CN209438438U - A kind of intermittent bubbling system of emulsifying device - Google Patents
A kind of intermittent bubbling system of emulsifying device Download PDFInfo
- Publication number
- CN209438438U CN209438438U CN201821597084.1U CN201821597084U CN209438438U CN 209438438 U CN209438438 U CN 209438438U CN 201821597084 U CN201821597084 U CN 201821597084U CN 209438438 U CN209438438 U CN 209438438U
- Authority
- CN
- China
- Prior art keywords
- tank
- leveling
- vacuum defoamation
- leveling vacuum
- vacuum
- 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.)
- Active
Links
Landscapes
- Degasification And Air Bubble Elimination (AREA)
Abstract
The utility model relates to a kind of intermittent bubbling systems of emulsifying device, for the deaeration of material in emulsion tank, including external circulation line, centrifugal pump and leveling vacuum defoaming device；One end of external circulation line is connect as Matter Transfer import with emulsification pot bottom, the other end is exported as Matter Transfer and is connect at the top of emulsion tank, leveling vacuum defoaming device include leveling vacuum defoamation tank and with the tank connected vacuum device of leveling vacuum defoamation, the screen placed in the leveling vacuum defoamation tank equipped with multiple-layer horizontal, centrifugal pump and leveling vacuum defoamation tank are sequentially arranged along flow direction of material in outer circulating tube road.Compared with prior art, the utility model carries out deaeration twice to material by centrifugal pump and leveling vacuum defoamation tank, solves the problems, such as that the bubble of emulsification pot bottom not can be removed.
Description
Technical field
The utility model relates to the deaeration technical fields of emulsifying device, more particularly, to a kind of intermittent deaeration of emulsifying device
System.
Background technique
The problem of daily use chemicals industry product, bubble is the difficult point of technology, and existing technology is concentrated mainly on whole tank object
Material is completed by the process of vacuum defoamation, and efficiency is very low, and upper layer bubble can be imported bottom (in emulsion tank by the process stirred
Material situation may refer to Fig. 1), it more difficult to carry out the processing of deaeration.And during whole tank material deaeration, bottoms material
The removing for the bubble being had is to be most difficult to and time-consuming maximum de-aeration.
Utility model content
The purpose of this utility model is exactly to provide a kind of emulsifying device to overcome the problems of the above-mentioned prior art
Intermittent bubbling system.
The purpose of this utility model can be achieved through the following technical solutions:
A kind of intermittent bubbling system of emulsifying device, for the deaeration of material in emulsion tank, including external circulation line, centrifugation
Pump and leveling vacuum defoaming device；
One end of the external circulation line is connect as Matter Transfer import with emulsification pot bottom, and the other end is as material
It is connect at the top of loop exit and emulsion tank,
The leveling vacuum defoaming device include leveling vacuum defoamation tank and with the tank connected pumping of leveling vacuum defoamation
Vacuum mechanism, the interior screen placed equipped with multiple-layer horizontal of the leveling vacuum defoamation tank,
The centrifugal pump and leveling vacuum defoamation tank is sequentially arranged along flow direction of material in outer circulating tube road.
Preferably, the leveling vacuum defoamation tank is flat tank body.It is flat to refer to tank body height much smaller than tank body
Cross sectional dimensions.
Preferably, the flat tank body is flat rectangular shape tank body or round flat tank body.
Preferably, the leveling vacuum defoamation tank has material inlet and material outlet, the material inlet and object
Material outlet is relatively arranged on the side wall of leveling vacuum defoamation tank, and material outlet is located at the side bottom of leveling vacuum defoamation tank
Portion.
Preferably, the screen has the hollow slots of multiple parallel long strip types.
Preferably, which further includes reflux line, and the reflux line is vertically arranged in emulsion tank, top and outer
The Matter Transfer of circulation line exports connection, and bottom end is bent to emulsion tank inner sidewall.
Preferably, the vacuum device is water-ring vacuum pump.
