CN206121573U - Mixing arrangement of colloid material - Google Patents
Mixing arrangement of colloid material Download PDFInfo
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- CN206121573U CN206121573U CN201620997157.0U CN201620997157U CN206121573U CN 206121573 U CN206121573 U CN 206121573U CN 201620997157 U CN201620997157 U CN 201620997157U CN 206121573 U CN206121573 U CN 206121573U
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- housing
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- colloid material
- mixing arrangement
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Abstract
The utility model relates to a mixing arrangement of colloid material belongs to chemical industry equipment technical field. In order to solve the present problem uneven and that the continuity is poor of mixing, provide a mixing arrangement of colloid material and include that the cross -section is the circular shape casing, the casing has casing no. 1 and casing no. 2, and casing no. 1 lies in the top of casing no. 2, and is equipped with feed port no. 1 and feed port no. 2 on the casing lateral wall, casing no. 1 is connected with casing no. 2, and the top of casing no. 1 is equipped with the motor, is equipped with the stirring structure in the casing, and the lower extreme internal diameter of casing no. 1 is lighter than the upper end internal diameter of casing no. 2, and the stirring structure includes puddler and the sieve no. 1 that is the tube -shape, and the one end and the motor of puddler link firmly mutually, the other end has the stirring thick liquid, is located the inner chamber of casing no. 2, and sieve no. 1 links firmly with the puddler mutually, and sieve no. 1 is located on the inner chamber of casing no. 2, the diameter of sieve no. 1 is greater than the lower extreme internal diameter of casing no. 1, a plurality of through -holes no. 1 have been offered to circumference on the lateral wall of sieve no. 1. But has the effect of misce bene and serialization production.
Description
Technical field
This utility model is related to a kind of mixing arrangement of colloid material, belongs to technical field of chemical.
Background technology
In field of medicine and chemical technology, most of feed product, through stirring mixed processing, makes mixing using front usual needs
Actual production is put into again after uniform.However, for some high viscosity colloid materials, due to viscosity it is higher, when itself and low viscosity thing
When material is mixed, mixed uniformly effect is extremely difficult to.Therefore, would generally be according to the viscous of material in general mixed process
Degree, the affinity between mixability and each component, mixing speed and temperature control are adjusting, and whipping process is excessively complicated.
At present, the dispersion mixing for high-viscosity material is processed and generally uses two kind equipments, and one is by using common shape
The agitator of formula carries out conventional mixed processing, and the incorporation time needed for its shortcoming is longer, and mixing efficiency is low, and material mixing
Uniformity is also bad;Two is the equipment for using high shear force, but its mechanical energy for producing is larger, and energy consumption is too high.Such as Chinese patent
(Authorization Notice No.:CN204469607U a kind of agitating device suitable for high viscosity colloid) is disclosed, a material pot is set,
Material inlet is provided with the top of the material pot, bottom is provided with material outlet;It is provided with above the material pot and stirs
Motor is mixed, the stirring motor is connected with the upper end for stretching into the shaft inside material pot, and the lower end of the shaft is fixed
In the bottom of material pot;It is fixed with straight leaf agitator and anchor gate stirrer successively from top to bottom on the shaft;
Coil pipe is wound with the outer wall of the material pot, steam inlet and steam (vapor) outlet are provided with the coil pipe.It passes through to arrange straight
Formula stirring slurry and anchor formula stirring slurry can play certain uniform immixture carrying out the effect of Double stirring, but it is still deposited
In the low shortcoming of incorporation time length and efficiency, but also there is a problem of poor continuity, it is impossible to realize quantity-produced effect.
The content of the invention
This utility model is for defect present in above prior art, there is provided a kind of mixing arrangement of colloid material, solution
Problem certainly is how to realize the effect that high-viscosity material uniformly mixes with continuous prodution.
The purpose of this utility model technical scheme is that, a kind of mixing arrangement of colloid material,
Including the rounded housing in section, the housing has housing one and housing two, and the housing one is located at the top of housing two, and
Housing side wall is provided with charging hole one and charging hole two;The housing one is connected with housing two, the housing one
Inner chamber connects with the inner chamber of housing two, and the top of the housing one is provided with motor, and in the housing stirring structure is provided with, and it is special
Levy and be, the bottom diameter of the housing one is less than the upper-end inner diameter of housing two, the stirring structure includes puddler and in cylinder
The sieve plate one of shape, one end and the motor of the puddler are fixedly connected with;The other end of the puddler has stirring slurry, and described stirs
Inner chamber of the slurry positioned at housing two is mixed, the sieve plate one is fixedly connected with puddler, and the sieve plate one is located on the inner chamber of housing two
End;The bottom diameter with diameter greater than housing one of the sieve plate one, on the side wall of the sieve plate one some through holes are circumferentially offered
One.
