NO179752B - Means for impregnating cellulosic fibrous materials - Google Patents
Means for impregnating cellulosic fibrous materials Download PDFInfo
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- NO179752B NO179752B NO891708A NO891708A NO179752B NO 179752 B NO179752 B NO 179752B NO 891708 A NO891708 A NO 891708A NO 891708 A NO891708 A NO 891708A NO 179752 B NO179752 B NO 179752B
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- water
- solution
- melamine
- agent
- condensate
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- 239000002657 fibrous material Substances 0.000 title claims description 5
- 239000000243 solution Substances 0.000 claims abstract description 37
- 229920000877 Melamine resin Polymers 0.000 claims abstract description 22
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 15
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000000203 mixture Substances 0.000 claims abstract description 11
- IVJISJACKSSFGE-UHFFFAOYSA-N formaldehyde;1,3,5-triazine-2,4,6-triamine Chemical compound O=C.NC1=NC(N)=NC(N)=N1 IVJISJACKSSFGE-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000007864 aqueous solution Substances 0.000 claims abstract description 8
- 239000001913 cellulose Substances 0.000 claims abstract description 5
- 229920002678 cellulose Polymers 0.000 claims abstract description 5
- 239000003795 chemical substances by application Substances 0.000 claims description 27
- 238000005470 impregnation Methods 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 27
- 229920005989 resin Polymers 0.000 claims description 23
- 239000011347 resin Substances 0.000 claims description 23
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 16
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 claims description 10
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 8
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 6
- YNAVUWVOSKDBBP-UHFFFAOYSA-N Morpholine Chemical compound C1COCCN1 YNAVUWVOSKDBBP-UHFFFAOYSA-N 0.000 claims description 6
- 230000002378 acidificating effect Effects 0.000 claims description 5
- 150000001298 alcohols Chemical class 0.000 claims description 5
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 4
- 239000006185 dispersion Substances 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- 239000000080 wetting agent Substances 0.000 claims description 4
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 3
- 229920001577 copolymer Polymers 0.000 claims description 3
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 claims description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 2
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 2
- 125000005397 methacrylic acid ester group Chemical group 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- 150000001412 amines Chemical class 0.000 claims 1
- 229920003180 amino resin Polymers 0.000 claims 1
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 abstract description 14
- 239000003960 organic solvent Substances 0.000 abstract description 10
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 abstract description 2
- 239000002253 acid Substances 0.000 abstract description 2
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 239000004744 fabric Substances 0.000 abstract 1
- 239000000835 fiber Substances 0.000 abstract 1
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 12
- 239000011541 reaction mixture Substances 0.000 description 5
- 230000008961 swelling Effects 0.000 description 5
- BNCADMBVWNPPIZ-UHFFFAOYSA-N 2-n,2-n,4-n,4-n,6-n,6-n-hexakis(methoxymethyl)-1,3,5-triazine-2,4,6-triamine Chemical compound COCN(COC)C1=NC(N(COC)COC)=NC(N(COC)COC)=N1 BNCADMBVWNPPIZ-UHFFFAOYSA-N 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 235000006408 oxalic acid Nutrition 0.000 description 4
- 230000035515 penetration Effects 0.000 description 4
- -1 amine salts Chemical class 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- MBHRHUJRKGNOKX-UHFFFAOYSA-N [(4,6-diamino-1,3,5-triazin-2-yl)amino]methanol Chemical class NC1=NC(N)=NC(NCO)=N1 MBHRHUJRKGNOKX-UHFFFAOYSA-N 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000011888 foil Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 239000002966 varnish Substances 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 125000005037 alkyl phenyl group Chemical group 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000006266 etherification reaction Methods 0.000 description 1
- 150000002191 fatty alcohols Chemical class 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004922 lacquer Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical compound CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 150000004072 triols Chemical class 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G12/00—Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen
- C08G12/02—Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes
- C08G12/40—Chemically modified polycondensates
- C08G12/42—Chemically modified polycondensates by etherifying
- C08G12/424—Chemically modified polycondensates by etherifying of polycondensates based on heterocyclic compounds
- C08G12/425—Chemically modified polycondensates by etherifying of polycondensates based on heterocyclic compounds based on triazines
- C08G12/427—Melamine
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L61/00—Compositions of condensation polymers of aldehydes or ketones; Compositions of derivatives of such polymers
- C08L61/20—Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen
- C08L61/32—Modified amine-aldehyde condensates
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Paper (AREA)
- Phenolic Resins Or Amino Resins (AREA)
- Materials For Medical Uses (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Abstract
Description
Oppfinnelsen gjelder et middel for impregnering av celluloseholdige fiberstoffer på grunnlag av en vandig løsning av et melamin-formaldehyd-kondensat som minst delvis er foretret med alkohol, som spesielt egner seg for impregnering av tykt papir med høy flatevekt. The invention relates to an agent for impregnating cellulose-containing fiber materials based on an aqueous solution of a melamine-formaldehyde condensate that is at least partially etherified with alcohol, which is particularly suitable for impregnating thick paper with a high basis weight.
