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NO148988B - PROCEDURE FOR THE MANUFACTURE OF COMPOSITE FILES - Google Patents

PROCEDURE FOR THE MANUFACTURE OF COMPOSITE FILES Download PDF

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Publication number
NO148988B
NO148988B NO781209A NO781209A NO148988B NO 148988 B NO148988 B NO 148988B NO 781209 A NO781209 A NO 781209A NO 781209 A NO781209 A NO 781209A NO 148988 B NO148988 B NO 148988B
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Norway
Prior art keywords
isocyanate
foil
amino group
groups
component
Prior art date
Application number
NO781209A
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Norwegian (no)
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NO148988C (en
NO781209L (en
Inventor
Hans Bauriedel
Rainer Hasenkamp
Original Assignee
Henkel Kgaa
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Application filed by Henkel Kgaa filed Critical Henkel Kgaa
Publication of NO781209L publication Critical patent/NO781209L/en
Publication of NO148988B publication Critical patent/NO148988B/en
Publication of NO148988C publication Critical patent/NO148988C/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • 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
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/28Layered products comprising a layer of synthetic resin comprising synthetic resins not wholly covered by any one of the sub-groups B32B27/30 - B32B27/42
    • B32B27/285Layered products comprising a layer of synthetic resin comprising synthetic resins not wholly covered by any one of the sub-groups B32B27/30 - B32B27/42 comprising polyethers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/30Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
    • B32B27/302Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising aromatic vinyl (co)polymers, e.g. styrenic (co)polymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/30Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
    • B32B27/304Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers comprising vinyl halide (co)polymers, e.g. PVC, PVDC, PVF, PVDF
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/32Layered products comprising a layer of synthetic resin comprising polyolefins
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/34Layered products comprising a layer of synthetic resin comprising polyamides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/36Layered products comprising a layer of synthetic resin comprising polyesters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B7/00Layered products characterised by the relation between layers; Layered products characterised by the relative orientation of features between layers, or by the relative values of a measurable parameter between layers, i.e. products comprising layers having different physical, chemical or physicochemical properties; Layered products characterised by the interconnection of layers
    • B32B7/04Interconnection of layers
    • B32B7/12Interconnection of layers using interposed adhesives or interposed materials with bonding properties
    • 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
    • C09J175/08Polyurethanes from polyethers
    • 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
    • C09J175/12Polyurethanes from compounds containing nitrogen and active hydrogen, the nitrogen atom not being part of an isocyanate group
    • 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
    • C09J5/00Adhesive processes in general; Adhesive processes not provided for elsewhere, e.g. relating to primers
    • C09J5/04Adhesive processes in general; Adhesive processes not provided for elsewhere, e.g. relating to primers involving separate application of adhesive ingredients to the different surfaces to be joined
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2323/00Polyalkenes
    • B32B2323/04Polyethylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2323/00Polyalkenes
    • B32B2323/10Polypropylene

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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)
  • Laminated Bodies (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Lining Or Joining Of Plastics Or The Like (AREA)
  • Manufacture Of Alloys Or Alloy Compounds (AREA)
  • Compositions Of Oxide Ceramics (AREA)
  • Inorganic Insulating Materials (AREA)

Description

Oppfinnelsen vedrører en fremgangsmåte til fremstilling av sammensatte folier under anvendelse av oppløsningsmiddel-frie klebestoffer på basis av flerfunksjonene isocyanater og flerfunksjonene reaksjonsdyktige aminer. The invention relates to a method for the production of composite foils using solvent-free adhesives based on multifunctional isocyanates and multifunctional reactive amines.

Sammensatte folier fremstilles vanligvis ved hjelp av oppløsningsmiddelholdige kasjeringsklebestoffer som påføres ved hjelp av valser på foliebanen. Derved foregår etter fordampning av oppløsningsmidlet en forening med den annen bane under korttidig trykk. Som klebestoffer ved denne som tørrkasjering kjente fremgangsmåte anvendes omtrent utelukkende oppløsningsmiddelholdige polyuretan-systemer i form av fuktighetsherdende isocyanatendeplas-serte prepolymere eller tokomponentede polyol/polyisocyanat-blandinger. De nyeste, begrensninger for oppløsningsmiddelavgivning i atmosfæren nødvendiggjør absorpsjon eller etterforbrenning av oppløsningsmiddel/luftblandingene som omstendelig fremgangsmåte-trinn. Composite foils are usually produced using solvent-containing casing adhesives which are applied by means of rollers to the foil web. Thereby, after evaporation of the solvent, a union with the other web takes place under short-term pressure. As adhesives in this method known as dry lamination, almost exclusively solvent-containing polyurethane systems in the form of moisture-curing isocyanate-deplaced prepolymers or two-component polyol/polyisocyanate mixtures are used. The latest limitations on solvent release into the atmosphere necessitate absorption or post-combustion of the solvent/air mixtures as cumbersome process steps.

Oppfinnelsens oppgave var å finne et klebestoffsystem for sammensatt foliefremstilling som er fri for oppløsningsmiddel og derved kan forarbeides brann- resp. eksplosjonssikrere samt videre muliggjør en mer økonomisk fremgangsmåte. The invention's task was to find an adhesive system for composite foil production that is solvent-free and can thereby be processed fire- or more explosion-proof and also enables a more economical method.

Det var en ytterligere oppgave for foreliggende opp-finnelse å tilveiebringe en fremgangsmåte til fremstilling av sammensatte folier som på teknologisk enklere måte fører til klare3 klebefaste sammensatte folier. It was a further task for the present invention to provide a method for the production of composite foils which in a technologically simpler way leads to clear3 adhesive-resistant composite foils.

Denne oppgave løses ifølge oppfinnelsen ved at man This task is solved according to the invention by

på en av de to folier som skal sammenklebes påfører en eller flere minst to endeplasserte isocyanatgruppeholdige polyetere, hvis molekylvekt ligger mellom 2000 og 5000 og på den annen folie på-fører en eller flere minst to reaksjonsdyktige aminogruppeholdige lengrekjedede forbindelser, idet det molare forhold mellom iso- on one of the two foils to be glued together, one or more apply at least two end-positioned polyethers containing isocyanate groups, whose molecular weight is between 2000 and 5000, and on the other foil, one or more apply at least two reactive amino group-containing longer-chain compounds, the molar ratio between iso -

cyanatgrupper og aminogrupper ligger mellom 1:1 og 5:1 og begge komponenter foreligger sammen i en mengde fra 0,5 til 5,0 g/m<2>cyanate groups and amino groups lie between 1:1 and 5:1 and both components are present together in an amount from 0.5 to 5.0 g/m<2>

og de to folielag sammentrykkes i kort tid. and the two foil layers are compressed for a short time.

Egnede, for fremgangsmåten ifølge oppfinnelsen, brukbare minst bifunksjonelle isocyanater kan på i og for seg kjent måte fremstilles ved omsetning av vannfrie polyeterdioler med minst bifunksjonelle isocyanater. Foretrukne polyeterdioler avleder seg fra 2 til 4 karbonatomholdige glykoler. Følgelig kommer det på tale polyetylen- og/eller polypropylenglykol og/ eller polytetrametylenglykol (fremstilt ved ringåpningspolymeri-sasjon av tetrahydrofuran). I første rekke kommer det i betrakt-ning relativt lavmolekylære diisocyanater for omsetning med polyeterdioler som hexametylendiisocyanat, trimetylhexametylendiiso-cyanat, dicyklohexylmetandiisocyanat, isoforondiisocyanat, toluylendiisocyanat (isomerblanding) og flere andre. Av praktiske, spesielt toksikologiske grunner er difenylmetandiisocyanat foretrukket . Suitable at least bifunctional isocyanates usable for the method according to the invention can be prepared in a manner known per se by reacting anhydrous polyetherdiols with at least bifunctional isocyanates. Preferred polyetherdiols are derived from 2 to 4 carbon atom containing glycols. Consequently, we are talking about polyethylene and/or polypropylene glycol and/or polytetramethylene glycol (produced by ring-opening polymerization of tetrahydrofuran). In the first place, relatively low molecular weight diisocyanates come into consideration for reaction with polyetherdiols such as hexamethylene diisocyanate, trimethylhexamethylene diisocyanate, dicyclohexylmethane diisocyanate, isophorone diisocyanate, toluylene diisocyanate (isomer mixture) and several others. For practical, especially toxicological reasons, diphenylmethane diisocyanate is preferred.

For dannelsen av isocyanat-adduktene egner seg fortrinnsvis et omsetningsforhold fra 1,8:1 til 2,2:1 (mol diisocyanat: mol diol). Et mindre omsetningsforhold er prinsipielt også mulig, forutsatt at det derved ikke danner seg et for høy viskøst addukt, ved hvis anvendelse ikke mer er gitt en1 god maskinell kasjering. Et eventuelt større omsetningsforhold enn 2,2:1 vil prinsipielt også være tolererbart, hvis av toksikologiske grunner ikke besto noen betenkeligheter på grunn av at det da foreligger høyt innhold av fritt diisocyanat. A conversion ratio of 1.8:1 to 2.2:1 (mol diisocyanate: mol diol) is preferably suitable for the formation of the isocyanate adducts. A lower turnover ratio is in principle also possible, provided that a too high viscous adduct is not thereby formed, with the use of which no more than 1 good mechanical casing is provided. A possible greater turnover ratio than 2.2:1 would in principle also be tolerable, if for toxicological reasons there were no concerns due to the high content of free diisocyanate.