The mixing arrangement of this colloid material is in order that high viscosity colloid material can uniformly mix;On the one hand, by making shell
The bottom diameter of body one is less than the upper-end inner diameter of housing two, and makes in the lower end with diameter greater than housing one of sieve plate therein
Footpath, enables the material with certain viscosity that guarantee is entered from charging aperture completely by sieve plate one, then is taken to by motor and stir
When mixing bar rotation, the quick rotation of sieve plate one is made, in the presence of having centrifugal force and shearing force, so that the side that material passes through sieve plate one
Wall tapping carries out entering back into after dispersion discharge in housing two, by the shearing force of the high speed of sieve plate one, is discharging colloid material
During realize the effect of quick mixing, realization is completely dispersed the efficiency of mixing;Meanwhile, the stirring slurry of lower section can also be to Jing
The material crossed after the dispersion mixing of sieve plate one is processed carries out secondary stirring mixing, so as to equivalent to reaching dual stirring and dispersion is mixed
The efficiency of conjunction.On the other hand, this mixing arrangement can directly carry out next process after integrally mixing completely, with continuous metaplasia
The effect of product.
In the mixing arrangement of above-mentioned colloid material, the through hole one is equally arranged in strip, and the through hole one
Row.Purpose is, in order to realize the effect of rapid dispersion and mixing, to enable material mixing evenly and improve mixing efficiency
Effect.
In the mixing arrangement of above-mentioned colloid material, used as another embodiment, the through hole one is rounded, and described
Through hole one is uniformly distributed on the side wall of sieve plate one.Equally, the effect of rapid dispersion and mixing can be realized, makes have mixing equal
Uniform efficient advantage.
In the mixing arrangement of above-mentioned colloid material, the lower end exit of the housing two is provided with the filter plate of flat, institute
State and open up on filter plate some through holes two, the filter plate is fixedly connected with housing two, and the edge of the filter plate is interior with housing two
Wall is brought into close contact.Purpose makes in order that mixed colloid material carries out disperseing decomposite process again, makes realization evenly
Mixed effect, equivalent to the advantage for playing triple mixing.
In the mixing arrangement of above-mentioned colloid material, preferably, the upper end aperture of each through hole two is less than through hole two
Lower end aperture.By way of using reducing, it is more beneficial for carrying out colloid material dispersion mixing, improves the uniformity of mixing.
In the mixing arrangement of above-mentioned colloid material, also including U-tube, one end and the lower end of housing two of the U-tube
Export department is connected, and the port height of the U-tube other end is located at the height between sieve plate one and stirring slurry.It is U-shaped by making
The port height of pipe is located at the height between sieve plate one and stirring slurry, ensure that the more preferable submergence of colloid material in housing two
Stirring slurry, equivalent to making stirring slurry completely when not in colloid material, so that ensureing that more fully stirring mixes, and improves mixing
Uniformity;Meanwhile, the colloid material in housing two will not be made the submergence of sieve plate one again, mix the dispersion for not interfering with sieve plate one
Performance is closed, just further ensures the effect of dual mixing, improve the uniformity of mixing.
In sum, this utility model compared with prior art, with advantages below:
1. the mixing arrangement of this colloid material, by the way that well-mixed work can be played to colloid material using sieve plate one
With, and the stirring mixing with reference to stirring slurry itself to colloid material, dual mixing can be played a part of, make mixing more abundant,
So as to also function to the effect of mix homogeneously;Meanwhile, colloid material can be directly used for next process after mixing, realize serialization
The effect of production.
2. the mixing arrangement of this colloid material can play triple dispersion mixings by arranging filter plate, make mixing more abundant,
So as to reach the effect of mix homogeneously.
3. the mixing arrangement of this colloid material is by arranging U-tube, and makes the height of its port be located at sieve plate one with stirring
Height between slurry, can fully ensure that stirring mixed of the stirring slurry to colloid material, improve the uniformity of mixing.
