CN209478660U - A kind of mixer with Screw Extrusion structure - Google Patents

A kind of mixer with Screw Extrusion structure Download PDF

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Publication number
CN209478660U
CN209478660U CN201821865288.9U CN201821865288U CN209478660U CN 209478660 U CN209478660 U CN 209478660U CN 201821865288 U CN201821865288 U CN 201821865288U CN 209478660 U CN209478660 U CN 209478660U
Authority
CN
China
Prior art keywords
banburying chamber
mixing material
screw extrusion
extrusion structure
extruder barrel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201821865288.9U
Other languages
Chinese (zh)
Inventor
张春梅
严伟
罗军
刘渊
杨春林
曾加
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guiyang University
Original Assignee
Guiyang University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Guiyang University filed Critical Guiyang University
Priority to CN201821865288.9U priority Critical patent/CN209478660U/en
Application granted granted Critical
Publication of CN209478660U publication Critical patent/CN209478660U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/06Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
    • B29B7/10Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
    • B29B7/18Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/183Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft having a casing closely surrounding the rotors, e.g. of Banbury type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/22Component parts, details or accessories; Auxiliary operations
    • B29B7/24Component parts, details or accessories; Auxiliary operations for feeding
    • B29B7/246Component parts, details or accessories; Auxiliary operations for feeding in mixers having more than one rotor and a casing closely surrounding the rotors, e.g. with feeding plungers

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

The utility model discloses the mixers that one of processing of high molecular material forming field has Screw Extrusion structure, this device includes banburying chamber, the oval rotor of opposite revolution there are two being set in banburying chamber, banburying chamber is divided into left banburying chamber and right banburying chamber by two oval rotors, the top of banburying chamber is equipped with top bolt, top bolt axial sides are designed with Screw Extrusion structure, it is characterized by: the Screw Extrusion structure includes extruder barrel, feed opening is successively arranged in the material direction of the supply in the extruder barrel, screw rod, mixing material inlet and mixing material outlet, the screw rod is connected with actuator, the extruder barrel and banburying chamber pass through mixing material inlet vertical connection, extruder barrel tail portion and banburying chamber pass through mixing material outlet vertical connection, feed opening is located at right above the middle part of extruder barrel.Relative to traditional mixer, the present apparatus is sealed and is squeezed out by screw rod, is realized the purpose to feed at any time, is improved efficiency.

