CN106731942A - Inhale powder formula mixing dispersion disperse pump - Google Patents
Inhale powder formula mixing dispersion disperse pump Download PDFInfo
- Publication number
- CN106731942A CN106731942A CN201710072913.8A CN201710072913A CN106731942A CN 106731942 A CN106731942 A CN 106731942A CN 201710072913 A CN201710072913 A CN 201710072913A CN 106731942 A CN106731942 A CN 106731942A
- Authority
- CN
- China
- Prior art keywords
- powder
- rotor
- liquid
- rotating disk
- pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/60—Pump mixers, i.e. mixing within a pump
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/41—Emulsifying
Abstract
The present invention relates to inhale powder formula mixing dispersion disperse pump, including the pump housing, base and it is arranged on the motor of the rotation of drive shaft on base, the main shaft stretches into pump housing inner chamber, powder import, liquid-inlet and discharging opening are provided with the pump housing, it is provided with the rotor of the main axis in the inserting end of main shaft, powder and liquid are sucked the rotor both sides by the rotor from the powder import and liquid-inlet respectively in the negative pressure that the rotation of pump housing inner chamber is produced, then mixing and emulsifying, then from discharging opening outflow under rotor centrifugal force effect.In pump housing inner chamber, the rotor of rotation produces negative pressure, powder and liquid is inhaled into rotor outside is oriented to behind rotor both sides, and mixed material can throw away from discharging opening under the centrifugal action of rotor；It follows that the present invention need not provide extra charging and discharging pressure, energy consumption is greatlyd save.
Description
Technical field
The present invention relates to disperse pump, powder formula mixing dispersion disperse pump is specifically inhaled.
Background technology
Influence the relative motion linear velocity that one of key factor of mulser emulsifying effectiveness is stator, rotor, reality industry
Improve the linear velocity of rotor in practice by speed change and converter plant, but by rotor machining precision and rolling, lubrication and
The bottleneck limitation of seal member performance, the manufacturing cost for increasing substantially linear velocity is very high.In traditional chemical industry powder
In liquid Hybrid Production Process, light powder is mixed into the liquid of requirement, manually poured into or vacuum suction.Due to
Powder proportion is smaller, and can form floating, wall built-up, skinning in kettle and liquid surface when stirred tank is poured into the phenomenon such as unite, and make
Into emulsification degree not enough, dispersion and emulsion effect on driving birds is not good, upper, middle and lower dispersion mixing is uneven, and mixing time is more long, have suspension, dead angle
And energy consumption it is excessive the shortcomings of.
The content of the invention
For above-mentioned technical problem, it is an object of the invention to provide a kind of good, the well mixed suction powder formula of emulsifying effectiveness
Mixing dispersion disperse pump.
The present invention solve the technical scheme that is used of above-mentioned technical problem for：Inhale powder formula mixing dispersion disperse pump, including pump
Body, base and the motor of the rotation of drive shaft on base is arranged on, the main shaft stretches into pump housing inner chamber, powder is provided with the pump housing
Import, liquid-inlet and discharging opening, are provided with the rotor of the main axis in the inserting end of main shaft, and the rotor revolves in pump housing inner chamber
Powder and liquid are sucked the rotor both sides by raw negative pressure of changing the line of production from the powder import and liquid-inlet respectively, then mix breast
Change, then from discharging opening outflow under rotor centrifugal force effect.
Preferably, being provided with the end cap of canned pump intracoelomic cavity in the rotor side, the powder is provided with the end cap
Body import.
Preferably, the rotor includes the rotating disk on main shaft, in the rotating disk side adjacent with the end cap
Several grooves are radially offered on face, feed cavity, the powder import and the feed cavity are formed between the rotating disk and the end cap
Communicate, powder flows to rotating disk outside from after powder import suction feed cavity along the groove.
Preferably, the groove depth of each groove is gradually deepened from center of turntable to periphery.
Preferably, arc of the blade formed between two adjacent grooves in circumferential skewing.
Preferably, blade surface axial direction indent.
Preferably, the rotating disk another side is circumferentially-spaced to be distributed with several teeth, the another side and the pump housing shape
Into admission chamber, the liquid-inlet is connected with the admission chamber, another along rotating disk after liquid sucks the admission chamber from the liquid-inlet
The teeth groove of one side flows to rotating disk outside, and mixes with the powder flowed on the outside of the rotating disk.
