Heat cure furane resins compare production system surely
Technical field
It is fixed than production system that the utility model is related to resins synthesis production fields more particularly to a kind of heat cure furane resins
System.
Background technology
Furane resins refer to with furan nucleus furfuryl alcohol and furfural make raw material production resinae general name, have protrude
Corrosion resistance, heat resistance and its raw material sources extensively, simple production process the advantages that, cause the attention of people.It is wide at present
It is general to be applied to metallurgical casting industry, in moulding, such as the production of many auto parts machineries, water heating bathroom, tire-mold, using
After furan resin-sand art shapes, good economic effect is obtained.And mixing arrangement is often required to use when furane resins production,
It after need to proportionally tank body being added in different material when use, then is mixed by agitating device, but current mixture manufacturing
Apparatus structure is simple, and raw material often concentrates a certain region dropped down onto in tank body after being added, and needing long agitation just can make it mixed
It closes uniform.And single stirrer paddle is often set in tank body, when use, easily causes rotating vortex, influences mixing effect.
Chinese Patent Application No. is:201720224085.0 disclosed a kind of furane resins production reaction kettle, packet
It includes tank body, agitating shaft is set in tank body, the riser being from top to bottom sequentially distributed, the first agitating device, the are provided on agitating shaft
Two agitating devices are provided with charge door and filling opening on tank body, and charge door and filling opening bottom are provided with and extend to tank inner chamber
The inclination supporting plate at middle part, riser setting are tilting below supporting plate, and the first agitating device includes the upright bar being arranged in bottom of the riser, is stood
Bar is provided with screw blade by several connecting plates and stirring axis connection in upright bar, the second agitating device stirs for anchor formula
Device, the first agitating device extend in the cavity that the second agitating device surrounds;It is both provided on riser, connecting plate and inclination supporting plate
Through-hole.
Above-mentioned technical proposal carries out material dispersion by portrait and the first agitating device, then through the first agitating device and second
Agitating device carries out diversified stirring to mixture, to avoid the appearance of vortex;However its carry out material dispersion be will be a large amount of
Different material it is random break up, to be difficult to ensure the various pieces ratio uniform of mixture, therefore it is in whipping process
In also need longer mixing time to realize being uniformly mixed for material, while its to be mixed into time longer discontinuity mixed
It closes, therefore, above-mentioned technical proposal production efficiency is low, and proportioning is coarse.
Utility model content
The purpose of this utility model is in view of the deficiencies of the prior art, to provide a kind of heat cure furane resins Ding Bisheng
Production system, while being determined respectively than output with auxiliary material by major ingredient output precision and auxiliary material feeder assembly progress major ingredient, by multiple
Stirring diverging portion is mixed in a manner of coating with auxiliary material after carrying out major ingredient stirring output, solves low production efficiency of the existing technology
Under, match coarse technical problem.
In order to solve the above technical problems, the utility model provides the following technical solutions:
Heat cure furane resins are fixed than production system, including mixing bunker and actuating unit, further include:
Mixed organization, the mixed organization are set to the inside of the mixing bunker comprising major ingredient output precision and auxiliary
Expect feeder assembly, the major ingredient output precision includes major ingredient buffering chamber, multiple pressurization parts for being set on the major ingredient buffering chamber and
It is respectively arranged at the stirring diverging portion of the pressurization part side;
It is dissipated after the pressurized portion's supercharging of major ingredient inside the major ingredient buffering chamber, then after the stirring of agitated diverging portion defeated
Go out, the major ingredient unit of multiple umbrellas is formed in the outside of the major ingredient buffering chamber;Auxiliary material is set in the auxiliary material feeder assembly
On multiple jet ports spray after, into the major ingredient unit.
Wherein, the major ingredient buffering chamber rotation is arranged and is connected with the actuating unit, and the pressurization part is uniformly fixed
It is set on the inner wall of the major ingredient buffering chamber, while the major ingredient buffering chamber rotation carries out major ingredient stir process, in described
The side of pressurization part forms pressor areas.
Wherein, the stirring diverging portion includes the multiple delivery outlets being uniformly opened on the major ingredient buffering chamber outer circumference surface
And it is rotatably dispose in the agitating paddle in the delivery outlet, the delivery outlet is located in the pressor areas.
In addition, the pressurization part is the arc plate structure being vertically arranged, and its cambered surface extending direction and the master
Expect that the rotation direction of buffering chamber is identical, the agitating paddle is arranged for propeller arrangement.
