WO2016095823A1 - 一种复合热熔胶网膜及其制备工艺 - Google Patents

一种复合热熔胶网膜及其制备工艺 Download PDF

Info

Publication number
WO2016095823A1
WO2016095823A1 PCT/CN2015/097640 CN2015097640W WO2016095823A1 WO 2016095823 A1 WO2016095823 A1 WO 2016095823A1 CN 2015097640 W CN2015097640 W CN 2015097640W WO 2016095823 A1 WO2016095823 A1 WO 2016095823A1
Authority
WO
WIPO (PCT)
Prior art keywords
melt adhesive
hot melt
composite
adhesive web
spinneret
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.)
Ceased
Application number
PCT/CN2015/097640
Other languages
English (en)
French (fr)
Inventor
李哲龙
朱万育
马星全
雷何记
曾作祥
张勇健
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.)
KUNSHAN TIANYANG HOT MELT ADHESIVE CO Ltd
SHANGHAI TIANYANG HOT MELT ADHESIVE CO Ltd
East China University of Science and Technology
Original Assignee
KUNSHAN TIANYANG HOT MELT ADHESIVE CO Ltd
SHANGHAI TIANYANG HOT MELT ADHESIVE CO Ltd
East China University of Science and Technology
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 KUNSHAN TIANYANG HOT MELT ADHESIVE CO Ltd, SHANGHAI TIANYANG HOT MELT ADHESIVE CO Ltd, East China University of Science and Technology filed Critical KUNSHAN TIANYANG HOT MELT ADHESIVE CO Ltd
Priority to CH00792/17A priority Critical patent/CH712138B1/de
Priority to KR1020177020144A priority patent/KR101937389B1/ko
Priority to DE112015005639.4T priority patent/DE112015005639T5/de
Priority to US15/537,305 priority patent/US10472547B2/en
Publication of WO2016095823A1 publication Critical patent/WO2016095823A1/zh
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J7/00—Adhesives in the form of films or foils
    • C09J7/10—Adhesives in the form of films or foils without carriers
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J11/00—Features of adhesives not provided for in group C09J9/00, e.g. additives
    • C09J11/02—Non-macromolecular additives
    • C09J11/04—Non-macromolecular additives inorganic
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J7/00—Adhesives in the form of films or foils
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J11/00—Features of adhesives not provided for in group C09J9/00, e.g. additives
    • C09J11/02—Non-macromolecular additives
    • C09J11/06—Non-macromolecular additives organic
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J11/00—Features of adhesives not provided for in group C09J9/00, e.g. additives
    • C09J11/08—Macromolecular additives
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J123/00—Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers
    • C09J123/02—Adhesives based on homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Adhesives based on derivatives of such polymers not modified by chemical after-treatment
    • C09J123/04—Homopolymers or copolymers of ethene
    • C09J123/06—Polyethylene
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D4/00—Spinnerette packs; Cleaning thereof
    • D01D4/02—Spinnerettes
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00—Formation of filaments, threads, or the like
    • D01D5/08—Melt spinning methods
    • D01D5/084—Heating filaments, threads or the like, leaving the spinnerettes
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00—Formation of filaments, threads, or the like
    • D01D5/08—Melt spinning methods
    • D01D5/088—Cooling filaments, threads or the like, leaving the spinnerettes
    • D—TEXTILES; PAPER
    • D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/005—Synthetic yarns or filaments
    • D04H3/007—Addition polymers
    • D—TEXTILES; PAPER
    • D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/005—Synthetic yarns or filaments
    • D04H3/009—Condensation or reaction polymers
    • D—TEXTILES; PAPER
    • D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/08—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
    • D04H3/16—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between thermoplastic filaments produced in association with filament formation, e.g. immediately following extrusion
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24—Acids; Salts thereof
    • C08K3/26—Carbonates; Bicarbonates
    • C08K2003/265—Calcium, strontium or barium carbonate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24—Acids; Salts thereof
    • C08K3/26—Carbonates; Bicarbonates
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/34—Silicon-containing compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00—Use of organic ingredients
    • C08K5/04—Oxygen-containing compounds
    • C08K5/13—Phenols; Phenolates
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00—Use of organic ingredients
    • C08K5/04—Oxygen-containing compounds
    • C08K5/13—Phenols; Phenolates
    • C08K5/134—Phenols containing ester groups
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2301/00—Additional features of adhesives in the form of films or foils
    • C09J2301/20—Additional features of adhesives in the form of films or foils characterized by the structural features of the adhesive itself
    • C09J2301/202—Additional features of adhesives in the form of films or foils characterized by the structural features of the adhesive itself the adhesive being in the form of fibres
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2301/00—Additional features of adhesives in the form of films or foils
    • C09J2301/30—Additional features of adhesives in the form of films or foils characterized by the chemical, physicochemical or physical properties of the adhesive or the carrier
    • C09J2301/304—Additional features of adhesives in the form of films or foils characterized by the chemical, physicochemical or physical properties of the adhesive or the carrier the adhesive being heat-activatable, i.e. not tacky at temperatures inferior to 30°C
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2301/00—Additional features of adhesives in the form of films or foils
    • C09J2301/30—Additional features of adhesives in the form of films or foils characterized by the chemical, physicochemical or physical properties of the adhesive or the carrier
    • C09J2301/312—Additional features of adhesives in the form of films or foils characterized by the chemical, physicochemical or physical properties of the adhesive or the carrier parameters being the characterizing feature
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2423/00—Presence of polyolefin
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2477/00—Presence of polyamide
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00—Formation of filaments, threads, or the like
    • D01D5/08—Melt spinning methods
    • D—TEXTILES; PAPER
    • D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2321/00—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D10B2321/02—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins
    • D10B2321/021—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins polyethylene
    • D—TEXTILES; PAPER
    • D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2321/00—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D10B2321/02—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins
    • D10B2321/022—Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins polypropylene