The working principle of the utility model is:
By material from emulsification pot bottom output, an evacuation and centrifugal degassing is carried out by centrifugal pump, and with the power of centrifugal pump,
It is delivered to leveling vacuum defoamation tank, in the leveling vacuum defoamation tank, carries out short time stop, provides vacuum pressure with vacuum pump
Power makes a small amount of Material carry out de-bubble within the shortest time, i.e., secondary deaeration, and is separated by multilayer screen, due to still
Material density is larger, assembles in leveling Debubbling tank lower layer, by the material after deaeration, exports from lower layer, is back to emulsion tank upper layer,
Complete closed loop cycle is formed, is handled repeatedly with this, multiple batches of intermittent deaeration is formed.
The reason of selecting flat tank body is that the liquid level in tank can in this way reduced, in the treatment process of flattening,
It improves a lot for the efficiency of product deaeration, and excessive occupied area is that feasibility is low, so material is carried out
The intermittent processing of deaeration in batches.
Compared with prior art, the utility model has the following beneficial effects:
1. the utility model solves the problems, such as that the bubble of emulsification pot bottom not can be removed.
2. inventory per treatment is reduced, deaeration is easier to by leveling vacuum defoamation tank, it is more efficient.
3. the utility model soap base, gel class difficulty deaeration product treatment on, efficiency improve 20% or more.
4. screening function is increased, by deaeration by the multilayer screen in leveling vacuum defoamation tank (i.e. density is big)
Material carries out sedimentation aggregation, is then refluxed for entering emulsion tank upper layer, has ensured the reliability of material.
5. the deaeration material for flowing back into emulsion tank is guided to emulsification pot sidewall by reflux line, be allowed to along
Side wall slowly flows down, and avoids in reflux course and causes to blister again since material directly falls.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the schematic top plan view of the screen of the utility model；
In figure, 1 is emulsion tank, and 11 be agitating paddle, and 2 be external circulation line, and 21 be Matter Transfer import, and 22 be Matter Transfer
Outlet, 3 be centrifugal pump, and 4 be leveling vacuum defoamation tank, and 41 be screen, and 411 be hollow slots, and 42 be material inlet, and 43 go out for material
Mouthful, 5 be reflux line.
Specific embodiment
The utility model is described in detail in the following with reference to the drawings and specific embodiments.
Embodiment 1
A kind of intermittent bubbling system of emulsifying device, as shown in Figure 1, the deaeration for material in emulsion tank 1, including follow outside
Endless tube road 2, centrifugal pump 3 and leveling vacuum defoaming device, wherein；
One end of external circulation line 2 is connect as Matter Transfer import 21 with 1 bottom of emulsion tank, and the other end is followed as material
Ring outlet 22 with connected at the top of emulsion tank 1,
Leveling vacuum defoaming device includes leveling vacuum defoamation tank 4 and vacuumizes with what leveling vacuum defoamation tank 4 was connect
Mechanism, the interior screen 41 placed equipped with multiple-layer horizontal of leveling vacuum defoamation tank 4,
Centrifugal pump 3 and leveling vacuum defoamation tank 4 are sequentially arranged along flow direction of material on external circulation line 2.
Leveling vacuum defoamation tank 4 in the present embodiment is flat tank body.Flat tank body can be flat rectangular shape tank
Body or round flat tank body.Round flat tank body is selected in the present embodiment, bottom surface is circle, and height is much smaller than diameter.
Top of the tank designs top in the arc-shaped, in favor of the evolution of gas.The center of top of tank body is equipped with gas vent, is used for and pumping
Vacuum mechanism (not shown) connects, and the vacuum device in the present embodiment is water-ring vacuum pump, also can choose other
Vacuum generating device.
Leveling vacuum defoamation tank 4 has material inlet 42 and material outlet 43, and material inlet 42 and material outlet 43 are opposite
It is set on the side wall of leveling vacuum defoamation tank 4, and material outlet 43 is located at the side bottom of leveling vacuum defoamation tank 4.Grid
Plate 41 has the hollow slots 411 of multiple parallel long strip types, as shown in Figure 2.
