CN108394080B - Distributor structure for preparing multilayer CPP film - Google Patents

Distributor structure for preparing multilayer CPP film Download PDF

Info

Publication number
CN108394080B
CN108394080B CN201810371093.7A CN201810371093A CN108394080B CN 108394080 B CN108394080 B CN 108394080B CN 201810371093 A CN201810371093 A CN 201810371093A CN 108394080 B CN108394080 B CN 108394080B
Authority
CN
China
Prior art keywords
fluid
cpp film
shunting
cone
layer
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.)
Active
Application number
CN201810371093.7A
Other languages
Chinese (zh)
Other versions
CN108394080A (en
Inventor
张建林
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.)
Suzhou Rongdaxin New Material Technology Co ltd
Original Assignee
Suzhou Rongdaxin New Material 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 Suzhou Rongdaxin New Material Technology Co ltd filed Critical Suzhou Rongdaxin New Material Technology Co ltd
Priority to CN201810371093.7A priority Critical patent/CN108394080B/en
Publication of CN108394080A publication Critical patent/CN108394080A/en
Application granted granted Critical
Publication of CN108394080B publication Critical patent/CN108394080B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • B29C48/50Details of extruders
    • B29C48/695Flow dividers, e.g. breaker plates
    • B29C48/70Flow dividers, e.g. breaker plates comprising means for dividing, distributing and recombining melt flows
    • B29C48/705Flow dividers, e.g. breaker plates comprising means for dividing, distributing and recombining melt flows in the die zone, e.g. to create flow homogeneity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/10Polymers of propylene
    • B29K2023/12PP, i.e. polypropylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2007/00Flat articles, e.g. films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2009/00Layered products

Landscapes

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

Abstract

In order to solve the problem that the co-extrusion of a plurality of CPP films is difficult to realize because the current distributor has uneven distribution technology, especially when the single-layer CPP film is lower than 15um, the invention provides a distributor structure for preparing the multi-layer CPP film, which adopts a mode of multiple distribution cones for distributing and converging again, so that the polypropylene molten liquid can be uniformly distributed, and the thickness of each layer of CPP film can reach 5 um-15 um. Therefore, the original single-layer CPP film can be replaced by the multi-layer CPP film, and the material cost is not increased.