Definitions

  • the invention relates to a composite hot melt adhesive mesh film and a preparation process thereof, in particular to a composite hot melt adhesive mesh film for bonding metal and non-polar materials and a preparation process thereof, which are prepared by the invention.
  • the composite hot melt adhesive mesh film is especially suitable for the bonding and bonding of metal materials such as stainless steel, aluminum and copper with non-polar polymers such as polyethylene and polypropylene.
  • Hot melt adhesive mesh film is a kind of material with good corrosion resistance, aging resistance, good thermal stability and good tensile, anti-breaking and good water permeability, so it is widely used in clothing, automotive, electronics and other industries.
  • CN 101240148 B provides a method for preparing a hot melt adhesive web, comprising melting a hot melt adhesive material, adding a crystal nucleating agent, extruding, spinning, air drafting, pendulum forming, etc.
  • the invention relates to preparing a hot melt adhesive web by using a copolyamide hot melt adhesive as a raw material.
  • CN 101967733 B provides a preparation method of a hot melt adhesive web film, which is prepared by controlling the melting temperature, the spinning speed, the infrared temperature, etc. of the hot melt adhesive to prepare a hot melt adhesive web having uniform pore diameter and stable weight.
  • it relates to a method for preparing a hot melt adhesive web using a polyester hot melt adhesive as a raw material.
  • CN 103059792 B provides a polyester elastomer hot melt adhesive for bonding polar polymers and metallic materials and a process for the preparation thereof.
  • CN1699491A also discloses a preparation method of a hot melt adhesive film, which is especially suitable for a double-sided hot melt adhesive film for painting and painting.
  • the object of the present invention is to overcome the defects of the prior art and provide a composite hot-melt adhesive mesh film and a preparation process thereof.
  • the composite hot-melt adhesive mesh film prepared by the invention has high bonding strength and long-lasting bonding. It is especially suitable for the bonding and bonding of metal materials such as stainless steel, aluminum and copper with non-polar polymers such as polyethylene and polypropylene.
  • Composite hot melt adhesive mesh film which is composed of polyamide hot melt adhesive mesh film and polyolefin hot melt adhesive mesh film.
  • the polyamide hot melt adhesive used in the polyamide hot melt adhesive film has a DSC final melting point of 116- 130 ° C, the melt flow rate is 30-50g/10min / 160 ° C;
  • the polyolefin hot melt adhesive film used in the composition of the polyolefin hot melt adhesive in mass percentage including: compatibilizer 8-15%, polyethylene 50-70%, other polyolefins 3-10%, initiator 0.2-0.8%, silane coupling agent 0.7-1.3%, tackifier 8-20%, inorganic filler 1.0-10%, antioxidant 0.4-0.8% ;
  • the above compatibilizer is selected from the group consisting of maleic anhydride grafted high density polyethylene, maleic anhydride grafted low density polyethylene, maleic anhydride grafted polypropylene, and maleic anhydride grafted linear low density polyethylene. Said maleic anhydride grafting ratio of 0.8-1.2%;
  • the polyethylene is selected from the group consisting of high density polyethylene, low density polyethylene and linear low density polyethylene, and has a melt flow rate of 0.9-7 g/10 min / 190 ° C;
  • the other polyolefin is selected from the group consisting of ethylene-octene copolymer, polypropylene, and polystyrene, and has a melt flow rate of 1.6-14 g/10 min/190 ° C;
  • the above initiator is selected from the group consisting of benzoyl peroxide, di-tert-butyl peroxide and azobisisobutyronitrile;
  • the above silane coupling agent is selected from one of vinyltrimethoxysilane and ⁇ -aminopropyltrimethoxysilane;
  • the above tackifier is selected from the group consisting of rosin 145, terpene resin and hydrogenated carbon five resin;
  • the above inorganic filler is selected from one of talc, kaolin and nano calcium carbonate;
  • the above antioxidant is selected from one of the antioxidant 1010, the antioxidant BHT, and the antioxidant 264.
  • a preparation process of a composite hot-melt adhesive web film wherein the polyamide hot melt adhesive and the polyolefin hot melt adhesive used in the composite hot melt adhesive are selected as raw materials, and the following steps are performed:
  • the above-mentioned polyamide hot melt adhesive is spun onto the conveyor belt at a first preset speed by the first spinneret under the traction of the first airflow plate, and then heated by the first infrared heating zone to form a first layer of the mesh membrane;
  • the above-mentioned polyolefin hot melt adhesive is sprayed onto the conveyor belt at a second preset speed by the second spinneret under the traction of the second airflow, and is combined with the first layer of the reticulated membrane and then passed through the second Heating in the infrared heating zone to form a double-layer composite web;
  • the temperature of the first spinneret is less than the temperature of the second spinneret, the temperature of the first spinneret is 170-210 ° C, and the temperature of the second spinneret is 180-230 ° C;
  • the first preset speed is greater than the second preset speed, the first preset speed is 15-30 m/min, and the second preset speed is 10-25 m/min;
  • the first air flow rate is greater than the second air flow speed, and the first air flow and the second air flow speed are in the range of 30-120 m/min;
  • the temperature of the first infrared heating zone is higher than the temperature of the second infrared heating zone, the temperature of the first infrared heating zone is 90-120 ° C, and the temperature of the second infrared heating zone is 60-90 ° C;
  • the speed of the above conveyor belt is 12-20 m/min, and the distance between the first spinneret and the second spinneret is 0.7-1.3 m.
  • the composite hot melt adhesive web film and the preparation process thereof provided by the invention adopt a specific formula, so that a polar polyamide hot melt adhesive and a non-polar poly-containing polymer containing a compatibilizer are used.
  • the olefin is effectively melted, and the composite hot-melt adhesive web film prepared according to the invention has high bonding strength and long-lasting bonding, and is particularly suitable for non-polar materials such as stainless steel, aluminum, copper and the like, and polyethylene, polypropylene and the like. Bonding of polymers.
  • the preparation process proposed by the invention from the raw material pretreatment to the final preparation of the hot melt adhesive mesh film product, is completed in a set production process, which can greatly reduce production failure, high production efficiency and low cost.
  • Figure 1 is a flow chart of the preparation process proposed by the present invention.
  • Composite hot melt adhesive mesh film which is composed of polyamide hot melt adhesive mesh film and polyolefin hot melt adhesive mesh film, and the polyamide hot melt adhesive used is under Differential Scanning Calorimetry (DSC)
  • DSC Differential Scanning Calorimetry
  • a preparation process of a composite hot melt adhesive web film which respectively heats the above polyamide hot melt adhesive and polyolefin After the molten rubber is melted, it is pumped into the first spinneret and the second spinneret which are independent of each other; both spinnerets are disposed above the conveyor belt, and the second spinneret is located in the first spinning belt along the conveying direction of the conveyor belt Downstream of the plate, the distance between the two spinnerets is 0.7m, the conveyor belt (for example, a steel wire belt) works, and the conveying speed is adjusted to 12m/min; the first spinneret is opened, and the inner temperature is adjusted to 170 ° C, and the air flow is For example, the compressed air) speed is adjusted to 120m/min, so that the spinning speed is 20m/min under the action of airflow traction and the discharge pressure of the spinneret, and the polyamide hot melt adhesive is from the first spinneret and in the airflow.
  • the conveyor belt for example, a steel
  • the mesh film is heated by a first infrared heating zone at a temperature of 100 ° C to form a first layer of the mesh film, and the first infrared heating zone can be located, for example, in two spinnerets a suitable position between the two; open the second spinneret, adjust the internal temperature to 180 ° C, air flow (for example, compressed air) speed of 85 m / min, so that the spinning speed is 12 m / min, polyolefin hot melt from The second spinneret is spun to the conveyor belt under the traction of the air stream, and is transmitted to The first layer of the web at the second spinneret is thermally composited, and then heated by a second infrared heating zone having a temperature of 60 ° C to form a double-layered web, which may be located, for example, on the second spinneret. Downstream; then cooled, crystallized, and wound to form a composite hot melt adhesive film product that is
  • a composite hot melt adhesive mesh film which is composed of a polyamide hot melt adhesive mesh film and a polyolefin hot melt adhesive mesh film.
  • the polyamide hot melt adhesive used has a DSC final melting point of 116 ° C and a melt flow rate of 50 g / 10min/160°C; the composition of the polyolefin hot melt adhesive used and the mass percentage of each component are:
  • the conveyor belt (for example, a steel belt) works to adjust the conveying speed to 12m/min; the first spinneret is opened, the internal temperature is adjusted to 170 ° C, the spinning speed is 20 m / min, and the air flow (for example a compressed air) speed of 120 m / min, polyamide hot melt adhesive from the first spinneret and under the traction of the air stream to the conveyor belt to form a network film; the mesh film through a temperature of 100 ° C of the first infrared heating zone Heating to form a first layer of web; opening the second spinneret, adjusting the internal temperature to 180 ° C, spinning speed of 12 m / min, air flow (for example, compressed air
  • a composite hot melt adhesive web comprising a polyamide hot melt adhesive web and a polyolefin hot melt adhesive web film.
  • the polyamide hot melt adhesive has a DSC final melting point of 130 ° C and a melt flow rate of 45 g / 10min/160°C; the composition of the polyolefin hot melt adhesive used and the mass percentage of each component are:
  • a preparation process of a composite hot-melt adhesive web which is respectively melted by the above-mentioned polyamide hot melt adhesive and polyolefin hot melt adhesive, and pumped into mutually independent first spinneret and second spinneret; two spinnerets With a spacing of 1.1 m, the conveyor belt (for example, a steel belt) works to adjust the conveying speed to 17 m/min; the first spinneret is opened, the internal temperature is adjusted to 190 ° C, the spinning speed is 23 m / min, and the air flow (for example For a compressed air) speed of 115 m / min, the polyamide hot melt adhesive is spun from the first spinneret and under the traction of the air stream to the conveyor belt to form a reticulated membrane; the reticulated membrane passes through a first infrared heating zone at a temperature of 120 ° C Heating to form the first layer of the web; opening the second spinneret, adjusting the internal temperature to 210 ° C, the spinning
  • a composite hot melt adhesive mesh film which is composed of a polyamide hot melt adhesive mesh film and a polyolefin hot melt adhesive mesh film.
  • the polyamide hot melt adhesive used has a DSC final melting point of 124 ° C and a melt flow rate of 35 g / 10min/160°C; the composition of the polyolefin hot melt adhesive used and the mass percentage of each component are:
  • a preparation process of a composite hot-melt adhesive web which is respectively melted by the above-mentioned polyamide hot melt adhesive and polyolefin hot melt adhesive, and pumped into mutually independent first spinneret and second spinneret; two spinnerets
  • the distance between the conveyor belts is 1.3m, the conveyor belt (for example, steel wire belt) works, and the conveying speed is adjusted to 20m/min; the first spinneret is opened, the internal temperature is adjusted to 200 ° C, the spinning speed is 26 m / min, and the air flow (for example For compressed air) speed of 100m/min, the polyamide hot melt adhesive is spun from the first spinneret and pulled by the airflow to the conveyor belt to form a reticulated membrane; the reticulated membrane passes through a first infrared heating zone at a temperature of 110 °C.
  • Heating to form a first layer of web opening the second spinneret, adjusting the internal temperature to 230 ° C, spinning speed of 18 m / min, air flow (for example, compressed air) speed of 80 m / min, polyolefin hot melt adhesive Spinning from the second spinneret and under the traction of the airflow to the conveyor belt, and thermally recombining with the first layer of the reticulum, followed by heating through a second infrared heating zone at a temperature of 90 ° C to form a double-layered web; then cooled, Crystallization solidification, winding formation, final composite for bonding metals and non-polar materials Melt omentum products.
  • the hot melt adhesive web obtained in the above examples was bonded to the 180° peel strength of PE/aluminum, PP/aluminum, PE/stainless steel and PP/stainless steel at 160 ° C, 0.30 MPa and hot pressing for 120 s.
  • the specific test results are shown in the table below. 1:
  • the composite hot-melt adhesive web film prepared according to the invention has high bonding strength and long-lasting bonding stability, and is particularly suitable for metal materials such as stainless steel, aluminum, copper and the like, and polyethylene. Adhesive bonding of non-polar polymers such as polypropylene. Moreover, the preparation process proposed by the invention, from the raw material pretreatment to the final preparation of the hot melt adhesive mesh film product, is completed in a set production process, which can greatly reduce production failure, high production efficiency and low cost.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Adhesives Or Adhesive Processes (AREA)
  • Adhesive Tapes (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Laminated Bodies (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

一种复合热熔胶网膜及其制备工艺，特别是一种用于粘接金属与非极性材料用复合热熔胶网膜及其制备工艺，该网膜由极性的聚酰胺热熔胶和含有增容剂的非极性的聚烯烃热熔胶网膜复合而成，其粘接强度大，粘接持久稳定，特别适用于不锈钢、铝、铜等金属材料与聚乙烯、聚丙烯等非极性聚合物的粘接复合。同时，所述制备工艺从原料预处理到最后制成热熔胶网膜产品，均在一套生产流程中完成，可以大大减少生产故障，生产效率高，成本低。

Description

一种复合热熔胶网膜及其制备工艺 技术领域
本发明涉及一种复合热熔胶网膜及其制备工艺，特别是涉及一种用于粘接金属与非极性材料用的复合热熔胶网膜及其制备工艺，通过本发明所制得的复合热熔胶网膜，特别适用于不锈钢、铝、铜等金属材料与聚乙烯、聚丙烯等非极性聚合物的粘接复合。
背景技术
热熔胶网膜是一种耐腐蚀、耐老化、热稳定性好并具有良好的抗拉、抗顶破以及良好的透水性能的材料，因此广泛应用于服装、汽车、电子等行业。
CN 101240148 B提供了一种热熔胶网膜的制备方法，包括热熔胶原料的熔融，加入结晶成核剂，挤压，纺丝，气流牵伸，摆丝成网等工序，该专利特别涉及利用共聚酰胺热熔胶为原料制备热熔胶网膜。CN 101967733 B提供了一种热熔胶网膜的制备方法，通过控制热熔胶的熔融温度，喷丝速度，红外温度等，制备出孔径均匀，克重稳定的热熔胶网膜，该专利尤其涉及利用聚酯热熔胶为原料制备热熔胶网膜的方法。CN 103059792 B提供了一种用以粘接极性聚合物和金属材料的聚酯弹性体热熔胶及其制备方法。CN1699491A亦公开了一种热熔胶膜的制备方法，尤其适用于书画装裱用的双面热熔胶膜。
随着工业化的进展，越来越多的领域要求把极性材料与非极性材料粘接在一起，既可以降低成本，又可以扩大材料的应用领域。而目前常规的热熔胶相关产品，如网膜或胶膜基本上都是针对于粘接极性材料，对非极性材料的粘接性很差。
发明内容
本发明的目的在于克服现有技术的缺陷，提供一种复合热熔胶网膜及其制备工艺，通过本发明所制得的复合热熔胶网膜，其粘接强度大，粘接持久稳定，特别适用于不锈钢、铝、铜等金属材料与聚乙烯、聚丙烯等非极性聚合物的粘接复合。
本发明所采用的技术方案如下:
一种复合热熔胶网膜，由聚酰胺热熔胶网膜及聚烯烃热熔胶网膜复合而成，该聚酰胺热熔胶网膜所用聚酰胺热熔胶的DSC终熔点为116-130℃，熔体流动速率为30-50g/10min/160℃；该聚烯烃热熔胶网膜所用聚烯烃热熔胶的成分按质量百分比计，包括：增容剂8-15％，聚乙烯50-70％，其他聚烯烃3-10％，引发剂0.2-0.8％，硅烷偶联剂0.7-1.3％，增黏剂8-20％，无机填料1.0-10％，抗氧化剂0.4-0.8％；
上述增容剂选自马来酸酐接枝高密度聚乙烯、马来酸酐接枝低密度聚乙烯、马来酸酐接枝聚丙烯、马来酸酐接枝线性低密度聚乙烯中的一种，所述马来酸酐接枝率为0.8-1.2％；
上述聚乙烯选自高密度聚乙烯、低密度聚乙烯和线性低密度聚乙烯中的一种，其熔体流动速率为0.9-7g/10min/190℃；
上述其他聚烯烃选自乙烯-辛烯共聚物、聚丙烯、聚苯乙烯中的一种，其熔体流动速率为1.6-14g/10min/190℃；
上述引发剂选自过氧化苯甲酰、过氧化二叔丁基和偶氮二异丁腈中的一种；
上述硅烷偶联剂选自乙烯基三甲氧基硅烷和γ-氨基丙基三甲氧基硅烷中的一种；
上述增黏剂选自松香145、萜烯树脂和氢化碳五树脂中的一种；
上述无机填料选自滑石粉、高岭土和纳米碳酸钙中的一种；
上述抗氧化剂选自抗氧化剂1010、抗氧化剂BHT和抗氧化剂264中的一种。
一种复合热熔胶网膜的制备工艺，选取上述复合热熔胶所用的聚酰胺热熔胶及聚烯烃热熔胶作为原料，进行下述步骤处理：
(1)分别将聚酰胺热熔胶、聚烯烃热熔胶熔融后泵入到两个独立的第一喷丝板和第二喷丝板内；
(2)上述聚酰胺热熔胶经第一喷丝板在第一气流的牵引下以第一预设速度喷丝到传送带上，然后经过第一红外加热区加热，形成第一层网膜；
(3)上述聚烯烃热熔胶经第二喷丝板在第二气流的牵引下以第二预设速度喷丝丝到传送带上，并趁热与第一层网膜复合，然后经过第二红外加热区加热，形成双层复合网膜；
(4)上述双层复合网膜经冷却、结晶固化、收卷，形成热熔胶网膜产品；
上述第一喷丝板的温度小于上述第二喷丝板的温度，上述第一喷丝板的温度为170-210℃，第二喷丝板的温度范围为180-230℃；
上述第一预设速度大于第二预设速度，第一预设速度为15-30m/min，第二预设速度为10-25m/min；
上述第一气流速度大于第二气流速度，第一气流及第二气流的速度范围为30-120m/min；
上述第一红外加热区的温度高于所述第二红外加热区的温度，第一红外加热区温度为90-120℃，第二红外加热区温度为60-90℃；
上述传送带的速度为12-20m/min，第一喷丝板与第二喷丝板之间的距离为0.7-1.3m。
本发明的有益效果：本发明所提出的复合热熔胶网膜及其制备工艺，由于采用了特定的配方，使得极性的聚酰胺热熔胶和含有增容剂的非极性的聚 烯烃有效熔融，根据本发明所制得的复合热熔胶网膜，其粘接强度大，粘接持久稳定，特别适用于不锈钢、铝、铜等金属材料与聚乙烯、聚丙烯等非极性聚合物的粘接复合。同时，本发明所提出的制备工艺，从原料预处理到最后制成热熔胶网膜产品，均在一套生产流程中完成，可以大大减少生产故障，生产效率高，成本低。
附图说明
图1为本发明所提出的制备工艺流程图。
具体实施方式
实施例1
一种复合热熔胶网膜，由聚酰胺热熔胶网膜及聚烯烃热熔胶网膜复合而成，所用聚酰胺热熔胶在差示扫描量热法(Differential Scanning Calorimetry,DSC)下测得的DSC终熔点为122℃，熔体流动速率为30g/10min/160℃；所用聚烯烃热熔胶的组分及各组分的质量百分比为：
Figure PCTCN2015097640-appb-000001
一种复合热熔胶网膜的制备工艺，分别将上述聚酰胺热熔胶和聚烯烃热 熔胶熔融后泵入到相互独立的第一喷丝板和第二喷丝板；两喷丝板均设于传送带的上方，且沿传送带的传送方向，第二喷丝板位于第一喷丝板的下游，两喷丝板之间间距0.7m，传送带(例如为钢丝带)工作，调整其传送速度为12m/min；开启第一喷丝板，调整其内温度为170℃，将气流(例如为压缩空气)速度调整为120m/min，从而在气流牵引以及喷丝板的出料压力的作用下使得喷丝速度为20m/min，聚酰胺热熔胶从第一喷丝板并在气流牵引下喷丝到传送带形成网状膜；该网状膜经过温度为100℃的第一红外加热区加热，形成第一层网膜，所述第一红外加热区例如可位于两喷丝板之间的某个合适位置；开启第二喷丝板，调整其内温度为180℃，气流(例如为压缩空气)速度为85m/min，从而喷丝速度为12m/min，聚烯烃热熔胶从第二喷丝板并在气流牵引下喷丝到传送带，并与传送至第二喷丝板处的第一层网膜趁热复合，随后经过温度为60℃的第二红外加热区加热形成双层网膜，所述第二红外加热区例如可位于第二喷丝板的下游；然后经冷却、结晶固化，收卷形成最终用于粘接金属与非极性材料用的复合热熔胶网膜产品。
根据实施例配方及制备工艺所得产品标记为A。
实施例2
一种复合热熔胶网膜，由聚酰胺热熔胶网膜及聚烯烃热熔胶网膜复合而成，所用聚酰胺热熔胶的DSC终熔点为116℃，熔体流动速率为50g/10min/160℃；所用聚烯烃热熔胶的组分及各组分的质量百分比为：
Figure PCTCN2015097640-appb-000002
Figure PCTCN2015097640-appb-000003