Description

A kind of mixer with Screw Extrusion structure
Technical field
The utility model belongs to processing of high molecular material forming field, in particular to a kind of with the close of Screw Extrusion structure Mill.
Background technique
Polymer material molding processing includes the processing and forming of rubber, plastics, chemical fibre and its composite material.Rubber tool There is unique high resiliency;Plastics have light weight, specific strength high;Chemical fibre has the characteristics such as high-modulus, high intensity.They are also With excellent electric property and superior chemical stability, wearability, air impermeability and impermeability, shock-absorbing and eliminate the noise, every The performances such as sound.The application of high molecular material be unable to do without corresponding contour machining equipment, is that rubber industry, plastics industry and chemistry are fine Tie up the important component of industry.
Closed experienced glue machine abbreviation mixer, also known as masticator, are mainly used for plasticating and being kneaded for rubber.Mixer is one Kind be equipped with a pair of of specific shape and the opposite rotor turned round, under adjustable temperature and the air-tight state of pressure intermittence to polymerization The machinery that object material is plasticated and is kneaded mainly is filled by banburying chamber, rotor, rotor seals, charging material pressing device, discharging It sets, the part such as transmission device and base forms.
It is in sealing state in banburying chamber's mixing process, when charging, needs to suspend mixing, opens gallery ports charging, so After close tight gallery ports, then start to be kneaded, thus cannot feed at any time in mixing process.And side wall needs to bear in mixing process Larger pressure, thus feed opening at any time can not be set.But if setting one can seal, bear pressure, and can add at any time The structure of material, so that it may solve the above problems.Screw extruder can generate larger pressure in extrusion process, and can be at any time Charging, and extruder head or side wall are in sealing state.Based on this, utility model people devises a kind of with Screw Extrusion The mixer of structure.
Utility model content
To solve the above-mentioned problems, the purpose of the utility model is to provide what one kind can feed at any time to have Screw Extrusion The mixer of structure.
To achieve the goals above, the technical solution of the utility model is as follows: a kind of mixing with Screw Extrusion structure Machine, including banburying chamber are set in banburying chamber there are two the oval rotor of opposite revolution, and banburying chamber is divided by two oval rotors Left banburying chamber and right banburying chamber, the top of banburying chamber are equipped with top bolt, and top bolt axial sides are designed with Screw Extrusion structure, the spiral shell It includes extruder barrel that bar, which squeezes out structure, be successively arranged in the material direction of the supply in the extruder barrel feed opening, screw rod, Mixing material inlet and mixing material outlet, the screw rod are connected with actuator, and the extruder barrel passes through close with banburying chamber Material inlet vertical connection, extruder barrel tail portion and banburying chamber are refined by mixing material outlet vertical connection, feed opening is located at Right above the middle part of extruder barrel.
The technical principle of this programme is as follows: when feeding for the first time, material flows successively through top bolt, feed opening, screw rod and mixing object Expect entrance, when material enters banburying chamber by mixing material inlet, operator starts mixer and Screw Extrusion knot at this time Structure, oval rotor is stirred and squeezes to material after mixer starting.Oval rotor major part material in rotation exists It is kneaded in banburying chamber, and oval rotor can splash fraction material when rotated, this partial material is from mixing material inlet Into Screw Extrusion structure, by Screw Extrusion, banburying chamber is then reentered by mixing material outlet.Screw Extrusion at this time The effect that structure is completed sealing and squeezed out.
Sealing and extrusion due to screw extruder, being kneaded material will not be leaked by Screw Extrusion structure.When need When feeding, addO-on therapy is added in Screw Extrusion structure by feed opening, add materials at this time in Screw Extrusion structure Mixing material acted on and mixing by Screw Extrusion, then into banburying chamber, thus achieved the purpose that feed at any time.
Using generated after the technical program it is following the utility model has the advantages that 1, relative to traditional mixer, the present apparatus passes through screw rod It is sealed and squeezes out, realize the purpose to feed at any time, improve efficiency.
2, when feeding again, screw rod keeps rotation, is squeezed material, and this extruding belongs to the pre- place to material Reason, alleviates the work load of oval rotor, improves the service life of device.
3, when feeding again, because of the splashing effects of oval rotor, newly added material is contaminated in extruder barrel It has added materials with what the splashing of oval rotor was taken out of, above two material is mixed when screw rod rotates at this time, is improved The mixing efficiency of material.
4, for according to the admixture of material, add materials first with part mixing material mix, then with other mixtures Material mixing, the uniformity for the mixing that is conducive to add materials improve the quality of product.
Further, the screw position is vertical with oval rotor axial direction, and mixing material inlet is located at left banburying chamber Highest point, mixing material outlet is located at the highest point of right banburying chamber.Because mixing material inlet is located at the highest of left banburying chamber Place, so the indoor material of left mixing only could enter extruder barrel by mixing material inlet when being splashed to highest point Interior, remaining material to splash is affected by gravity down drops back into left banburying chamber again, alleviates the burden of screw rod, improves making for device Use the service life.