Det er f.eks. kjent fra DE-OS 2005166 å fremstille vann-løselige, foretrede metylolmelaminer under medanvendelse av en 2- eller 3-verdig alkohol og en 1-verdig alkohol. Produktene tjener spesielt til tekstilutrustning, som midler som gir grep ved utrustning av materialer av syntesefibre og som tilsetnings-produkt for klebestoffer. It is e.g. known from DE-OS 2005166 to prepare water-soluble etherified methylol melamines using a 2- or 3-hydric alcohol and a 1-hydric alcohol. The products serve particularly for textile equipment, as agents that provide grip when equipping materials made of synthetic fibers and as an additive product for adhesives.
Det er også kjent fra DE-AS 1932528 og DE-OS 3430248 å anvende vandige resp. vandig-alkaliske løsninger av melamin-formaldehyd-forkondensater til impregnering av papir-baner, som etter tørking forarbeides til sjiktpresstoffer eller anvendes til overflate-behandling av treverkstoffer. Papirbanene er ikke særlig tykke, for det meste ca. 0,1 mm tykke, og videreforarbeides enkeltvis eller ved påhverandrelegging av flere sjikt. Kvaliteten av impregneringsharpiksene, impregneringsmetodene og videre-forarbeidelsesmetodene er tallrike og har allerede nådd en høy perfeksj onsgrad. It is also known from DE-AS 1932528 and DE-OS 3430248 to use aqueous or aqueous-alkaline solutions of melamine-formaldehyde pre-condensates for the impregnation of paper webs, which after drying are processed into layered press materials or used for the surface treatment of wood materials. The paper webs are not very thick, mostly approx. 0.1 mm thick, and can be further processed individually or by overlapping several layers. The quality of the impregnation resins, impregnation methods and further processing methods are numerous and have already reached a high degree of perfection.
Vanskeligere er impregneringsprosessen når det anvendes tykkere papirer, f.eks. slike med tykkelser på 0,1 til 0,7 mm, som substrat. Det er lett å innse at motsatte krav, som grundig penetrering og impregneringshastighet, er vanskeligere å oppfylle med tykkere papirer og at særlige forholdsregler er nødvendige, for å oppnå spaltningsfrie og elastiske produkter. Derfor tilsettes vanligvis impregneringsløsningene av handelsvanlige harpikser organiske løsningsmidler, f.eks. metanol, etanol eller isopropanol, for å oppnå en god og rask inntrengning av harpiksen i papiret. Medanvendelsen av organiske løsningsmidler har bl.a. de ulemper, at de ved tørking belaster avluften og miljøet og i tillegg utgjør tap av råstoffer. The impregnation process is more difficult when thicker papers are used, e.g. such with thicknesses of 0.1 to 0.7 mm, as substrate. It is easy to realize that opposite requirements, such as thorough penetration and impregnation speed, are more difficult to fulfill with thicker papers and that special precautions are necessary to achieve split-free and elastic products. Therefore, organic solvents, e.g. methanol, ethanol or isopropanol, to achieve good and rapid penetration of the resin into the paper. The combined use of organic solvents has, among other things, the disadvantages are that, when dried, they burden the exhaust air and the environment and, in addition, constitute a loss of raw materials.
Det lå til grunn for foreliggende oppfinnelse å tilveiebringe midler for impregnering av celluloseholdige fiberstoffer, som også egner seg for impregnering av tykkere bærestoffer, spesielt tykkere papirer, også uten medanvendelse av organiske løsnings-midler som alkoholer, og allikevel gir en god inntrengning av impregneringsharpiksen i papiret ved vanlige gjennomløps-hastigheter, bevirker liten svelling av papiret med god hefting til bærematerialer, videre en spaltningsfasthet og tilstrekkelig elastisitet hos det impregnerte papiret med en god planstilling så vel som at det oppviser god lakkholdeevne og tilstrekkelig holdbarhet for impregneringsløsningen. It was the basis of the present invention to provide means for impregnating cellulose-containing fibrous materials, which are also suitable for impregnating thicker carriers, especially thicker papers, also without the co-use of organic solvents such as alcohols, and still provide a good penetration of the impregnation resin in the paper at normal throughput speeds, causes little swelling of the paper with good adhesion to support materials, further a splitting resistance and sufficient elasticity of the impregnated paper with a good flatness as well as that it exhibits good varnish retention and sufficient durability for the impregnation solution.
Det ble nå funnet at et middel for impregnering av celluloseholdige fiberstoffer på grunnlag av en vandig løsning av et melamin-formaldehyd-kondensat som minst delvis er foretret med alkohol, i høy grad oppfyller den stilte oppgave, når midlet er fremstilt ved å omsette It has now been found that an agent for impregnating cellulose-containing fiber materials based on an aqueous solution of a melamine-formaldehyde condensate which has been at least partially etherified with alcohol, to a large extent fulfills the stated task, when the agent is prepared by reacting
A - en løsning som høyst opptar 50 vekt%, regnet på harpiksmengden, av vann uten å danne to faser, av et ved omsetning av dens alkaliske, vandige løsning med metanol foretret melamin-formaldehyd-kondensat, hvor 4,5-6 hydrogenatomer i A - a solution which takes up at most 50% by weight, calculated on the amount of resin, of water without forming two phases, of a by reaction of its alkaline aqueous solution with methanol etherified melamine-formaldehyde condensate, where 4.5-6 hydrogen atoms in
melaminet er substituert med N-metoksymetylgrupper, med the melamine is substituted with N-methoxymethyl groups, med
B - minst ett mol, pr. mol av kondensatet, av en vannløselig B - at least one mole, per moles of the condensate, of a water-soluble
2- eller 3-verdig alkohol ved 50-100°C ved sur pH-verdi til det oppstår en ubegrenset vannblandbar tilstand i løsningen, i hvilken harpiksen danner en klar løsning med vann i ethvert blandingsforhold. 2- or 3-hydric alcohol at 50-100°C at acidic pH until an unlimited water-miscible state occurs in the solution, in which the resin forms a clear solution with water in any mixing ratio.
Utgangsløsningen av det foretrede melamin-formaldehyd-kondensatet (A) kan fremstilles på i og for seg kjent måte, f.eks. ved kondensasjon av et mol melamin med minst 4,5 mol, foretrukket The starting solution of the etherified melamine-formaldehyde condensate (A) can be prepared in a manner known per se, e.g. by condensation of one mole of melamine with at least 4.5 moles, preferred
5 til 10 mol formaldehyd i alkalisk, vandig løsning og etter-følgende en eller flere gangers foretring av metylolgruppene i kondensatet med tilsatt overskudd av vannløselig, enverdig, alifatisk alkohol, spesielt metanol eller etanol, f.eks. 10 mol metanol pr. mol melamin, i surt miljø, f.eks. ved en pH-verdi på 4 til 6,5. Etter delvis avdestillering av alkohol-vann-blandingen oppstår et vannuforenlig produkt eller et produkt som bare er begrenset vannforenlig, d.v.s. som maksimalt opptar 50 vekt% vann beregnet på harpiksmengden, uten å danne to faser. 5 to 10 mol of formaldehyde in alkaline, aqueous solution and subsequent etherification of the methylol groups in the condensate one or more times with an added excess of water-soluble, monovalent, aliphatic alcohol, especially methanol or ethanol, e.g. 10 moles of methanol per moles of melamine, in an acidic environment, e.g. at a pH value of 4 to 6.5. After partial distillation of the alcohol-water mixture, a water-incompatible product or a product that is only partially water-compatible, i.e. which takes up a maximum of 50% by weight of water calculated on the amount of resin, without forming two phases.