As an improvement, the major ingredient output precision further includes being fixedly installed in the mixing bunker and the major ingredient buffering chamber
Outer circumference surface seal the baffle that is equipped with, the through-hole with the intermittent communicated setting of the delivery outlet is offered on the baffle, should
Through-hole is correspondingly arranged with the jet port, forms preliminary blending space between the two.
As an improvement, the auxiliary material feeder assembly is coaxially disposed with major ingredient output precision, and the auxiliary material feeder assembly is located at
The outside of major ingredient output precision comprising auxiliary material temporary storing bin and the multiple feedings being rotatably dispose in inside the auxiliary material temporary storing bin
Portion, the feeding portion are driven by the actuating unit and are operated synchronously with the major ingredient buffering chamber, and the jet port is opened in described
On the madial wall of auxiliary material temporary storing bin.
As an improvement, further including the blender being set in the mixing bunker and below the major ingredient output precision
Structure, which includes the compression unit of fixed setting, the catalyst storage silo that is equipped with the compression unit and with the master
The mixing component that material buffering chamber is fixedly connected.
Wherein, the compression unit is horizontally disposed piston dish structure, and the catalyst storage silo is opening up and can
The cylinder barrel structure moved up and down, which, which includes the multiple boss for being set to its bottom, is opened in catalyst deposits
Multiple spouts on warehouse outer circumference surface and the return spring being set between the catalyst storage silo and compression unit, it is described convex
Platform, spout and jet port are located in same perpendicular.
It is arranged in addition, the mixing component is opening up umbrella-shaped structure, outer circumference surface is interior with the mixing bunker
Wall is equipped with, the mixing component include the multiple collecting boards for being arranged on surface, with the boss discontinuous connection setting and
The driving wheel that the catalyst storage silo moves upwards and the blanking port for being opened in its center, the collecting board is pushed to be
Arc panel is arranged and its extending direction is identical as the rotation direction of mixing component.
The beneficial effects of the utility model:
(1) major ingredient buffering chamber is in rotation process in the present invention, by being fixedly installed on its internal multiple pressurization
Output forms the major ingredient unit of umbrella after the stirring of stirring diverging portion after the pressurized of portion's progress major ingredient, and auxiliary material is sprayed through jet port
Enter in mainstream unit after going out, major ingredient is mixed in a manner of coating with auxiliary material;The pressurization part is uniformly fixedly installed on described
On the inner wall of major ingredient buffering chamber, major ingredient buffering chamber uniform rotation forms the pressor areas with constant pressure, is sprayed through delivery outlet
Major ingredient amount it is constant, in conjunction with the auxiliary material feeding portion operated synchronously with major ingredient buffering chamber, form major ingredient and mixed with the fixed ratio of auxiliary material, separately
The outer delivery outlet is circumference respectively with jet port and is correspondingly arranged that therefore, the utility model is formed continuously in operation process
Major ingredient mixed with the fixed ratio of auxiliary material, solve that production efficiency of the existing technology is low, match coarse technical problem.
(2) rabbling mechanism includes the compression unit of fixed setting, is urged with what the compression unit was equipped in the present invention
The mixing component of agent storage silo and umbrella-shaped structure, major ingredient storage silo drives mixing component rotation while rotation, by stirring
Mixing interruption during the driving wheel on component moves in a circle pushes catalyst storage silo to move up, compressed portion and catalysis
The cooperation of agent storage silo mixes quantitative catalyst with certain proportion with the main and supplementary materials mixture in dropping process, meanwhile, by
Mixing component drives mixed material rotation mixing after carrying out mixed material undertaking with rotating manner, is received mixed material by collecting board
It exports after collection, while avoiding material stirring and mixedly appear vortex, the different mixtures material on mixing component is concentrated
Mixing, implementation phase mixing, further increases each Material and article holding frame mixing match uniformity of the utility model;
In conclusion the utility model has many advantages, such as that simple in structure, proportion speed, production efficiency are high.
Description of the drawings
It is required in being described below to embodiment for the clearer technical solution for illustrating the utility model embodiment
The attached drawing used is briefly described, it should be apparent that, drawings discussed below is only some embodiments of the utility model,
For for those of ordinary skill in the art, without creative efforts, it can also obtain according to these attached drawings
Obtain other accompanying drawings.
Fig. 1 is the utility model fault structure schematic diagram;
Fig. 2 is the utility model schematic cross-sectional view;
Fig. 3 is enlarged diagram at A in Fig. 2;
Fig. 4 is B-B direction schematic diagrams in Fig. 2;
Fig. 5 is feeding portion overall structure diagram;
Fig. 6 is feeding portion front view;
Fig. 7 is rabbling mechanism close-up schematic view;
Fig. 8 is mixing component vertical view.
Specific implementation mode
The technical scheme in the embodiment of the utility model is clearly and completely illustrated below in conjunction with the accompanying drawings.
Embodiment one
The embodiments of the present invention are described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning
Same or similar element or element with the same or similar functions are indicated to same or similar label eventually.Below by ginseng
The embodiment for examining attached drawing description is exemplary, it is intended to for explaining the utility model, and should not be understood as to the utility model
Limitation.
As shown in Fig. 1,2,3 and 4, heat cure furane resins are fixed than production system, including mixing bunker 1 and actuating unit 2, also
Including:
Mixed organization 3, the mixed organization 3 are set to the inside of the mixing bunker 1 comprising major ingredient output precision 31 with
And auxiliary material feeder assembly 32, the major ingredient output precision 31 include major ingredient buffering chamber 313, are set on the major ingredient buffering chamber 313
Multiple pressurization parts 311 and be respectively arranged at the stirring diverging portion 312 of 311 side of pressurization part, in major ingredient buffering chamber 313
After multiple pressurization parts 311 of the major ingredient in portion through being uniformly arranged carry out partial Pressure, after agitated diverging portion 312 is tentatively stirred
Diverging output;In the present embodiment, 311 quantity of the pressurization part is three, is only a kind of preferred implementation in the present embodiment
Mode;
After the pressurized portion 311 of major ingredient inside the major ingredient buffering chamber 313 is pressurized, then agitated diverging portion 312 is stirred
Output is dissipated after mixing, and the major ingredient unit 310 of multiple umbrellas is formed in the outside of the major ingredient buffering chamber 313;Auxiliary material be set in
After multiple jet ports 320 on the auxiliary material feeder assembly 32 spray, into the major ingredient unit 310, as a kind of preferred
Embodiment, the jet port 320 is three in same level, and is laid around the axis of major ingredient buffering chamber 313
It sets.
Wherein, as shown in Fig. 1,2 and 4, the rotation of major ingredient buffering chamber 313 is arranged and is connected with the actuating unit 2,
The pressurization part 311 is uniformly fixedly installed on the inner wall of the major ingredient buffering chamber 313, the major ingredient buffering chamber 313 rotate into
While row major ingredient stir process, pressor areas 3111 is formed in the side of the pressurization part 311, the pressurization part 311 is set to
On the inside of the major ingredient buffering chamber 313 and to inner process, the pressurization part 311 be uniformly arranged on major ingredient buffering chamber 311 and
Positioned at same level, major ingredient buffering chamber 3131 rotates, and is rotated by pressurization part 311 and carries out major ingredient mixing.
Wherein, as shown in Figure 1,2 and 3, the stirring diverging portion 312 includes uniformly being opened in the major ingredient buffering chamber 313
Multiple delivery outlets 3121 on outer circumference surface and the agitating paddle 3122 being rotatably dispose in the delivery outlet 3121, the delivery outlet
3121 are located in the pressor areas 3111, are sprayed along delivery outlet 3121 after the major ingredient in pressor areas 3111 is pressurized, by leading
The directed flow driving agitating paddle 3122 of material operates, and sprayed after major ingredient is stirred, into blending space 315 and auxiliary material
Mixing.
In addition, the pressurization part 311 is the arc plate structure being vertically arranged as illustrated in fig. 1 and 2, and its cambered surface is prolonged
It is identical as the rotation direction of the major ingredient buffering chamber 313 to stretch direction, the agitating paddle 3122 is arranged for propeller arrangement;Major ingredient is slow
Storage 313 drives pressure plate 311 to rotate while rotation, is oriented to major ingredient by arc panel, the arc of major ingredient arcuately plate
Downwards movement form pressor areas 3111, flow through delivery outlet 3121 high speed major ingredient stream act on propeller-driven its rotation it is same
When, by the angle setting structure of propeller blade, major ingredient is made to dissipate ejection outward along its surface.