Further, the installation direction of the screw rod is parallel with oval rotor axial direction, mixing material inlet and mixing Material outlet is located at the highest point of banburying chamber.The technical program reaches identical effect using different structures, improves device Service life.
Further, the Screw Extrusion structure is parallel to each other.In same plane even with always when ensure that material transmitting Line reduces energy consumption, has saved resource.
Further, the direction of the screw rod rotary extrusion is identical or opposite.Improve controllability.
Further, the actuator is motor, and the motor is placed in outside extruder barrel, and motor is located at screw rod radial direction Side.Reduce the volume for squeezing out barrel, convenient for squeezing out barrel maintenance or replacement.
Detailed description of the invention
Fig. 1 is the semi-cutaway of Screw Extrusion structure and traditional mixer positional relationship in embodiment one;
Fig. 2 is the top view of Screw Extrusion structure and oval rotor-position relationship in Fig. 1;
Fig. 3 is the sectional view of Screw Extrusion structure and banburying chamber's positional relationship in embodiment 2.
Specific embodiment
It is further described below by specific embodiment:
Appended drawing reference in Figure of description includes: banburying chamber 1, oval rotor 2, right banburying chamber 3, left banburying chamber 4, electricity Machine 5, extruder barrel 6, screw rod 7, mixing material inlet 8, mixing material outlet 9, feed opening 10, top bolt 11.
Embodiment one:
Embodiment is substantially as shown in Fig. 1: a kind of mixer with Screw Extrusion structure, including banburying chamber 1, banburying chamber There are two the oval rotors 2 of opposite revolution, two oval rotors 2 to divide banburying chamber 1 for left banburying chamber 4 for rotation connection in 1 With right banburying chamber 3, the top of banburying chamber 1 is equipped with top bolt 11, and top 11 axial sides of bolt are all placed with Screw Extrusion structure, screw rod Squeezing out structure includes extruder barrel 6, and feed opening 10, mixing object are successively opened in the material direction of the supply in extruder barrel 6 Expect entrance 8 and mixing material outlet 9, wherein extruder barrel 6 and banburying chamber 1 are squeezed out by 8 vertical connection of mixing material inlet By 9 vertical connection of mixing material outlet, feed opening 10 is being located at the middle part of extruder barrel 6 just for 6 tail portion of machine barrel and banburying chamber 1 Top squeezes out the screw rod 7 for being rotatably connected in barrel and placing perpendicular to oval rotor 2, and the quantity of screw rod 7 is 2, wherein one Screw rod 7 is located between 10 mixing material inlet 8 of feed opening, another screw rod 7 be located at mixing material outlet 9 and feed opening 10 it Between, two screw rods 7 are all connected with the motor 5 of model VTB63-4a, and 7 position of screw rod and oval 2 axial direction of rotor hang down Directly.
Specific implementation process is as follows:
As shown in Fig. 2, when feeding for the first time, material flows successively through top bolt 11, feed opening 10, screw rod 7 and mixing material and enters Mouth 8, when material enters banburying chamber 1 by mixing material inlet 8, operator starts mixer at this time and screw rod 7 squeezes out knot Structure, oval rotor 2 is stirred and squeezes to material after mixer starting.Oval rotor 2 major part material in rotation It is kneaded in banburying chamber 1, and oval rotor 2 can splash fraction material when rotated, this partial material is from mixing material Entrance 8 enters screw rod 7 and squeezes out structure, squeezes out by screw rod 7, then reenters banburying chamber 1 by mixing material outlet 9.This When screw rod 7 squeeze out structure complete sealing and squeeze out effect.
Sealing and extrusion due to Screw Extrusion structure, being kneaded material will not be leaked by Screw Extrusion structure.When When needing to feed, addO-on therapy is added in Screw Extrusion structure by feed opening 10, is added materials at this time and Screw Extrusion knot Mixing material in structure is mixed by the extrusion of screw rod 7, and then material enters in banburying chamber 1, thus reached with When the purpose that feeds.
When subsequent charge, because of the splashing effects of oval rotor 2, newly added material is contaminated in extruder barrel 6 It has added materials with what the splashing of oval rotor 2 was taken out of, above two material has been mixed when screw rod 7 rotates at this time, according to For the admixture of material, adds materials and first mixed with part mixing material, then be kneaded materials with other and mix, be conducive to add The uniformity for adding material to mix.
Embodiment two:
As shown in Fig. 3, the difference between this embodiment and the first embodiment lies in, 7 position of screw rod and oval 2 axis of rotor Parallel to direction, mixing material inlet 8 is located at the highest point of left banburying chamber 4, and mixing material outlet 9 is located at right banburying chamber 3 most Eminence.
Specific implementation process is as follows:
Because mixing material inlet 8 is located at the highest point of left banburying chamber 4, the material in left banburying chamber 4 is only flying It could be entered in extruder barrel 6 by mixing material inlet 8 when splashing highest point, remaining material to splash is affected by gravity down Again left banburying chamber 4 is dropped back into, the burden of screw rod 7 is alleviated, improves the service life of device.
Above-described is only the embodiments of the present invention, and the common sense such as well known specific structure and characteristic are herein in scheme It does not describe excessively.It should be pointed out that for those skilled in the art, in the premise for not departing from the utility model structure Under, several modifications and improvements can also be made, these also should be considered as the protection scope of the utility model, these all will not influence The effect and patent practicability that the utility model is implemented.This application claims protection scope should be with the content of its claim Subject to, the records such as specific embodiment in specification can be used for explaining the content of claim.

Claims (6)

1. a kind of mixer with Screw Extrusion structure, including banburying chamber, set that there are two the ellipses of opposite revolution in banburying chamber Banburying chamber is divided into left banburying chamber and right banburying chamber by shape rotor, two oval rotors, and the top of banburying chamber is equipped with top bolt, pushes up bolt Axial sides are designed with Screw Extrusion structure, it is characterised in that: the Screw Extrusion structure includes extruder barrel, the extrusion Feed opening, screw rod, mixing material inlet and mixing material outlet, the spiral shell are successively arranged in the material direction of the supply in machine barrel Bar is connected with actuator, the extruder barrel and banburying chamber and passes through mixing material inlet vertical connection, extruder barrel tail portion With banburying chamber by mixing material outlet vertical connection, feed opening is located at right above the middle part of extruder barrel.
2. a kind of mixer with Screw Extrusion structure according to claim 1, it is characterised in that: the screw position Vertical with oval rotor axial direction, mixing material inlet is located at the highest point of left banburying chamber, and mixing material outlet is located at the right side The highest point of banburying chamber.
3. a kind of mixer with Screw Extrusion structure according to claim 1, it is characterised in that: the peace of the screw rod Fill that direction is parallel with ellipse rotor axial direction, mixing material inlet and mixing material outlet are located at the highest point of banburying chamber.
4. a kind of mixer with Screw Extrusion structure according to claim 1-3, it is characterised in that: described Screw Extrusion structure is parallel to each other.
5. according to a kind of described in any item mixers with Screw Extrusion structure of Claims 2 or 3, it is characterised in that: institute The direction for stating screw rod rotary extrusion is identical or opposite.
6. a kind of mixer with Screw Extrusion structure according to claim 1, it is characterised in that: the actuator is Motor, the motor are placed in outside extruder barrel, and motor is located at screw rod radial direction side.
CN201821865288.9U 2018-11-13 2018-11-13 A kind of mixer with Screw Extrusion structure Expired - Fee Related CN209478660U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821865288.9U CN209478660U (en) 2018-11-13 2018-11-13 A kind of mixer with Screw Extrusion structure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821865288.9U CN209478660U (en) 2018-11-13 2018-11-13 A kind of mixer with Screw Extrusion structure

Publications (1)

Publication Number Publication Date
CN209478660U true CN209478660U (en) 2019-10-11

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ID=68115697

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821865288.9U Expired - Fee Related CN209478660U (en) 2018-11-13 2018-11-13 A kind of mixer with Screw Extrusion structure

Country Status (1)

Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114393731A (en) * 2022-01-21 2022-04-26 郭辅建 Plasticator using plastic as raw material
CN115383931A (en) * 2022-10-28 2022-11-25 河北尚华塑料科技有限公司 Plastic forming banburying type extruder

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114393731A (en) * 2022-01-21 2022-04-26 郭辅建 Plasticator using plastic as raw material
CN115383931A (en) * 2022-10-28 2022-11-25 河北尚华塑料科技有限公司 Plastic forming banburying type extruder

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GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20191011

Termination date: 20201113