一种复合热熔胶网膜的制备工艺，分别将上述聚酰胺热熔胶和聚烯烃热熔胶熔融后泵入到相互独立的第一喷丝板和第二喷丝板；两喷丝板之间间距0.7m，传送带(例如为钢丝带)工作，调整其传送速度为12m/min；开启第一喷丝板，调整其内温度为170℃，喷丝速度为20m/min，气流(例如为压缩空气)速度为120m/min，聚酰胺热熔胶从第一喷丝板并在气流牵引下喷丝到传送带形成网状膜；该网状膜经过温度为100℃的第一红外加热区加热，形成第一层网膜；开启第二喷丝板，调整其内温度为180℃，喷丝速度为12m/min，气流(例如为压缩空气)速度为85m/min，聚烯烃热熔胶从第二喷丝板并在气流牵引下喷丝到传送带，并与第一层网膜趁热复合，随后经过温度为60℃的第二红外加热区加热形成双层网膜；然后经冷却、结晶固化，收卷形成最终用于粘接金属与非极性材料用的复合热熔胶网膜产品。
根据实施例配方及制备工艺所得产品标记为B。
实施例3
一种复合热熔胶网膜，由聚酰胺热熔胶网膜及聚烯烃热熔胶网膜复合而成，所用聚酰胺热熔胶的DSC终熔点为130℃，熔体流动速率为45g/10min/160℃；所用聚烯烃热熔胶的组分及各组分的质量百分比为：
Figure PCTCN2015097640-appb-000004
Figure PCTCN2015097640-appb-000005
一种复合热熔胶网膜的制备工艺，分别将上述聚酰胺热熔胶和聚烯烃热熔胶熔融后泵入到相互独立的第一喷丝板和第二喷丝板；两喷丝板之间间距1.1m，传送带(例如为钢丝带)工作，调整其传送速度为17m/min；开启第一喷丝板，调整其内温度为190℃，喷丝速度为23m/min，气流(例如为压缩空气)速度为115m/min，聚酰胺热熔胶从第一喷丝板并在气流牵引下喷丝到传送带形成网状膜；该网状膜经过温度为120℃的第一红外加热区加热，形成第一层网膜；开启第二喷丝板，调整其内温度为210℃，喷丝速度为16m/min，气流(例如为压缩空气)速度为90m/min，聚烯烃热熔胶从第二喷丝板并在气流牵引下喷丝到传送带，并与第一层网膜趁热复合，随后经过温度为80℃的第二红外加热区加热形成双层网膜；然后经冷却、结晶固化，收卷形成最终用于粘接金属与非极性材料用的复合热熔胶网膜产品。
根据实施例配方及制备工艺所得产品标记为C。
实施例4
一种复合热熔胶网膜，由聚酰胺热熔胶网膜及聚烯烃热熔胶网膜复合而成，所用聚酰胺热熔胶的DSC终熔点为124℃，熔体流动速率为35g/10min/160℃；所用聚烯烃热熔胶的组分及各组分的质量百分比为：
Figure PCTCN2015097640-appb-000006
Figure PCTCN2015097640-appb-000007
一种复合热熔胶网膜的制备工艺，分别将上述聚酰胺热熔胶和聚烯烃热熔胶熔融后泵入到相互独立的第一喷丝板和第二喷丝板；两喷丝板之间间距1.3m，传送带(例如为钢丝带)工作，调整其传送速度为20m/min；开启第一喷丝板，调整其内温度为200℃，喷丝速度为26m/min，气流(例如为压缩空气)速度为100m/min，聚酰胺热熔胶从第一喷丝板并在气流牵引下喷丝到传送带形成网状膜；该网状膜经过温度为110℃的第一红外加热区加热，形成第一层网膜；开启第二喷丝板，调整其内温度为230℃，喷丝速度为18m/min，气流(例如为压缩空气)速度为80m/min，聚烯烃热熔胶从第二喷丝板并在气流牵引下喷丝到传送带，并与第一层网膜趁热复合，随后经过温度为90℃的第二红外加热区加热形成双层网膜；然后经冷却、结晶固化，收卷形成最终用于粘接金属与非极性材料用的复合热熔胶网膜产品。
根据实施例配方及制备工艺所得产品标记为D。
性能测试
考察上述实施例得到的热熔胶网膜在160℃、0.30MPa、热压120s粘接PE/铝、PP/铝、PE/不锈钢、PP/不锈钢的180°剥离强度，具体测试结果见下表1：
Figure PCTCN2015097640-appb-000008
表1热熔胶网膜对不同基材的粘接强度
从上表中，可明显看出：根据本发明所制得的复合热熔胶网膜，其粘接强度大，粘接持久稳定，特别适用于不锈钢、铝、铜等金属材料与聚乙烯、聚丙烯等非极性聚合物的粘接复合。且本发明所提出的制备工艺，从原料预处理到最后制成热熔胶网膜产品，均在一套生产流程中完成，可以大大减少生产故障，生产效率高，成本低。

Claims (13)

  1. 一种复合热熔胶网膜，其特征在于，由聚酰胺热熔胶网膜及聚烯烃热熔胶网膜复合而成，其中，所述聚酰胺热熔胶网膜所用的聚酰胺热熔胶的DSC终熔点为116-130℃，熔体流动速率为30g/10min/160℃至50g/10min/160℃；所述聚烯烃热熔胶网膜所用的聚烯烃热熔胶的成分按质量百分比计，包括：增容剂8-15％，聚乙烯50-70％，其他聚烯烃3-10％，引发剂0.2-0.8％，硅烷偶联剂0.7-1.3％，增黏剂8-20％，无机填料1.0-10％，抗氧化剂0.4-0.8％。
  2. 如权利要求1所述的复合热熔胶网膜，其特征在于，所述增容剂选自马来酸酐接枝高密度聚乙烯、马来酸酐接枝低密度聚乙烯、马来酸酐接枝聚丙烯、马来酸酐接枝线性低密度聚乙烯中的一种，且马来酸酐接枝率为0.8-1.2％。
  3. 如权利要求1所述的复合热熔胶网膜，其特征在于，所述聚乙烯选自高密度聚乙烯、低密度聚乙烯和线性低密度聚乙烯中的一种，其熔体流动速率为0.9g/10min/190℃至7g/10min/190℃。
  4. 如权利要求1所述的复合热熔胶网膜，其特征在于，所述其他聚烯烃选自乙烯-辛烯共聚物、聚丙烯、聚苯乙烯中的一种，其熔体流动速率为1.6g/10min/190℃至14g/10min/190℃。
  5. 如权利要求1所述的复合热熔胶网膜，其特征在于，所述引发剂选自过氧化苯甲酰、过氧化二叔丁基和偶氮二异丁腈中的一种。
  6. 如权利要求1所述的复合热熔胶网膜，其特征在于，所述无机填料选自滑石粉、高岭土和纳米碳酸钙中的一种。
  7. 一种复合热熔胶网膜的制备工艺，其特征在于，将权利要求1～6任一项所述的复合热熔胶网膜所用的聚酰胺热熔胶及聚烯烃热熔胶作为原料，进行下述步骤处理：
    (1)分别将聚酰胺热熔胶、聚烯烃热熔胶熔融后泵入到两个独立的第一喷丝板和第二喷丝板内；
    (2)所述聚酰胺热熔胶经第一喷丝板在第一气流的牵引下以第一预设速度喷丝到传送带上，然后经过第一红外加热区加热，形成第一层网膜；
    (3)所述聚烯烃热熔胶经第二喷丝板在第二气流的牵引下以第二预设速度喷丝到所述传送带上，并趁热与第一层网膜复合，然后经过第二红外加热区加热，形成双层复合网膜；
    (4)所述双层复合网膜经冷却、结晶固化、收卷，形成热熔胶网膜产品。
  8. 如权利要求7所述的复合热熔胶网膜的制备工艺，其特征在于，所述第一喷丝板的温度小于所述第二喷丝板的温度，所述第一预设速度大于所述第二预设速度，所述第一气流速度大于所述第二气流速度，所述第一红外加热区的温度高于所述第二红外加热去的温度。
  9. 如权利要求8所述的复合热熔胶网膜的制备工艺，其特征在于，所述第一喷丝板的温度为170-210℃，所述第二喷丝板的温度范围为180-230℃。
  10. 如权利要求8所述的复合热熔胶网膜的制备工艺，其特征在于，所述第一预设速度为15-30m/min，所述第二预设速度为10-25m/min。
  11. 如权利要求8所述的复合热熔胶网膜的制备工艺，其特征在于，所述第一气流及第二气流的速度范围为30-120m/min。
  12. 如权利要求8所述的复合热熔胶网膜的制备工艺，其特征在于，所述第一红外加热区温度为90-120℃，第所述二红外加热区温度为60-90℃。
  13. 如权利要求7所述的复合热熔胶网膜的制备工艺，其特征在于，所述第一喷丝板及所述第二喷丝板之间的距离为0.7-1.3m，所述传送带的传送速度为12-20m/min。
PCT/CN2015/097640 2014-12-19 2015-12-16 一种复合热熔胶网膜及其制备工艺 Ceased WO2016095823A1 (zh)

Priority Applications (4)

Application Number Priority Date Filing Date Title
CH00792/17A CH712138B1 (de) 2014-12-19 2015-12-16 Verbund-Heissschmelz-Klebenetzfilm und Herstellungsverfahren desselben.
KR1020177020144A KR101937389B1 (ko) 2014-12-19 2015-12-16 복합 고온 용융 접착성 메쉬 필름 및 이를 제조하는 방법
DE112015005639.4T DE112015005639T5 (de) 2014-12-19 2015-12-16 Verbund-heissschmelz-klebenetzfilm und herstellungsverfahren desselben
US15/537,305 US10472547B2 (en) 2014-12-19 2015-12-16 Composite hot-melt adhesive net film and manufacturing process thereof

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
CN201410795228 2014-12-19
CN201410795228.4 2014-12-19
CN201510106668.9 2015-03-12
CN201510106668.9A CN104711772B (zh) 2014-12-19 2015-03-12 一种复合热熔胶网膜及其制备工艺

Publications (1)

Publication Number Publication Date
WO2016095823A1 true WO2016095823A1 (zh) 2016-06-23

Family

ID=53411475

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2015/097640 Ceased WO2016095823A1 (zh) 2014-12-19 2015-12-16 一种复合热熔胶网膜及其制备工艺

Country Status (6)

Country Link
US (1) US10472547B2 (zh)
KR (1) KR101937389B1 (zh)
CN (1) CN104711772B (zh)
CH (1) CH712138B1 (zh)
DE (1) DE112015005639T5 (zh)
WO (1) WO2016095823A1 (zh)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE202016103409U1 (de) 2016-06-28 2017-09-29 Rehau Ag + Co Kantenleiste für Möbelstücke
CN108178995B (zh) * 2017-12-26 2020-06-23 上海邦中高分子材料有限公司 一种高阻隔瓶用粘接树脂及其制备方法
CN110229635A (zh) * 2018-03-05 2019-09-13 张文耀 可贴附于对象上的整合硅片及其制造方法
CN110699013B (zh) * 2019-11-04 2021-03-23 巢进化学(上海)有限公司 一种用于粘结金属与塑料的热熔胶及其制备方法
CN112895653B (zh) * 2019-11-19 2023-07-25 天洋新材(上海)科技股份有限公司 一种交联改性共聚酰胺热熔胶网膜及其制备和使用方法
CN113527784B (zh) * 2020-04-14 2022-12-09 中国石油化工股份有限公司 用于土工膜表面加糙的复合材料和糙面土工膜及各自的制备方法
CN111925538B (zh) * 2020-06-22 2021-03-16 常州百佳年代薄膜科技股份有限公司 纳米级胶膜微片段、自增强胶膜、制备工艺、光伏组件
CN112210312A (zh) * 2020-09-19 2021-01-12 江苏惠沣环保科技有限公司 一种粘合pp材质的热熔胶膜制备工艺及装置
CN115873519B (zh) * 2022-12-30 2023-07-07 广州鹿山新材料股份有限公司 铝蜂窝板用粘接胶膜及其制备方法、铝蜂窝板及其应用

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6042902A (en) * 1997-10-20 2000-03-28 Hoechst Celanese Corporation Adhesives for making multilayer films comprising liquid crystalline polymers and poly(ethylene terephthalate) or polycarbonate
CN101429413A (zh) * 2008-11-18 2009-05-13 广州市鹿山化工材料有限公司 一种金属与塑料粘接的双层复合热熔胶膜
CN101463243A (zh) * 2009-01-15 2009-06-24 上海天洋热熔胶有限公司 网膜用聚酰胺热熔胶及其制备方法
CN101967733A (zh) * 2010-09-02 2011-02-09 上海天洋热熔胶有限公司 一种热熔胶网膜的制备方法