When emulsion tank 1 works, material is stirred by agitating paddle 11, and upper layer bubble can be imported bottom by the process of stirring,
Conventional vaccum-pumping equipment is caused to be difficult this part bubble removal.The present embodiment exports material from 1 bottom of emulsion tank, passes through
Centrifugal pump 3 carries out an evacuation and centrifugal degassing, and with the power of centrifugal pump 3, is delivered to leveling vacuum defoamation tank 4, true in the leveling
In empty Debubbling tank 4, short time stop is carried out, vacuum pressure is provided with vacuum pump, carries out a small amount of Material within the shortest time
De-bubble, i.e., secondary deaeration, and separated by multilayer screen 41, since still material density is larger, in leveling vacuum defoamation tank 4
Material after deaeration is exported from lower layer, is back to 1 upper layer of emulsion tank, forms complete closed loop cycle by lower layer's aggregation, anti-with this
Multiple processing forms multiple batches of intermittent deaeration.The reason of selecting flat tank body is that the liquid level in tank can in this way reduced,
In the treatment process of flattening, improve a lot for the efficiency of product deaeration, and excessive occupied area is feasibility
Low, it is handled so material is carried out intermittent deaeration in batches.
In the present embodiment, which further includes reflux line 5, and reflux line 5 is vertically arranged in emulsion tank 1, top with
22 connection of Matter Transfer outlet of external circulation line 2, bottom end is bent to 1 inner sidewall of emulsion tank.By reflux line, will flow back into
Enter emulsion tank deaeration material guide to emulsification pot sidewall on, be allowed to slowly flow down along side wall, avoid in reflux course by
It directly falls in material and causes to blister again.
The above-mentioned description to embodiment be intended to facilitate those of ordinary skill in the art to understand and use it is practical new
Type.Person skilled in the art obviously easily can make various modifications to these embodiments, and described herein
General Principle is applied in other embodiments without having to go through creative labor.Therefore, the utility model is not limited to above-mentioned reality
Example is applied, those skilled in the art's announcement according to the present utility model does not depart from the improvement and repair that the utility model scope is made
Changing should all be within the protection scope of the utility model.
Claims (7)
1. a kind of intermittent bubbling system of emulsifying device, the deaeration for material in emulsion tank (1), which is characterized in that including outer
Circulation line (2), centrifugal pump (3) and leveling vacuum defoaming device；
One end of the external circulation line (2) is connect as Matter Transfer import (21) with emulsion tank (1) bottom, and the other end is made
It exports for Matter Transfer and is connect at the top of (22) and emulsion tank (1),
The leveling vacuum defoaming device includes leveling vacuum defoamation tank (4) and connect with leveling vacuum defoamation tank (4)
Vacuum device, the interior screen (41) placed equipped with multiple-layer horizontal of the leveling vacuum defoamation tank (4),
The centrifugal pump (3) and leveling vacuum defoamation tank (4) is sequentially arranged along flow direction of material on external circulation line (2).
2. the intermittent bubbling system of a kind of emulsifying device according to claim 1, which is characterized in that the leveling vacuum
Debubbling tank (4) is flat tank body.
3. the intermittent bubbling system of a kind of emulsifying device according to claim 2, which is characterized in that the flat tank
Body is flat rectangular shape tank body or round flat tank body.
4. the intermittent bubbling system of a kind of emulsifying device according to claim 2, which is characterized in that the leveling vacuum
Debubbling tank (4) has material inlet (42) and material outlet (43), and the material inlet (42) and material outlet (43) are opposite
It is set on the side wall of leveling vacuum defoamation tank (4), and material outlet (43) is located at the side bottom of leveling vacuum defoamation tank (4)
Portion.