Det må påses at de dannede isocyanatforbindelser ved forarbeidelsen ikke overstiger en viskositet på ca. 10.000 cp. -Eventuelt kan man påføre disse reaksjonskomponenter også ved for-høyede temperaturer inntil ca. 80°C. Vanligvis vil man imidlertid foretrekke temperaturer fra'50 til 65°C. It must be ensured that the isocyanate compounds formed during processing do not exceed a viscosity of approx. 10,000 cp. - Optionally, these reaction components can also be applied at elevated temperatures up to approx. 80°C. Generally, however, temperatures from 50 to 65°C will be preferred.

Kasjeringssammenklebingen som bare gjennomføres med de minst to endeplasserte isocyanatgruppeholdige addukter som isocyanatkomponenter i kombinasjon med de nedenfor nevnte aminforbindel-ser som aminkomponent gir tilstrekkelig klebefastheter. Det har imidlertid vist seg at denne lar seg øke betraktelig, når det tilsettes 0,5 til 20, fortrinnsvis 1,0 til 10 vektprosent av en forbindelse med minst tre isocyanatgrupper til -isocyanat-adduktet, The case bonding which is only carried out with the at least two end-positioned isocyanate group-containing adducts as isocyanate components in combination with the below-mentioned amine compounds as amine component provides sufficient adhesive strengths. However, it has been shown that this can be increased considerably, when 0.5 to 20, preferably 1.0 to 10 percent by weight of a compound with at least three isocyanate groups is added to the -isocyanate adduct,

idet vektmengden refereres til isocyanat-adduktet. Med de så- the amount by weight being referred to the isocyanate adduct. With those so-

ledes modifiserte isocyanatkomponenter oppnår man spesielt en høyere begynnelsesklebrighet, men også en forbedret sluttkleb-fasthet. Som tilsetningsforbindelser med minst tre isocyanatgrupper egner det seg omsetningsprodukter av flerfunksjonene alkoholer og diisocyanater (omsetningsforhold: 1 mol diisocyanat pr. hydroksylgruppe) f.eks. omsetningsproduktet av trimetylol- modified isocyanate components are used, in particular a higher initial tackiness is achieved, but also an improved final tackiness. Reaction products of multifunctional alcohols and diisocyanates are suitable as additive compounds with at least three isocyanate groups (reaction ratio: 1 mol of diisocyanate per hydroxyl group), e.g. the turnover product of trimethylol-

propan og toluylendiisocyanat samt omsetningsprodukter av et mol vann og tre mol diisocyanat, f.eks. utgående fra hexametylendiisocyanat, videre også andre aromatiske triisocyanater som M,4',V'-triisocyanatotrifenylmetan og likeledes polyisocyanater som poly-metylenpolyfenylisocyanat. propane and toluylene diisocyanate as well as reaction products of one mole of water and three moles of diisocyanate, e.g. starting from hexamethylene diisocyanate, also other aromatic triisocyanates such as M,4',V'-triisocyanatotriphenylmethane and likewise polyisocyanates such as polymethylenepolyphenylisocyanate.

For at de resulterende isocyanatblandinger ved maskinell kasjering lett skal påføre seg på foliebanene, bør de-for nedsettelse av forarbeidelsesviskositetene oppvarmes i påførings-karet. En temperaturøkning til maksimalt 80°C bør derved ikke overskrides. Vanligvis er det helt tilstrekkelig med en tempera- In order for the resulting isocyanate mixtures to be easily applied to the foil webs by machine casing, they should be heated in the application vessel to reduce the processing viscosities. A temperature rise to a maximum of 80°C should therefore not be exceeded. Usually, it is quite sufficient with a tempera-

tur på ca. 60°C. Inntil denne temperatur ble det ved kasjering med de i det oppførte eksempel 1 omtalte isocyanatkomponenter ved målinger på kasjeringsmaskinene fastslått at det i arbeidsplass-atmosfæren ikke opptrådte isocyanatkonsentrasjoner som oversteg den tillatelige MAK-verdi på 0,02 ppm. trip of approx. 60°C. Up to this temperature, when casing with the isocyanate components mentioned in example 1, measurements on the casing machines determined that there were no isocyanate concentrations in the workplace atmosphere that exceeded the permissible MAK value of 0.02 ppm.

