CN206273561U - A kind of mixer dedusting recovery system - Google Patents
A kind of mixer dedusting recovery system Download PDFInfo
- Publication number
- CN206273561U CN206273561U CN201620986918.2U CN201620986918U CN206273561U CN 206273561 U CN206273561 U CN 206273561U CN 201620986918 U CN201620986918 U CN 201620986918U CN 206273561 U CN206273561 U CN 206273561U
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- China
- Prior art keywords
- recovery system
- bucket
- mixer
- weighing bucket
- agitator tank
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Abstract
The utility model provides a kind of mixer dedusting recovery system.Mixer dedusting recovery system includes the deduster that agitator tank and suction opeing are connected with agitator tank, also include for the weighing bucket to agitator tank feed, the discharging opening of the ash bucket of deduster is by weighing bucket and agitator tank UNICOM, the system can be measured so as to re-use the dust collected in dust collector ash hopper by flyash weighing bucket, play and save material, refuse reclamation, the effect of reduction production cost.
Description
Technical field
The utility model is related to a kind of mixer dedusting recovery system.
Background technology
Mixer is for sand, stone, flyash or cement etc., being stirred according to certain proportioning.Mixer works
Because various dust from flying, air pollution has also jeopardized the healthy of staff than more serious at scene, so being adopted in production
Take the dust that certain measure will fly upward to be collected, an applying date is 2015.09.09, Application No.
201520696972.9 Chinese patent discloses a kind of improved concrete mixer, and the mixer includes agitator tank, charging
Mouth and feed pipe, feed pipe are extend into inside charging aperture, and charging aperture is connected with dedusting located at stirring upper box part above charging aperture
Device is deduster, and dust arrester is ash bucket including collecting tank, and collecting tank side is provided with suction inlet i.e. suction opeing, and suction inlet is stretched into
To inside charging aperture, collect pot bottom and be provided with feed opening i.e. discharging opening, feed opening is connected with feed pipe.The device can be to coagulation
The dust produced in native whipping process is recycled, but because the dust collected directly enters feed pipe by feed opening
In, therewith into agitator tank, the proportion scale of each composition in concrete can be destroyed, so that the performance of concrete is influenceed, from
And cause the waste of material.
Utility model content
The purpose of this utility model is to provide a kind of mixer dedusting recovery system, and the device can be solved to dust
After recycling, it is impossible to clearly control the problem of the mixed proportion of various cooperation powders in mixer.
To achieve the above object, the technical scheme of the utility model mixer dedusting recovery system is：Mixer dedusting is returned
Receipts system includes the deduster that is connected with agitator tank of agitator tank and suction opeing, also including for the weighing bucket to agitator tank feed,
The discharging opening of the ash bucket of deduster is by weighing bucket and agitator tank UNICOM.
The discharge outlet of the ash bucket of deduster is provided with outlet valve.
The outlet valve is Pneumatic butterfly valve.
The deduster is main moving pulse deduster.
The weighing bucket includes cement weighing bucket and flyash weighing bucket.
The discharging opening and flyash weighing bucket UNICOM.
The discharging opening is by flexible pipe and weighing bucket UNICOM
The beneficial effects of the utility model are：Because the discharging opening of deduster is by weighing bucket and agitator tank UNICOM, Ke Yitong
Weighing bucket is crossed to weigh the dust for reclaiming, after removing the weight of the part dust, can be according between various powders
Proportion relation, other powders to needing to mix are allocated by weight, thus reach what is collected in dust collector ash hopper
Dust is measured so as to re-use by flyash weighing bucket, is played and is saved material, refuse reclamation, reduction production cost
Effect.
Brief description of the drawings
Fig. 1 is the structural representation of embodiment one of the utility model mixer dedusting recovery system；
Fig. 2 is the right view of Fig. 1.
Specific embodiment
Implementation method of the present utility model is described further below in conjunction with the accompanying drawings.
The specific embodiment one of mixer dedusting recovery system of the present utility model, as shown in Figure 1 to Figure 2, mixer is removed
Dust recovery system include three platforms, respectively stir platform, with bed of material platform and dedusting support platform.
On stirring platform, mixer includes agitator tank 1 to mixer, is put according to certain ratio by by various dispensings
In agitator tank, by the stirring of mixer blade, blending turns into uniform compound.
Mixer top is communicated with the dust collection pipeline 2 for upwardly extending, and dust collection pipeline 2 is passed through and extended upwardly to bed of material platform
Dedusting support platform, dedusting support platform is provided with deduster, and in the present embodiment, deduster is main moving pulse deduster, can
Drawn via dust collection pipeline 2 with to the airborne dust produced in agitator tank 1.
Active pulse dust collector includes suction opeing and discharging opening, and suction opeing and the dust collection pipeline 2 of active pulse dust collector connect
It is logical, the downward UNICOM's agitator tank of discharging opening, and circulation loop is formed, circulation loop is realized by the outlet valve located at discharge outlet
On and off, outlet valve is Pneumatic butterfly valve 4, and in other embodiments, outlet valve can also be other valves such as magnetic valve.
Active pulse dust collector also includes the ash bucket for collecting adsorption of dust, and discharging opening is located at ash bucket bottom, absorption
Dust is accumulated in ash bucket, and can be discharged or be temporarily stored into collection bucket by the control dust of the Pneumatic butterfly valve of discharge outlet.
In the present embodiment, ash bucket is cone bucket 3, and in the state of the closing of Pneumatic butterfly valve 4, active pulse dust collector is through dust suction
Pipeline 2 draws the dust collection for coming up in cone bucket 3, is flown upward everywhere this avoid the airborne dust produced in whipping process, favorably
In the working environment of protection working site, safeguard work personnel's is healthy, and the dust that it also avoid in ash bucket is adsorbed winged
Raise, while it also avoid in the case where Pneumatic butterfly valve is not provided with, the problem that the dust in weighing bucket is also adsorbed.
The discharging opening of cone bucket 3 connects downwards ash-unloading tube road 5, and connection flexible pipe 6 in the lower end of ash-unloading tube road 5 is connected with below flexible pipe 6
Weighing bucket, weighing bucket is located at on bed of material platform, and in the present embodiment, weighing bucket is two, is respectively cement weighing bucket 9 and flyash weighing bucket
10, flexible pipe 6 is connected with flyash weighing bucket.
In the course of work that mixer mixes cement with flyash, active pulse dust collector is constantly in working condition,
Pneumatic butterfly valve 4 is closed simultaneously, and the stirring airborne dust inside mixer is accumulated in the presence of active pulse dust collector by dust collection pipeline 2
Gather in deduster bottom cone bucket 3, now the Dust in cone bucket includes cement and flyash；Because cement grade compares fine coal
Grey label is high, and in order to ensure the mixing quality of concrete, cement and flyash mixed dust to collecting all serve as into fine coal
Ash；When dispensing is started, Pneumatic butterfly valve 4 is opened, the dust in cone bucket is all served as into flyash and is entered into flyash and claim
Bucket, Pneumatic butterfly valve is closed after flyash weighing bucket reaches required weighing value；After opening Pneumatic butterfly valve 4, the powder collected in cone bucket 3
Dirt is entered into flyash weighing bucket 10 via ash-unloading tube road 5 and flexible pipe 6.
The both sides of cement weighing bucket and flyash weighing bucket are separately installed with weighing balance 11, claim by the powder in weighing bucket
Weight, each composition that can be exactly to mixing carries out ratio control；After dust enters in flyash weighing bucket, by weigher 11
Weigh, after the amount required for reaching, close Pneumatic butterfly valve 4 and stop to blanking in flyash weighing bucket.
According to certain proportion relation, required cement weight is calculated according to flyash weight, then in cement weighing bucket
It is middle to claim to obtain required a certain amount of cement.
Cement weighing bucket or flyash weighing bucket lower section are provided with off-load opening, and off-load opening is provided with off-load valve, by off-load
Valve is connected with conjunction hopper 7, and the dust in cement weighing bucket or flyash weighing bucket after weighing is fed downwardly into conjunction hopper 7
In, subsequently enter agitator tank 1；Agitator tank 1 is connected with water tank 8, is supplied water by agitator tank 1, each to what is proportionally prepared
Dispensing is planted to be stirred.Stirring airborne dust is carried out into recycling, is saved material, reduces cost makes waste material effectively recycle,
With good economic benefit.
Used as the specific embodiment two of the utility model mixer dedusting recovery system, the difference with embodiment one exists
In, Pneumatic butterfly valve is opened, the dust that will be collected into all is discharged into weighing bucket, is weighed by the dust in weighing bucket, according to
Gross weight by being discharged into dust carries out the proportioning of each dispensing.
Used as the specific embodiment three of the utility model mixer dedusting recovery system, the difference with embodiment one exists
In the discharge outlet of dust collector ash hopper is provided with Pneumatic butterfly valve and discharging opening is directly connected by pipeline with agitator tank, and centre does not set
Weighing bucket is put, the powder for adsorbing is not weighed, i.e., only prevent the generation of the phenomenon that the dust that need not be adsorbed is drawn.
Used as the specific embodiment four of the utility model mixer dedusting recovery system, the difference with embodiment one exists
In weighing bucket is provided only with one, is used to collect the dust opened and leak down from ash bucket after Pneumatic butterfly valve, and other need to participate in mixing
After powder is weighed by the other modes outside mixer dedusting recovery system, it is added in weighing bucket.
Claims (7)
1. the deduster that a kind of mixer dedusting recovery system, including agitator tank and suction opeing are connected with agitator tank, its feature
It is：The mixer dedusting recovery system is also included for the weighing bucket to agitator tank feed, the discharging opening of the ash bucket of deduster
By weighing bucket and agitator tank UNICOM.
2. mixer dedusting recovery system according to claim 1, it is characterised in that：The discharge outlet of the ash bucket of deduster
It is provided with outlet valve.
3. mixer dedusting recovery system according to claim 2, it is characterised in that：The outlet valve is Pneumatic butterfly valve.
4. mixer dedusting recovery system according to claim 3, it is characterised in that：The deduster is removed for main moving pulse
Dirt device.
5. the mixer dedusting recovery system according to claim 1-4 any one, it is characterised in that：The weighing bucket includes
Cement weighing bucket and flyash weighing bucket.
6. mixer dedusting recovery system according to claim 5, it is characterised in that：The discharging opening and flyash weighing bucket
UNICOM.
7. mixer dedusting recovery system according to claim 6, it is characterised in that：The discharging opening is by flexible pipe and title
Bucket UNICOM.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620986918.2U CN206273561U (en) | 2016-08-30 | 2016-08-30 | A kind of mixer dedusting recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620986918.2U CN206273561U (en) | 2016-08-30 | 2016-08-30 | A kind of mixer dedusting recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206273561U true CN206273561U (en) | 2017-06-23 |
Family
ID=59063601
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620986918.2U Expired - Fee Related CN206273561U (en) | 2016-08-30 | 2016-08-30 | A kind of mixer dedusting recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206273561U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106182438A (en) * | 2016-08-30 | 2016-12-07 | 郑州三和水工机械有限公司 | Blender dedusting recovery system |
| CN109369149A (en) * | 2018-11-21 | 2019-02-22 | 浙江大东吴集团建设有限公司 | Using the haydite materials mixing corollary equipment group of mud class waste |
-
2016
- 2016-08-30 CN CN201620986918.2U patent/CN206273561U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106182438A (en) * | 2016-08-30 | 2016-12-07 | 郑州三和水工机械有限公司 | Blender dedusting recovery system |
| CN109369149A (en) * | 2018-11-21 | 2019-02-22 | 浙江大东吴集团建设有限公司 | Using the haydite materials mixing corollary equipment group of mud class waste |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170623 Termination date: 20190830 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |