CN206746451U - Powder device is converted in glutinous rice flour integration - Google Patents
Powder device is converted in glutinous rice flour integration Download PDFInfo
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- CN206746451U CN206746451U CN201720567796.8U CN201720567796U CN206746451U CN 206746451 U CN206746451 U CN 206746451U CN 201720567796 U CN201720567796 U CN 201720567796U CN 206746451 U CN206746451 U CN 206746451U
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- backwind tube
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- cyclone separator
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Abstract
The utility model discloses a kind of glutinous rice flour integration to convert powder device, including mixing barrel, air conveyer flume, cyclone separator and tangential air return structure, mix and be provided with feed hopper at the top-feed mouth of barrel, the feeding mouth of the bottom discharging mouth and air conveyer flume that mix barrel connects；The charging aperture of cyclone separator and the discharge port of air conveyer flume connect；Tangential air return structure includes the main backwind tube being connected with the gas outlet of cyclone separator, main backwind tube is sequentially provided with first backwind tube, second backwind tube, the 3rd backwind tube and the 4th backwind tube along air-flow trend, mixing barrel and first backwind tube, second backwind tube, the connecting portion of the 3rd backwind tube and the 4th backwind tube are respectively equipped with tangent air inlet, the air intake directions of four tangent air inlets along counterclockwise with to mix barrel level tangent.The utility model can improve the uniformity converted powder efficiency and convert powder mixing, and save manpower, improve working environment.
Description
Technical field
Glutinous rice flour production technical field is the utility model is related to, more particularly to powder device is converted in a kind of glutinous rice flour integration.
Background technology
Glutinous rice flour is the raw-food material that the people are commonly used, with soft, tough cunning, fragrant glutinous and famous, it can make dumplings,
The based food and family's snack on Lantern Festival.Glutinous rice flour is that production procedure is typically as follows：Glutinous rice → wash rice → immersion → milling → sieving
→ press filtration → broken → drying → finished product.And in order to meet the different nutritional need of people, powder can be blended into finished product glutinous rice flour
The nourishing additive agent or food additives of shape, more using manually powder is converted at present, its labor intensity is big, and working environment is poor, and converts powder
Mixture homogeneity afterwards is bad.
Utility model content
The utility model is in order to solve the problems of the prior art, there is provided powder device is converted in a kind of glutinous rice flour integration, is improved
Convert powder efficiency and convert the uniformity of powder mixing, and save manpower, improve working environment.
In order to solve the above technical problems, the utility model adopts the following technical scheme that：Powder device is converted in glutinous rice flour integration, bag
Mixing barrel, air conveyer flume, cyclone separator and tangential air return structure are included, mixing barrel is the cylindrical tube of vertical
Structure, mix and feed hopper is provided with the top-feed mouth of barrel, mix the bottom discharging mouth of barrel and entering for air conveyer flume
Material mouth connects；Cyclone separator includes being arranged on the charging aperture of sidepiece, is arranged on the discharging opening of bottom and is arranged on going out for top
Gas port, the charging aperture of cyclone separator and the discharge port of air conveyer flume connect, and the discharging opening of cyclone separator is connected with storage
Hopper；Tangential air return structure includes main backwind tube be connected with the gas outlet of cyclone separator, main backwind tube along air-flow trend according to
It is secondary to be provided with first backwind tube, second backwind tube, the 3rd backwind tube and the 4th backwind tube, first backwind tube, second
The sidepiece of branch backwind tube, the 3rd backwind tube and the 4th backwind tube with the mixing barrel be connected, and mixing barrel and the
One backwind tube, second backwind tube, the connecting portion of the 3rd backwind tube and the 4th backwind tube are respectively equipped with tangent air inlet,
The air intake direction of four tangent air inlets along counterclockwise with to mix barrel level tangent, and four tangent air inlets are along mixing barrels
Axially spaced-apart arrangement.
Axial uniform intervals arrangement of four tangent air inlets along mixing barrel.
Circumference of four tangent air inlets along mixing barrel is uniformly distributed.
Charging control valve is equipped at the top-feed mouth of the mixing barrel.
The beneficial effects of the utility model：
The utility model is carried by mixing barrel, air conveyer flume, cyclone separator and the cooperation of tangential air return structure
It is high to convert powder efficiency and convert the uniformity of powder mixing, and manpower has been saved, improve working environment.
