | Totally-enclosed, interior circulation, from depositing dust granulating system and method |
-
2012
- 2012-10-29 CN CN 201220556888 patent/CN202983819U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105149070A (en) * | 2015-09-15 | 2015-12-16 | 山东东源新材料科技有限公司 | Pneumatic transmitting and fine grinding system for producing vanadium-free rare earth based titanium-tungsten powder |
| CN105149070B (en) * | 2015-09-15 | 2018-06-22 | 山东东源新材料科技有限公司 | A kind of Geldart-D particle for producing no vanadium rare-earth-based titanium tungsten powder, fine grinding system |
| CN105833977A (en) * | 2016-05-04 | 2016-08-10 | 枣庄市金山机械有限公司 | Planar sand making system |
| CN107497575A (en) * | 2017-08-02 | 2017-12-22 | 广东省长大公路工程有限公司 | A kind of aggregate production line |
| CN109527628A (en) * | 2018-12-12 | 2019-03-29 | 宜昌天工智能机械股份有限公司 | Totally-enclosed, interior circulation, from depositing dust granulating system and method |
| CN109527628B (en) * | 2018-12-12 | 2023-09-26 | 宜昌天工智能机械股份有限公司 | Totally-enclosed, internal-circulation and self-dust-falling granulating system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130612 Termination date: 20151029 |
|
| EXPY | Termination of patent right or utility model |