It should be noted that as shown in Fig. 2,3 and 4, major ingredient buffering chamber 313 is in rotation process, by being fixedly installed on it
Output forms the master of umbrella after stirring diverging portion 312 is stirred after the pressurized of the internal progress major ingredient of multiple pressurization parts 311
Material unit 310, auxiliary material enter after the ejection of jet port 320 in mainstream unit 310, and major ingredient is mixed in a manner of coating with auxiliary material
It closes;The pressurization part 311 is uniformly fixedly installed on the inner wall of the major ingredient buffering chamber 313, and major ingredient buffering chamber 313 at the uniform velocity turns
It is dynamic, the pressor areas 3111 with constant pressure is formed, the major ingredient amount sprayed through delivery outlet 3121 is constant, is cached in conjunction with major ingredient
The auxiliary material feeding portion 32 that storehouse 313 operates synchronously forms major ingredient and is mixed with the fixed ratio of auxiliary material, in addition the delivery outlet 3121 and injection
Mouthfuls 320 for circle distribution and are correspondingly arranged, and therefore, the utility model forms determining for continuous major ingredient and auxiliary material in operation process
It than mixing, solves that production efficiency of the existing technology is low, matches coarse technical problem.
Further, as shown in Figures 2 and 3, the major ingredient output precision 31 further includes being fixedly installed in the mixing bunker 1
Seal the baffle 314 being equipped with the outer circumference surface of the major ingredient buffering chamber 313, offered on the baffle 314 with it is described defeated
The through-hole 3141 of 3121 intermittent communicated settings is exported, which is correspondingly arranged with the jet port 320, is formed between the two
Preliminary blending space 315;The baffle 314 is cylindrical tube structure, is sheathed on the outer circumference surface of major ingredient buffering chamber 313, main
Buffering chamber 313 is expected in rotation process, and delivery outlet 3121 and the through-hole 3141 being set on baffle 314 are intermittent communicated, are led
The interruption of material is sprayed, wherein when delivery outlet 3121 is closed state, major ingredient pressurized is carried out by pressurization part 311, so that it is guaranteed that
The intensity of major ingredient and the stability of spray volume are sprayed, while realizing the stability of major ingredient unit 310.
Further, as shown in Fig. 1,2,4,5 and 6, the auxiliary material feeder assembly 32 is coaxially set with major ingredient output precision 31
It sets, and the auxiliary material feeder assembly 32 is located at the outside of major ingredient output precision 31 comprising auxiliary material temporary storing bin 321 and rotation are set
Be placed in multiple feeding portions 322 inside the auxiliary material temporary storing bin 321, the feeding portion 322 driven by the actuating unit 2 and with it is described
Major ingredient buffering chamber 313 operates synchronously, and the jet port 320 is opened on the madial wall of the auxiliary material temporary storing bin 321;In this implementation
In example, the jet port 320 is located at the lower end of auxiliary material temporary storing bin 321 and major ingredient buffering chamber 313, and two with delivery outlet 3121
Person is distributed in a ring, and the feeding portion 322 is the inclined plate structure that both sides are equipped with auxiliary material buffering chamber 321 respectively, is turning
During dynamic, auxiliary material guiding is carried out by inclined plate, auxiliary material is made to be moved downwards along inclined plate, forms higher-pressure region, and between jet port 320
Disconnection is logical, carries out the quantitative output of auxiliary material interruption, major ingredient buffering chamber 313 is rotated synchronously with feeding portion 322, to make major ingredient and auxiliary material
Synchronous spray mixing.
Embodiment two
As illustrated in fig. 1 and 2, wherein identical with embodiment one or corresponding component uses attached drawing corresponding with embodiment one
Label hereafter only describes the distinctive points with embodiment one for simplicity;The difference of the embodiment two and embodiment one exists
In:Further include being set in the mixing bunker 1 and positioned at the rabbling mechanism 4 of 31 lower section of the major ingredient output precision, the blender
Structure 4 includes the compression unit 41 of fixed setting, the catalyst storage silo 42 being equipped with the compression unit 41 and delays with the major ingredient
The mixing component 43 that storage 313 is fixedly connected;In the present embodiment, mixing component 43 is fixedly connected with major ingredient buffering chamber 313, is
Simplified the utility model structure reduces production cost, only a kind of preferred embodiment, mixing component 43 and major ingredient buffering chamber
Connecting shaft between 313 is each passed through compression unit 41 and catalyst storage silo 42.
