CN102350746A - Non-meshing double-mixing rotor for continuous internal mixer - Google Patents
Non-meshing double-mixing rotor for continuous internal mixer Download PDFInfo
- Publication number
- CN102350746A CN102350746A CN201110270353XA CN201110270353A CN102350746A CN 102350746 A CN102350746 A CN 102350746A CN 201110270353X A CN201110270353X A CN 201110270353XA CN 201110270353 A CN201110270353 A CN 201110270353A CN 102350746 A CN102350746 A CN 102350746A
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- section
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- mixing
- banburying
- engagement
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
- B29B7/465—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft each shaft comprising rotor parts of the Banbury type in addition to screw parts
Abstract
The invention relates to a non-meshing double-mixing rotor for a continuous internal mixer. The rotor comprises a pair of rotor bodies rotating relatively, wherein each rotor body is provided with a material discharging section, a material conveying section and an additive adding section respectively; a first internal mixing section used for dispersing and preheating materials is arranged on the material conveying section and the additive adding section respectively; a second internal mixing section used for melting and mixing the materials is arranged between the material discharging section and the additive adding section; both the first internal mixing section and the second internal mixing section are provided with double-ended positive and negative direction threads; and the additive adding section and the material conveying section have threaded shapes. The rotor is a non-meshing rotor which increases promotes the dispersion and preheating of the materials to ensure that the materials difficult to disperse are uniformly mixed, have capacities of forcible conveying and plasticizing and strong mixing; the rotor is suitable for high-devolatilization components and particularly suitable for mixing the materials which are difficult to disperse; the non-meshing double-mixing rotor and an evolved type rotor thereof can be used for mixing a material which has a high shearing rate and a high temperature, and can also be used for mixing a material which has a low shearing rate and is more sensitive to temperature.
Description
Technical field
What the present invention relates to is a kind of rotor structure, and what be specifically related to is that a kind of continous way banbury is with the two mixed rotors of material.
Background technology
Banbury is one of capital equipment of using of plastics compounding, can be divided into two types of batch (-type) and continous ways by operation principle.It is made up of banburying chamber, rotor, floating weight (material pressing device), following top bolt (device for discharging), heating-cooling device and transmission system etc.Its operation principle is: compound gets into banburying chamber by loading hopper; At gap, rotor and the banburying chamber inwall gap of two counterrotating rotors, rotor and up and down in the gap of top bolt; Receive shearing, kneading and the rubbing action of continuous variation, make plastics give birth to heat and plastify, and mix.
The main structure parameters of banbury is rotating speed, diameter, length and the banbury total capacity of rotor; Rotor is the key working part of mixing roll, and its structure is that shape relates to the whether reasonable quality (dispersion and the uniformity coefficient of compounding ingredient in rubber) that directly influences energy consumption, production capacity and sizing material.And the general use of existing continous way banbury is mostly birotor is it is that a plurality of sheet rib bodies are set on the basis of rotor; The rib body is all along rotor pilum spiral extension; Two rotors rotate in opposite directions in the course of work; The rib body of rotor is meshing with each other, and raw material is along with rotor rotation receives promotion, extruding and friction.But the birotor of this structure in use; For mixing shearing rate and the high material of temperature; Be difficult to disperse when in banbury, mixing; Mix inhomogeneous; Mixed process is unstable, causes discharging unstable, its inefficiency; Even cause the rotor infringement, influence the production process of whole logistics.
Summary of the invention
The problem that is difficult to disperse to make its mixing to mixing shearing rate and the high material of temperature; The continous way banbury that the present invention seeks to be to provide a kind of and mix, possess forced conveyance plasticizing capacity and strong mixing ability is with the two mixed rotors of non-engagement; Be suitable for high devolatilization composition, be particularly suitable for the mixing of the material of difficulties in dispersion.
To achieve these goals, the present invention realizes through following technical scheme:
The continous way banbury is with the two mixed rotors of non-engagement; Comprise a pair of counterrotating rotor block; It is characterized in that; The additive that on every roots rotor body, is respectively equipped with discharge zone, the mass transport section that is arranged on the rotor block other end that is arranged on rotor block one end and is arranged in the rotor block stage casing adds section; Add section at described mass transport section and additive and be provided with the first banburying section that is used for material dispersed and preheating, be provided with the fusion that is used for material, the second banburying section of mixing between said discharge zone and additive add section; The said first banburying section and the second banburying section are the forward and reverse screw thread of double end, are used for material dispersed and preheating; The multiple thread of said mass transport Duan Weifei engagement, said additive adds section and mass transport Duan Jun is screw-like.
According to above-mentioned continous way banbury with the two mixed rotors of non-engagement, wherein, the screw thread that the forward and reverse screw thread of said double end is made up of forward and many ribs of direction spiral.