5. the intermittent bubbling system of a kind of emulsifying device according to claim 1, which is characterized in that the screen (41)
Hollow slots (411) with multiple parallel long strip types.
6. the intermittent bubbling system of a kind of emulsifying device according to claim 1, which is characterized in that the system further includes back
Flow tube road (5), the reflux line (5) are vertically arranged in emulsion tank (1), and the material on top and external circulation line (2) follows
Ring exports (22) connection, and bottom end is bent to emulsion tank (1) inner sidewall.
7. the intermittent bubbling system of a kind of emulsifying device according to claim 1, which is characterized in that the evacuator
Structure is water-ring vacuum pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821597084.1U CN209438438U (en) | 2018-09-29 | 2018-09-29 | A kind of intermittent bubbling system of emulsifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821597084.1U CN209438438U (en) | 2018-09-29 | 2018-09-29 | A kind of intermittent bubbling system of emulsifying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209438438U true CN209438438U (en) | 2019-09-27 |
Family
ID=68009379
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821597084.1U Active CN209438438U (en) | 2018-09-29 | 2018-09-29 | A kind of intermittent bubbling system of emulsifying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209438438U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111357827A (en) * | 2020-03-31 | 2020-07-03 | 无锡赫普轻工设备技术有限公司 | Novel online egg and bean curd production integrated equipment system |
| CN114733232A (en) * | 2022-03-24 | 2022-07-12 | 济南天诺液压气动设备有限公司 | Vacuum continuous defoaming device |
-
2018
- 2018-09-29 CN CN201821597084.1U patent/CN209438438U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111357827A (en) * | 2020-03-31 | 2020-07-03 | 无锡赫普轻工设备技术有限公司 | Novel online egg and bean curd production integrated equipment system |
| CN114733232A (en) * | 2022-03-24 | 2022-07-12 | 济南天诺液压气动设备有限公司 | Vacuum continuous defoaming device |
| CN114733232B (en) * | 2022-03-24 | 2024-03-19 | 济南天诺液压气动设备有限公司 | Vacuum continuous defoaming device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN209438438U (en) | A kind of intermittent bubbling system of emulsifying device | |
| CN208786384U (en) | Reaction kettle with anti-function of foaming | |
| JP2001513018A (en) | Tank stirrer with air bubbler | |
| CN108939617A (en) | A kind of liquid phase separating device and its application method | |
| CN107029574A (en) | Medicament jar | |
| CN210078914U (en) | Gallium indium tin liquid alloy bubble removing device | |
| CN208770515U (en) | A kind of storage blood blood filtration device | |
| CN201454161U (en) | Oil-water separation system | |
| EP0033407B1 (en) | A device for creating circulation within a body of liquid, and an apparatus for treating sewage or the like in a body of liquid | |
| RU184794U1 (en) | OIL PIT FOR OIL-FIELD PREPARATION OF OIL | |
| CN217781084U (en) | Jasmine essential oil extraction device | |
| CN211960493U (en) | Degassing device for milk processing | |
| JPH0938407A (en) | Mixing and deforming device of multistage liquid flowing plate type | |
| US5364784A (en) | Method for delivering oxygen to a cell culture medium | |
| CN217077740U (en) | Novel clarification equipment is eluriated in succession to high efficiency | |
| CN213475473U (en) | Waste liquid separation device | |
| JPH11514925A (en) | Complete reactor for liquid purification | |
| CN208361930U (en) | A kind of air-lift device | |
| CN219752108U (en) | Compact oil sludge separation system | |
| CN212308931U (en) | Coating vacuum defoaming device | |
| CN207342256U (en) | A kind of plasticizer oily-water seperating equipment | |
| CN209828288U (en) | Can concentrate enrichment facility of private customized traditional chinese medicine | |
| CN218058642U (en) | Novel oil-based mud is handled device | |
| CN207877352U (en) | It is a kind of to rush version water purification installation | |
| CN214168078U (en) | Extraction tank and extraction system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |