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WO1991014727A1 - Cross-linkable adhesive composition - Google Patents

Cross-linkable adhesive composition Download PDF

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Publication number
WO1991014727A1
WO1991014727A1 PCT/EP1991/000577 EP9100577W WO9114727A1 WO 1991014727 A1 WO1991014727 A1 WO 1991014727A1 EP 9100577 W EP9100577 W EP 9100577W WO 9114727 A1 WO9114727 A1 WO 9114727A1
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WO
WIPO (PCT)
Prior art keywords
composition according
ethylene
copolymer
blocked
polymer
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/EP1991/000577
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French (fr)
Inventor
Gerald Marie Vanhaeren
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.)
ExxonMobil Chemical Ltd
ExxonMobil Chemical Patents Inc
Original Assignee
Exxon Chemical Ltd
Exxon Chemical Patents Inc
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Publication of WO1991014727A1 publication Critical patent/WO1991014727A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J175/00Adhesives based on polyureas or polyurethanes; Adhesives based on derivatives of such polymers
    • C09J175/04Polyurethanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/4009Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
    • C08G18/4063Mixtures of compounds of group C08G18/62 with other macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/62Polymers of compounds having carbon-to-carbon double bonds
    • C08G18/6204Polymers of olefins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/62Polymers of compounds having carbon-to-carbon double bonds
    • C08G18/6212Polymers of alkenylalcohols; Acetals thereof; Oxyalkylation products thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/62Polymers of compounds having carbon-to-carbon double bonds
    • C08G18/6216Polymers of alpha-beta ethylenically unsaturated carboxylic acids or of derivatives thereof
    • C08G18/622Polymers of esters of alpha-beta ethylenically unsaturated carboxylic acids
    • C08G18/6225Polymers of esters of acrylic or methacrylic acid
    • C08G18/6229Polymers of hydroxy groups containing esters of acrylic or methacrylic acid with aliphatic polyalcohols
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/77Polyisocyanates or polyisothiocyanates having heteroatoms in addition to the isocyanate or isothiocyanate nitrogen and oxygen or sulfur
    • C08G18/78Nitrogen
    • C08G18/79Nitrogen characterised by the polyisocyanates used, these having groups formed by oligomerisation of isocyanates or isothiocyanates
    • C08G18/791Nitrogen characterised by the polyisocyanates used, these having groups formed by oligomerisation of isocyanates or isothiocyanates containing isocyanurate groups
    • C08G18/792Nitrogen characterised by the polyisocyanates used, these having groups formed by oligomerisation of isocyanates or isothiocyanates containing isocyanurate groups formed by oligomerisation of aliphatic and/or cycloaliphatic isocyanates or isothiocyanates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/80Masked polyisocyanates
    • C08G18/8061Masked polyisocyanates masked with compounds having only one group containing active hydrogen
    • C08G18/807Masked polyisocyanates masked with compounds having only one group containing active hydrogen with nitrogen containing compounds
    • C08G18/8074Lactams
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2170/00Compositions for adhesives
    • C08G2170/20Compositions for hot melt adhesives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2666/00Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
    • C08L2666/02Organic macromolecular compounds, natural resins, waxes or and bituminous materials
    • C08L2666/26Natural polymers, natural resins or derivatives thereof according to C08L1/00 - C08L5/00, C08L89/00, C08L93/00, C08L97/00 or C08L99/00

Definitions

  • This invention relates to cross-linkable compositions which may be applied as a film or as a melt and subsequently cured at a temperature above the application temperature.
  • Hot melt adhesives based on ethylene-vinyl acetate copolymers are known. Although effective for certain applications, they fail in certain assembly applications due to their poor cohesive properties at temperatures of above about 60°C. In these cases, the bond strength develops on cooling but the cohesive properties are always limited at a given temperature due to the thermoplastic nature of the hot melt components.
  • compositions capable of providing high adhesion with good heat resistance are suggested in Japanese Patent Publication 58-217575 (Yunichika) which discloses a hot-melt adhesive comprising firstly a saponified ethylene/vinyl acetate copolymer, secondly a polyisocyanate having at least two masked isocyanate groups per molecule and thirdly, a terpene phenol resin and/or a liquid polybutadiene having at least two hydroxyl groups per molecule.
  • the reactive copolymer may have a melt flow index as from 0.5 to 200.
  • the saponified EVA has 10 mol % of vinyl alcohol units and has a melt index of 170 in the example 1.
  • a wide variety of masking agents are disclosed.
  • EP 30594 (Bayer) discloses a coating powder containing hydrolysed vinyl acetate copolymer and polyuretonimines obtained by reaction of polycarbodiimides and di- and tri-isocyanates.
  • GB 1079749 describes a cross-linkable coating composition (for moulding into pipes and hoses and for cables and wires for example) not as such suitable for hot melt adhesive compositions containing a polymer of a monoethylenically unsaturated monomer and units having certain functional groups a.o. hydroxyl, and a polyisocyanate generator including aromatic internally blocked isocyanates such as specified uretidione aromatic dimers and alkylene uretidione dimers in general.