During utility model works, air conveyer flume is first opened, air-flow caused by air conveyer flume operating enters
Cyclone separator is simultaneously discharged from its gas outlet, and the air-flow of discharge is through successively through main backwind tube, branch backwind tube（First backwind tube,
Second backwind tube, the 3rd backwind tube and the 4th backwind tube）And corresponding tangent air inlet entrance mixing barrel, and
Mix and swirling eddy counterclockwise is formed in barrel；When the nourishing additive agent or food additives of glutinous rice flour and powdery are through feed hopper
Into after mixing barrel, mixture of powders can rotate with mixing during whereabouts, afterwards mixture of powders air inlet
Conveying skewed slot is transported to cyclone separator, and a certain degree of mixing can be also produced in course of conveying mixture of powders；Into rotation
The mixture of powders of wind separator is separated with gas, in separation process, mixture of powders further mixed and from
The discharging opening discharge of cyclone separator, the mixture of powders of discharge complete uniform mixing, efficiently powder operation are converted so as to realize；
And air-flow can turn again to mixing barrel derived from the gas outlet of cyclone separator, cycle operation is realized.
Axial uniform intervals arrangement of four tangent air inlets along mixing barrel, four tangent air inlets edges mix barrel
Circumferentially it is uniformly distributed, above-mentioned design makes caused swirling eddy in mixing barrel more uniform.
Charging control valve is equipped with the top-feed mouth of the mixing barrel, to control charging rate.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the top view that barrel position is mixed in Fig. 1.
Embodiment
Structure of the present utility model and the course of work are further described below in conjunction with the accompanying drawings.
As depicted in figs. 1 and 2, powder device is converted in glutinous rice flour integration of the present utility model, including mixing barrel 5, air are defeated
Skewed slot 6, cyclone separator 7 and tangential air return structure are sent, mixing barrel 5 is the cylindrical tube structure of vertical, mixes barrel 5
Top-feed mouth at be provided with feed hopper 8, the bottom discharging mouth of mixing barrel 5 is connected with the feeding mouth of air conveyer flume 6；Rotation
Wind separator 7 includes being arranged on the charging aperture 10 of sidepiece, is arranged on the discharging opening 11 of bottom and is arranged on the gas outlet 12 on top,
The charging aperture 10 of cyclone separator 7 is connected with the discharge port of air conveyer flume 6, and the discharging opening 11 of cyclone separator 7 is connected with
Storage bin hopper 9；Tangential air return structure includes the main backwind tube 13 being connected with the gas outlet 12 of cyclone separator 7, the main edge of backwind tube 13
Air-flow trend be sequentially provided with first return air 1 manage, second backwind tube 2, the 3rd backwind tube 3 and the 4th backwind tube 4, first
1, second backwind tube 2 of branch backwind tube, the 3rd backwind tube 3 and the 4th backwind tube 4 connect with the sidepiece for mixing barrel 5
Connect, and mix the company of 1, second backwind tube 2 of barrel 5 and first backwind tube, the 3rd backwind tube 3 and the 4th backwind tube 4
Socket part is respectively equipped with tangent air inlet 14, and the air intake direction of four tangent air inlets 14 is along counterclockwise with mixing 5 horizontal phase of barrel
Cut, and axial uniform intervals of four tangent air inlets 14 along mixing barrel 5 are arranged, while four tangent air inlets 14 are along mixing
The circumference of barrel 5 is uniformly distributed.
In the present embodiment, mix and be equipped with charging control valve at the top-feed mouth of barrel 5, to control charging rate.
During utility model works, air conveyer flume 6 is first opened, air conveyer flume 6 operates caused air-flow and entered
Enter cyclone separator 7 and discharged from its gas outlet 12, the air-flow of discharge is through successively through main backwind tube 13, branch backwind tube（First
1, second backwind tube 2 of backwind tube, the 3rd backwind tube 3 and the 4th backwind tube 4）And corresponding tangent air inlet 14 enters
Barrel 5 is mixed, and swirling eddy counterclockwise is formed in mixing barrel 5；When glutinous rice flour and the nourishing additive agent or food of powdery
Product additive is after feed hopper 8 enters mixing barrel 5, and mixture of powders can rotate with mixing during whereabouts, afterwards
Mixture of powders air inlet conveying skewed slot 6 is transported to cyclone separator, and one can be also produced in course of conveying mixture of powders
Determine the mixing of degree；Mixture of powders into cyclone separator 7 is separated with gas, in separation process, powder mixing
Thing is further mixed and is discharged into storage bin hopper 9 from the discharging opening 11 of cyclone separator 7, and the mixture of powders of discharge has been
Into uniform mixing, efficiently powder operation is converted so as to realize；And it can be returned again from air-flow derived from the gas outlet 12 of cyclone separator 7
To mixing barrel 5, cycle operation is realized.
The utility model is by mixing matching somebody with somebody for barrel 5, air conveyer flume 6, cyclone separator 7 and tangential air return structure
Close, improve the uniformity converted powder efficiency and convert powder mixing, and saved manpower, improve working environment.
Above example is only to illustrative and not limiting the technical solution of the utility model, although with reference to above-described embodiment pair
The utility model is described in detail, it will be understood by those within the art that：The utility model can still be entered
Row modification or equivalent substitution, without departing from any modification or partial replacement of spirit and scope of the present utility model, it all should
Cover among right of the present utility model.
Claims (4)
1. powder device is converted in glutinous rice flour integration, it is characterised in that：Including mixing barrel, air conveyer flume, cyclone separator and
Tangential air return structure, mixing barrel are the cylindrical tube structure of vertical, mix and charging is provided with the top-feed mouth of barrel
Bucket, the feeding mouth of the bottom discharging mouth and air conveyer flume that mix barrel connect；Cyclone separator includes being arranged on sidepiece
Charging aperture, the discharging opening for being arranged on bottom and the gas outlet for being arranged on top, the charging aperture of cyclone separator and air conveying are oblique
The discharge port connection of groove, the discharging opening of cyclone separator are connected with storage bin hopper；Tangential air return structure includes and cyclone separator
The main backwind tube of gas outlet connection, main backwind tube are sequentially provided with first backwind tube, second backwind tube, the 3rd along air-flow trend
Branch backwind tube and the 4th backwind tube, first backwind tube, second backwind tube, the 3rd backwind tube and the 4th backwind tube are equal
With it is described mixing barrel sidepiece be connected, and mixing barrel and first backwind tube, second backwind tube, the 3rd backwind tube and
The connecting portion of 4th backwind tube is respectively equipped with tangent air inlet, and the air intake direction of four tangent air inlets is along counterclockwise with mixing
Barrel level is tangent, and axially spaced-apart arrangement of four tangent air inlets along mixing barrel.
2. powder device is converted in glutinous rice flour integration according to claim 1, it is characterised in that：Four tangent air inlets edge mixing
The axial uniform intervals arrangement of barrel.
3. powder device is converted in glutinous rice flour integration according to claim 2, it is characterised in that：Four tangent air inlets edge mixing
The circumference of barrel is uniformly distributed.
4. powder device is converted in the glutinous rice flour integration according to any one of claim 1-3, it is characterised in that：The compound
Charging control valve is equipped at the top-feed mouth of cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720567796.8U CN206746451U (en) | 2017-05-22 | 2017-05-22 | Powder device is converted in glutinous rice flour integration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720567796.8U CN206746451U (en) | 2017-05-22 | 2017-05-22 | Powder device is converted in glutinous rice flour integration |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206746451U true CN206746451U (en) | 2017-12-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720567796.8U Expired - Fee Related CN206746451U (en) | 2017-05-22 | 2017-05-22 | Powder device is converted in glutinous rice flour integration |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206746451U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107950877A (en) * | 2018-01-04 | 2018-04-24 | 重庆市荣记三民斋桃片有限公司 | Glutinous rice flour returns powder device |
| CN112056228A (en) * | 2020-09-17 | 2020-12-11 | 河南农业职业学院 | Electric automatization material feeding unit |
| CN112432349A (en) * | 2020-11-13 | 2021-03-02 | 广东美的白色家电技术创新中心有限公司 | Air supply mechanism and air conditioner |
| CN114272833A (en) * | 2021-12-02 | 2022-04-05 | 曾令波 | Automatic proportioning device of voltage stabilization type concrete additive |
-
2017
- 2017-05-22 CN CN201720567796.8U patent/CN206746451U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107950877A (en) * | 2018-01-04 | 2018-04-24 | 重庆市荣记三民斋桃片有限公司 | Glutinous rice flour returns powder device |
| CN112056228A (en) * | 2020-09-17 | 2020-12-11 | 河南农业职业学院 | Electric automatization material feeding unit |
| CN112432349A (en) * | 2020-11-13 | 2021-03-02 | 广东美的白色家电技术创新中心有限公司 | Air supply mechanism and air conditioner |
| CN112432349B (en) * | 2020-11-13 | 2022-04-01 | 广东美的白色家电技术创新中心有限公司 | Air supply mechanism and air conditioner |
| CN114272833A (en) * | 2021-12-02 | 2022-04-05 | 曾令波 | Automatic proportioning device of voltage stabilization type concrete additive |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171215 Termination date: 20210522 |