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1427056A (zh) * 2001-12-10 2003-07-02 方大集团股份有限公司 复合热熔胶膜
CN1401721A (zh) * 2002-09-06 2003-03-12 广州市鹿山化工材料有限公司 一种聚烯烃热熔胶粘剂及使用该热熔胶粘剂的复合结构胶片
US20050003197A1 (en) 2003-07-03 2005-01-06 Good David J. Hot melt adhesive
JP2006111256A (ja) 2004-09-17 2006-04-27 Eidai Kako Kk 吸音マット及びその製造方法
CN100513504C (zh) 2005-05-27 2009-07-15 庄廷生 一种双面热熔胶膜及其制备工艺
CN101240148B (zh) 2008-02-21 2012-02-22 上海天洋热熔胶有限公司 热熔胶网膜的制备方法
JP5342803B2 (ja) 2008-04-15 2013-11-13 永大化工株式会社 マット及びその製造方法
CN201745183U (zh) * 2010-05-14 2011-02-16 上海天洋热熔胶有限公司 一种热熔胶网膜成型、传送及收卷装置
CN102441973A (zh) * 2011-08-17 2012-05-09 东莞市雄林新材料科技有限公司 一种热熔胶贴合tpu的生产工艺
CN102505346A (zh) * 2011-11-14 2012-06-20 成都彩虹环保科技有限公司 多组分复合纤维的无纺布制造装置
CN103059792B (zh) 2012-12-25 2014-08-20 广州鹿山新材料股份有限公司 一种用于粘接极性聚合物和金属材料的聚酯弹性体热熔胶及其制备方法

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6042902A (en) * 1997-10-20 2000-03-28 Hoechst Celanese Corporation Adhesives for making multilayer films comprising liquid crystalline polymers and poly(ethylene terephthalate) or polycarbonate
CN101429413A (zh) * 2008-11-18 2009-05-13 广州市鹿山化工材料有限公司 一种金属与塑料粘接的双层复合热熔胶膜
CN101463243A (zh) * 2009-01-15 2009-06-24 上海天洋热熔胶有限公司 网膜用聚酰胺热熔胶及其制备方法
CN101967733A (zh) * 2010-09-02 2011-02-09 上海天洋热熔胶有限公司 一种热熔胶网膜的制备方法

Also Published As

Publication number Publication date
DE112015005639T5 (de) 2017-09-07
CN104711772A (zh) 2015-06-17
CH712138B1 (de) 2018-07-31
KR20170098267A (ko) 2017-08-29
CN104711772B (zh) 2018-02-27
KR101937389B1 (ko) 2019-01-10
US10472547B2 (en) 2019-11-12
US20170349792A1 (en) 2017-12-07

Similar Documents

Publication Publication Date Title
WO2016095823A1 (zh) 一种复合热熔胶网膜及其制备工艺
CN100534787C (zh) 一种纸塑无胶复合用双向拉伸聚丙烯薄膜及其制备方法
CN104772956B (zh) 一种轻量包装膜及其制备方法
CN113621204B (zh) 一种bopp双面热封镭射防伪基膜及其制备方法
CN101704308A (zh) 聚烯烃三层复合微孔膜及其制备方法
CN106739347B (zh) 一种具有多层仿生形态的高分子材料及其制备方法
CN105172299B (zh) 蒸煮膜制作方法
CN115891354A (zh) 一种高光泽高层间牢度的铝塑片材及其制备方法
CN102873950A (zh) 一种高表面能的双向拉伸聚丙烯薄膜及其制造方法
CN106273972A (zh) 一种高剥离强度的bopp预涂膜及其制备方法
CN115122740A (zh) 一种阻隔性热熔胶膜及其制备方法
CN112895653B (zh) 一种交联改性共聚酰胺热熔胶网膜及其制备和使用方法
CN102950858A (zh) 一种热封型双向拉伸聚丙烯镀铝基膜及其制造方法
CN113071179A (zh) 高阻隔带拉伸膜及其生产方法
CN104480637B (zh) 一种热熔胶网膜的制备工艺
CN105773989A (zh) 一种塑料薄膜的制备工艺
CN204725965U (zh) 一种防水卷材用耐高温离型复合膜
CN110385905A (zh) 一种含有双保护核心阻隔层的叠层共挤膜及其生产工艺
CN107415191B (zh) 一种聚丙烯/聚乙烯/聚丙烯多层膜的制备方法
CN110964451B (zh) 一种铝箔胶带加工工艺
JPS59215833A (ja) 超高分子量ポリエチレン多孔質フイルムの製造方法
CN115871302A (zh) 一种新能源电池铝塑膜用的流延聚丙烯复合膜及制备方法
CN211710252U (zh) 一种聚酰胺复合薄膜和易于冲压成型的铝塑复合膜
CN117924826A (zh) 珠光膜用聚丙烯组合物及其制备方法与应用、聚丙烯珠光膜
CN106003995A (zh) 一种塑料薄膜的制备工艺

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 15869330

Country of ref document: EP

Kind code of ref document: A1

WWE Wipo information: entry into national phase

Ref document number: 15537305

Country of ref document: US

WWE Wipo information: entry into national phase

Ref document number: 112015005639

Country of ref document: DE

Ref document number: 10201700000792

Country of ref document: CH

ENP Entry into the national phase

Ref document number: 20177020144

Country of ref document: KR

Kind code of ref document: A

122 Ep: pct application non-entry in european phase

Ref document number: 15869330

Country of ref document: EP

Kind code of ref document: A1