Preferably, the end cap is axially fixed is provided with emulsification set, emulsification set gap is set in outside the rotating disk
Side, the emulsification put radially offer several through holes, the emulsification set and the pump housing between form discharging chamber, the discharging chamber with
The discharging opening connection；Powder and liquid flow to the gap entered between emulsification set and rotating disk behind rotating disk outside, in the gap
Powder and liquid carry out mixing and emulsifying by the relative motion between rotating disk and emulsification set, then under the influence of centrifugal force from institute
State several through holes and enter discharging chamber, then flowed out from the discharging opening.
Preferably, the rotor also includes the material stirring disc being fixedly connected with another side described in rotating disk, in the material stirring disc
Between offer for flowing to the liquid pass hole that the liquid of the teeth groove passes through, the material stirring disc perisporium is provided with and several stretches into the discharging
Material toggling tooth in chamber.
Preferably, the material path hole wall is circumferentially distributed several double wedges.
As can be known from the above technical solutions, the rotor in the rotation of pump housing inner chamber produces negative pressure, powder and liquid is inhaled into and is turned
Rotor outside is oriented to behind sub- both sides, then again in the gap in outside by the relative motion of rotor and emulsification set, makes powder and liquid
Body disperses rapidly, emulsifies, and forms well mixed material, agglomerating so as to avoid material coalescence, and in the centrifugation masterpiece of rotor
Can be thrown away from discharging opening with lower mixed material；It follows that the present invention need not provide extra charging and discharging pressure, greatly save
Energy consumption.
Brief description of the drawings
Fig. 1 is a kind of contour structures schematic diagram of preferred embodiment of the invention.
Fig. 2 is A-A cross section structure diagrams in Fig. 1.
Fig. 3 is the dimensional structure diagram of rotor in the present invention.
Fig. 4 is the dimensional structure diagram of Fig. 3 sides.
Fig. 5 is the dimensional structure diagram of end cap in the present invention.
Specific embodiment
The present invention is discussed in detail with reference to Fig. 1, Fig. 2, Fig. 3, Fig. 4 and Fig. 5：
Inhale powder formula mixing dispersion disperse pump, including the pump housing 11, base 1 and be arranged on the motor 3 of the rotation of drive shaft 2 on base,
Motor cover 4 is provided with the outside of motor, to protect motor；The main shaft stretches into pump housing inner chamber, and powder import is provided with the pump housing
12nd, liquid-inlet 13 and discharging opening 14, are provided with the rotor 5 of the main axis in the inserting end of main shaft, and the rotor is in the pump housing
Powder and liquid are sucked the rotor both sides by the negative pressure that chamber rotation is produced from the powder import and liquid-inlet respectively, are then mixed
Emulsification is closed, then from discharging opening outflow under rotor centrifugal force effect.Rotor can be formed by high speed rotation in pump housing inner chamber
Negative pressure, the purpose of powder and liquid is automatically drawn into so as to reach.Rotor of the invention can be carried out within the most short time to material
Dispersion, shearing, emulsification treatment so that diameter of particle distribution significantly narrows, so that fine product steady in a long-term is obtained,
And in being applied to, high-volume on-line continuous production.
The present invention is provided with the end cap 7 of canned pump intracoelomic cavity in the rotor side, and the powder is provided with the end cap
Import, to facilitate into powder；The rotor 5 includes the rotating disk 51 on the main shaft, the rotating disk it is adjacent with the end cap one
Several grooves 52 are radially offered on side, feed cavity 8 is formed between the rotating disk and the end cap, the powder import is entered with this
Material chamber communicates, and powder flows to rotating disk outside from after powder import suction feed cavity along the groove.In implementation process,
The groove depth of each groove is gradually deepened from center of turntable to periphery, it is ensured that powder flows out along groove, convenient discharging, and can
Prevent powder from resting in feed cavity for a long time.The blade 53 formed between two adjacent grooves makes in the arc of circumferential skewing
Rotating disk is similar to helical form, is conducive to producing negative pressure higher during turntable rotation.Blade surface axial direction indent, on the one hand causes
Feed cavity volume is bigger, has using charging；On the other hand in turntable rotation, female parts can produce vortex, so as to produce negative
Pressure.