Description

Distributor structure for preparing multilayer CPP film
Technical Field
The invention relates to processing equipment of an aluminum-plastic composite film, in particular to a distributor structure for producing a multilayer CPP film in the aluminum-plastic composite film.
Background
In general, an aluminum-plastic composite film is a composite material composed of an outer nylon layer, an intermediate aluminum foil layer and an inner heat-sealing layer, wherein the layers are bonded through an adhesive. However, the lithium ion battery may have leakage of corrosive liquid or hydrofluoric acid during use, the inner heat-sealing layer of the common aluminum-plastic composite film is easily penetrated by the corrosive liquid or the hydrofluoric acid to cause short circuit, the inner heat-sealing layer of the common aluminum-plastic composite film is easily penetrated by the corrosive liquid or the hydrofluoric acid because the inner heat-sealing layer of the aluminum-plastic composite film is mainly a CPP film, the CPP film is a cast polypropylene film and has the characteristics of a thermoplastic polymer material, and in the production and processing processes, residues are carried out in a certain link of mechanical equipment due to incomplete plasticization of raw materials or extrusion and circulation processes, or the raw materials are decomposed in advance due to dead corners of a flow channel or excessively high friction temperature, so that 'fish eyes' can be generated; or the local plasticizing temperature is too high, so that a shiny white light spot, namely a so-called 'crystal point', appears on the surface of the film, the connection between the CPP film and the whole body of the CPP film at the position of the 'fish eye' or the 'crystal point' is not completely closed, and the corrosion liquid or hydrofluoric acid is easy to permeate from the 'fish eye' or the 'crystal point' when the part is relatively weak.
In order to solve the problem, the conventional method in the industry is to add an anti-corrosion treatment layer between an intermediate layer aluminum foil layer and an inner layer heat-sealing layer of an aluminum-plastic composite film, and the anti-corrosion treatment layer is combined with the aluminum foil layer and the inner layer hot air layer through an adhesive.
However, if a corrosion-resistant treatment layer is added, not only is the material cost increased, that is, an additional corrosion-resistant layer is added, but also an adhesive with a corrosion-resistant effect is preferably used; this also increases the cost of the process, since the addition of a tie layer requires the addition of at least one additional adhesive application line, which is relatively costly and relatively inefficient.
In view of this, it is proposed to replace a single-layer CPP film with a multi-layer CPP film in the aluminum-plastic composite film industry, which has the advantage that due to the physical characteristics of the CPP itself, the probability of generating "fish-eyes" or "crystal points" is relatively small, and if the CPP is stacked in multiple layers, the probability of hydrofluoric acid or corrosive liquid passing through all CPP films is greatly reduced. However, the current distributor has uneven flow distribution technology, and especially when the single-layer CPP film layer is lower than 15um, the single-layer CPP film layer is difficult to be uniformly distributed, so that the co-extrusion of the multi-layer CPP film layer is difficult to realize.
Disclosure of Invention
In order to solve the above problems, the present invention provides a dispenser structure for preparing a multilayer CPP film, which can uniformly distribute a polypropylene melt and make the thickness of each CPP film reach 5um to 15 um. Therefore, the original single-layer CPP film can be replaced by the multi-layer CPP film, and the material cost is not increased.
A dispenser structure for producing a multilayer CPP film, comprising: raw materials import (10), reposition of redundant personnel awl (11, 12, 14, 15), shunt tubes (111, 112, 114, 115), center tube (113), current-limiting awl (13), its characterized in that: at least two shunting cones (11, 12) are sequentially and concentrically sleeved on a central tube (113), wherein one end of a first shunting cone (11) is connected with a raw material inlet (10), the other section of the first shunting cone (11) is concentrically nested at one end of a second shunting cone (12), each time the fluid passes through one shunting cone (11, 12, 14, 15), the fluid is divided into more than or equal to 2 symmetrical strands and is transmitted along the axial direction through the shunting tubes (111, 112, 114, 115), a flow limiting cone (13) is sleeved at the tail end of the central tube (113), the fluid passing through the flow limiting cone (13) and the preceding shunting tubes (111, 114) can be combined to form a fluid I, the fluid passing through the flow limiting cone (13) and the preceding shunting tubes (112, 115) can be combined to form a fluid II, and the fluid I and the fluid II respectively enter the same layer of an extruder die head through the shunting tubes.
Furthermore, the shunting cones (11, 12, 14, 15) can be respectively and independently provided with shunting rings (16). The diverter ring (16) can fix the diverter cones (11, 12, 14, 15).
Further, the diameter of the central tube (113) is larger than that of the shunt tubes (111, 112, 114, 115).
Further, the fluid I and the fluid II can be divided after passing through the dividing cones (14, 15) respectively, and the divided liquids are conveyed to the same layer of the die head of the extruder.
Furthermore, the distributor structure for preparing the multilayer CPP film can divide the molten PP fluid into 2-20 parts; preferably, the molten PP fluid is divided into 3 to 12 parts.
By adopting the distributor structure for preparing the multilayer CPP film, the molten PP raw material is divided by at least two shunting cones (11, 12), and then is respectively and independently combined with the shunting pipes (111, 114) to form a fluid I and combined with the shunting pipes (112, 115) to form a fluid II, so that the fluid is more stable, the formula distribution is more uniform, the bottleneck that the existing CPP film is difficult to be thinner can be solved, and the multilayer ultrathin CPP film co-extrusion is realized.
Description of the drawings:
the embodiments are further described with reference to the accompanying drawings, in which:
FIG. 1 is a schematic view showing a dispenser structure for preparing a multilayer CPP film according to embodiment 1.
Description of main components:
a raw material inlet 10; a first tap cone 11; a second skimmer cone 12; a current limiting cone 13; a tap cone 14; a spreader cone 15; a diverter ring 16; a shunt tube 111; a shunt tube 112; a center tube 113; a shunt tube 114; a shunt tube 115; a draft tube 211; a draft tube 212; a draft tube 213; a draft tube 214; a draft tube 215; draft tube 216
The following detailed description will further illustrate the invention in conjunction with the above-described figures.
Detailed Description
Specific embodiment example 1:
as shown in FIG. 1, there is a schematic diagram of a dispenser structure for preparing a multilayer CPP film, which includes: raw materials import (10), reposition of redundant personnel awl (11, 12, 14, 15), shunt tubes (111, 112, 114, 115), center tube (113), current-limiting awl (13), its characterized in that: two shunting cones (11, 12) are sequentially and concentrically sleeved on a central tube (113), wherein one end of the first shunting cone (11) is connected with a raw material inlet (10), the other section of the first shunting cone (11) is concentrically nested at one end of the second shunting cone (12), each time the fluid passes through one shunting cone (11, 12, 14, 15), the fluid is divided into 2 strands and is transmitted along the axial direction through a shunting tube (111, 112, 114, 115), a flow limiting cone (13) is sleeved at the tail end of the central tube (113), the fluid passing through the flow limiting cone (13) and the preceding shunting tubes (111, 114) can be combined into a strand of fluid I, the fluid passing through the flow limiting cone (13) and the preceding shunting tubes (112, 115) can be combined into a strand of fluid II, the fluid I and the fluid II can respectively pass through the shunting cones (14, 15) and then are shunted and enter the same layer of an extruder die head through the shunting tubes (211-216), six-layer co-extruded CPP films can be formed in this way. And the thickness of each layer can be 10 um.
Specific embodiment example 2:
a dispenser for preparing a multilayer CPP film, comprising: raw materials import (10), reposition of redundant personnel awl (11, 12, 14, 15), shunt tubes (111, 112, 114, 115), center tube (113), current-limiting awl (13), its characterized in that: two shunting cones (11, 12) are sequentially and concentrically sleeved on a central tube (113), wherein one end of the first shunting cone (11) is connected with a raw material inlet (10), the other section of the first shunting cone (11) is concentrically nested at one end of the second shunting cone (12), each time the fluid passes through one shunting cone (11, 12, 14, 15), the fluid is divided into 2 strands and is transmitted along the axial direction through a shunting tube (111, 112, 114, 115), a flow limiting cone (13) is sleeved at the tail end of the central tube (113), the fluid passing through the flow limiting cone (13) and the front shunting tube (111, 114) can be combined into a strand of fluid I, the fluid passing through the flow limiting cone (13) and the front shunting tube (112, 115) can be combined into a strand of fluid II, and the fluid I and the fluid II can respectively pass through the two shunting tubes to enter the same layer of an extruder die head, so that a two-layer CPP co-extruded film can be formed, and each layer is 12um thick.
Therefore, the distributor structure for preparing the multilayer CPP film can uniformly distribute the polypropylene molten liquid and enable the thickness of each layer of CPP film to reach 5-15 um. Therefore, the original single-layer CPP film can be replaced by the multi-layer CPP film, and the material cost is not increased.
The above-mentioned embodiments only express several embodiments of the present invention, and the description thereof is more specific and detailed, but not construed as limiting the scope of the present invention. It should be noted that, for a person skilled in the art, several variations and modifications can be made without departing from the inventive concept, which falls within the scope of the present invention. Therefore, the protection scope of the present patent shall be subject to the appended claims.