Den annen reaksjonskomponent som anvendes for fremgangsmåten ifølge oppfinnelsen er et i det minste bifunksjonelt amin. Det må minst være tilstede to aminogrupper som såvel kan være primære som også sekundære. Slike forbindelser er kjent resp. fremstilles på kjent måte. The second reaction component used for the method according to the invention is an at least bifunctional amine. At least two amino groups must be present, which can be both primary and secondary. Such compounds are known resp. produced in a known manner.

En foretrukket grunnstruktur for aminoforbindelsene A preferred basic structure for the amino compounds

er polyeterdiolene eller også oligomere glykoler. I henhold til en hensiktsmessig utførelsesform går man frem således at"det på polyeterdiolene tilleirés acrylnitril. De derved resulterende addukter hydrogeneres deretter på kjent måte, idet det av nitril-gruppene dannes primære aminogrupper. Foretrukket for fremstillingen av de to reaksjonskomponenter av det oppløsningsmiddelfrie kasjeringsklebestoff er oligomere glykoler resp. polyeterglykoler som avleder seg fra polyetylenglykol, polypropylenglykol og polytetrametylen-glykol av en molekylvekt mellom ca. 200 og ^500, spesielt 300 og 2000. are the polyetherdiols or also oligomeric glycols. According to an appropriate embodiment, the procedure is that "acrylonitrile is added to the polyetherdiols. The resulting adducts are then hydrogenated in a known manner, with the nitrile groups forming primary amino groups. Preferred for the production of the two reaction components of the solvent-free casing adhesive is oligomeric glycols or polyether glycols derived from polyethylene glycol, polypropylene glycol and polytetramethylene glycol of a molecular weight between about 200 and ^500, especially 300 and 2000.

Videre er det mulig å gå ut fra relativt lavmolekylære diaminer med en kjedelengde fra 2 til 18 karbonatomer, som delvis også kan være erstattet med oksygenatomer og omsette disse med minst to med amin reaksjonsdyktige funksjonelle gruppe-holdige forbindelser (kjedeforlenging). Slike aminer er eksempelvis Furthermore, it is possible to proceed from relatively low-molecular-weight diamines with a chain length of 2 to 18 carbon atoms, which may also be partially replaced with oxygen atoms, and to react these with at least two amine-reactive functional group-containing compounds (chain extension). Examples of such amines are

De funksjonelle grupper av kjedeforlengningsmidlene kan derved f.eks. være epoksyd- eller isocyanatrester eller også ot,^-umettede estere eller halogenatomer. De OH-grupper, sekundære aminogrupper resp. urinstoffgrupperinger resp. innførte ester-grupperinger som danner seg ved denne reaksjon kan under tiden virke gunstig på klebingen resp. fastheten av klebeforbindelsen. The functional groups of the chain extenders can thereby e.g. be epoxide or isocyanate residues or also ot,^-unsaturated esters or halogen atoms. The OH groups, secondary amino groups or urea groupings or introduced ester groupings which are formed by this reaction can in the meantime have a beneficial effect on the adhesion resp. the firmness of the adhesive connection.

I tilfelle diepoksyd eller diglycidylforbindels.e In case of diepoxide or diglycidyl compound.e

hvori R betyr en alifatisk eller cykloalifatisk rest inntil ca. in which R means an aliphatic or cycloaliphatic residue up to approx.

25 karbonatomer som f.eks. metylen, etylen, propylen, neopentylen, hexametylen, dodecametylen, cyklohexylen, dicyklohexyl, metylen-dicyklohexyl eller også en dietylen- eller trietylenglykoleterest og det diprimære amin tilsvarende den generelle formel f^N-IV<->NI^25 carbon atoms such as e.g. methylene, ethylene, propylene, neopentylene, hexamethylene, dodecamethylene, cyclohexylene, dicyclohexyl, methylene-dicyclohexyl or also a diethylene or triethylene glycol ether residue and the diprimary amine corresponding to the general formula f^N-IV<->NI^

hvori R' eksempelvis betyr en etylen-, tetrametylen-, hexametylen-, dietylenglykoleter-, diisopropylenglykoleter- eller også trietylen-glykoleterrest får man to endeplasserte, primære aminogruppeholdige forbindelser med den generelle formel I tilfelle kjedeforlengelse med isocyanater som f.eks. toluylen-, hexametylen- og isoforodiisocyanat får man to endeplasserte aminogrupper samt urinstoffgruppeholdige forbindelser med den generelle formel in which R' means, for example, an ethylene, tetramethylene, hexamethylene, diethylene glycol ether, diisopropylen glycol ether or also triethylene glycol ether residue, two terminally placed, primary amino group-containing compounds with the general formula are obtained In case of chain extension with isocyanates such as e.g. toluylene, hexamethylene and isophorodiisocyanate gives two end-placed amino groups as well as urea group-containing compounds with the general formula

hvori R' har den ovennevnte betydning, mens R betyr resten av det anvendte isocyanat. in which R' has the above meaning, while R means the remainder of the isocyanate used.

Reaksjoner for kjedeforlengelse for egnede aminer Chain extension reactions for suitable amines

er videre omtalt i BRD-søknad nr. P 25 49 371.4. is further mentioned in BRD application no. P 25 49 371.4.

I mange tilfelle kan det være hensiktsmessig til de aminogruppeholdige lengrekjedede forbindelser å tilsette 1 til 50 vektprosent, fortrinnsvis 1 til 15 vektprosent vann. Derved kan det bevirkes en økning resp. en tidligere oppnåelse av sluttfastheten og påvirke den sammensatte folies forseglingsevne på gunstig måte. In many cases, it may be appropriate to add 1 to 50 percent by weight, preferably 1 to 15 percent by weight, of water to the amino group-containing longer-chain compounds. This can cause an increase or an earlier achievement of the final strength and favorably influence the sealing ability of the composite film.

Med maskinell kasjering danner det seg spontant en tilstrekkelig høy begynnelsesklebrighet således at det ikke opp-trer noen delaminering eller "teleskopering" av den sammensatte folie ved oppvikling. I løpet av syv dager etter fremstillingen oppnår klebefastheten ved lagring ved værelsestemperatur sin slutt-verdi. Klebestoff-filmene er deretter kjemisk nettdannet og viser et forhold som forpakningsteknisk tilfredsstiller alle krav med hensyn til forbindelsesklebing og varmebestandighet som er en forutsetning for forseglbarheten. De ferdige sammensetninger ut-merker seg videre ved meget gode optiske egenskaper. Således har f.eks. gjennomsiktige sammensetninger en høy transparens. Forøvrig hyppig opptredende kasjeringsfeil som "fiskeøyne-" eller "appelsin-skallstruktur" lar seg ikke fastslå på sammensetningene. With mechanical lamination, a sufficiently high initial stickiness is spontaneously formed so that no delamination or "telescoping" of the composite foil occurs during winding. Within seven days of production, the adhesive strength reaches its final value when stored at room temperature. The adhesive films are then chemically cross-linked and show a condition that, in terms of packaging, satisfies all requirements with regard to joint bonding and heat resistance, which is a prerequisite for sealability. The finished compositions are further distinguished by very good optical properties. Thus, e.g. transparent compositions a high transparency. Incidentally, frequently occurring casing errors such as "fish-eye" or "orange-peel structure" cannot be determined on the compositions.

Med det omtalte tokomponentede kasjeringsklebestoff lar det seg fremstille alle sammensetninger av kunststoffolier With the mentioned two-component casing adhesive it is possible to produce all compositions of plastic foils

som polyetylen-, polypropylen-, polyester-, polyvinylklorid-, polystyren-, polyamidfolier osv. Videre er det mulig fremstilling av sammensatte folier under anvendelse av metallfolier, f.eks. aluminiumfolie eller også forskjellige celleglass resp. papir. such as polyethylene, polypropylene, polyester, polyvinyl chloride, polystyrene, polyamide foils, etc. It is also possible to produce composite foils using metal foils, e.g. aluminum foil or different cellular glass resp. paper.

Fremgangsmåten vil ifølge oppfinnelsen forklares According to the invention, the method will be explained

ved hjelp av de følgende eksempler. De i eksem- using the following examples. Those in eczema

plene som "aminopropylerte" polypropylenglykoler betegnede forbindelser ble fremstilt ved tilleiring av acrylnitril til glykol og etterfølgende katalytisk hydrogenering. Compounds designated as "aminopropylated" polypropylene glycols were prepared by addition of acrylonitrile to glycol and subsequent catalytic hydrogenation.

Eksempel 1 Example 1

Komponent A Component A

2000 g isocyanat-addukt av polypropylenglykol med molekylvekt 2000 g isocyanate adduct of polypropylene glycol with molecular weight

2000 og difenylmetan-4,4'-diisocyanat i 'molforhold 1:2 og 2000 and diphenylmethane-4,4'-diisocyanate in a molar ratio of 1:2 and

100 g omsetningsprodukt av 3 mol héxame/tylendiisocyanat og 100 g reaction product of 3 mol hexame/tylene diisocyanate and

1 mol vann. 1 mole of water.

Innholdet av frie isocyanatgrupper: 4,2 % resp. 1,0 mékvivalenter/g Viskositet ved 23°C: 25.000 cp The content of free isocyanate groups: 4.2% resp. 1.0 méquivalents/g Viscosity at 23°C: 25,000 cp

" 50°C: 8.000 cp " 50°C: 8,000 cp

" 60°C: 2.500 cp " 60°C: 2,500 cp

(hver gang Brookfield-viskositet) (each time Brookfield viscosity)

Komponent B Component B

300 g aminopropylert polypropylenglykol (gjennomsnittlig molekylvekt 400) 300 g aminopropylated polypropylene glycol (average molecular weight 400)

500 g aminopropylert polypropylenglykol (gjennomsnittlig molekylvekt 2000) 500 g aminopropylated polypropylene glycol (average molecular weight 2000)

Amininnhold: 2,5 mA/g Amine content: 2.5 mA/g

1,68 g/m^ av den til 60°C oppvarmede komponent A ble påført på polyesterfolie (folietykkelse 12 um) og 0,35 g/m p av komponent B ved værelsestemperatur på ved Coronautladning forbehandlet polyetylenf olie av lav tetthet (f olietykkelse 50 ^im) idet påføringen foregikk maskinelt. Det molare forhold mellom isocyanat-og aminkomponent utgjorde referert til isocyanat- til aminogrupper, 1,9:1. De belagte sider av folien ble sammentrykket over valser. 1.68 g/m² of component A heated to 60°C was applied to polyester foil (foil thickness 12 µm) and 0.35 g/m² of component B at room temperature on low-density polyethylene foil pretreated by corona discharge (foil thickness 50 ^im) as the application took place mechanically. The molar ratio between the isocyanate and amine component, referred to isocyanate to amino groups, was 1.9:1. The coated sides of the foil were compressed over rollers.

Klebefilmen viser en høy spontan begynnelsesklebrighet (30 sekunder etter sammenklebing ble det målt en skålklebfasthet på 30 p/15 mm ved en avtrekningshastighet på 100 mm/min.). The adhesive film shows a high spontaneous initial tack (30 seconds after gluing, a cup tack of 30 p/15 mm was measured at a pull-off speed of 100 mm/min).

Etter åtte timers kasjeringsvarighet lot komponentene seg ved dannelsen av en jevntblivende høy begynnelsesklebrighet videre godt forarbeide. Betinget av viskositetsøkningen øket paføringsmengden av isocyanatkomponentene til 1,92 g/m 2, mens påføringsmengden av aminkomponentene forble konstant med 0,35 g/m p. Herav fremkommer molart påføringsforhold på 2,2:1. After eight hours of encapsulation, the components allowed themselves to be processed further due to the formation of a consistently high initial stickiness. Due to the increase in viscosity, the application amount of the isocyanate components increased to 1.92 g/m 2 , while the application amount of the amine components remained constant at 0.35 g/m p. This results in a molar application ratio of 2.2:1.

Etter syv dagers lagring ved værelsestemperatur hadde det innstilt seg skålklebfasthet på 350 p/15 mm. Denne verdi ble fastslått såvel ved et sammensatt avsnitt som var fremstilt til--' å begynne med som også ved en som var blitt fremstilt ved slutten av den åtte timers kasjeringstid. After seven days of storage at room temperature, a cup adhesive strength of 350 p/15 mm had been established. This value was determined both by a composite section produced at the beginning and also by one produced at the end of the eight hour casing time.

Eksempel 2 Example 2

Komponent A Component A

Isocyanat-addukt av polypropylenglykol (gjennomsnittlig molekylvekt 2000) og difenylmetan-4,4'-diisocyanat i molforhold 1:2. Isocyanate adduct of polypropylene glycol (average molecular weight 2000) and diphenylmethane-4,4'-diisocyanate in a molar ratio of 1:2.

Innhold av frie isocyanatgrupper: 3,4 % resp. 0,8l m/ekvivalenter/g Viskositet ved 23°C: 20.000 cp. Content of free isocyanate groups: 3.4% resp. 0.8l m/equivalents/g Viscosity at 23°C: 20,000 cp.

" " 60°C: 2.000 cp " " 60°C: 2,000 cp

Komponent B Component B

300 g aminopropylert polypropylenglykol (gjennomsnittlig molekylvekt 400) 300 g aminopropylated polypropylene glycol (average molecular weight 400)

500 g aminopropylert polypropylenglykol (gjennomsnittlig molekylvekt 2000) 500 g aminopropylated polypropylene glycol (average molecular weight 2000)

Amininnhold: 2,5 mA/g Amine content: 2.5 mA/g

2,1 g/m^ av den til 60°C oppvarmede komponent A ble påført på aluminiumsfolie (folietykkelse 12 mm) og 0,4 g/m 2 av komponent B ble påført på coronautladning forbehandlet polyetylenfolie av lav tetthet (folietykkelse 50 pm). Det molare forhold mellom komponentene utgjør 1,7 : 1 (isocyanat : amingruppe). 2.1 g/m^ of the 60°C heated component A was applied to aluminum foil (foil thickness 12 mm) and 0.4 g/m 2 of component B was applied to corona discharge pretreated low density polyethylene foil (foil thickness 50 pm) . The molar ratio between the components is 1.7:1 (isocyanate: amine group).

Ved sammenføring av de belagte foliesider ble det oppnådd en tilstrekkelig høy begynnelsesklebrighet (strekkskålfast-het: 6p/15 mm ved 100 mm/min. avtrekningshastighet 30 sekunder etter fremstilling). When joining the coated foil sides, a sufficiently high initial tackiness was achieved (tensile cup strength: 6p/15 mm at 100 mm/min. pull-off speed 30 seconds after production).

Etter syv dagers lagring var sluttfastheten (250"p/ 15 mm) oppnådd. After seven days of storage, the final strength (250"p/ 15 mm) was achieved.

Eksempel 3 Example 3

Komponent A Component A

2000 g isocyanat-addukt av polypropylenglykol (gjennomsnittlig molekylvekt 3000) og difenylmetan-4,4'-diisocyanat i molforhold 1:2 og 2000 g isocyanate adduct of polypropylene glycol (average molecular weight 3000) and diphenylmethane-4,4'-diisocyanate in a molar ratio of 1:2 and

100 g omsetningsprodukt av 3 mol hexametylendiisocyanat og 1 mol vann 100 g reaction product of 3 mol hexamethylene diisocyanate and 1 mol water

Innhold av fri isocyanatgrupper: 3,3 % resp. 0,79 mA/g Viskositet ved 23°C: 29-000 cp Content of free isocyanate groups: 3.3% resp. 0.79 mA/g Viscosity at 23°C: 29-000 cp

" " 60°C: 6.000 cp " " 60°C: 6,000 cp

Komponent B Component B

Aminopropylert polypropylenglykol (gjennomsnittlig molekylvekt Aminopropylated polypropylene glycol (average molecular weight

400) 400)

Amininnhold: 5 m ekvivalenter/g Amine content: 5 m equivalents/g

2,56-g/m^ av den til 60°C oppvarmede komponent A ble påført på polyesterfolie (folietykkelse 9 Mm) °S 0,2 g/m pav komponent B ble påført på aluminiumsfolie (folietykkelse 12 jim). Det molare forhold mellom de to komponenter utgjorde derved, referert til isocyanat- og aminogruppen 2:1. 2.56-g/m² of the 60°C heated component A was applied to polyester foil (foil thickness 9 µm) °S 0.2 g/m pav component B was applied to aluminum foil (foil thickness 12 µm). The molar ratio between the two components, referred to the isocyanate and amino group, was therefore 2:1.

Begynnelsesklebrighet (30 sekunder etter sammenklebing): 15 p/15 mm Initial tackiness (30 seconds after gluing): 15 p/15 mm

Sluttfasthet (etter syv dager): 300 p/15 mm. Final strength (after seven days): 300 p/15 mm.

Eksempel 4 Example 4

Komponent A Component A

2000 g isocyanat-addukt av polypropylenglykol (gjennomsnittlig molekylvekt 2000) og difenyl-4,4'-diisocyanat i molforhold 1:2 og 2000 g isocyanate adduct of polypropylene glycol (average molecular weight 2000) and diphenyl-4,4'-diisocyanate in a molar ratio of 1:2 and

100 g omsetningsprodukt av 3 mol hexametylendiisocyanat og 1 mol vann 100 g reaction product of 3 mol hexamethylene diisocyanate and 1 mol water

Innhold av fri isocyanatgruppe: 4,2 % resp. 1,0 mA/g Viskositet ved 23°C: 25.000 cp Content of free isocyanate group: 4.2% resp. 1.0 mA/g Viscosity at 23°C: 25,000 cp

" " 60°C: 2.500 cp " " 60°C: 2,500 cp

Komponent B Component B

300 g aminopropylert polypropylenglykol (gjennomsnittlig molekylvekt 400) 300 g aminopropylated polypropylene glycol (average molecular weight 400)

500 g aminopropylert polypropylenglykol (gjennomsnittlig molekylvekt 2000) og 500 g aminopropylated polypropylene glycol (average molecular weight 2000) and

20 g vann 20 g of water

Amininnhold: 2,44 m ekvivalenter/g Amine content: 2.44 m equivalents/g

2,17 g/m^ av den til 60°C oppvarmede komponent A ble påført på polyesterfolie (folietykkelse 12 ym) og 0,41 g/m<2 >av komponent B ble ved værelsestemperatur påført ved coronautladning forbehandlet polyetylenfolie av lav tetthet (folietykkelse 40 ym). Det molare forhold av komponentene utgjør 2,2 : 1 (isocyanat : amin). 2.17 g/m^ of component A heated to 60°C was applied to polyester foil (foil thickness 12 ym) and 0.41 g/m<2> of component B was applied at room temperature by corona discharge to pre-treated polyethylene foil of low density ( foil thickness 40 ym). The molar ratio of the components is 2.2:1 (isocyanate:amine).

Begynnelsesklebrighet (30 sekunder etter sammenklebing): Initial tackiness (30 seconds after bonding):

10 p/ 15 mm 10 p/ 15 mm

Sluttfasthet (etter tre dager): 380 p/15 mm. Final strength (after three days): 380 p/15 mm.

Claims (4)

1. Fremgangsmåte til fremstilling av sammensatte folier under anvendelse av oppløsningsmiddelfrie klebestoffer på basis av isocyanatklebere, karakterisert ved at man på en av de to folier som skal sammenklebes påfører en eller flere, minst to endeplasserte isocyanatgruppeholdige polyetere,hvis molekylvekt ligger mellom 2000 og 5000 og på den annen folie påfører en eller flere, minst to reaksjonsdyktige aminogruppeholdige langkjedede forbindelser, idet det molare, forhold mellom isocyanatgrupper og aminogrupper ligger mellom 1:1 og 5:1 og begge komponenter foreligger til sammen i en mengde fra 0,5-5,0 g/m 2 og de to dannede folieoverflater sammentrykkes i kort- tid.1. Method for the production of composite foils using solvent-free adhesives based on isocyanate adhesives, characterized in that on one of the two foils to be glued together one or more, at least two terminally placed isocyanate group-containing polyethers are applied, whose molecular weight is between 2000 and 5000 and on the other foil, one or more, at least two reactive amino group-containing long-chain compounds are applied, the molar ratio between isocyanate groups and amino groups being between 1:1 and 5:1 and both components are present together in an amount from 0.5-5, 0 g/m 2 and the two foil surfaces formed are compressed for a short time. 2. Fremgangsmåte ifølge krav 1, karakterisert ved at man til den isocyanatgruppeholdige polyeter setter 0,5-20, fortrinnsvis 1-10 vekt-% av en forbindelse som minst har tre isocyanatgrupper, idet mengden refereres til den isocyanatgruppeholdige polyeter.2. Process according to claim 1, characterized in that 0.5-20, preferably 1-10% by weight of a compound which has at least three isocyanate groups is added to the polyether containing isocyanate groups, the amount being referred to the polyether containing isocyanate groups. 3. Fremgangsmåte ifølge krav 1 og 2, karakterisert ved at man som minst to reaksjonsdyktige aminogruppeholdige forbindelser anvender omsetningsprodukter av polyetere med acrylnitril som deretter ble hydrogener!;.3. Method according to claims 1 and 2, characterized in that reaction products of polyethers with acrylonitrile which then became hydrogens are used as at least two reactive amino group-containing compounds. 4. Fremgangsmåte ifølge krav 1-4, karakterisert ved at den aminogruppeholdige forbindelse tilsettes 1-50, fortrinnsvis 1-15 vekt-% vann, idet mengden refereres til den aminogruppeholdige forbindelse.4. Method according to claims 1-4, characterized in that the amino group-containing compound is added 1-50, preferably 1-15% by weight of water, the amount being referred to the amino group-containing compound.
NO781209A 1977-04-27 1978-04-05 PROCEDURE FOR THE MANUFACTURE OF COMPOSITE FILES NO148988C (en)

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NL8601404A (en) * 1986-05-30 1987-12-16 Papier Plastic Coating Groning DATA-CARRYING CARD, METHOD FOR MAKING SUCH CARD AND DEVICE FOR CARRYING OUT THIS METHOD
CA1279249C (en) * 1986-05-30 1991-01-22 Randall C. Rains Two component polyurethane adhesive
US4743672A (en) * 1987-02-26 1988-05-10 Ashland Oil, Inc. Sag resistant, two component urethane adhesives
US4876308A (en) * 1988-02-18 1989-10-24 Gencorp Inc. Polyurethane adhesive for a surface treatment-free fiber reinforced plastic
CN106257984B (en) * 2014-05-08 2019-08-30 陶氏环球技术有限责任公司 Can be used for bonding glass can humectation solidify polyurethane adhesive compositions acceleration solidification
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US3668173A (en) * 1969-12-10 1972-06-06 Allied Chem Novel polyurethane-urea composition
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