Av de foretrede N-metylol-melaminer som anvendes ved fremstilling av impregneringsmidlet har heksakismetoksymetylmelamin vist seg egnet. Of the etherified N-methylol melamines used in the production of the impregnating agent, hexakismethoxymethylmelamine has proven suitable.
Viskositeten i de vandige løsningene av det foretrede utgangs-kondensatet (A) ligger fordelaktig på 2500 til 7000 mPa.s, spesielt 3000 til 5000 mPa.s, målt i en ca. 95%ig løsning (95% ikke-flyktige andeler) etter DIN 53 018 (rotasjons-viskosimeter). The viscosity of the aqueous solutions of the etherified starting condensate (A) is advantageously 2500 to 7000 mPa.s, especially 3000 to 5000 mPa.s, measured in an approx. 95% solution (95% non-volatile components) according to DIN 53 018 (rotational viscometer).
Omsetningen av den foretrede kondensatløsningen med 2- og/ eller 3-verdig alkohol (B) foregår under oppvarming av løsningen til 50 til 100°C og foretrukket 70 til 95°C ved en sur pH-verdi i løsningen, foretrukket ved en pH-verdi på 3,0 til 6,5 og spesielt 3,5 til 5, hvorved denne innstilles ved tilsetning av en uorganisk syre som salt-, svovel- eller fosfor-syre eller foretrukket en organisk syre, spesielt en dikarbok-sylsyre som maleinsyre og foretrukket oksalsyre. Til slutt må det oppnås en temperatur ved hvilken den lavere monoalkoholen avdampes. The reaction of the etherified condensate solution with 2- and/or 3-valent alcohol (B) takes place while heating the solution to 50 to 100°C and preferably 70 to 95°C at an acidic pH value in the solution, preferably at a pH value of 3.0 to 6.5 and especially 3.5 to 5, whereby this is set by adding an inorganic acid such as hydrochloric, sulfuric or phosphoric acid or preferably an organic acid, especially a dicarboxylic acid such as maleic acid and preferably oxalic acid. Finally, a temperature must be reached at which the lower monoalcohol evaporates.
Som vannløselige 2- eller 3-verdige alkoholer (B) egner seg for omsetningen særlig vannløselige alkoholer med 2 til 6 C-atomer og foretrukket etylenglykol, di- og trietylenglykol så vel som glyserol. Men også andre vannløselige glykoler er egnet, f.eks. polyetylenglykoler, eller trioler, som ved omsetningen overfører harpiksløsningen til en ubegrenset vannblandbar tilstand. Mengden av polyalkohol (B) for omsetningen er minst 1 mol pr. mol melamin i impregneringsharpiks (A) i løsningen som skal omsettes og fordelaktig 1 til 5 mol pr. mol melamin. Omsetningen gjennomføres med fordel under omrøring og så lenge at vannuforenligheten eller den bare begrensede vannforenligheten som foreligger til å begynne med er gått over til en ubegrenset vannblandbarhet resp. full vannfortynnbarhet, noe som i alminnelighet skjer på ca. 2 til 5 timer. As water-soluble 2- or 3-hydric alcohols (B), water-soluble alcohols with 2 to 6 C atoms and preferably ethylene glycol, di- and triethylene glycol as well as glycerol are suitable for the reaction. But other water-soluble glycols are also suitable, e.g. polyethylene glycols, or triols, which during the reaction transfer the resin solution to an unlimited water-miscible state. The quantity of polyalcohol (B) for the turnover is at least 1 mol per moles of melamine in impregnation resin (A) in the solution to be reacted and advantageously 1 to 5 moles per moles of melamine. The turnover is advantageously carried out while stirring and for as long as the water incompatibility or the only limited water compatibility that exists to begin with has changed to an unlimited water miscibility resp. full water dilutability, which generally occurs in approx. 2 to 5 hours.
Den ubegrenset vannblandbare tilstanden til impregnerings-harpiksløsningen blir dermed oppnådd på det tidspunkt harpiksen danner en klar løsning med vann i et hvert blandingsforhold. The unlimited water-miscible state of the impregnation resin solution is thus achieved at the time the resin forms a clear solution with water in any mixing ratio.
Etter oppnåelse av den ubegrensede vannfortynnbarheten avkjøles impregneringsharpiksløsningen. Den resulterende impregnerings-harpiksløsningen viser etter omsetningen en klart senket viskositet sammenlignet med utgangsløsningen, som ofte ligger ved bare 1/4 til 2/3 av viskositetsverdien i utgangs-løsningen (i mPa.s). After achieving the unlimited water dilutability, the impregnation resin solution is cooled. The resulting impregnation resin solution shows after the reaction a clearly lowered viscosity compared to the starting solution, which is often only 1/4 to 2/3 of the viscosity value in the starting solution (in mPa.s).
Impregneringsharpiksløsningene ifølge oppfinnelsen inneholder ingen tilsatte, organiske løsningsmidler som monoalkoholer, og utgjør derfor ingen belastning på miljøet ved anvendelsen. The impregnation resin solutions according to the invention contain no added organic solvents such as monoalcohols, and therefore pose no burden on the environment during use.
For mange anvendelser kan midlet med fordel tilsettes fuktemidler, for det meste i en mengde under 1 vekt%, f.eks. fettalkohol-etoksylat eller alkylfenyletoksylat eller blandinger av disse. For many applications, the agent can advantageously be added to wetting agents, mostly in an amount below 1% by weight, e.g. fatty alcohol ethoxylate or alkylphenyl ethoxylate or mixtures thereof.
Fordelaktig inneholder midlet i form av den impregneringsløsning som skal anvendes videre et tilsatt, surt virkende herdemiddel av kjent type, som syrer, ammoniakk- eller aminsalter som er spalt-bare i varmen, av hvilke p-toluensulfonsyre og dens aminsalter, og helst blandinger av morfolin og p-toluensulfon-syre har vist seg særlig fordelaktig. Advantageously, the agent in the form of the impregnation solution to be used further contains an added, acid-acting curing agent of a known type, such as acids, ammonia or amine salts which are decomposable in the heat, of which p-toluenesulfonic acid and its amine salts, and preferably mixtures of morpholine and p-toluenesulfonic acid have proved particularly advantageous.
Fordelaktige midler i form av impregneringsløsninger inneholder på 100 vektdeler av impregneringsharpiksen (ca. 80 vektlig) 0-100 vektdeler vann, 3-6 vektdeler p-toluensulfonsyre (50%ig) og 0,2 til 0,6 vektdeler fuktemiddel. Advantageous agents in the form of impregnation solutions contain 0-100 parts by weight of water, 3-6 parts by weight of p-toluenesulfonic acid (50%) and 0.2 to 0.6 parts by weight of wetting agent per 100 parts by weight of the impregnation resin (approx. 80 by weight).
For økning av holdbarheten kan midlene resp. impregne-ringsmiddelløsningene også tilsettes opptil ca. 2, fore-trukket 0,1 til 1, vekt% magnesiumklorid. To increase durability, the funds or the impregnating agent solutions are also added up to approx. 2, preferably 0.1 to 1% by weight of magnesium chloride.
Særlig for forbedring av lakkholdeevnen og elastisiteten er det også ofte fordelaktig å tilsette resp. blande midlene ifølge oppfinnelsen med en vandig dispersjon av et polymerisat eller kopolymerisat av en akryl- eller metakrylsyreester, foretrukket i mengder på opptil ca. 10 vekt% av midlet, f.eks. et kopolymerisat på basis av N-butylakrylat, akrylnitril, metakryl-syre og metakrylamid. Especially for improving the paint's holding power and elasticity, it is also often advantageous to add resp. mixing the agents according to the invention with an aqueous dispersion of a polymer or copolymer of an acrylic or methacrylic acid ester, preferably in amounts of up to approx. 10% by weight of the agent, e.g. a copolymer based on N-butyl acrylate, acrylonitrile, methacrylic acid and methacrylamide.
