CN102126281A - Serial type extruder - Google Patents

Serial type extruder Download PDF

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Publication number
CN102126281A
CN102126281A CN2010106049348A CN201010604934A CN102126281A CN 102126281 A CN102126281 A CN 102126281A CN 2010106049348 A CN2010106049348 A CN 2010106049348A CN 201010604934 A CN201010604934 A CN 201010604934A CN 102126281 A CN102126281 A CN 102126281A
Authority
CN
China
Prior art keywords
extruder
tandem
machine barrel
head
charging aperture
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.)
Pending
Application number
CN2010106049348A
Other languages
Chinese (zh)
Inventor
陈锬
郑明嘉
杨志骅
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.)
MIANYANG DONGFANG SPECIAL ENGINEERING PLASTIC Co Ltd
Kingfa Science and Technology Co Ltd
Shanghai Kingfa Science and Technology Co Ltd
Original Assignee
MIANYANG DONGFANG SPECIAL ENGINEERING PLASTIC Co Ltd
Kingfa Science and Technology Co Ltd
Shanghai Kingfa Science and Technology Co Ltd
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 MIANYANG DONGFANG SPECIAL ENGINEERING PLASTIC Co Ltd, Kingfa Science and Technology Co Ltd, Shanghai Kingfa Science and Technology Co Ltd filed Critical MIANYANG DONGFANG SPECIAL ENGINEERING PLASTIC Co Ltd
Priority to CN2010106049348A priority Critical patent/CN102126281A/en
Publication of CN102126281A publication Critical patent/CN102126281A/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/375Plasticisers, homogenisers or feeders comprising two or more stages
    • B29C48/385Plasticisers, homogenisers or feeders comprising two or more stages using two or more serially arranged screws in separate barrels

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

The invention discloses a serial type extruder. In the invention, the nose of a first extruder is in side sealing connection with a second section barrel of a second extruder; and the nose of the second extruder is in side sealing connection with a second section barrel of a third extruder. The serial type extruder is characterized in that multiple stages of extruders are adopted, which can greatly improve the retention time of materials; a connecting section is provided with a heating and cooling device which can be used for heating or cooling the materials; and the extruders can be vacuumized to remove residual micromolecules in the materials.

Description

A kind of tandem extruder
Technical field
The present invention relates to a kind of extruder, particularly a kind of tandem extruder.
Background technology
With extruder to polymer react extrude processing can serialization production, and equipment investment is little, output height, thereby use very extensive.But reaction is extruded and is required material fully to mix, the time of staying is long, this just requires screw slenderness ratio long as much as possible, but no matter be single screw rod or twin-screw and multiscrew at present, draw ratio is all less, is difficult to reach the very long time of staying, therefore reaction conversion ratio is lower, monomer residue is more, can not prepare the higher response type polymer of ask for something, has limited the range of application that reaction is extruded.At present, a kind of method that addresses this problem is the screw extruder of preparation superelevation draw ratio, but screw strength, screw rod and barrel cooperate and the solution difficulty of the technical problem such as be in transmission connection of screw rod very big, have only the external producer of minority to produce, investment is high, apparatus expensive, maintaining is also extremely complicated, can not satisfy large-scale popularization and application.
Chinese patent 200920043494.6 discloses a kind of tandem single screw extrusion machine, its machine barrel is made up of the first rank machine barrel and the second rank machine barrel, the first rank extrusion screw rod is installed in the first rank machine barrel, basis, second rank screw rod is installed in the second rank machine barrel, the delivery outlet of the first rank machine barrel links to each other by the input port of pipeline with the second rank machine barrel, and charging aperture is positioned on the first rank machine barrel.Its weak point is that pipeline is comparatively tortuous, makes to change extremely complexity of screw rod, is not suitable for the production multiple product.
Summary of the invention
Mother of the present invention is to provide a kind of tandem extruder, improves residence time of material, is beneficial to little molecule devolatilization, convenient other component that adds in reaction.
Tandem extruder of the present invention, the head of first extruder carry out lateral seal with the second joint machine barrel of second extruder and are connected, and the head of second extruder carries out lateral seal with the second joint machine barrel of the 3rd extruder and is connected.
In addition, the draw ratio of first extruder and second extruder is the screw diameter of the screw diameter of the 40/1~56/1, the 3rd extruder greater than first extruder and second extruder; The second joint machine barrel of the head of first extruder and second extruder carries out lateral seal and is connected to the tubular metal sealing and is connected linkage section band heating-cooling device; The base of first extruder, second extruder or the 3rd extruder is established pulley and slide rail; First extruder is provided with charging aperture, and the charging aperture of second extruder links to each other with the discharging opening of first extruder, and the charging aperture of the 3rd extruder links to each other with the discharging opening of second extruder; Contain at least two vacuum ports on the 3rd extruding machine barrel.
The invention has the advantages that:
1. adopt multistage extruder, can improve the time of staying of material greatly;
2. linkage section band heating-cooling device can carry out heats cold or but operation to adding material;
3. can vacuumize extruder, thereby can remove little molecule residual in the material.
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Description of drawings
Fig. 1 is the structural representation of extruder of the present invention.
The specific embodiment
The specific embodiment with the tandem extrusion equipment is extruded in reaction involved in the present invention, is described in detail as follows with reference to accompanying drawing:
Combined type extrusion equipment involved in the present invention mainly is composed in series successively by three parallel dual-screw extruding machines, the head 5 of first extruder 1 seals with the charge door 4 of second extruder 3 and is connected, the head 8 of second extruder 3 is connected with the charge door 7 of the 3rd extruder 6, is connected to the tubular metal sealing and connects.First extruder 1 and second extruder 3 are selected the extruder of threaded diameter model of the same race for use, and draw ratio is 40/1~56/1; The 3rd extruder 6 selects for use screw diameter greater than preceding two screw diameter.
The base of first extruder 1, second extruder 3 or the 3rd extruder 6 is established pulley and slide rail; Contain at least two vacuum ports 9 on the 3rd extruder 6 barrels.
After extruder involved in the present invention reaches needed temperature, at first open the 3rd extruder 6 to the rotating speed that needs, open second extruder 3 again, open first extruder 1 at last, materials mixed is added charge door 2, material reacts after the 1 abundant plasticizing of first extruder mixes, fed second extruder 3 by linkage section by screw compulsory, material is proceeded sufficient reaction at second extruder 3, fed the 3rd extruder 6 by linkage section by screw compulsory again, the screw diameter of the 3rd extruder 6 is big, the barrel internal pressure reduces rapidly, and under the continuous stirring of screw rod, little molecule is overflowed fast, the device that is evacuated at vacuum port 9 is got rid of, and material is extruded extruding dies after reaction finishes.