  • the blocked products have a rate of decomposition varying with temperature which causes cross-linking at temperatures above 120°C.
  • EP-A-0041.192 (Siemens) describes the production of crosslinked polyolefin based cable and wire insulation and sheet production by crosslinking hydroxyl containing polyolefin with blocked polyisocyanate.
  • EP-A-0294.271 (Atochem) describes a crosslinkable adhesive composition based on ethylene vinyl acetate copolymer containing primary hydroxyl functionalities.
  • the terpolymer is obtained by introducing, by grafting or direct copolymerization, an ethylenic monomer containing a primary hydroxyl such as 2-hydroxy ethyl acrylate or methacrylate.
  • the copolymer contains from 0.02 to 0.15 moles of primary hydroxyl per 100 gms.
  • the adhesive composition also contains a blocked polyisocyanate and a tackifying resin which may be used as blocking agent of the polyisocyanate.
  • the preferred polyisocyanates are diisocyanates such as toluene diisocyanate, diphenylmethane diisocyanate, hexamethylene diisocyanate or isophorone diisocyanate.
  • EP-A-0302.620 discloses the use of saponified EVA's having at least 5 % wt % of vinyl alcohol derived units (14.75 wt % and 10 wt % in Examples) cured with an internally blocked polyisocyanate in the presence of a viscosity reducing component.
  • the saponified EVA may have a viscosity of from 1 to 100 Pa.s, preferably 4 to 40 Pa.s, at 180°C and have a preferred melt flow index of from 10 to 2500.
  • Japanese Patent publication 4640419 (Miura) relates to heat reactive, heat sensitive elastomer composition in which saponified EVA is crosslinked by an isocyanate adduct including lactam derivatives with a decomposition promoter.
  • Example 1 uses an EVA with 11.2 wt % of vinyl alcohol derived units. Phenol adducts are used in the Examples which release volatile phenols in use.
  • thermoplastic adhesive composition comprising:
  • ingredients such as carbon black, and fillers such as calcium carbonate and silicates can also be added to impart particular properties to the compound.
  • the copolymer (a) is a polymer having monomeric units of ethylene and of vinyl alcohol, and optionally vinyl acetate, the melt viscosity being from 1 to 50 Pa.s at 180°C, preferably from 3 to 40 Pa.s at 180°C.
  • Ethylene vinyl alcohol copolymers contain at least 0.10 mole of hydroxyl functionality per 100 gm of copolymer (or 4.4 wt% vinyl alcohol), preferably at least 0.16 mole OH per 100 gm of copolymer (or 7.0 wt% vinyl alcohol units).
  • One example is a terpolymer (viscosity 25 Pa.s at 180°C, MFR at 125°C under 325 gm load of 6.4 gm/10 min.) with 10 % vinyl alcohol (or 0.227 moles per 100 gms), 88.75 % ethylene and 1.2 wt% vinyl acetate.
  • the m.p. is 101.5°C (by DSC).
  • Another terpolymer contains 13.7 wt% vinyl alcohol (or 0.311 mole per 100 gms), 82.3 % ethylene and 4.0 wt% vinyl acetate (viscosity 5.8 Pa.s at 180°C, MFR at 125°C under 325 gm of 30.4 gm/10 min., DSC m.p. 91°C). Copolymers of the above stated type help to provide a suitable characteristic to the hot melt adhesive compostion.
  • copolymers including those referred to above may be copolymers of ethylene and vinyl alcohol obtained by hydrolysis or transesterification of ethylene-vinyl carboxylate (e.g. ethylene-vinyl acetate) copolymer.
  • the degree of hydrolysis can be partial or total, partial hydrolysis leaving some ester groups in the polymer.
  • the carboxylic acid from which the carboxylate is derived has from 1 to 6 carbon atoms per molecule and the especially preferred vinyl carboxylate from which the vinyl alcohol is derived is vinyl acetate.
  • the transesterification may be effected by reaction in the melt stage at about 100oC with, for example, n-butanol using sodium methylate as a catalyst.
  • the preferred copolymers of ethylene and vinyl alcohol are obtained from ethylene vinyl acetate copolymers having a melt flow index (ASTM D1238 52 T) of 250 to 3000, preferably from 400 to 2000, and comprise preferably at least 70 wt % of ethylene and at least 7 wt % of vinyl alcohol units.
  • the copolymer (a) containing hydroxyl functionality may also be a copolymer of ethylene and 2-hydroxyethyl acrylate or methacrylate.
  • Such copolymers can be obtained by polymerization of ethylene in presence of the hydroxyalkylacrylate at high pressure and temperature and using an appropriate peroxide or perester as initiator.
  • the desired polymer viscosity or melt flow rate can be obtained by using known molecular weight modifiers.
  • the second component (b) of the adhesive composition is a mixture containing trimeric isocyanurate groups and at least two terminally blocked isocyanate groups. It contains at least 10 wt% of isocyanurate derived from an aliphatic or cycloaliphatic diisocyanate, and di-, tri-, tetra-, penta- and possibly hexaisocyanates as a mixture.
  • the isocyanate groups are blocked with an extraneous blocking agent which is released on heating.
  • the polyisocyanate has no free isocyanate groups and the rate of unblocking and hence crosslinking can be varied by controlling curing temperature.
  • the isocyanate By being blocked or masked, the isocyanate can be protected from reacting with the alcohol functions of the copolymer and reactive groups of the third component until the decomposition temperature of the blocked polyisocyanate is reached.
  • the blocked polyisocyanate may contain other groups than the blocked isocyanates which do not dissociate on heating. Aliphatic or cycloaliphatic polyisocyanates are preferred.
  • the blocked polyisocyanate compound is used at a mole ratio OH:NCO of from 4 to 16; especially from 8 to 16 and especially above 10. Good compositions can be obtained using lower amounts of cross-linking agent. Isocyanurate derivatives are used advantageously because they can contain more than two blocked isocyanate groups per molecule.
  • Typical compounds suitable for the invention are :
  • the blocking agent can be lactam, such as ⁇ -caprolactam or -valerolactams or ⁇ -butyrolactam,preferably ⁇ - caprolactam.
  • IPDI B 1530 A product particularly useful for the invention and believed to have the composition shown above, is marketed by Chemische Werke Huls AG as IPDI B 1530. It is based on 3-isocyanatomethyl-3,3,5-trimethyl- cyclohexylisocyanate also called isophorone diisocyanate and abbreviated as IPDI, it contains approximately 15 wt% of blocked isocyanate.
  • the blocking agent is
  • the adhesive composition may contain a third component, and optionally further components, to decrease the viscosity of the formulation at temperatures below the curing temperature to facilitate handling, to preferably act as an adhesion promoter or to alter the physical properties of the cured compound such as providing a different modulus.
  • the optional third component of the film or hot melt composition is an hydrocarbon tackifier resin such as the Escorez (Registered Trade Mark) resins commercialised by Exxon Chemical International or synthetic or natural terpene tackifiers.
  • a low molecular weight polyhydroxy compound may optionally also be added.
  • Suitable polyhydroxy compounds are tri-, or tetra- functional polyether polyols used in the manufacture of polyurethanes. It has been found that a particularly suitable polyether is a 300 gm/mole molecular weight adduct of propylene oxide and glycerol (hydroxyl number 56 mgr KOH/gr). Low molecular weight polypropylene oxide polyols are well known and are commercially available. In preparing the film or hot melt adhesive composition, the blocked polyisocyanate should be mixed at a temperature below that at which the isocyanate begins to unblock to an appreciable extent. Temperatures from 120 to 130°C have been found adequate when using IPDI B 1530.
  • typical quantities of the components are 40 to 90 wt %, preferably 50 to 75 weight % of the ethylene copolymer, 10 to 60 weight %, preferably 25 to 50 weight % of the tackifying resin based on the total weight of the two components.
  • typical quantities of the polyhydroxy compound are 1 to 10 weight percent of the total weight of the three components.
  • composition containing only the ethylene copolymer and the blocked polyisocyanate can be processed and applied as a film
  • the composition containing the ethylene copolymer, the blocked polyisocyanate and the tackifying resin and optionally the low molecular weight polyhydroxy compound can be applied as a film or as a hot melt, both at a temperature below which appreciable heat activation of the blocked polyisocyanate takes place, and cured after application by heating to a temperature where the blocked polyisocyanate unblocks sufficiently quickly.
  • temperatures in the range 150°C to 200°C are adequate.
  • Table 1 sets ethylene copolymers A, B, C, D used for making formulations of the examples, their composition, melting peak temperature as determined by differential scanning calorimetry, melt viscosity (Brookfield viscometer RV, Thermosel), and melt flow rate at 125°C, 325 gm load.
  • the formulations given in Table 2 consist of the ethylene copolymers A, B or C and IPDI B 1530 mixed in a laboratory scale mixer by melting the ethylene copolymer first at 130°C, and introducing the IPDI B 1530 which was mixed for typically 6 minutes.
  • the mixtures were then pressed to form a 0.1-0.2 mm thick film, which was then applied between 0.09 mm aluminum foils as a substrate.
  • the assembly was placed in a heated press at 180°C for 30 minutes under a pressure of 1-5 kg/cm 2 so as to produce an adhesive layer of 60 to 130 microns depending on the viscosity of the polymer used.
  • the adhesion T-peel strength, lap shear strength at 100°C and 150°C and Peel Adhesion Failure Temperature (PAFT) were measured and the results are given in Table 3 for the different compositions.
  • the T-peel strength was determined using a tensometer at a pulling speed of 5.08 cm per minute and a 2 cm wide strip specimen.
  • the lap shear strength was determined on a 2.54 cm x 2.54 cm bond area, and an adhesive layer about 10 micron thick, using a tensometer at a pulling speed of 5.08 cm per minute.
  • the tensometer was equipped with a heated chamber and the tests were carried out at 100°C and 150°C.
  • the Peel Adhesion Failure Temperature was carried out using a 2.5 cm wide and 2.5 cm long adhesive bond in the T-peel mode and 0.5 kg load. The temperature was raised continuously at 24°C per hour rate. PAFT is the temperature at which the bond failed. Tests carried out on the ethylene copolymer alone, or on the compositions of Table 2 before heating at 180°C for 30 minutes indicated less than 2N/2cm adhesion T-peel strength.
  • compositions given in Table 2 give after cure rubber-like stress-strain behavior, the cured compositions exhibit high tensile strength, high elongation and high energy at break, significantly higher than the uncured polymer.
  • Table 4 gives the tensile strength, elongation and energy at break after 25 minutes cure at 180°C.
  • the corresponding values for uncured polymer B are 9.29 MPa tensile at break, 60 % elongation at break, and 0.34 Joule energy at break; they are 6.28 MPa, 164 % and 0.56 Joule respectively for polymer C.
  • the adhesive composition may contain as third component an hydrocarbon tackifier resin.
  • hydrocarbon tackifier resin is Escorez R 1310 from Exxon Chemical.
  • the melt viscosity at 140°C is 31.3 Pa.s
  • the melt viscosity at 140°C is 16.0 Pa.s. um
  • compositions containing an hydrocarbon tackifier are cured strong adhesive bonds at elevated temperatures are obtained.
  • a low molecular weight polyethylene oxide polyol or polypropylene oxide polyol containing at least three hydroxyl groups per mole may also be added to the compositions. It reduces the viscosity of the hot melt composition and makes the film more tacky whilst maintaining good cured adhesive properties as illustrated by the data given in Table 9.
  • the particular polyether triol used in these samples is an adduct of propylene oxide and glycerol, viscosity at 25°C is 800 mPa.s, hydroxyl number is 56 ⁇ 2.
  • lactam blocked polyisocyanate isocyanurate derivatives a system is provided which permits low viscosity EVOH polymers to be processed with a crosslinking system in a hot melt formulation with low, if any, viscosity reducing agent. Good processing stability can be achieved at the same time as good ultimate thermal stability and low volatile generation during curing.
  • the selection of a blocking agent which unblocks the isocyanate groups at the appropriate rate is critical and lactams are very desirable for hot melt adhesive purposes. It is desirable, as the invention permits, to achieve a high crosslinking efficiency and good adhesive and physical properties with a low concentration of blocked polyisocyanate.
  • the blocked polyisocyanate of the type used in this invention can be used at significantly lower concentration than blocked diisocynates or internally blocked polyisocyanates.
  • the amount of blocking agent released during the cross-linking reaction is also minimized which may be beneficial. It is speculated although not demonstrated that blocked polyisocyanates containing two and more than two isocyanates generate a more efficient crosslinking reaction than diisocyanates.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Abstract

A curable adhesive composition includes (a) a copolymer of at least 50 wt% ethylene and containing from 0.10 to 0.35 mole of hydroxyl functionality per 100 gm of polymer; (b) a compound containing isocyanurate groups and at least two terminally blocked isocyanate groups; (c) optionally a hydrocarbon tackifying resin, and optionally a low molecular weight hydroxy-terminated polyalkylene oxide containing at least three hydroxyl groups or other viscosity reducing agent.

Description

CROSS-LINKABLE ADHESIVE COMPOSITION
Field of invention
This invention relates to cross-linkable compositions which may be applied as a film or as a melt and subsequently cured at a temperature above the application temperature.
Background of invention
Hot melt adhesives based on ethylene-vinyl acetate copolymers are known. Although effective for certain applications, they fail in certain assembly applications due to their poor cohesive properties at temperatures of above about 60°C. In these cases, the bond strength develops on cooling but the cohesive properties are always limited at a given temperature due to the thermoplastic nature of the hot melt components.
Compositions capable of providing high adhesion with good heat resistance are suggested in Japanese Patent Publication 58-217575 (Yunichika) which discloses a hot-melt adhesive comprising firstly a saponified ethylene/vinyl acetate copolymer, secondly a polyisocyanate having at least two masked isocyanate groups per molecule and thirdly, a terpene phenol resin and/or a liquid polybutadiene having at least two hydroxyl groups per molecule. The reactive copolymer may have a melt flow index as from 0.5 to 200. The saponified EVA has 10 mol % of vinyl alcohol units and has a melt index of 170 in the example 1. A wide variety of masking agents are disclosed. EP 30594 (Bayer) discloses a coating powder containing hydrolysed vinyl acetate copolymer and polyuretonimines obtained by reaction of polycarbodiimides and di- and tri-isocyanates.