Ved anvendelsen av midlene ifølge oppfinnelsen oppviser impregneringsløsningen fordelaktig en pH-verdi fra 3 til 6. When using the agents according to the invention, the impregnation solution advantageously exhibits a pH value of from 3 to 6.
Impregneringsharpiksløsningene ifølge oppfinnelsen gir en fordelaktig impregnering av også tykkere papir uten den ellers vanlige tilsetningen av alkoholer som isopropanol eller av andre organiske løsningsmidler med god, jevnt bibeholdt kvalitet på de fremstilte kantfilmene. Dermed fremstilte møbelkanter er elastiske, har liten papirsvelling og er også spaltningsfaste. Ved forarbeidelsen av impregneringsmidlet ifølge oppfinnelsen er det ingen miljøbelastning av organiske løsningmidler, og den avgitte mengde formaldehyd er også redusert. Brukeren kan således unngå avgassrensing og etterforbrenningsanlegg. The impregnation resin solutions according to the invention provide an advantageous impregnation of even thicker paper without the otherwise usual addition of alcohols such as isopropanol or of other organic solvents with good, uniformly maintained quality of the produced edge films. Furniture edges produced in this way are elastic, have little paper swelling and are also split-resistant. During the processing of the impregnation agent according to the invention, there is no environmental impact from organic solvents, and the amount of formaldehyde released is also reduced. The user can thus avoid exhaust gas cleaning and afterburning facilities.
Ytterligere fordeler ved oppfinnelsen fremgår av de etterfølgende eksempler og sammenligningsforsøk som beskriver oppfinnelsen. De deri angitte deler og prosenter beregnes på vekt om ikke annet er angitt. Further advantages of the invention can be seen from the following examples and comparative tests which describe the invention. The parts and percentages stated therein are calculated by weight unless otherwise stated.
Eksempel 1 Example 1
I en 2-liters trehalskolbe med rører, termometer og tilbake-løpskjøler ble 400 g (1,14 mol beregnet på melamin) av teknisk heksakismetoksymetylmelamin med et molforhold melamin: formaldehydrmetoksylgrupper = 1:5,7:5,2 = (viskositet: 4000 mPa.s) tilsatt 150 g (1,41 mol) dietylenglykol. Etter tilsetning av 0,2 g oksalsyre ble blandingen oppvarmet til 90°C. Derved ble det inn-stilt en pH-verdi på 4,2. In a 2-liter wooden-necked flask with stirrer, thermometer and reflux condenser, 400 g (1.14 mol calculated for melamine) of technical hexakismethoxymethylmelamine with a molar ratio of melamine:formaldehyde methoxyl groups = 1:5.7:5.2 = (viscosity: 4000 mPa.s) added 150 g (1.41 mol) diethylene glycol. After adding 0.2 g of oxalic acid, the mixture was heated to 90°C. A pH value of 4.2 was thereby set.
Reaksjonsblandingen ble omrørt ved 90°C så lenge at vann-uf orenligheten i starten var gått over til en fullstendig vannfortynnbarhet. For å oppnå dette var det nødvendig med 1-2 timer. Etter oppnåelse av vannfortynnbarheten ble reaksjons-blandingen avkjølt til romtemperatur. The reaction mixture was stirred at 90°C for so long that the water impurity at the start had changed to complete water dilutability. To achieve this, 1-2 hours were needed. After achieving the water dilutability, the reaction mixture was cooled to room temperature.
Det ble oppnådd 550 g av en impregneringsharpiksløsning ifølge oppfinnelsen med etterfølgende egenskaper: Ikke-flyktige andeler (2 g prøve, tørket i 2 timer ved 125°C) : 82,1%, viskositet: 740 mPa.s, vannfortynnbarhet: 1: uendelig. 550 g of an impregnation resin solution according to the invention were obtained with the following properties: Non-volatile fractions (2 g sample, dried for 2 hours at 125°C) : 82.1%, viscosity: 740 mPa.s, water dilutability: 1: infinite .
Eksempel 2 Example 2
I en 2-liters trehalskolbe med rører, termometer og tilbake-løpskjøler ble 400 g (1,14 mol beregnet på melamin) av teknisk heksakismetoksymetylmelamin med et molforhold melamin: formaldehyd:metoksylgrupper = 1:5,7:5,2 (viskositet: 4.320 mPa.s) tilsatt 150 g (1,23 mol) trietylenglykol og oppvarmet til 90°C etter tilsetning av 0,2 g oksalsyre. In a 2-liter wooden-necked flask with stirrer, thermometer and reflux condenser, 400 g (1.14 mol calculated on melamine) of technical hexakismethoxymethylmelamine with a molar ratio of melamine:formaldehyde:methoxyl groups = 1:5.7:5.2 (viscosity: 4,320 mPa.s) added 150 g (1.23 mol) triethylene glycol and heated to 90°C after addition of 0.2 g oxalic acid.
Reaksjonsblandingen ble omrørt så lenge ved 90°C at vann-uf orenligheten fra starten var gått over til en fullstendig vannfortynnbarhet. 4 timer var nødvendig for dette. Etter oppnådd vannfortynnbarhet ble reaksjonsblandingen avkjølt til rom-temperatur. The reaction mixture was stirred at 90°C for such a long time that the water impurity from the start had changed to complete water dilutability. 4 hours were needed for this. After achieving water dilutability, the reaction mixture was cooled to room temperature.
Det ble oppnådd 550 g av en impregneringsharpiksløsning ifølge oppfinnelsen med følgende egenskaper: Ikke-flyktige andeler (2 g prøve, tørket i 2 timer med 125°C) : 82,2%, viskositet: 550 g of an impregnation resin solution according to the invention were obtained with the following properties: Non-volatile components (2 g sample, dried for 2 hours at 125°C) : 82.2%, viscosity:
210 mPa.s, vannfortynnbarhet: 1: uendelig. 210 mPa.s, water dilutability: 1: infinite.
Eksempel 3 Example 3
I en 2-liters trehalskolbe med rører, termometer og tilbakeløps-kjøler ble 400 g (1,14 mol beregnet på melamin) av teknisk heksakismetoksymetylmelamin med et molforhold melamin: formaldehyd: metoksylgrupper =1 : 5,7 : 5,2 (viskositet: 4500 mPa.s) tilsatt 150 g (1,65 mol) glyserol og oppvarmet til 90°C etter tilsetning av 0,2 g oksalsyre. In a 2-liter wooden-necked flask with stirrer, thermometer and reflux condenser, 400 g (1.14 mol calculated for melamine) of technical hexakismethoxymethylmelamine with a molar ratio of melamine: formaldehyde: methoxyl groups = 1 : 5.7 : 5.2 (viscosity: 4500 mPa.s) added 150 g (1.65 mol) glycerol and heated to 90°C after addition of 0.2 g oxalic acid.
Blandingen ble omrørt så lenge ved 90°C at vannuforenligheten i starten var gått over til en fullstendig vannfortynnbarhet. 4 timer var nødvendig for dette. Etter oppnåelse av vannfortynnbarheten ble reaksjonsblandingen avkjølt til rom-temperatur. The mixture was stirred at 90°C for such a long time that the initial water incompatibility had changed to complete water dilutability. 4 hours were needed for this. After achieving the water dilutability, the reaction mixture was cooled to room temperature.
Det ble oppnådd 550 g av en impregneringsharpiksløsning ifølge oppfinnelsen med følgende egenskaper: Ikke-flyktige andeler (2 g prøve, tørket i 2 timer ved 125°C) : 75,2 %, viskositet: 250 mPa.s, vannfortynnbarhet: 1: uendelig. 550 g of an impregnation resin solution according to the invention were obtained with the following properties: Non-volatile fractions (2 g sample, dried for 2 hours at 125°C) : 75.2%, viscosity: 250 mPa.s, water dilutability: 1: infinite .
Anvendelseseksempel 1 Application example 1
En blanding av 100 deler av den harpiksløsningen som er fremstilt ifølge eksempel 2, 3 deler av en blanding av morfolin og p-toluensulfonsyre (vektforhold 1 : 1) og 0,4 deler av en fukte-middelløsning (Kauropal<®> 930/931 i blandingsforhold 2:1) hadde en pH-verdi på 3,8. Geleringstiden var 5 min. Impregnerings-viskositeten lå på 13 sekunders utløpstid i et 4 mm DIN-beger ved 25°C. Impregneringsløsningens holdbarhet var minst 24 timer. A mixture of 100 parts of the resin solution prepared according to example 2, 3 parts of a mixture of morpholine and p-toluenesulfonic acid (weight ratio 1:1) and 0.4 parts of a wetting agent solution (Kauropal<®> 930/931 in a mixture ratio of 2:1) had a pH value of 3.8. The gelation time was 5 min. The impregnation viscosity was 13 seconds run time in a 4 mm DIN cup at 25°C. The durability of the impregnation solution was at least 24 hours.