Claims (5)

1. A dispenser structure for producing a multilayer CPP film, comprising: raw materials import (10), reposition of redundant personnel awl (11, 12, 14, 15), shunt tubes (111, 112, 114, 115), center tube (113), current-limiting awl (13), its characterized in that: at least two shunting cones (11, 12) are sequentially and concentrically sleeved on a central pipe (113), wherein one end of a first shunting cone (11) is connected with a raw material inlet (10), the other section of the first shunting cone (11) is concentrically nested at one end of a second shunting cone (12), each time the fluid passes through one shunting cone (11, 12, 14, 15), the fluid is divided into more than two symmetrical streams which are transmitted along the axial direction through the shunting pipes (111, 112, 114, 115), a flow limiting cone (13) is sleeved at the tail end of the central pipe (113), and the fluid passing through the flow limiting cone (13) and the front shunt pipes (111, 114) are combined into a jet of fluid I, simultaneously, the fluid passing through the flow limiting cone (13) and the front shunt tubes (112, 115) are combined into a fluid II, and the fluid I and the fluid II respectively enter the same layer of the die head of the extruder through the flow guide tube; the fluid I and the fluid II can be divided after passing through the dividing cones (14 and 15) respectively, and the divided liquid is conveyed to the same layer of the die head of the extruder.
2. The dispenser structure for producing a multilayer CPP film according to claim 1, wherein: and shunt rings (16) are respectively and independently arranged on the shunt cones (11, 12, 14 and 15).
3. The dispenser structure for producing a multilayer CPP film according to claim 1, wherein: the diameter of the central tube (113) is larger than that of the shunt tubes (111, 112, 114, 115).
4. The dispenser structure for producing a multilayer CPP film according to claim 1, wherein: the distributor structure for preparing the multilayer CPP film divides the molten PP fluid into 2-20 parts.
5. The dispenser structure for producing a multilayer CPP film according to claim 1, wherein: the distributor structure for preparing the multilayer CPP film divides molten PP fluid into 3-12 parts.
CN201810371093.7A 2018-04-24 2018-04-24 Distributor structure for preparing multilayer CPP film Active CN108394080B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810371093.7A CN108394080B (en) 2018-04-24 2018-04-24 Distributor structure for preparing multilayer CPP film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810371093.7A CN108394080B (en) 2018-04-24 2018-04-24 Distributor structure for preparing multilayer CPP film

Publications (2)

Publication Number Publication Date
CN108394080A CN108394080A (en) 2018-08-14
CN108394080B true CN108394080B (en) 2021-10-12

Family

ID=63100360

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810371093.7A Active CN108394080B (en) 2018-04-24 2018-04-24 Distributor structure for preparing multilayer CPP film

Country Status (1)

Country Link
CN (1) CN108394080B (en)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0279321A2 (en) * 1987-02-14 1988-08-24 BEKUM Maschinenfabriken GmbH Co-extrusion head
DE3704698A1 (en) * 1987-02-14 1988-08-25 Bekum Maschf Gmbh Coextrusion head
CN2242780Y (en) * 1995-06-01 1996-12-18 山东省莱州市精工塑料厂 Die special for processing Double-wall pipeline
CN102033277A (en) * 2010-07-07 2011-04-27 中纤伟业科技发展(北京)有限公司 Eccentricity-adjustment-free optical cable manufacturing die
CN103538237A (en) * 2012-07-16 2014-01-29 宁波康润机械科技有限公司 Co-extrusion die
CN203567157U (en) * 2013-10-29 2014-04-30 山东东信塑胶有限公司 Plastic co-extrusion die for producing large-caliber pipes
CN107336418A (en) * 2017-07-17 2017-11-10 苏州金纬管道科技有限公司 Assembling die for plastic extruder
CN107351346A (en) * 2017-07-17 2017-11-17 苏州金纬管道科技有限公司 A kind of assembling die for plastic extruder
CN107635619A (en) * 2015-03-19 2018-01-26 波士顿科学国际有限公司 Foley's tube is entered back under inner membrance

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0279321A2 (en) * 1987-02-14 1988-08-24 BEKUM Maschinenfabriken GmbH Co-extrusion head
DE3704698A1 (en) * 1987-02-14 1988-08-25 Bekum Maschf Gmbh Coextrusion head
CN2242780Y (en) * 1995-06-01 1996-12-18 山东省莱州市精工塑料厂 Die special for processing Double-wall pipeline
CN102033277A (en) * 2010-07-07 2011-04-27 中纤伟业科技发展(北京)有限公司 Eccentricity-adjustment-free optical cable manufacturing die
CN103538237A (en) * 2012-07-16 2014-01-29 宁波康润机械科技有限公司 Co-extrusion die
CN203567157U (en) * 2013-10-29 2014-04-30 山东东信塑胶有限公司 Plastic co-extrusion die for producing large-caliber pipes
CN107635619A (en) * 2015-03-19 2018-01-26 波士顿科学国际有限公司 Foley's tube is entered back under inner membrance
CN107336418A (en) * 2017-07-17 2017-11-10 苏州金纬管道科技有限公司 Assembling die for plastic extruder
CN107351346A (en) * 2017-07-17 2017-11-17 苏州金纬管道科技有限公司 A kind of assembling die for plastic extruder

Also Published As

Publication number Publication date
CN108394080A (en) 2018-08-14

Similar Documents

Publication Publication Date Title
RU2500532C2 (en) Female die, system and method for joint extrusion of multiple fluid layers
JP2641930B2 (en) Multilayer extrusion forming method and apparatus
KR101824294B1 (en) Concentric co-extrusion die and a method of extruding a multilayer thermoplastic film
GB1414470A (en) Apparatus for extruding multi-layer tubular films
AU2010221451A1 (en) Multilayer, heat-shrinkable film comprising a plurality of microlayers and method for its fabrication
US20100173031A1 (en) Die, system, and method for coextruding a plurality of fluid layers
JP3471924B2 (en) Spiral die and method of manufacturing laminate using the same
CN107415192A (en) The extrusion method of multilayer water supply line
CN110126411B (en) Film and preparation method and application thereof
CN108394080B (en) Distributor structure for preparing multilayer CPP film
CN204183848U (en) Multi-layer co-extrusion film-blowing equipment
CN103322340B (en) Double-layer coextrusion polyethylene spirally enwound structure-wall tubular product and production method thereof and manufacturing mechanism
CN102179934A (en) Processing method for bonding fluorine plastic to surface of polyethylene glycol terephthalate layer and relevant processing equipment
CA2491264A1 (en) Device for producing multilayer blown film
CN215849512U (en) Preparation system of compound PETG thermal contraction membrane
JP2002240126A (en) Method for forming resin film
CA3016083A1 (en) Coextrusion mandrel for extrusion die
US20120160728A1 (en) Multi-Segment, Heat-Shrinkable Barrier Film Comprising a Plurality of Microlayers
CN116252450A (en) Wall thickness adjusting device of multi-layer co-extrusion light pipe machine head
JPH10129004A (en) Ink supply tube and its manufacture
CN115416380A (en) Continuous fiber prepreg tape composite thick-wall pipe and manufacturing process and manufacturing equipment thereof
CN117901370A (en) Multilayer coextrusion blown film production equipment and production process thereof
IT201900011502A1 (en) SYSTEM FOR THE PRODUCTION BY BUBBLE EXTRUSION OF A FILM CONTAINING AT LEAST ONE LAYER OF HOT MELT AND / OR HIGH MELT FLOW INDEX POLYMER
JPH04368833A (en) Novel simultaneous extrosion device, its method and related film and package
JPH10129005A (en) Ink supply tube and its manufacture

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant