CN107998992A - A kind of heat cure furane resins are fixed than production system and technique - Google Patents
A kind of heat cure furane resins are fixed than production system and technique Download PDFInfo
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- CN107998992A CN107998992A CN201711270774.6A CN201711270774A CN107998992A CN 107998992 A CN107998992 A CN 107998992A CN 201711270774 A CN201711270774 A CN 201711270774A CN 107998992 A CN107998992 A CN 107998992A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/085—Feeding reactive fluids
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/10—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by stirrers or by rotary drums or rotary receptacles or endless belts
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G14/00—Condensation polymers of aldehydes or ketones with two or more other monomers covered by at least two of the groups C08G8/00 - C08G12/00
- C08G14/02—Condensation polymers of aldehydes or ketones with two or more other monomers covered by at least two of the groups C08G8/00 - C08G12/00 of aldehydes
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Abstract
The present invention relates to chemical production technical field, more particularly to a kind of heat cure furane resins are fixed than production system and technique, one of which heat cure furane resins compare production system surely, including actuating unit, cache mechanism and output mechanism, cache mechanism includes major ingredient buffering chamber, auxiliary material temporarily stores up and blending space；During the work time, screening assembly is driven to be moved with catalyst output precision while actuating unit driving compression assembly movement, major ingredient is flowed out through output section and the introduction part being arranged on the temporary warehouse of auxiliary material respectively with auxiliary material, liquid fluidization tower that is opposite and being staggered up and down is formed respectively in blending space, and mixed liquor contacts mixing in dropping process with through catalyst derived from catalyst output precision；While quantitatively output by compression assembly progress auxiliary material interruption, driving screening assembly and catalyst output precision, realize that major ingredient is determined ratio with catalyst after being mixed with auxiliary material and mixed, and solve the problems, such as to match coarse, mixing inequality between each raw material existing in the prior art.
Description
Technical field
The present invention relates to chemical production technical field, more particularly to a kind of heat cure furane resins are fixed than production system and work
Skill.
Background technology
Furane resins refer to the general name for making the resinae of raw material production with the furfuryl alcohol with furan nucleus and furfural, have and 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 during furane resins production,
After different material proportionally need to being added tank body during use, then it is mixed by agitating device, but current mixture manufacturing
Apparatus structure is simple, and a certain region dropped down onto in tank body is often concentrated after adding for raw material, it is necessary to which long agitation can just make it mixed
Uniform, existing mixing arrangement is closed, there is stirring inequality, and causes resin each several part proportioning uneven, so as to influence resin quality.
Chinese Patent Application No. is：201720221468.2 a kind of disclosed novel furan production of resins reaction kettle,
Stirring frame includes arc rabble and the vertical rabble for being connected to arc rabble both ends in the reaction kettle, in vertical rabble
Between weld two layers of oblique paddle agitating paddle, oblique paddle agitating paddle includes two panels blade respectively, there is that several are small on every blade
Hole, the aperture gross area are the 50% of whole blade area；The centre position of oblique paddle agitating paddle and arc rabble is equipped with peace
Hole is filled, oblique paddle agitating paddle is set on the outside of agitating shaft by mounting hole, and arc rabble is set in agitating shaft by mounting hole
Bottom, the bottom of arc rabble is concordant with reaction kettle autoclave body bottom.
While above-mentioned technical proposal carries out mixed liquor stirring by stirring frame, pass through the axial direction of oblique paddle agitating paddle generation
Power carries out the exchange up and down of mixed liquor, so as to improve the mixing uniformity of mixed liquor；It is well known that the mixing for mixture is equal
Even property, its stirring can only improve its mixing uniformity, and more dosages with the mixing time to mixture, needed for it
Mixing time is longer, therefore the prior art is more promotes the lifting of yield with when shorter incorporation time with more coarse,
Therefore exist and match that coarse, mixing is uneven, caused by furane resins poor quality the problem of.
The content of the invention
The purpose of the present invention is in view of the deficiencies of the prior art, there is provided a kind of heat cure furane resins are fixed than production system
System and technique, while quantitatively output by compression assembly progress auxiliary material interruption, driving screening assembly and catalyst output precision,
Realize that major ingredient is determined ratio with catalyst after being mixed with auxiliary material and mixed, solve to match between each raw material existing in the prior art it is coarse,
The problem of mixing is uneven.
In order to solve the above technical problems, the present invention provides following technical solution：
A kind of heat cure furane resins are fixed than production system, including actuating unit, including：
Cache mechanism, the cache mechanism include major ingredient buffering chamber, auxiliary material temporarily store up and be arranged at it is mixed between both
Close space；
Output mechanism, the output machine include compression assembly, are connected with the compression assembly and are equipped with the master
Expect the screening assembly on buffering chamber and the catalyst output precision being connected with the screening assembly；
During the work time, screening assembly and catalyst output group are driven while the movement of actuating unit driving compression assembly
Part moves, and makes to be opened in the output section on screening assembly with being connected inside major ingredient buffering chamber, major ingredient is with auxiliary material respectively through output section
With the introduction part outflow being arranged on the temporary warehouse of auxiliary material, liquid fluidization tower that is opposite and being staggered up and down is formed respectively in blending space,
In the mixed liquor formed below of the blending space, the mixed liquor in dropping process with through being urged derived from catalyst output precision
Agent contact mixing.
Wherein, the compression assembly includes the first compression unit being arranged in the temporary warehouse of the auxiliary material and is arranged at described mixed
The second compression unit in space is closed, first compression unit passes through in distribution up and down and between the two connecting rod phase with the second compression unit
Connection, second compression unit are located at the outside of the catalyst output precision.
In addition, first compression unit and the second compression unit be section for splayed and opening up circular slanting it is hardened
Structure is set, and the outer circumference surface of both contacts setting, first pressure with the temporary warehouse of auxiliary material with the lateral wall of mixing sky respectively
Contracting portion and the second compression unit form the first compressional zone and the second compressional zone respectively during moving down, under it.
As an improvement, the temporary warehouse of auxiliary material is coaxially disposed with the major ingredient buffering chamber, it includes surge bunker and positioned at this
Below the surge bunker and compression bin that communicates therewith, first compressional zone is located in the compression bin, and the introduction part is arranged at
The compression bin, it is interior and be connected with first compressional zone.
As an improvement, the catalyst output precision includes being arranged at the catalyst caching below the major ingredient buffering chamber
Room, be opened in the multiple catalyst flow jeting ports being uniformly arranged on the outdoor periphery of catalyst caching and around its axis, the catalysis
Agent flow jeting port and the intermittent communicated setting of the through hole being fixedly installed on below major ingredient buffering chamber, the catalyst flow jeting port, introduction part
And output section is in same perpendicular.
As an improvement, the screening assembly is set for annular tube structure, and its outer circumference surface with the major ingredient buffering chamber
Sealing is equipped with, which is fixedly connected with catalyst caching room, and the output section is included around screening assembly axis
Line is uniformly opened in multiple head piece groups on its periphery.
Specifically, the output section includes the multiple head piece groups being uniformly opened in around screening assembly axis on its periphery,
The head piece group is set for vertically uniform intervals and multiple recirculation holes with being connected inside the major ingredient buffering chamber, described to lead
Entering portion includes some auxiliary feed outlets being correspondingly arranged with the recirculation hole.
As an improvement, the output mechanism further includes the major ingredient mixing group being rotatably dispose in inside the major ingredient buffering chamber
Part, the major ingredient electric hybrid module include the first mixing part and the second mixing part below first mixing part, and described first stirs
Portion to be mixed to set for canted coil paddle structure, second mixing part includes the stirring rod that some axis around it are uniformly arranged, and
In the setting that is staggered up and down between adjacent stirring rod.
As an improvement, the major ingredient buffering chamber includes mixing bunker setting up and down and output storehouse, first mixing part with
Second mixing part respectively positioned at the mixing bunker with output storehouse in, the output storehouse include be opened on its outer circumference surface and with it is described
Multiple major ingredient delivery outlets of the intermittent communicated setting of recirculation hole.
A kind of heat cure furane resins are fixed than production technology, comprise the following steps：
(a) major ingredient mixing portion, the major ingredient synthesized by various materials enter in mixing bunker, by the first mixing part to revolve
After the mode of turning is broken up, pressurized delivered is driven through the second mixing part and is exported in a manner of rotating centrifugal through recirculation hole to storehouse is exported；
(b) auxiliary material output par, c, the auxiliary material in compression bin move down the first formed pressure through the first compression unit
Contracting area acts on, and auxiliary material is sprayed along auxiliary feed outlet；
(c) main materials and auxiliary materials mixing portion, the major ingredient and auxiliary material exported respectively through step (a) and step (b), in blending space
Interior to be mixed to form mixed liquor in a manner of upper and lower superposition staggeredly, which contacts mixing in dropping process with weighed catalyst；
(d) catalyst output par, c, drives catalyst caching room to move up, with pressure while compression assembly moves up
Contracting mode sprays catalyst of the inside, is contacted with the mixed liquor formed through step (c)；
(e) secondary mixing portion, the catalyst action sprayed through catalyst caching room fall within the after main materials and auxiliary materials mixed liquor
On two compression units, secondary mixing is carried out to mixed solution with upper and lower motion mode by the second compression unit.
Beneficial effects of the present invention：
(1) in the present invention output mechanism include being arranged at compression assembly inside the temporary warehouse of the auxiliary material, with the compression
Component is connected and is equipped with the screening assembly on the major ingredient buffering chamber and the catalysis being connected with the screening assembly
Agent output precision；While driving mechanism drives compression assembly up and down motion, the movement of catalyst output precision is driven；Compression assembly
While moving downward the first compressional zone formed by the first compression unit and export auxiliary material of the inside through introduction part, it is in
Major ingredient in major ingredient buffering chamber is opposite with auxiliary material through output section and is mixed with upper and lower stacked system, so as to improve major ingredient and auxiliary material
Proportion speed and mixing uniformity, in the upward motion process of compression assembly, drive catalyst output precision to move upwards, with master
Expect that the piston method of operation is formed on buffering chamber bottom, to catalyst of the inside while catalyst caching room is moved upwards
Compression makes its ejection, and mixing is contacted with the major ingredient in its outside dropping process, auxiliary material mixed liquor, the major ingredient of formation stages, auxiliary
Material and catalyst are determined than mixing, and solution is existing in the prior art because matching coarse, mixing inequality between each auxiliary material, caused by
The problem of furane resins poor quality；
(2) the first compression unit and the second compression unit are that opening up circular slanting harden structure is set in the present invention, the
While it compresses its bottom auxiliary material of going out during first compression portion moves down, its outer circumference surface is to the temporary warehouse of auxiliary material
Lateral wall carries out blade coating formula cleaning, avoids the bonding of auxiliary material and bulkhead and influences normally to produce；Other second compression unit is in mixed
Close in space and positioned at the outside of catalyst caching room, and positioned at the lower section of the first compression unit, institute's shape after major ingredient is mixed with auxiliary material
Into mixed liquor wander during, the catalyst ejector sprayed by catalyst flow jeting port is fallen within the second compression unit, then by
The ramp structure of two compression units, carries out the unhurried current of mixed liquor, is formed while mixed liquor is wandered along the second compression unit upper surface
Lamelliform liquid structure, realizes the mixing again of mixed liquor, while by the mixed liquor collection of the diverse location on the second compression unit
Middle mixing, further improves the mixing uniformity of mixed liquor；In addition, while the second compression unit moves downward, it is in the bottom
Mixed solution through its ramp effect, mixed liquor in the bottom is extruded to the periphery, its upward motion mode of structure, again
The mixing of solution levels is carried out to mixed solution, improves its mixing uniformity；
(3) major ingredient electric hybrid module includes the first mixing part and second stirring below first mixing part in the present invention
Mix portion, the first mixing part is that canted coil paddle structure is set, since major ingredient is mixed to form for various materials, for improve its material it
Between mixing uniformity, during major ingredient is delivered to major ingredient buffering chamber, major ingredient is fallen within the first mixing part, is fallen within after it is broken up
After being stirred mixing by the second mixing part in mixing bunker, into output storehouse below through formed in solution mixed process from
Mental power function is sprayed through recirculation hole, is canted coil paddle structure additionally, due to the first mixing part, it is in rotation process, lower section
Pressure area is formed, is acted on major ingredient, so as to improve the ejection dynamics of major ingredient, improves the mixed effect of major ingredient and auxiliary material；
In conclusion the present invention has the advantages that simple in structure, proportion speed, is uniformly mixed.
Brief description of the drawings
For the technical solution of the clearer explanation embodiment of the present invention, required use in being described below to embodiment
Attached drawing be briefly described, it should be apparent that, drawings discussed below is only some embodiments of the present invention, for ability
For the those of ordinary skill in domain, without creative efforts, it is attached other can also to be obtained according to these attached drawings
Figure.
Fig. 1 is overall structure diagram of the present invention；
Fig. 2 is major ingredient buffering chamber sectional structure view；
Fig. 3 just cuts open structure diagram for the present invention；
Fig. 4 cuts open structure diagram for present invention survey；
Fig. 5 is enlarged diagram at A in Fig. 4；
Fig. 6 is enlarged diagram at B in Fig. 4；
Fig. 7 is compression assembly structure diagram；
Fig. 8 is compression assembly and screening assembly fit structure schematic diagram；
Fig. 9 is major ingredient electric hybrid module structure diagram；
The process flow chart of Figure 10 example IVs.