Rotating disk another side of the invention is circumferentially-spaced to be distributed with several teeth 54, the another side and the pump housing formed into
Sap cavity 9, the liquid-inlet is connected with the admission chamber, another along rotating disk after liquid sucks the admission chamber from the liquid-inlet
The teeth groove 55 of side flows to rotating disk outside, and mixes with the powder flowed on the outside of the rotating disk；The end cap is axially fixed setting
There is emulsification set 6, emulsification set gap is set in the rotating disk outside, and the emulsification puts and radially offers several through holes 61, should
Discharging chamber 62 is formed between emulsification set and the pump housing, the discharging chamber is connected with the discharging opening；Powder flows to rotating disk with liquid
The gap entered behind outside between emulsification set and rotating disk, powder passes through the phase between rotating disk and emulsification set with liquid in the gap
Motion is disperseed, mixed, emulsified, then under the influence of centrifugal force, compound is entered from several through holes after emulsification
Discharging chamber, then flowed out from the discharging opening.
Rotor of the invention also includes the material stirring disc 56 being fixedly connected with another side described in rotating disk, is opened in the middle of the material stirring disc
It is provided with for flowing to the liquid pass hole 57 that the liquid of the teeth groove passes through, the material stirring disc perisporium is provided with and several stretches into the discharging chamber
Compound dispersion after emulsification can be prevented it from reuniting, influence discharging by interior material toggling tooth 58, the material toggling tooth of rotation.The punishment in advance
Hole hole wall is circumferentially distributed several double wedges 59, and several double wedges can be stirred to liquid, is conducive to liquid to be flowed to rotating disk outside.
Liquid and powder disperse any poly- block thing that may be present by high shear rotor emulsifying systems of the invention, obtain completely wet
Profit and finely dispersed material, greatly shorten the production time, reduce production cost.
The present invention produces negative pressure using the rotor of disperse pump special construction when high speed rotates, by powder and liquid while
Even ground suction pump intracoelomic cavity, and disperseed by high speed shear in moment, make powder show no sign of being agglomerated into soon in liquid flowing
The time of shape thing is just sufficiently uniformly distributed in liquid stream, therefore in the absence of any powder not moistened completely, will not also be made
Into skinning, so as to obtain moistening and finely dispersed material completely.
Above-mentioned implementation method is used for illustrative purposes only, and is not limitation of the present invention, relevant technical field
Those of ordinary skill, without departing from the spirit and scope of the present invention, can be so that various changes can be made and modification, therefore institute
Having equivalent technical scheme should also belong to scope of the invention.
Claims (10)
1. inhale powder formula mixing dispersion disperse pump, including the pump housing, base and be arranged on the motor of drive shaft rotation on base, it is special
Levy and be：The main shaft stretches into pump housing inner chamber, and powder import, liquid-inlet and discharging opening are provided with the pump housing, in stretching for main shaft
Enter end to be provided with the rotor of the main axis, the rotor rotates the negative pressure for producing by powder and liquid respectively from institute in pump housing inner chamber
State powder import and liquid-inlet suck the rotor both sides, then mixing and emulsifying, then rotor centrifugal force effect under from it is described go out
Material mouth flows out.
2. powder formula mixing dispersion disperse pump is inhaled according to claim 1, it is characterised in that：It is provided with the rotor side close
The end cap of envelope pump housing inner chamber, is provided with the powder import on the end cap.
3. powder formula mixing dispersion disperse pump is inhaled according to claim 2, it is characterised in that：The rotor includes being arranged on main shaft
On rotating disk, radially offer several grooves on the rotating disk one side adjacent with the end cap, the rotating disk and the end cap
Between form feed cavity, the powder import is communicated with the feed cavity, powder from the powder import suction feed cavity after, along institute
State groove and flow to rotating disk outside.
4. powder formula mixing dispersion disperse pump is inhaled according to claim 3, it is characterised in that：The groove depth of each groove from turn
Disk center gradually deepens to periphery.
5. powder formula mixing dispersion disperse pump is inhaled according to claim 3, it is characterised in that：Formed between two adjacent grooves
Blade is in the arc of circumferential skewing.
6. powder formula mixing dispersion disperse pump is inhaled according to claim 5, it is characterised in that：Blade surface axial direction indent.
7. powder formula mixing dispersion disperse pump is inhaled according to any one in claim 3 to 6, it is characterised in that：The rotating disk
Another side is circumferentially-spaced to be distributed with several teeth, and the another side and the pump housing form admission chamber, the liquid-inlet with should
Admission chamber is connected, and after liquid sucks the admission chamber from the liquid-inlet, rotating disk outside is flowed to along the teeth groove of rotating disk another side,
And mix with the powder flowed on the outside of the rotating disk.