Description of the drawings
Fig. 1 is the cross section structure diagram of the mixing arrangement of this colloid material.
Fig. 2 is the amplification dimensional structure diagram of the sieve plate one of the mixing arrangement of this colloid material.
Fig. 3 is that the another kind of of the sieve plate one of the mixing arrangement of this colloid material amplifies dimensional structure diagram.
Fig. 4 be the mixing arrangement of this colloid material Fig. 1 in mplifying structure schematic diagram at A.
In figure, 1, housing;11st, housing one;111st, charging aperture one;112nd, charging aperture two;12nd, housing two;2nd, motor;3rd, stir
Mix bar;31st, stirring slurry;4th, sieve plate one;41st, through hole one;5th, filter plate;51st, through hole two;6th, U-tube.
Specific embodiment
Below by specific embodiments and the drawings, the technical solution of the utility model is described in further detail, but
It is that this utility model is not limited to these embodiments.
With reference to shown in Fig. 1-Fig. 4, the mixing arrangement of this colloid material includes the rounded housing 1 in section, and housing 1 has shell
Body 1 and housing 2 12, housing 1 is located at the top of housing 2 12, and the side wall of housing 1 is provided with the He of charging hole 1
Charging hole 2 112;Housing 1 is connected with housing 2 12, and inner chamber and the inner chamber of housing 2 12 of housing 1 connect, shell
The top of body 1 is provided with motor 2, housing 1 and is provided with stirring structure, and the bottom diameter of housing 1 is upper less than housing 2 12
End internal diameter, the stirring structure includes puddler 3 and tubular sieve plate 1, and one end and the motor 2 of puddler 3 are fixedly connected with;Stir
The other end for mixing bar 3 has stirring slurry 31, and stirring slurry 31 is located at the inner chamber of housing 2 12, and sieve plate 1 is mutually solid with puddler 3
Connect, and sieve plate 1 is located at the inner chamber upper end of housing 2 12;The bottom diameter with diameter greater than housing 1 of sieve plate 1, the sieve
Some through holes 1 are circumferentially offered on the side wall of plate 1.Housing 1 above is connected preferably by method with housing 2 12
Orchid is attached, and is easy to follow-up dismounting and maintenance.It is of course also possible to pass through to adjust housing 1 with the upper end of housing 2 12
Bore, makes to carry out tight fit connection by the way of socket;Motor therein 2 can adopt common motor, but examine
The viscosity for considering colloid material is different, therefore, preferably with the motor 2 of frequency conversion, be conducive to turning when more easily adjusting stirring
Speed;Stirring slurry therein 31 can adopt the structure of multi-form, such as using the stirring slurry 31 that anchor frame or SANYE are pusher.Separately
Outward, sieve plate 1 is fixedly connected with puddler 3, can be fixedly connected with both by way of welding.Certainly, the top of housing 1
Other parts, such as pressure gauge can also be installed according to actual needs.
In particular, the through hole 1 wherein on the side wall of sieve plate 1 is equally arranged in strip, and through hole 1
Row.Used as another embodiment, through hole 1 is rounded, and through hole 1 is uniformly distributed on the side wall of sieve plate 1, equal energy
Preferable dispersion mixing is enough realized, mixing is made evenly.
Further, the lower end exit for making housing 2 12 is provided with the filter plate 5 of flat, opens up some on filter plate 5
Through hole 2 51, filter plate 5 is fixedly connected with housing 2 12, and the edge of filter plate 5 is brought into close contact with the inwall of housing 2 12.Filter plate 5 with
Housing 2 12 can be connected by friction tight mode, it is also possible to make what filter plate 5 and housing 2 12 were fixedly connected with by bolt
Mode.It is preferred that, the upper end aperture of each through hole 2 51 is made less than the lower end aperture of through hole 2 51.The size in aperture can be with root
Viscosity according to colloid mixture material is different, carries out suitable adjustment.The mixing arrangement of this colloid material can also be made includes U
Type pipe 6, one end of U-tube 6 is connected with the export department of the lower end of housing 2 12, and the port height of the other end of U-tube 6 is located at sieve plate
Height between one 4 and stirring slurry 31.Wherein, one end of U-tube 6 can pass through flange phase with the export department of the lower end of housing 2 12
Connection, convenient detachable and installation, also helps the installation and maintenance of filter plate.