With the two mixed rotors of non-engagement, wherein, the cross sectional shape of said discharge zone is oval according to above-mentioned continous way banbury.
With the two mixed rotors of non-engagement, wherein, said additive adds the spiro rod length of the spiro rod length of section less than the mass transport section according to above-mentioned continous way banbury.
With the two mixed rotors of non-engagement, wherein, the reach of the said second banburying section is less than the reach of the first banburying section according to above-mentioned continous way banbury.
The present invention is non-meshing rotor; Through the first banburying section and the second banburying section are set; Its draw ratio can change; Material dispersed and preheating have been increased; Make difficulties in dispersion material mix, possess forced conveyance plasticizing capacity and strong mixing ability, be suitable for high devolatilization composition, be particularly suitable for the mixing of the material of difficulties in dispersion; This kind of and differentiation type rotor thereof can mixing shearing rate and the high materials of temperature, also can mixing low shearing rate and the material more responsive to temperature.
Description of drawings
Describe the present invention in detail below in conjunction with the accompanying drawing and the specific embodiment;
Fig. 1 is a structural representation of the present invention.
The specific embodiment
For technological means, creation characteristic that the present invention is realized, reach purpose and effect and be easy to understand and understand, below in conjunction with the specific embodiment, further set forth the present invention.
Referring to Fig. 1; Continous way banbury of the present invention is with the two mixed rotors of non-engagement; It is non-meshing rotor; Comprise a pair of counterrotating rotor block 1; On every roots rotor body 1, be respectively equipped with the discharge zone E that is arranged on rotor block 1 one ends, an additive adding section C who is arranged on the mass transport section A of rotor block 1 other end and is arranged on rotor block 1 stage casing; Between mass transport section A and additive adding section C, be provided with the first banburying section B, be used for material dispersed and preheating; Discharge zone E and additive add between the section C and are provided with the fusion that is used for material, the second banburying section D that mixes; The first banburying section B and the second banburying section D are the forward and reverse screw thread of double end, are used for material dispersed and preheating.
In the present embodiment, the screw thread that the forward and reverse screw thread of double end is made up of forward and many ribs of direction spiral, the reach of this second banburying section D is less than the reach of the first banburying section B, the dispersion of increase and preheating.Above-mentioned mass transport section A is the multiple thread of non-engagement, that is, the non-engaging twin-screw section mainly is a mass transport; Said additive adds section C and mass transport section A all is screw-like, and additive adds the spiro rod length of the spiro rod length of section C less than mass transport section A, and additive adds section C through additive and adds.The spiral shell rib 2 of the mass transport section A of present embodiment is provided with four, and the spiral shell rib 12 that additive adds section C is provided with three.
In addition, in the present embodiment, the cross sectional shape of discharge zone E is oval, and screw thread all is not set on it, is used for the discharging of material.
When the present invention used, material was delivered to an additive adding section C through the conveying of mass transport section A in dispersion and preheating through the first banburying section B; Additive adds thus; Through the second banburying section D fusion, mixing, it is mixed then, discharge material through discharge zone E at last.
What the present invention adopted is non-meshing rotor; Because of whenever circling, need shear 3-5 time material rotor through the first banburying section B and the second banburying section D; Improved shear efficiency; Help breaing up of bulk material; Also help the mixing and the dispersion of different component; Possess forced conveyance plasticizing capacity and strong mixing ability; Be suitable for high devolatilization composition; Be particularly suitable for the mixing of the material of difficulties in dispersion; This kind of and differentiation type rotor thereof can mixing shearing rate and the high materials of temperature, also can mixing low shearing rate and the material more responsive to temperature.
More than show and described basic principle of the present invention and principal character and advantage of the present invention.The technical staff of the industry should understand; The present invention is not restricted to the described embodiments; That describes in the foregoing description and the specification just illustrates principle of the present invention; Under the prerequisite that does not break away from spirit and scope of the invention; The present invention also has various changes and modifications, and these variations and improvement all fall in the scope of the invention that requires protection.The scope of the claimed invention by the appended claims and their equivalents defined ?
.
Claims (5)
1. the continous way banbury is with the two mixed rotors of non-engagement; Comprise a pair of counterrotating rotor block; It is characterized in that; The additive that on every roots rotor body, is respectively equipped with discharge zone, the mass transport section that is arranged on the rotor block other end that is arranged on rotor block one end and is arranged in the rotor block stage casing adds section; Add section at described mass transport section and additive and be provided with the first banburying section that is used for material dispersed and preheating, be provided with the fusion that is used for material, the second banburying section of mixing between said discharge zone and additive add section; The said first banburying section and the second banburying section are the forward and reverse screw thread of double end; The multiple thread of said mass transport Duan Weifei engagement, said additive adds section and mass transport Duan Jun is screw-like.