Embodiment
The technical solution in the embodiment of the present invention is clearly and completely illustrated below in conjunction with the accompanying drawings.
Embodiment one
The embodiment of the present invention is described below in detail, the example of the embodiment is shown in the drawings, wherein from beginning to end
Same or similar label represents same or similar element or has the function of same or like element.Below with reference to attached
The embodiment of figure description is exemplary, it is intended to for explaining the present invention, and is not considered as limiting the invention.
As shown in Fig. 1,2,3,4,5 and 6, a kind of heat cure furane resins are fixed than production system, including actuating unit 1, bag
Include：
Cache mechanism 2, the cache mechanism 2 include major ingredient buffering chamber 21, the temporary warehouse 22 of auxiliary material and are arranged at both
Between blending space 23；
Output mechanism 3, the output mechanism 3 is including setting compression assembly 31, being connected and coordinate with the compression assembly 31 sets
The screening assembly 32 being placed on the major ingredient buffering chamber 21 and the catalyst output precision 33 being connected with the screening assembly 32；
During the work time, actuating unit 1 drives compression assembly 31 to drive screening assembly 32 and catalyst while moving
Output precision 33 moves, and the inside of the output section 321 for making to be opened on screening assembly 32 and major ingredient buffering chamber 21 connects, major ingredient with it is auxiliary
Material is flowed out through output section 321 and the introduction part 221 being arranged on the temporary warehouse 22 of auxiliary material respectively, and phase is formed respectively in blending space 23
Pair and the liquid fluidization tower that is staggered up and down, in the mixed liquor formed below of the blending space 23, the mixed liquor is in dropping process
Mixing is contacted with through catalyst derived from catalyst output precision 33.
Wherein, as shown in Figures 3 and 4, the compression assembly 31 includes the first pressure being arranged in the temporary warehouse 22 of the auxiliary material
Contracting portion 311 and the second compression unit 312 being arranged in the blending space 23,311 and second compression unit of the first compression unit
312 in being distributed and being connected between the two by connecting rod 310 up and down, and second compression unit 312 is located at catalyst output
The outside of component 33；In the present embodiment, 310 quantity of connecting rod is two, and is symmetrical arranged, and is opened up on the temporary warehouse 22 of auxiliary material
There is the through hole that connecting rod 310 passes through.
In addition, as shown in Fig. 3,4 and 7,311 and second compression unit 312 of the first compression unit is that section is splayed
And opening up circular slanting harden structure is set, and the outer circumference surface of both warehouse 22 temporary with auxiliary material and blending space 23 respectively
Lateral wall contact set, 311 and second compression unit 312 of the first compression unit is during moving down, its lower shape respectively
Into the first compressional zone 313 and the second compressional zone 314；First compressional zone, 313 and second compressional zone 314 occurs for discontinuity,
Both disappears in 31 upward motion process of compression assembly, and first compression unit 311 is equipped with compression bin 223.
Further, as shown in Figures 2 and 3, the temporary warehouse 22 of the auxiliary material is coaxially disposed with the major ingredient buffering chamber 21, it is wrapped
Include surge bunker 222 and positioned at the lower section of surge bunker 222 and the compression bin 223 communicated therewith, first compressional zone 313 is located at institute
To state in compression bin 223, the introduction part 221 is arranged at the compression bin 223, interior and be connected with first compressional zone 313,
The temporary warehouse 22 of the auxiliary material is set for annular in the present embodiment, and the sectional dimension D of surge bunker 222 is more than compression bin 223
Sectional dimension d.
It should be noted that as shown in Fig. 4,5 and 6, output mechanism 3 includes being arranged inside the temporary warehouse 22 of the auxiliary material
Compression assembly 31, be connected with the compression assembly 31 and be equipped with the screening assembly 32 on the major ingredient buffering chamber 21 and
The catalyst output precision 33 being connected with the screening assembly 32；While driving mechanism 1 drives the up and down motion of compression assembly 31,
Catalyst output precision 33 is driven to move；Compression assembly 31 moves downward the first compressional zone 313 formed by the first compression unit 311
While auxiliary material of the inside is exported through introduction part 221, major ingredient in major ingredient buffering chamber 21 through output section 321 with
Auxiliary material is opposite and is mixed with upper and lower stacked system, so as to improve the proportion speed and mixing uniformity of major ingredient and auxiliary material, compresses
In 31 upward motion process of component, drive catalyst output precision 33 to move upwards, work is formed with the bottom of major ingredient buffering chamber 21
The method of operation is filled in, its ejection is made to catalyst compression of the inside while catalyst caching room 331 is moved upwards, with
Major ingredient, the contact mixing of auxiliary material mixed liquor in its outside dropping process, major ingredient, auxiliary material and the catalyst of formation stages are fixed than mixed
Close, solve it is existing in the prior art coarse, mixing is uneven because being matched between each auxiliary material, caused by furane resins poor quality
The problem of.
Embodiment two
As shown in Fig. 2,4 and 6, wherein identical with embodiment one or corresponding component is using corresponding with embodiment one attached
Icon is remembered, for simplicity, hereafter only describes the distinctive points with embodiment one；The difference of the embodiment two and embodiment one
It is：The catalyst output precision 33 includes being arranged at the catalyst caching room 331 of the lower section of major ingredient buffering chamber 21, opens up
The multiple catalyst flow jeting ports 332 being uniformly arranged on 331 outer circumference surface of room and around its axis, the catalyst are cached in the catalyst
Flow jeting port 332 and the 211 intermittent communicated setting of through hole for being fixedly installed on the lower section of major ingredient buffering chamber 21, the catalyst flow jeting port
332nd, introduction part 221 and output section 321 are in same perpendicular, in the present embodiment, the catalyst flow jeting port 332 with
Through hole 211 is preferably three, and the circumferencial direction for caching room 331 and major ingredient buffering chamber 21 along catalyst respectively is uniformly arranged.
Further, as shown in Fig. 3,4 and 5, the screening assembly 32 is set for annular tube structure, and itself and the major ingredient
The outer circumference surface sealing of buffering chamber 21 is equipped with, which is fixedly connected with catalyst caching room 331；It is described
Output section 321 includes the multiple head piece groups 322 being uniformly opened in around 32 axis of screening assembly on its periphery；On compression assembly 31
Synchronous drive screening assembly 32 is moved along the outer circumference surface of major ingredient buffering chamber 21 in lower motion process, and major ingredient and auxiliary material are synchronously defeated
Go out, be in contact in blending space 33.
Wherein, as shown in Fig. 3,5,6 and 8, the output section 321 includes uniformly being opened in its circle around 32 axis of screening assembly
Multiple head piece groups 322 on side face, the head piece group 322 set for vertically uniform intervals and with the major ingredient buffering chamber 21
Multiple recirculation holes 3221 of inside connection, the introduction part 221 include some auxiliary materials being correspondingly arranged with the recirculation hole 3221
Outlet 2211, in the present embodiment, auxiliary feed outlet 2211 are set for normally closed elasticity, i.e., it is in closure state under normal condition,
After its first internal compression unit 311 is formed, the auxiliary feed outlet 221 that elasticity is set is opened by its internal pressure, auxiliary material is sprayed
Go out.
It should be noted that as shown in figure 4, the first compression unit 311 and the second compression unit 312 are opening up annular
Inclined plate structure setting, while it compresses its bottom auxiliary material of going out during first time compression unit 311 moves down, its is cylindrical
Week carries out blade coating formula cleaning in face of the lateral wall of the temporary warehouse 22 of auxiliary material, avoids the bonding of auxiliary material and bulkhead and influences normally to produce；
Other second compression unit 312 is in blending space 23 and positioned at the outside of catalyst caching room 331, it is located at the first compression unit
311 lower section, during the mixed liquor that major ingredient is formed after being mixed with auxiliary material falls, is sprayed by catalyst flow jeting port 332
Catalyst ejector is fallen within the second compression unit 312, then the ramp structure by the second compression unit 312, carries out the unhurried current of mixed liquor,
Mixed liquor forms lamelliform liquid structure while being wandered along 312 upper surface of the second compression unit, realizes the mixing again of mixed liquor,
The mixed liquor of the diverse location on the second compression unit 312 is concentrated into mixing at the same time, further improves being uniformly mixed for mixed liquor
Property；In addition, while the second compression unit 312 moves downward, mixed solution in the bottom will be in it through its ramp effect
The mixed liquor of lower section extrudes to the periphery, its upward motion mode of structure, carries out the mixing of solution levels to mixed solution again
Stirring, improves its mixing uniformity.
Embodiment three
As shown in figure 3 and 9, wherein identical with embodiment two or corresponding component uses and two corresponding attached drawing of embodiment
Mark, for simplicity, hereafter only description and the distinctive points of embodiment two；The difference of the embodiment three and embodiment two exists
In：The output mechanism 3 further includes the major ingredient electric hybrid module 34 being rotatably dispose in inside the major ingredient buffering chamber 21, which mixes
Seaming element 34 includes the first mixing part 341 and positioned at the second mixing part 342 of the lower section of the first mixing part 341, and described first stirs
Mix portion 341 to set for canted coil paddle structure, second mixing part 342 includes the stirring that some axis around it are uniformly arranged
Rod 3421, and in the setting that is staggered up and down between adjacent stirring rod 3421；Multiple stirring rod 3421 are set to be staggered up and down, improve master
Expect the mixing quality between each layer in solution.
Further, as shown in Fig. 2,3 and 5, the major ingredient buffering chamber 21 includes mixing bunker 212 setting up and down and output
Storehouse 213, respectively positioned at the mixing bunker 212 with exporting in storehouse 213, this is defeated for 341 and second mixing part 342 of the first mixing part
Export 213 include be opened on its outer circumference surface and with multiple major ingredient delivery outlets of the 3221 intermittent communicated setting of recirculation hole
2131；Baffle plate assembly 32 is during moving up and down, and when recirculation hole 3221 is connected with major ingredient material delivery outlet 2131, major ingredient passes through successively
Major ingredient delivery outlet 2131 and recirculation hole 3221 spray, into blending space 33.
It should be noted that as shown in figure 3, major ingredient electric hybrid module 24 includes the first mixing part 341 and first is stirred positioned at this
The second mixing part 342 of the lower section of portion 341 is mixed, the first mixing part 341 is set for canted coil paddle structure, since major ingredient is a variety of things
Material is mixed to form, and to improve mixing uniformity between its material, during major ingredient is delivered to major ingredient buffering chamber 21, major ingredient is fallen within
On first mixing part 341, fallen within after it is broken up after being stirred mixing by the second mixing part 342 in mixing bunker 212, into it
Centrifugal force effect of the output storehouse 213 of lower section through being formed in solution mixed process is sprayed through recirculation hole 3221, additionally, due to the
One mixing part 341 is canted coil paddle structure, and in rotation process, pressure area formed below, acts on major ingredient for it, so as to carry
The ejection dynamics of high major ingredient, improves the mixed effect of major ingredient and auxiliary material.
Example IV
As shown in Figure 10, four a kind of heat cure furane resins are introduced calmly than production technology, including following step in conjunction with the embodiments
Suddenly：
(a) major ingredient mixing portion, the major ingredient synthesized by various materials enters in mixing bunker 212, by the first mixing part
After 341 break up in a rotative pattern, pressurized delivered is driven in a manner of rotating centrifugal through stream to storehouse 213 is exported through the second mixing part 342
Through hole 3221 exports；
(b) auxiliary material output par, c, the auxiliary material in compression bin 223 move down what is formed through the first compression unit 311
First compressional zone 313 acts on, and auxiliary material is sprayed along auxiliary feed outlet 2211；
(c) main materials and auxiliary materials mixing portion, the major ingredient and auxiliary material exported respectively through step a and step b, in blending space 23
Mixed liquor is mixed to form in a manner of upper and lower superposition staggeredly, which contacts mixing in dropping process with weighed catalyst；
(d) catalyst output par, c, drives catalyst to cache room 331 to moving up while compression assembly 31 moves up
It is dynamic, catalyst of the inside is sprayed with compress mode, is contacted with the mixed liquor formed through step (c)；
(e) secondary mixing portion, the catalyst action sprayed through catalyst caching room 331 fall after main materials and auxiliary materials mixed liquor
In on the second compression unit 312, concentrated and mixed with its inclined plate structure by the second compression unit 312.
Wherein, pressure differential is produced between first compressional zone 313 and blending space 23, auxiliary material is through the first compressional zone 313
Pressure acts on, and exporting 2211 directed flows along auxiliary material enters in blending space 23；The auxiliary feed outlet 2211 is normally closed elasticity
Set, 311 part of the first compression unit moves down the compression pressurization that process is the first compressional zone 313, the first compressional zone 313
Internal pressure reach auxiliary feed outlet 2211 elastic material elastic force it is critical after, auxiliary feed outlet 2211 is opened, auxiliary material along its spray.
In addition, compression is interrupted in the catalyst caching room 331 with yo-yo fashion to catalyst of the inside, urge
Agent is sprayed along catalyst flow jeting port 332 to be contacted with the main materials and auxiliary materials mixed liquor in dropping process, while by the jet power of its ejection
Drive part main materials and auxiliary materials mixed liquor to fall along parabolic path along the radial direction of catalyst caching room 331, realize that catalyst adds
While adding, mixed solution is mixed in a manner of radial diffusion.
In the present invention, it is to be understood that：Term " " center ", " longitudinal direction ", " transverse direction ", " length ", " width ", " thickness
Degree ", " on ", " under ", "front", "rear", "left", "right", " vertical ", " level ", " top ", " bottom ", " interior ", " outer ", " clockwise ",
The orientation or position relationship of instructions such as " counterclockwise " are based on orientation shown in the drawings or position relationship, are for only for ease of and retouch
State the present invention and simplify description, rather than instruction or imply signified equipment or specific orientation that element must have, Yi Te
Fixed azimuth configuration and operation, therefore be not considered as limiting the invention.
In addition, term " first ", " second " are only used for description purpose, and it is not intended that instruction or implying opposite important
Property or the implicit quantity for indicating indicated technical characteristic.Therefore, define " first ", the feature of " second " can be expressed or
Person implicitly includes one or more this feature.In description of the invention, " multiple " be meant that two or two with
On, unless otherwise specifically defined.
The foregoing is only a preferred embodiment of the present invention, but protection scope of the present invention be not limited thereto,
The change or replacement that any one skilled in the art can readily occur under the technical clarification of the present invention, such as will set
During the main body for having cap body is positioned over wiper mechanism, the cleaning solution of inside cavity is sprayed through importing component by cleaning assembly
Spill and on nib, the design concept to its cleaning treatment, should be covered by the protection scope of the present invention.Therefore, it is of the invention
Protection domain should be subject to the protection domain of claims.
Claims (10)
1. a kind of heat cure furane resins are fixed than production system, including actuating unit (1), it is characterised in that including：
Cache mechanism (2), the cache mechanism (2) include major ingredient buffering chamber (21), the temporary warehouse of auxiliary material (22) and are arranged at it
Blending space (23) between the two；
Output mechanism (3), the output mechanism (3) include compression assembly (31), are connected and coordinate with the compression assembly (31)
The screening assembly (32) being arranged on the major ingredient buffering chamber (21) and the catalyst being connected with the screening assembly (32) are defeated
Go out component (33)；
During the work time, screening assembly (32) and catalysis are driven while actuating unit (1) driving compression assembly (31) movement
Agent output precision (33) moves, and the output section (321) for making to be opened on screening assembly (32) inside major ingredient buffering chamber (21) with connecting
Logical, major ingredient is flowed out through output section (321) and the introduction part (221) being arranged on the temporary warehouse of auxiliary material (22) respectively with auxiliary material, mixed
Close space (23) and form liquid fluidization tower that is opposite and being staggered up and down respectively, in the mixing formed below of the blending space (23)
Liquid, the mixed liquor contact mixing in dropping process with through catalyst derived from catalyst output precision (33).
2. a kind of heat cure furane resins according to claim 1 compare production system surely, it is characterised in that the compression group
Part (31) includes the first compression unit (311) being arranged in the temporary warehouse of the auxiliary material (22) and is arranged at the blending space (23)
Interior the second compression unit (312), first compression unit (311) and the second compression unit (312) are in distribution up and down and between the two
It is connected by connecting rod (310), second compression unit (312) is located at the outside of the catalyst output precision (33).
3. a kind of heat cure furane resins according to claim 2 compare production system surely, it is characterised in that first pressure
Contracting portion (311) and the second compression unit (312) are that section is set for splayed and opening up circular slanting harden structure, and its two
The outer circumference surface of person contacts setting, first compression unit with the lateral wall of blending space (23) with the temporary warehouse of auxiliary material (22) respectively
(311) the first compressional zone (313) and second is formed respectively with the second compression unit (312) during moving down, under it to compress
Area (314).
4. a kind of heat cure furane resins according to claim 3 compare production system surely, it is characterised in that the auxiliary material is temporary
Warehouse (22) is coaxially disposed with the major ingredient buffering chamber (21), it includes surge bunker (222) and below the surge bunker (222)
And the compression bin (223) communicated therewith, first compressional zone (313) are located in the compression bin (223), the introduction part
(221) it is arranged on the compression bin (223), it is interior and be connected with first compressional zone (313).
5. a kind of heat cure furane resins according to claim 1 compare production system surely, it is characterised in that the catalyst
The catalyst that output precision (33) includes being arranged at below the major ingredient buffering chamber (21) caches room (331), is opened in the catalysis
The multiple catalyst flow jeting ports (332) being uniformly arranged on agent caching room (331) outer circumference surface and around its axis, the catalyst jet flow
Mouth (332) and through hole (211) the intermittent communicated setting being fixedly installed on below major ingredient buffering chamber (21), the catalyst flow jeting port
(332), introduction part (221) and output section (321) are in same perpendicular.
6. a kind of heat cure furane resins according to claim 5 compare production system surely, it is characterised in that the barrier group
Part (32) is that annular tube structure is set, and the outer circumference surface sealing of itself and the major ingredient buffering chamber (21) is equipped with, the barrier
Component (32) is fixedly connected with catalyst caching room (331), and the output section (321) is included around screening assembly (32) axis
The multiple head piece groups (322) being uniformly opened on its periphery.
7. a kind of heat cure furane resins according to claim 6 compare production system surely, it is characterised in that the output section
(321) the multiple head piece groups (322) being uniformly opened in around screening assembly (32) axis on its periphery, the head piece group are included
(322) it is the setting of vertically uniform intervals and multiple recirculation holes with being connected inside the major ingredient buffering chamber (21)
(3221), the introduction part (221) includes some auxiliary feed outlets (2211) being correspondingly arranged with the recirculation hole (3221).
8. a kind of heat cure furane resins according to claim 7 compare production system surely, it is characterised in that the output machine
Structure (3), which further includes, is rotatably dispose in the internal major ingredient electric hybrid module (34) of the major ingredient buffering chamber (21), the major ingredient electric hybrid module
(34) the first mixing part (341) and the second mixing part (342) below first mixing part (341) are included, described first
Mixing part (341) is set for canted coil paddle structure, and second mixing part (342) is uniformly arranged including some axis around it
Stirring rod (3421), and in being staggered setting up and down between adjacent stirring rod (3421).
9. a kind of heat cure furane resins according to claim 8 compare production system surely, it is characterised in that the major ingredient delays
Storage (21) includes mixing bunker (212) setting up and down and output storehouse (213), first mixing part (341) and the second stirring
Portion (342) is interior with output storehouse (213) positioned at the mixing bunker (212) respectively, which includes being opened in its excircle
On face and with multiple major ingredient delivery outlets (2131) of the recirculation hole (3221) intermittent communicated setting.
10. a kind of heat cure furane resins compare production technology surely, it is characterised in that comprise the following steps：
(a) major ingredient mixing portion, the major ingredient synthesized by various materials enters in mixing bunker (212), by the first mixing part
(341) after breaing up in a rotative pattern, pressurized delivered is driven with rotating centrifugal side to storehouse (213) is exported through the second mixing part (342)
Formula is exported through recirculation hole (3221)；
(b) auxiliary material output par, c, the auxiliary material in compression bin (223) move down what is formed through the first compression unit (311)
First compressional zone (313) acts on, and auxiliary material is sprayed along auxiliary feed outlet (2211)；
(c) main materials and auxiliary materials mixing portion, the major ingredient and auxiliary material exported respectively through step (a) and step (b), in blending space (23)
Interior to be mixed to form mixed liquor in a manner of upper and lower superposition staggeredly, which contacts mixing in dropping process with weighed catalyst；
(d) catalyst output par, c, drives catalyst caching room (331) to moving up while compression assembly (31) moves up
It is dynamic, catalyst of the inside is sprayed with compress mode, is contacted with the mixed liquor formed through step (c)；
(e) secondary mixing portion, the catalyst action sprayed through catalyst caching room (331) are fallen within after main materials and auxiliary materials mixed liquor
On second compression unit (312), secondary mixing is carried out to mixed solution with upper and lower motion mode by the second compression unit (312).
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| CN201711270774.6A CN107998992B (en) | 2017-12-05 | 2017-12-05 | Hot-curing furan resin fixed-ratio production system and process |
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| CN106040139A (en) * | 2016-06-29 | 2016-10-26 | 安徽省广德县华林造漆厂 | Reaction kettle |
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| US20070245934A1 (en) * | 2006-04-20 | 2007-10-25 | Brent Carman | Integrated biomass converter system |
| CN101020887A (en) * | 2006-12-14 | 2007-08-22 | 西北农林科技大学 | Fruit vinegar fermenting tank |
| CN102211893A (en) * | 2010-04-12 | 2011-10-12 | 刘跃魁 | Production method of novel paint and paint material by using same |
| WO2012146240A2 (en) * | 2011-04-27 | 2012-11-01 | Troester Gmbh & Co. Kg | Method and device for producing a rubber component |
| CN204354332U (en) * | 2014-12-24 | 2015-05-27 | 绵阳朗迪新材料有限公司 | A kind of mixing device produced for modified plastic material |
| CN204710334U (en) * | 2015-06-30 | 2015-10-21 | 济南悟通化学科技有限公司 | A kind of reactor being applicable to production 2-acetyl furan |
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