Wherein, as shown in figs. 2 and 7, the compression unit 41 is horizontally disposed piston dish structure, the catalyst storage silo
42 be cylinder barrel structure opening up and moving up and down, which includes being set to the multiple convex of its bottom
Platform 421, the multiple spouts 422 being opened on 42 outer circumference surface of catalyst storage silo and be set to the catalyst storage silo 42 with
Return spring 423 between compression unit 41, the boss 421, spout 422 and jet port 320 are located in same perpendicular, institute
It states spout 422 to be opened on the outer circumference surface of the catalyst storage silo 42, and is located at lower end, catalyst storage silo 42 is to moving up
In dynamic process, the seal cavity pressure between compression unit 41 increases, and after pressure reaches certain value, catalyst is through spout
422, which spray the mixture formed with major ingredient and auxiliary material, contacts, and realizes the quantitative proportioning of three kinds of materials.
In addition, as shown in FIG. 7 and 8, the mixing component 43 is that opening up umbrella-shaped structure is arranged, outer circumference surface with
The inner wall of the mixing bunker 1 is equipped with, which includes multiple collecting boards 431 and the institute for being arranged on surface
It states the setting of 421 discontinuous connection of boss and the driving wheel 432 that pushes the catalyst storage silo 42 to move upwards and is opened in it
The blanking port 433 of center, the collecting board 431 are the rotation side of arc panel setting and its extending direction and mixing component 43
To identical;43 section of the mixing component is opening up Figure of eight structure, falls within the mixed material of its upper surface along its surface
To center flow, while the circular movement pattern of structure mixing component 43, the mixed material fallen within by under on mixing component 43 pass through
Collecting board 431 is collected after breaing up, and realizes the secondary mixing of mixed material, mixed material is made to flow to center, mixed to improve
Close the mixing uniformity of material;In addition, many places mixed material in mixing bunker 1 concentrates on the centre bit of mixing component 43
It sets, and it is made to be mixed, further increase mixed material and integrally match uniformity.
It should be noted that as shown in Fig. 2,7 and 8, rabbling mechanism 4 includes compression unit 41 and compression of fixed setting
The mixing component 43 for the catalyst storage silo 42 and umbrella-shaped structure that portion 41 is equipped with, major ingredient storage silo 313 is in the same of rotation
When drive mixing component 43 rotate, during being moved in a circle by the driving wheel 432 on mixing component 43 interruption push catalysis
Agent storage silo 42 moves up, the cooperation of compressed portion 41 and catalyst storage silo 42 by quantitative catalyst with certain proportion with
Main and supplementary materials mixture mixing in dropping process, meanwhile, by mixing component 43 with band after rotating manner progress mixed material undertaking
Dynamic mixed material rotation mixing, exports after being collected mixed material by collecting board 431, avoids material stirring and mixedly appear vortex
While, concentrate mixing, implementation phase mixing to further increase this reality in the different mixtures material on mixing component 43
With novel each Material and article holding frame mixing match uniformity.
In the present invention, it is to be understood that:Term "center", " longitudinal direction ", " transverse direction ", " length ", " width ",
" thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside", " up time
The orientation or position relationship of the instructions such as needle ", " counterclockwise " are to be based on the orientation or positional relationship shown in the drawings, merely to just
It is described in description the utility model and simplifying, does not indicate or imply the indicated equipment or specific side that element must have
Position, with specific azimuth configuration and operation, therefore should not be understood as limiting the present invention.
In addition, term " first ", " second " are used for description purposes only, it is not understood to indicate or imply opposite important
Property or implicitly indicate the quantity of indicated technical characteristic.Therefore, define " first ", the feature of " second " can be expressed or
Person implicitly includes one or more this feature.In the description of the utility model, the meaning of " plurality " is two or two
More than a, unless otherwise specifically defined.
The preferable specific implementation mode of the above, only the utility model, but the scope of protection of the utility model is not
It is confined to this, the variation that any one skilled in the art can readily occur under the technical clarification of the utility model
Or replace, while such as being determined than output with auxiliary material by major ingredient output precision and auxiliary material feeder assembly progress major ingredient, stirred by multiple
It mixes diverging portion and carries out the design concept mixed with auxiliary material in a manner of cladding after major ingredient stirring output, should all cover in the utility model
Protection domain within.Therefore, the scope of protection of the utility model should be subject to the scope of protection of the claims.