Claims (6)

1. tandem extruder, it is characterized in that: the head (5) of first extruder (1) is connected with second joint machine barrel (4) lateral seal of second extruder (3), and the head (8) of second extruder (3) is connected with second joint machine barrel (7) lateral seal of the 3rd extruder (6).
2. tandem extruder according to claim 1, it is characterized in that: first extruder (1) is the screw diameter of the screw diameter of the 40/1~56/1, the 3rd extruder (6) greater than first extruder (1) and second extruder (3) with the draw ratio of second extruder (3).
3. tandem extruder according to claim 1, it is characterized in that: the second joint machine barrel (4) of the head (5) of first extruder (1) and second extruder (3) carries out lateral seal and is connected to the tubular metal sealing and is connected linkage section band heating-cooling device.
4. tandem extruder according to claim 1 is characterized in that: the base of first extruder (1), second extruder (3) or the 3rd extruder (6) is established pulley and slide rail.
5. tandem extruder according to claim 1, it is characterized in that: first extruder (1) is provided with charging aperture (2), the charging aperture (4) of second extruder (3) links to each other with the discharging opening of first extruder, and the charging aperture of the 3rd extruder (6) links to each other with the discharging opening of second extruder.
6. tandem extruder according to claim 1 is characterized in that: contain at least two vacuum ports (9) on the 3rd extruder (6) barrel.
CN2010106049348A 2010-12-25 2010-12-25 Serial type extruder Pending CN102126281A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010106049348A CN102126281A (en) 2010-12-25 2010-12-25 Serial type extruder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010106049348A CN102126281A (en) 2010-12-25 2010-12-25 Serial type extruder

Publications (1)

Publication Number Publication Date
CN102126281A true CN102126281A (en) 2011-07-20

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010106049348A Pending CN102126281A (en) 2010-12-25 2010-12-25 Serial type extruder

Country Status (1)

Country Link
CN (1) CN102126281A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103358529B (en) * 2012-04-09 2016-01-20 青岛福润德塑料挤出技术有限公司 Three-stage type efficiently plastifies filtering exhaust plastic extrusion system
CN107160582A (en) * 2017-07-17 2017-09-15 浙江晴天木塑科技有限公司 Multigroup number control granulation unit of natural fiber based high molecular polymer composites
CN108395571A (en) * 2017-02-07 2018-08-14 北京合众建业机电科技有限公司 A method of reclaimed rubber is produced using multistage extruder desulfurization
CN112405999A (en) * 2020-11-02 2021-02-26 南京越升挤出机械有限公司 Three-order extrusion device for series polymer foaming extrusion processing
WO2021196852A1 (en) * 2020-04-02 2021-10-07 苏州美梦机器有限公司 Material conveying system and method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN86205472U (en) * 1986-07-28 1987-12-16 青岛化工学院 Multi-screw rotary serial extruder
CN2686838Y (en) * 2004-03-05 2005-03-23 南京橡塑机械厂 Serial single-screw extruder
CN201960730U (en) * 2010-12-25 2011-09-07 金发科技股份有限公司 Serial type extruder

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN86205472U (en) * 1986-07-28 1987-12-16 青岛化工学院 Multi-screw rotary serial extruder
CN2686838Y (en) * 2004-03-05 2005-03-23 南京橡塑机械厂 Serial single-screw extruder
CN201960730U (en) * 2010-12-25 2011-09-07 金发科技股份有限公司 Serial type extruder

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103358529B (en) * 2012-04-09 2016-01-20 青岛福润德塑料挤出技术有限公司 Three-stage type efficiently plastifies filtering exhaust plastic extrusion system
CN108395571A (en) * 2017-02-07 2018-08-14 北京合众建业机电科技有限公司 A method of reclaimed rubber is produced using multistage extruder desulfurization
CN107160582A (en) * 2017-07-17 2017-09-15 浙江晴天木塑科技有限公司 Multigroup number control granulation unit of natural fiber based high molecular polymer composites
CN107160582B (en) * 2017-07-17 2023-11-24 浙江晴天木塑科技有限公司 Multi-group controlled granulator set for natural fiber-based high polymer composite material
WO2021196852A1 (en) * 2020-04-02 2021-10-07 苏州美梦机器有限公司 Material conveying system and method
CN112405999A (en) * 2020-11-02 2021-02-26 南京越升挤出机械有限公司 Three-order extrusion device for series polymer foaming extrusion processing

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Application publication date: 20110720