GB 1079749 (ICI) describes a cross-linkable coating composition (for moulding into pipes and hoses and for cables and wires for example) not as such suitable for hot melt adhesive compositions containing a polymer of a monoethylenically unsaturated monomer and units having certain functional groups a.o. hydroxyl, and a polyisocyanate generator including aromatic internally blocked isocyanates such as specified uretidione aromatic dimers and alkylene uretidione dimers in general. The blocked products have a rate of decomposition varying with temperature which causes cross-linking at temperatures above 120°C.
EP-A-0041.192 (Siemens) describes the production of crosslinked polyolefin based cable and wire insulation and sheet production by crosslinking hydroxyl containing polyolefin with blocked polyisocyanate.
EP-A-0294.271 (Atochem) describes a crosslinkable adhesive composition based on ethylene vinyl acetate copolymer containing primary hydroxyl functionalities. The terpolymer is obtained by introducing, by grafting or direct copolymerization, an ethylenic monomer containing a primary hydroxyl such as 2-hydroxy ethyl acrylate or methacrylate. The copolymer contains from 0.02 to 0.15 moles of primary hydroxyl per 100 gms. The adhesive composition also contains a blocked polyisocyanate and a tackifying resin which may be used as blocking agent of the polyisocyanate. The preferred polyisocyanates are diisocyanates such as toluene diisocyanate, diphenylmethane diisocyanate, hexamethylene diisocyanate or isophorone diisocyanate.
EP-A-0302.620 (Exxon) discloses the use of saponified EVA's having at least 5 % wt % of vinyl alcohol derived units (14.75 wt % and 10 wt % in Examples) cured with an internally blocked polyisocyanate in the presence of a viscosity reducing component. The saponified EVA may have a viscosity of from 1 to 100 Pa.s, preferably 4 to 40 Pa.s, at 180°C and have a preferred melt flow index of from 10 to 2500.
Japanese Patent publication 4640419 (Miura) relates to heat reactive, heat sensitive elastomer composition in which saponified EVA is crosslinked by an isocyanate adduct including lactam derivatives with a decomposition promoter. Example 1 uses an EVA with 11.2 wt % of vinyl alcohol derived units. Phenol adducts are used in the Examples which release volatile phenols in use.
It is amongst the aims of the invention to provide a hot melt adhesive composition curable by heating, which is stable before curing, which can be cured safely in a controllable manner at elevated temperatures appropriate to hot melt adhesive application, has a desired balance of properties for convenient application and provides a thermally stable bond. Summary of invention
According to this invention there is provided a hot melt adhesive composition comprising :
(a) a copolymer of at least 50 wt% ethylene and containing from 0.10 to 0.35 mole of hydroxyl functionality and having a melt viscosity of from 1 to 50 Pa.s at 180°C;
(b) a compound containing isocyanurate groups and at least two terminally blocked isocyanate groups;
(c) optionally a hydrocarbon tackifying resin, and optionally a low molecular weight hydroxy-terminated polyalkylene oxide containing at least three hydroxyl per mole.
Other ingredients such as carbon black, and fillers such as calcium carbonate and silicates can also be added to impart particular properties to the compound.
Suitably the copolymer (a) is a polymer having monomeric units of ethylene and of vinyl alcohol, and optionally vinyl acetate, the melt viscosity being from 1 to 50 Pa.s at 180°C, preferably from 3 to 40 Pa.s at 180°C. Ethylene vinyl alcohol copolymers contain at least 0.10 mole of hydroxyl functionality per 100 gm of copolymer (or 4.4 wt% vinyl alcohol), preferably at least 0.16 mole OH per 100 gm of copolymer (or 7.0 wt% vinyl alcohol units). One example is a terpolymer (viscosity 25 Pa.s at 180°C, MFR at 125°C under 325 gm load of 6.4 gm/10 min.) with 10 % vinyl alcohol (or 0.227 moles per 100 gms), 88.75 % ethylene and 1.2 wt% vinyl acetate. The m.p. is 101.5°C (by DSC). Another terpolymer contains 13.7 wt% vinyl alcohol (or 0.311 mole per 100 gms), 82.3 % ethylene and 4.0 wt% vinyl acetate (viscosity 5.8 Pa.s at 180°C, MFR at 125°C under 325 gm of 30.4 gm/10 min., DSC m.p. 91°C). Copolymers of the above stated type help to provide a suitable characteristic to the hot melt adhesive compostion.
The copolymers including those referred to above, may be copolymers of ethylene and vinyl alcohol obtained by hydrolysis or transesterification of ethylene-vinyl carboxylate (e.g. ethylene-vinyl acetate) copolymer. The degree of hydrolysis can be partial or total, partial hydrolysis leaving some ester groups in the polymer.
Usually the carboxylic acid from which the carboxylate is derived has from 1 to 6 carbon atoms per molecule and the especially preferred vinyl carboxylate from which the vinyl alcohol is derived is vinyl acetate. The transesterification may be effected by reaction in the melt stage at about 100ºC with, for example, n-butanol using sodium methylate as a catalyst.
The preferred copolymers of ethylene and vinyl alcohol are obtained from ethylene vinyl acetate copolymers having a melt flow index (ASTM D1238 52 T) of 250 to 3000, preferably from 400 to 2000, and comprise preferably at least 70 wt % of ethylene and at least 7 wt % of vinyl alcohol units. Suitably the copolymer (a) containing hydroxyl functionality may also be a copolymer of ethylene and 2-hydroxyethyl acrylate or methacrylate. Such copolymers can be obtained by polymerization of ethylene in presence of the hydroxyalkylacrylate at high pressure and temperature and using an appropriate peroxide or perester as initiator. The desired polymer viscosity or melt flow rate can be obtained by using known molecular weight modifiers.
The second component (b) of the adhesive composition is a mixture containing trimeric isocyanurate groups and at least two terminally blocked isocyanate groups. It contains at least 10 wt% of isocyanurate derived from an aliphatic or cycloaliphatic diisocyanate, and di-, tri-, tetra-, penta- and possibly hexaisocyanates as a mixture. The isocyanate groups are blocked with an extraneous blocking agent which is released on heating. Preferably the polyisocyanate has no free isocyanate groups and the rate of unblocking and hence crosslinking can be varied by controlling curing temperature.
By being blocked or masked, the isocyanate can be protected from reacting with the alcohol functions of the copolymer and reactive groups of the third component until the decomposition temperature of the blocked polyisocyanate is reached. The blocked polyisocyanate may contain other groups than the blocked isocyanates which do not dissociate on heating. Aliphatic or cycloaliphatic polyisocyanates are preferred.
Preferably the blocked polyisocyanate compound is used at a mole ratio OH:NCO of from 4 to 16; especially from 8 to 16 and especially above 10. Good compositions can be obtained using lower amounts of cross-linking agent. Isocyanurate derivatives are used advantageously because they can contain more than two blocked isocyanate groups per molecule.
Typical compounds suitable for the invention are :
Figure imgf000009_0001
where X is from 0 to 4, B is a blocking agent and R is
Figure imgf000009_0002
The blocking agent can be lactam, such as ε-caprolactam or -valerolactams or ɣ-butyrolactam,preferably ε- caprolactam.
These compounds are described in US 4302351. A product particularly useful for the invention and believed to have the composition shown above, is marketed by Chemische Werke Huls AG as IPDI B 1530. It is based on 3-isocyanatomethyl-3,3,5-trimethyl- cyclohexylisocyanate also called isophorone diisocyanate and abbreviated as IPDI, it contains approximately 15 wt% of blocked isocyanate. The blocking agent is
ε -caprolactam.
The adhesive composition may contain a third component, and optionally further components, to decrease the viscosity of the formulation at temperatures below the curing temperature to facilitate handling, to preferably act as an adhesion promoter or to alter the physical properties of the cured compound such as providing a different modulus.
The optional third component of the film or hot melt composition is an hydrocarbon tackifier resin such as the Escorez (Registered Trade Mark) resins commercialised by Exxon Chemical International or synthetic or natural terpene tackifiers. A low molecular weight polyhydroxy compound may optionally also be added.
Suitable polyhydroxy compounds are tri-, or tetra- functional polyether polyols used in the manufacture of polyurethanes. It has been found that a particularly suitable polyether is a 300 gm/mole molecular weight adduct of propylene oxide and glycerol (hydroxyl number 56 mgr KOH/gr). Low molecular weight polypropylene oxide polyols are well known and are commercially available. In preparing the film or hot melt adhesive composition, the blocked polyisocyanate should be mixed at a temperature below that at which the isocyanate begins to unblock to an appreciable extent. Temperatures from 120 to 130°C have been found adequate when using IPDI B 1530.
When the third component is present typical quantities of the components are 40 to 90 wt %, preferably 50 to 75 weight % of the ethylene copolymer, 10 to 60 weight %, preferably 25 to 50 weight % of the tackifying resin based on the total weight of the two components.
When a low molecular weight polyhydroxy compound is added, typical quantities of the polyhydroxy compound are 1 to 10 weight percent of the total weight of the three components.
The composition containing only the ethylene copolymer and the blocked polyisocyanate can be processed and applied as a film, the composition containing the ethylene copolymer, the blocked polyisocyanate and the tackifying resin and optionally the low molecular weight polyhydroxy compound can be applied as a film or as a hot melt, both at a temperature below which appreciable heat activation of the blocked polyisocyanate takes place, and cured after application by heating to a temperature where the blocked polyisocyanate unblocks sufficiently quickly. When using IPDI B 1530, temperatures in the range 150°C to 200°C are adequate. By using the compositions of this invention and curing them by heating at 150°C to 200ºC, it is found that strong adhesive bonds are obtained which are still effective at temperatures as high as 150°C when tested under shear conditions. Good bonding to metal surfaces can be achieved particularly. Examples
Table 1 sets ethylene copolymers A, B, C, D used for making formulations of the examples, their composition, melting peak temperature as determined by differential scanning calorimetry, melt viscosity (Brookfield viscometer RV, Thermosel), and melt flow rate at 125°C, 325 gm load.
