CN201791503U - Tandem power material homogenizing system - Google Patents
Tandem power material homogenizing system Download PDFInfo
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- CN201791503U CN201791503U CN2010205211913U CN201020521191U CN201791503U CN 201791503 U CN201791503 U CN 201791503U CN 2010205211913 U CN2010205211913 U CN 2010205211913U CN 201020521191 U CN201020521191 U CN 201020521191U CN 201791503 U CN201791503 U CN 201791503U
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- homogenizing
- grey storehouse
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- powder
- homogenizing unit
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Abstract
The utility model discloses a tandem power material homogenizing system, and belongs to the technical field of powder homogenization. The system at least comprises two stages of homogenizing units connected in series in front and back, the homogenizing units are ash bin arrays consisting of a plurality of ash bins with the same structure, the feeding hole of each ash bin in the homogenizing unit of each stage is connected to a material delivery and distribution device of the same stage, and the discharge hole of each ash bin in the homogenizing unit of each stage is connected to a delivery master pipe of the same stage. The system has low investment cost, and can be used by combining the conventional devices on the market; the system has good homogenizing effect, and the multistage homogenizing units are connected in series in use to prolong the homogenizing path and time so as to fulfill the purpose of increasing the homogenizing effect; and meanwhile, the plurality of ash pins are used in parallel to eliminate the time difference of the powder material.
Description
Technical field
The utility model relates to powder material homogenizing technology field, the specifically a kind of powder material of tandem efficiently homogenization system.
Background technology
The chemical composition that makes many kinds material by a certain percentage, cooperate even, stable process to be referred to as homogenizing.Make the chemical composition of single variety material, the process that the grade quality mixes be referred to as pre-homogenizing.
At present, at home and abroad no matter be mostly the production of powder product is interrupted, because factors such as technique for producing raw material, control system often are difficult to guarantee to have equal quality with a collection of product.
With aluminium powder, manufacture of cement is example, and the chemical composition of same batch raw material and mineral composition also have certain fluctuation, need carry out homogenizing in the hope of obtaining a batch of composition and performance relatively aluminium powder, the cement products of uniformity to it.
The unique effective ways that address this problem in the actual production are before product export it to be carried out homogenizing and handle.Existing general homogenization installation is a container-like homogenizing jar, and granular material is carried out simple one-level homogenizing; Perhaps adopt mechanical stirring homogenizing storehouse or pneumatic homogenizing storehouse that it is carried out homogenizing.Wherein a homogenizing homo-effect is poor, and stirring homogenizing storehouse or pneumatic homogenizing storehouse all need to use powerful drive motors, and energy consumption is big, and the equipment investment cost height has improved production cost.
The utility model content
The purpose of this utility model be to provide a kind of cost of investment low, use simple tandem powder material homogenization system, by effective combination, realize granular material is carried out the purpose of effective homogenizing to existing homogenizing single devices.
The technical scheme in the invention for solving the technical problem is: this kind tandem powder material homogenization system, it is characterized in that, at least comprise the homogenizing unit that is connected in series before and after the two-stage, described homogenizing unit is the grey storehouse array that is made of the identical grey storehouse of some structures, the charging aperture in each the grey storehouse in every grade of homogenizing unit is connected to mass transport and distributor at the same level, the discharging opening in each the grey storehouse in every grade of homogenizing unit is connected to delivery main at the same level, realizes in-line multistage homogenizing.
Mass transport and distributor before the described first order homogenizing unit link to each other with the powder field, and the delivery main behind the described final stage homogenizing unit is connected to the powder gathering-device.
The preferred cylinder vibratory sieve of described powder gathering-device.
The grey storehouse outlet of the grey storehouse import at each Hui Cang top and bottom is provided with the valve that can open and close respectively, and the grey storehouse in each grey storehouse exports the batcher of also connecting simultaneously.
The bucket elevator that connects successively before and after described mass transport and distributor comprise, rotation sizing screen, permanent-magnetic iron expeller and air cushion-belt conveyer.
In the described delivery main at different levels air cushion conveyor mechanism is set.
The beneficial effects of the utility model are:
1) low this system of cost of investment can utilize that existing equipment is used in combination on the present market, and has only conveying device to need power in the device therefor, and equipment cost is low, and maintenance cost is low.
2) the good multistage homogenizer group series connection of homo-effect is used and has been prolonged the path and the time of homogenizing, reaches the purpose that increases homo-effect; Simultaneously, the use arranged side by side of a plurality of grey storehouses can be eliminated the difference of granular material on time shaft.
Description of drawings
Fig. 1 is a schematic diagram of the present utility model;
Fig. 2 is a layout drawing of the present utility model;
Fig. 3 is the local layout drawing of first order homogenizing unit in the system.