2. continous way banbury according to claim 1 is characterized in that the screw thread that the forward and reverse screw thread of said double end is made up of forward and many ribs of direction spiral with the two mixed rotors of non-engagement.
3. continous way banbury according to claim 1 is characterized in that with the two mixed rotors of non-engagement the cross sectional shape of said discharge zone is oval.
4. continous way banbury according to claim 1 is characterized in that with the two mixed rotors of non-engagement said additive adds the spiro rod length of the spiro rod length of section less than the mass transport section.
5. continous way banbury according to claim 1 is characterized in that with the two mixed rotors of non-engagement the reach of the said second banburying section is less than the reach of the first banburying section.
Priority Applications (1)
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CN201110270353XA CN102350746A (en) | 2011-09-14 | 2011-09-14 | Non-meshing double-mixing rotor for continuous internal mixer |
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CN201110270353XA CN102350746A (en) | 2011-09-14 | 2011-09-14 | Non-meshing double-mixing rotor for continuous internal mixer |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106113305A (en) * | 2016-08-22 | 2016-11-16 | 益阳橡胶塑料机械集团有限公司 | Rubber compound continuous mixing machine rotor and rubber compound continuous mixing machine and application |
WO2017215598A1 (en) * | 2016-06-17 | 2017-12-21 | 东莞市昶丰机械科技有限公司 | New continuous mixer structure |
CN111673938A (en) * | 2020-05-15 | 2020-09-18 | 贾中奇 | Incongruous parallel double screw for stone paper continuous banburying granulator |
WO2023061337A1 (en) * | 2021-10-14 | 2023-04-20 | 无锡市博宇塑机有限公司 | Pvc floor, and production line and preparation method therefor |
WO2023061335A1 (en) * | 2021-10-14 | 2023-04-20 | 无锡市博宇塑机有限公司 | Pvc floor production line |
Citations (6)
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CN1169906A (en) * | 1996-05-17 | 1998-01-14 | 波米尼公司 | Method for continuously mixing polymer materials and associated machine with partially tangential and interpenetrating rotors |
US5947593A (en) * | 1996-12-24 | 1999-09-07 | Kabushiki Kaisha Kobe Seiko Sho | Twin-screw kneading apparatus |
CN1265936A (en) * | 1999-03-02 | 2000-09-13 | 株式会社神户制钢所 | Mixer rotor and the mixer having same |
CN1381344A (en) * | 2001-04-17 | 2002-11-27 | 郴州华嵘合成纸有限公司 | Dual-axle continuous pugging machine |
CN101426635A (en) * | 2005-11-16 | 2009-05-06 | 尤尼威蒂恩技术有限责任公司 | High speed and direct driven rotating equipment for polyolefin manufacturing |
CN202213076U (en) * | 2011-09-14 | 2012-05-09 | 昆山科信橡塑机械有限公司 | Non-meshing double mixing rotor of continuous internal mixer |
-
2011
- 2011-09-14 CN CN201110270353XA patent/CN102350746A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1169906A (en) * | 1996-05-17 | 1998-01-14 | 波米尼公司 | Method for continuously mixing polymer materials and associated machine with partially tangential and interpenetrating rotors |
US5947593A (en) * | 1996-12-24 | 1999-09-07 | Kabushiki Kaisha Kobe Seiko Sho | Twin-screw kneading apparatus |
CN1265936A (en) * | 1999-03-02 | 2000-09-13 | 株式会社神户制钢所 | Mixer rotor and the mixer having same |
CN1381344A (en) * | 2001-04-17 | 2002-11-27 | 郴州华嵘合成纸有限公司 | Dual-axle continuous pugging machine |
CN101426635A (en) * | 2005-11-16 | 2009-05-06 | 尤尼威蒂恩技术有限责任公司 | High speed and direct driven rotating equipment for polyolefin manufacturing |
CN202213076U (en) * | 2011-09-14 | 2012-05-09 | 昆山科信橡塑机械有限公司 | Non-meshing double mixing rotor of continuous internal mixer |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017215598A1 (en) * | 2016-06-17 | 2017-12-21 | 东莞市昶丰机械科技有限公司 | New continuous mixer structure |
CN106113305A (en) * | 2016-08-22 | 2016-11-16 | 益阳橡胶塑料机械集团有限公司 | Rubber compound continuous mixing machine rotor and rubber compound continuous mixing machine and application |
CN111673938A (en) * | 2020-05-15 | 2020-09-18 | 贾中奇 | Incongruous parallel double screw for stone paper continuous banburying granulator |
WO2023061337A1 (en) * | 2021-10-14 | 2023-04-20 | 无锡市博宇塑机有限公司 | Pvc floor, and production line and preparation method therefor |
WO2023061335A1 (en) * | 2021-10-14 | 2023-04-20 | 无锡市博宇塑机有限公司 | Pvc floor production line |
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Application publication date: 20120215 |