8. powder formula mixing dispersion disperse pump is inhaled according to claim 7, it is characterised in that：The end cap is axially fixed setting
There is emulsification to cover, emulsification set gap is set in the rotating disk outside, the emulsification puts and radially offers several through holes, the emulsification
Discharging chamber is formed between set and the pump housing, the discharging chamber is connected with the discharging opening；After powder flows to rotating disk outside with liquid
Gap between emulsification set and rotating disk, powder and liquid are by the relative motion between rotating disk and emulsification set in the gap
Mixing and emulsifying is carried out, then enters discharging chamber from several through holes under the influence of centrifugal force, then flow out from the discharging opening.
9. powder formula mixing dispersion disperse pump is inhaled according to claim 8, it is characterised in that：The rotor also includes and rotating disk institute
The material stirring disc that another side is fixedly connected is stated, confession is offered in the middle of the material stirring disc and is flowed to the liquid excessively that the liquid of the teeth groove passes through
Hole, the material stirring disc perisporium is provided with several material toggling tooths stretched into the discharging chamber.
10. powder formula mixing dispersion disperse pump is inhaled according to claim 9, it is characterised in that：The material path hole wall circumferentially divides
It is furnished with several double wedges.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710072913.8A CN106731942A (en) | 2017-02-10 | 2017-02-10 | Inhale powder formula mixing dispersion disperse pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710072913.8A CN106731942A (en) | 2017-02-10 | 2017-02-10 | Inhale powder formula mixing dispersion disperse pump |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106731942A true CN106731942A (en) | 2017-05-31 |
Family
ID=58955891
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710072913.8A Withdrawn CN106731942A (en) | 2017-02-10 | 2017-02-10 | Inhale powder formula mixing dispersion disperse pump |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106731942A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107583484A (en) * | 2017-09-28 | 2018-01-16 | 上海琥崧智能科技股份有限公司 | A kind of powder liquid on-line mixing device |
| CN108465388A (en) * | 2017-07-25 | 2018-08-31 | 深圳市尚水智能设备有限公司 | A kind of solid-liquid mixing device and the mixed method using the equipment |
| CN108722220A (en) * | 2018-08-15 | 2018-11-02 | 浙江兴盛机械有限公司 | A kind of emulsification rotor of arc angle |
| CN109269290A (en) * | 2018-10-31 | 2019-01-25 | 长沙万荣粉体设备科技有限公司 | A kind of rotor and depolymerizer |
| CN111773943A (en) * | 2020-07-07 | 2020-10-16 | 上海富昶电气有限公司 | Online dispersion auto sucking machine and slurrying system |
| CN113304670A (en) * | 2021-05-27 | 2021-08-27 | 松辰堂科技河北有限公司 | Aerosol generator |
| CN114226021A (en) * | 2022-01-07 | 2022-03-25 | 东莞市康搏智能装备有限公司 | Online grinding dispersion machine |
-
2017
- 2017-02-10 CN CN201710072913.8A patent/CN106731942A/en not_active Withdrawn
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108465388A (en) * | 2017-07-25 | 2018-08-31 | 深圳市尚水智能设备有限公司 | A kind of solid-liquid mixing device and the mixed method using the equipment |
| CN107583484A (en) * | 2017-09-28 | 2018-01-16 | 上海琥崧智能科技股份有限公司 | A kind of powder liquid on-line mixing device |
| CN108722220A (en) * | 2018-08-15 | 2018-11-02 | 浙江兴盛机械有限公司 | A kind of emulsification rotor of arc angle |
| CN109269290A (en) * | 2018-10-31 | 2019-01-25 | 长沙万荣粉体设备科技有限公司 | A kind of rotor and depolymerizer |
| CN109269290B (en) * | 2018-10-31 | 2024-02-23 | 长沙万荣粉体设备科技有限公司 | Rotor and depolymerization device |
| CN111773943A (en) * | 2020-07-07 | 2020-10-16 | 上海富昶电气有限公司 | Online dispersion auto sucking machine and slurrying system |
| CN113304670A (en) * | 2021-05-27 | 2021-08-27 | 松辰堂科技河北有限公司 | Aerosol generator |
| CN114226021A (en) * | 2022-01-07 | 2022-03-25 | 东莞市康搏智能装备有限公司 | Online grinding dispersion machine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20170531 |