Among the figure: 1 first order homogenizing unit, 2 second level homogenizing units, 3 third level homogenizers,
11 first mass transport and distributors, 12 second mass transport and distributors,
13 3 materials are carried and distributor, 4 powder gathering-devices, and 51 grey storehouses,
52 disk feeders, 53 first delivery mains, 54 first valves, 55 second valves,
61 bucket elevators, 62 rotation sizing screens, 63 permanent-magnetic iron expellers, 64 air cushion-belt conveyers.
Arrow is represented the flow direction of powder material among the figure.
The specific embodiment
As Fig. 1, Fig. 2, shown in Figure 3, this kind tandem powder material homogenization system, the first order homogenizing unit 1, second level homogenizing unit 2 and the third level homogenizer 3 that are connected in series before and after comprising.The structure of homogenizing units at different levels is identical, constitutes identical unit module.
Corresponding mass transport and distributor and delivery main are all arranged in homogenizing units at different levels, constitute a homogenizing module jointly.
The charging aperture of first order homogenizing unit connects first mass transport and distributor 11, and the discharging opening of first order homogenizing unit is connected to second mass transport and distributor 12 by first delivery main; Second mass transport and distributor 12 are connected to the charging aperture of second level homogenizing unit, and the discharging opening of second level homogenizing unit is connected to 3 material by second delivery main and carries and distributor 13; 3 material conveying and distributor 13 are connected to the charging aperture of third level homogenizing unit 3, and the discharging opening of third level homogenizing unit 3 is connected to powder gathering-device 4 by the 3rd delivery main.
Now the homogenizing module that constitutes with first order homogenizing unit is that example describes in detail:
First order homogenizing unit is made up of four vertical grey storehouses 51 that are set up in parallel, this ash storehouse is a vertical vessel cylindraceous, the top is provided with the import of grey storehouse, the bottom has funnelform grey storehouse outlet, on the inlet pipeline of ash storehouse first valve 54 is installed, second valve 55 and platform disk feeder 52 are installed on the outlet conduit of grey storehouse, valve is a magnetic valve, preferred star discharge valve can be accepted the control of control system.Four grey storehouse outlets in the first order homogenizing unit are connected to first delivery main 53 simultaneously, are provided with air cushion conveyor band mechanism in first delivery main 53 herein, are used for the transportation of powder material.First delivery main is delivered to the mass transport and the distributor of next stage with powder material, enters next stage homogenizing unit then, and each feed bin in the next stage homogenizing unit carries out again homocline operation to it.
The bucket elevator 61 that connects successively before and after mass transport and distributor comprise, rotation sizing screen 62, permanent-magnetic iron expeller 63 and air cushion-belt conveyer 64, main effect is that powder material is promoted and carries, also can adopt other equipment replacement, be purpose with the conveying that can realize powder material.The effect of bucket elevator is that material is promoted to height more than the Hui Cang top, after rotation sizing screen and the preliminary screening of permanent-magnetic iron expeller, again by with some arms that the air cushion-belt conveyer pipeline directly links to each other material being assigned in the array of the grey storehouse of the corresponding levels.Open and close by the star discharge valve of setting can programme-control correspondence, alternately fill front and back successively with a plurality of grey storehouse of one-level, so the material in each grey storehouse is discrepant from the different time periods; After all filling with the grey storehouse of one-level, open the star discharge valve of bottom simultaneously, simultaneously blowing is carried out in the grey storehouse with one-level, because funneling effect makes material obtain the homogenizing of the first order, material enters next stage homogenizing unit more then, finish multistage homogenizing successively, finally obtain homogenizing powder product completely.
Third level homogenizing unit is in final stage, and the 3rd delivery main's end is connected to powder gathering-device 4 in the third level homogenizing unit, and the preferred cylinder vibratory sieve of powder gathering-device is realized the powder after the homogenizing is collected and packed by the cylinder vibratory sieve herein.
Can the negative inspiratory pressure pipeline be set at lifting points such as rotation sizing screen, air cushion-belt conveyer, Hui Cang, powder gathering-devices simultaneously, the lifting dust is collected, form dust arrester.
Except that the described technical characterictic of specification, be the known technology of those skilled in the art.
Claims (6)
1. tandem powder material homogenization system, it is characterized in that, at least comprise the homogenizing unit that is connected in series before and after the two-stage, described homogenizing unit is the grey storehouse array that is made of the identical grey storehouse of some structures, the charging aperture in each the grey storehouse in every grade of homogenizing unit is connected to mass transport and distributor at the same level, and the discharging opening in each the grey storehouse in every grade of homogenizing unit is connected to delivery main at the same level.
2. tandem powder material homogenization system according to claim 1 is characterized in that, mass transport and distributor before the described first order homogenizing unit link to each other with the powder field, and the delivery main behind the described final stage homogenizing unit is connected to the powder gathering-device.
3. tandem powder material homogenization system according to claim 2 is characterized in that described powder gathering-device is the cylinder vibratory sieve.
4. tandem powder material homogenization system according to claim 1 and 2 is characterized in that, the grey storehouse outlet of the grey storehouse import at each Hui Cang top and bottom is provided with the valve that can open and close respectively, and the grey storehouse in each grey storehouse exports the batcher of also connecting simultaneously.
5. tandem powder material homogenization system according to claim 1 and 2 is characterized in that, the bucket elevator that connects successively before and after described mass transport and distributor comprise, rotation sizing screen, permanent-magnetic iron expeller and air cushion-belt conveyer.
6. tandem powder material homogenization system according to claim 2 is characterized in that, in the described delivery mains at different levels air cushion conveyor mechanism is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205211913U CN201791503U (en) | 2010-09-08 | 2010-09-08 | Tandem power material homogenizing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205211913U CN201791503U (en) | 2010-09-08 | 2010-09-08 | Tandem power material homogenizing system |
Publications (1)
| Publication Number | Publication Date |
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| CN201791503U true CN201791503U (en) | 2011-04-13 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2010205211913U Expired - Fee Related CN201791503U (en) | 2010-09-08 | 2010-09-08 | Tandem power material homogenizing system |
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| CN (1) | CN201791503U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102612934A (en) * | 2012-03-17 | 2012-08-01 | 中石油东北炼化工程有限公司吉林设计院 | Raw material storage device for tapioca chips |
| CN102688847A (en) * | 2012-04-26 | 2012-09-26 | 中石油东北炼化工程有限公司吉林设计院 | Dry cassava raw material screening device |
| CN103707430A (en) * | 2013-12-27 | 2014-04-09 | 福建三宏再生资源科技有限公司 | Multistage dispensing equipment applied to production of regenerative polypropylene |
| CN104016568A (en) * | 2014-05-30 | 2014-09-03 | 台嘉玻璃纤维有限公司 | Glass fiber bagged powder homogenizing system and homogenizing method |
| CN107175031A (en) * | 2017-06-07 | 2017-09-19 | 广西贺州永亨新材料有限公司 | A kind of calcium carbonate homogenization system |
| CN109692606A (en) * | 2019-02-13 | 2019-04-30 | 四川华义茶业有限公司 | A kind of even heap mixing system of light material |
| CN111136259A (en) * | 2020-01-09 | 2020-05-12 | 北京毅能创投科技有限公司 | Aluminum powder mixing method |
| CN111470787A (en) * | 2020-06-03 | 2020-07-31 | 中冶焦耐(大连)工程技术有限公司 | Light-burned magnesia homogenizing process and system for high-purity magnesia |
-
2010
- 2010-09-08 CN CN2010205211913U patent/CN201791503U/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102612934A (en) * | 2012-03-17 | 2012-08-01 | 中石油东北炼化工程有限公司吉林设计院 | Raw material storage device for tapioca chips |
| CN102688847A (en) * | 2012-04-26 | 2012-09-26 | 中石油东北炼化工程有限公司吉林设计院 | Dry cassava raw material screening device |
| CN103707430A (en) * | 2013-12-27 | 2014-04-09 | 福建三宏再生资源科技有限公司 | Multistage dispensing equipment applied to production of regenerative polypropylene |
| CN103707430B (en) * | 2013-12-27 | 2016-04-20 | 福建三宏再生资源科技有限公司 | Be applied to the multiple stage material compounding equipment that regeneration polypropylene fibre is produced |
| CN104016568A (en) * | 2014-05-30 | 2014-09-03 | 台嘉玻璃纤维有限公司 | Glass fiber bagged powder homogenizing system and homogenizing method |
| CN107175031A (en) * | 2017-06-07 | 2017-09-19 | 广西贺州永亨新材料有限公司 | A kind of calcium carbonate homogenization system |
| CN109692606A (en) * | 2019-02-13 | 2019-04-30 | 四川华义茶业有限公司 | A kind of even heap mixing system of light material |
| CN109692606B (en) * | 2019-02-13 | 2023-11-24 | 四川华义茶业有限公司 | Even heap compounding system of light material |
| CN111136259A (en) * | 2020-01-09 | 2020-05-12 | 北京毅能创投科技有限公司 | Aluminum powder mixing method |
| CN111136259B (en) * | 2020-01-09 | 2022-01-11 | 北京毅能创投科技有限公司 | Aluminum powder mixing method |
| CN111470787A (en) * | 2020-06-03 | 2020-07-31 | 中冶焦耐(大连)工程技术有限公司 | Light-burned magnesia homogenizing process and system for high-purity magnesia |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 256216, Ming County town, Binzhou City, Shandong province Zouping Economic Development Zone Patentee after: Jingang New Materials Co., Ltd. Address before: 256216, Ming County town, Binzhou City, Shandong province Zouping Economic Development Zone Patentee before: Zouping Jingang New Material Co., Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110413 Termination date: 20150908 |
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| EXPY | Termination of patent right or utility model |