When in use, open the motor 2 of the mixing arrangement of this colloid material make stirring stirring structure rotate, also with regard to when it is suitable
In making motor 2 drive puddler 3 to rotate, rotating speed can be adjusted correspondingly according to the difference of viscosity, then, then by screw rod
Feeder quantitatively sends into high viscosity colloid material in housing 1 from charging aperture 1, meanwhile, will be another kind of relative low viscous
Degree colloid material from charging aperture 2 112, simultaneously send in housing 1 by timing, and specific flow can be by arranging flow sensing
Device is controlled, then makes two kinds of colloids that housing 2 12 is entered after the high-speed rotation dispersion mixing of sieve plate 1, then makes colloid material
Carry out secondary mixing under the stirring action of stirring slurry 31 again, flow through filter plate 5, finally, pass through and entered down after U-tube 6
One procedure is directly placed in material reception tank.
Specific embodiment described in this utility model is only explanation for example to this utility model spirit.This practicality is new
Type person of ordinary skill in the field can make various modifications to described specific embodiment or supplement or adopt
Similar mode is substituted, but without departing from spirit of the present utility model or surmounts model defined in appended claims
Enclose.
Although some specific embodiments have been made a detailed description and have been cited to this utility model, to this area
For those of skill in the art, as long as it is obvious that can make various changes without departing from the spirit and scope of the present invention or correct.
Claims (6)
1. a kind of mixing arrangement of colloid material, including the housing (1) that section is rounded, the housing (1) is with housing one
(11) and housing two (12), the housing one (11) sets on the top of housing two (12), and the side wall of the housing one (11)
There are charging hole one (111) and charging hole two (112);The housing one (11) is connected with housing two (12), the housing one
(11) inner chamber connects with the inner chamber of housing two (12), and motor (2), the housing are provided with the top of the housing one (11)
(1) it is provided with stirring structure in, it is characterised in that the bottom diameter of the housing one (11) is less than in the upper end of housing two (12)
Footpath, the stirring structure includes puddler (3) and tubular sieve plate one (4), one end and the motor (2) of the puddler (3)
It is fixedly connected with;The other end of the puddler (3) has stirring slurry (31), and the stirring slurry (31) positioned at the interior of housing two (12)
Chamber, the sieve plate one (4) is fixedly connected with puddler (3), and the sieve plate one (4) is positioned at the inner chamber upper end of housing two (12);Institute
The bottom diameter with diameter greater than housing one (11) of sieve plate one (4) is stated, is circumferentially offered on the side wall of the sieve plate one (4) some
Through hole one (41).
2. the mixing arrangement of colloid material according to claim 1, it is characterised in that the through hole one (41) in strip,
And through hole one (41) is equally arranged.
3. the mixing arrangement of colloid material according to claim 1, it is characterised in that the through hole one (41) is rounded, and
Through hole one (41) is uniformly distributed on the side wall of sieve plate one (4).
4. according to claim 1 or 2 or 3 colloid material mixing arrangement, it is characterised in that under the housing two (12)
End exit is provided with the filter plate (5) of flat, and some through holes two (51), the filter plate (5) and shell are opened up on the filter plate (5)
Body two (12) is fixedly connected with, and the edge of the filter plate (5) is brought into close contact with the inwall of housing two (12).
5. the mixing arrangement of colloid material according to claim 4, it is characterised in that the upper end aperture of each through hole two (51)
Less than the lower end aperture of through hole two (51).
6. the mixing arrangement of colloid material according to claim 1, it is characterised in that also including U-tube (6), the U-tube
(6) one end is connected with the export department of the lower end of housing two (12), and the port height of U-tube (6) other end is located at sieve plate
Height between one (4) and stirring slurry (31).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620997157.0U CN206121573U (en) | 2016-08-30 | 2016-08-30 | Mixing arrangement of colloid material |
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CN201620997157.0U CN206121573U (en) | 2016-08-30 | 2016-08-30 | Mixing arrangement of colloid material |
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CN206121573U true CN206121573U (en) | 2017-04-26 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116987586A (en) * | 2023-07-28 | 2023-11-03 | 安及义实业(上海)有限公司 | Bioreactor and continuous flow reaction system |
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2016
- 2016-08-30 CN CN201620997157.0U patent/CN206121573U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116987586A (en) * | 2023-07-28 | 2023-11-03 | 安及义实业(上海)有限公司 | Bioreactor and continuous flow reaction system |
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