Figure imgf000013_0001
The formulations given in Table 2 consist of the ethylene copolymers A, B or C and IPDI B 1530 mixed in a laboratory scale mixer by melting the ethylene copolymer first at 130°C, and introducing the IPDI B 1530 which was mixed for typically 6 minutes.
The mixtures were then pressed to form a 0.1-0.2 mm thick film, which was then applied between 0.09 mm aluminum foils as a substrate. The assembly was placed in a heated press at 180°C for 30 minutes under a pressure of 1-5 kg/cm2 so as to produce an adhesive layer of 60 to 130 microns depending on the viscosity of the polymer used. The adhesion T-peel strength, lap shear strength at 100°C and 150°C and Peel Adhesion Failure Temperature (PAFT) were measured and the results are given in Table 3 for the different compositions.
The T-peel strength was determined using a tensometer at a pulling speed of 5.08 cm per minute and a 2 cm wide strip specimen.
The lap shear strength was determined on a 2.54 cm x 2.54 cm bond area, and an adhesive layer about 10 micron thick, using a tensometer at a pulling speed of 5.08 cm per minute. The tensometer was equipped with a heated chamber and the tests were carried out at 100°C and 150°C.
The Peel Adhesion Failure Temperature (PAFT) was carried out using a 2.5 cm wide and 2.5 cm long adhesive bond in the T-peel mode and 0.5 kg load. The temperature was raised continuously at 24°C per hour rate. PAFT is the temperature at which the bond failed. Tests carried out on the ethylene copolymer alone, or on the compositions of Table 2 before heating at 180°C for 30 minutes indicated less than 2N/2cm adhesion T-peel strength.
Figure imgf000016_0001
Figure imgf000017_0001
It is clear from the examples A-6 through A-16, B-4 through B-12, and C-4 through C-16 in Table 3, that high adhesion develops during cure as evidenced by T-peel strength results. High shear strength values at elevated temperature are also obtained after cure.
These films can still however be peeled-off at temperatures from 55 to 99ºC depending on composition.
Moreover it has been found that the compositions given in Table 2 give after cure rubber-like stress-strain behavior, the cured compositions exhibit high tensile strength, high elongation and high energy at break, significantly higher than the uncured polymer. Table 4 gives the tensile strength, elongation and energy at break after 25 minutes cure at 180°C. The corresponding values for uncured polymer B are 9.29 MPa tensile at break, 60 % elongation at break, and 0.34 Joule energy at break; they are 6.28 MPa, 164 % and 0.56 Joule respectively for polymer C.
The adhesive composition may contain as third component an hydrocarbon tackifier resin. One of the advantages of such a composition is that it can be applied either as a film between two substrates or as a hot melt. An example of hydrocarbon tackifier resin is EscorezR 1310 from Exxon Chemical. When compounded with EVOH B in a 60 parts polymer - 40 parts Escorez 1310, the melt viscosity at 140°C is 31.3 Pa.s, in a similar composition with EVOH C the melt viscosity at 140°C is 16.0 Pa.s. um
Figure imgf000019_0001
When compositions containing an hydrocarbon tackifier are cured strong adhesive bonds at elevated temperatures are obtained.
The examples given in Table 5 through 8 will illustrate compositions capable of forming such adhesive bonds, as well as the effect of cure temperature and cure time. All these examples were obtained using 90 micron aluminum foil as substrate.
A low molecular weight polyethylene oxide polyol or polypropylene oxide polyol containing at least three hydroxyl groups per mole may also be added to the compositions. It reduces the viscosity of the hot melt composition and makes the film more tacky whilst maintaining good cured adhesive properties as illustrated by the data given in Table 9. The particular polyether triol used in these samples is an adduct of propylene oxide and glycerol, viscosity at 25°C is 800 mPa.s, hydroxyl number is 56±2.
Using the lactam blocked polyisocyanate isocyanurate derivatives a system is provided which permits low viscosity EVOH polymers to be processed with a crosslinking system in a hot melt formulation with low, if any, viscosity reducing agent. Good processing stability can be achieved at the same time as good ultimate thermal stability and low volatile generation during curing. The selection of a blocking agent which unblocks the isocyanate groups at the appropriate rate is critical and lactams are very desirable for hot melt adhesive purposes. It is desirable, as the invention permits, to achieve a high crosslinking efficiency and good adhesive and physical properties with a low concentration of blocked polyisocyanate. The blocked polyisocyanate of the type used in this invention can be used at significantly lower concentration than blocked diisocynates or internally blocked polyisocyanates. The amount of blocking agent released during the cross-linking reaction is also minimized which may be beneficial. It is speculated although not demonstrated that blocked polyisocyanates containing two and more than two isocyanates generate a more efficient crosslinking reaction than diisocyanates.
Figure imgf000022_0001
Figure imgf000023_0001
Figure imgf000024_0001
Figure imgf000025_0001
Figure imgf000026_0001

Claims

1. A cross-linkable adhesive composition comprising :
(a) a copolymer of at least 50 wt% ethylene and containing from 0.10 to 0.35 mole of hydroxyl functionality per 100 gm of polymer;
(b) a compound containing isocyanurate groups and at least two terminally blocked isocyanate groups;
(c) optionally a hydrocarbon tackifying resin, and optionally a low molecular weight hydroxy- terminated polyalkylene oxide containing at least three hydroxyl groups or other viscosity reducing agent.
2. A composition according to claim 1 in which the copolymer (a) has a melt viscosity of from 1 to 50 Pa.s at 180°C and the compound (b) is a mixture of blocked polyisocyanates which mixture consists of at least 30 wt% of components containing three and more blocked isocyanate groups.
3. Composition according to Claim 1 or Claim 2, wherein the copolymer has a melt viscosity preferably of from 3 to 40 Pa.s at 180°C.
4. Composition according to any of the preceding claims wherein the blocked polyisocyanate is used at a mole ratio OH:NCO of 4 to 20.
5. Composition according to any of the preceding claims wherein the compound (b) contains blocked cycloaliphatic polyisocyanates.
6. Composition according to any of the preceding claims wherein the polymer is
(a) a partically or completely hydrolysed polymer of ethylene derived units and vinyl esters, preferably having from 70 to 93 wt% of ethylene, from 7 to 15 wt% of vinyl alcohol and from 0 to 15 wt% of vinyl alcohol and from 0 to 15 wt% of vinyl acetate; or
(b) a polymer containing at least 50 wt% of ethylene and 10 to 45 wt% of 2-hydroxyethyl acrylate or methacrylate.
7. Composition according to any of the preceding claims in which the tackifying resin is non- reactive with isocyanate optionally accompanied by a polyalkylene polyol of average molecular weight from 100 to 2000 containing at least three hydroxyl groups.
8. Composition according to anyone of the preceding claims which comprises 40 to 100 % of the ethylene copolymer, 0 to 60 wt % of the other components, and the blocked polyisocyanate in an amount so as to provide a OH:NCO ratio of from 4 to 20.
9. Composition according to claims 1, 2, 4, 5 and 8 in which the blocking compound is a lactam, such as ε-caprolactam.
PCT/EP1991/000577 1990-03-23 1991-03-21 Cross-linkable adhesive composition Ceased WO1991014727A1 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0819711A1 (en) * 1996-07-16 1998-01-21 Ato Findley S.A. One component polyurethane based adhesives showing improved initial cohesion
WO1999028363A1 (en) * 1997-12-01 1999-06-10 Henkel Kommanditgesellschaft Auf Aktien Modified polyurethane hotmelt adhesive
US6465104B1 (en) 1997-12-01 2002-10-15 Henkel Kommanditgesellschaft Auf Aktien Modified polyurethane hotmelt adhesive
US7005482B2 (en) * 2001-02-12 2006-02-28 Jowat Lobers Und Frank Gmbh & Co. Kg Self-supporting reactive hot-melt adhesive element

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0041192A1 (en) * 1980-06-03 1981-12-09 Siemens Aktiengesellschaft Method of producing crosslinked insulations and sheaths of cables and cords
EP0294271A1 (en) * 1987-06-05 1988-12-07 Elf Atochem S.A. Curable hot-melt adhesive composition, adhesive obtained, adhesion process

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0041192A1 (en) * 1980-06-03 1981-12-09 Siemens Aktiengesellschaft Method of producing crosslinked insulations and sheaths of cables and cords
EP0294271A1 (en) * 1987-06-05 1988-12-07 Elf Atochem S.A. Curable hot-melt adhesive composition, adhesive obtained, adhesion process

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0819711A1 (en) * 1996-07-16 1998-01-21 Ato Findley S.A. One component polyurethane based adhesives showing improved initial cohesion
US5922805A (en) * 1996-07-16 1999-07-13 Ato Findley S.A. Polyurethane-based single-component hot-melt adhesives with improved initial cohesion
JP3479588B2 (en) 1996-07-16 2003-12-15 アト フィンドレー ソシエテ アノニム Polyurethane-based single-component hot melt adhesives with improved initial cohesion
WO1999028363A1 (en) * 1997-12-01 1999-06-10 Henkel Kommanditgesellschaft Auf Aktien Modified polyurethane hotmelt adhesive
US6465104B1 (en) 1997-12-01 2002-10-15 Henkel Kommanditgesellschaft Auf Aktien Modified polyurethane hotmelt adhesive
US7005482B2 (en) * 2001-02-12 2006-02-28 Jowat Lobers Und Frank Gmbh & Co. Kg Self-supporting reactive hot-melt adhesive element

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