Med den ovenfornevnte blandingen ble 150-28 0 g/m<2> tungt kantpapir impregnert.Papiret tilføres harpiks til ca. 50%, d.v.s. blir brakt til en sluttvekt på 225 henholdsvis 420 g/m<2>. VC-verdien (rest-fuktighet) innstilles derved på 2-4%. With the above-mentioned mixture, 150-280 g/m<2> heavy edge paper was impregnated. The paper is fed with resin to approx. 50%, i.e. is brought to a final weight of 225 and 420 g/m<2> respectively. The VC value (residual moisture) is thereby set to 2-4%.
De oppnådde kantene har en tykkelsessvelling i vann på 13 og lar seg bøye over en dor til ca. 6 mm uten brudd. The edges obtained have a thickness swelling in water of 13 and can be bent over a mandrel to approx. 6 mm without breakage.
Anvendelseseksempler 2 og 3 og sammenlignings! orsøk 1 og 2 Application examples 2 and 3 and comparison! causes 1 and 2
Til sammenligning ble det for impregnering av papir anvendt impregneringsmidler med harpiks ifølge eksempel 1 (anvendelseseksempel 2 såvel som anvendelseseksempel 3 (under tilsetning av en handelsvanlig akryldispersjon)), og uten tilsetning av organiske løsningsmidler, såvel som et handelsvanlig impregneringsmiddel, som ble forarbeidet én gang under tilsetning av organisk løsnings-middel (sammenligningsforsøk 1), én gang uten tilsetning av organisk løsningsmiddel (sammenligningsforsøk 2). Impregneringsmidlene og egenskapene for de impregnerte papirene fremgår av den etterfølgende tabell. For comparison, for the impregnation of paper, impregnating agents with resin according to example 1 (application example 2 as well as application example 3 (with the addition of a commercially available acrylic dispersion)) were used, and without the addition of organic solvents, as well as a commercially available impregnating agent, which was prepared once during the addition of organic solvent (comparison experiment 1), once without the addition of organic solvent (comparison experiment 2). The impregnating agents and the properties of the impregnated papers appear in the following table.
Inntrengningstiden ble bestemt som den tid som gikk fra påføring av en svart papirbane (120 g/m<2>, 40 mm diameter) på impregnerings-løsningen (impregneringsmiddel) til fullstendig fukting. Papir-svellingen ble bestemt i %, idet tykkelsessvellingen ble målt med en mikrometerskrue etter 24 timers lagring i vann. Elastisiteten ble bestemt ved bøying av den tørkede filmen rundt dorer med avtagende diameter til filmen brakk. The penetration time was determined as the time from application of a black paper web (120 g/m<2>, 40 mm diameter) to the impregnating solution (impregnating agent) until complete wetting. The paper swelling was determined in %, the thickness swelling being measured with a micrometer screw after 24 hours of storage in water. The elasticity was determined by bending the dried film around mandrels of decreasing diameter until the film broke.
Spaltningsfastheten ble bestemt i en manuell skjæretest på de impregnerte foliene. Brudd loddrett på overflaten: bra, brudd parallelt med overflaten: dårlig. The splitting strength was determined in a manual cutting test on the impregnated foils. Fracture perpendicular to the surface: good, fracture parallel to the surface: poor.
Tabellen viser at impregneringsmidlene ifølge oppfinnelsen oppviser tilfredsstillende egenskaper. Tilsettes en akrylat-dispersjon (anvendelseseksempel 3) oppnås en særlig god såkalt lakkholdeevne, d.v.s. at et lakkstrøk på folien ikke synker inn. The table shows that the impregnation agents according to the invention exhibit satisfactory properties. If an acrylate dispersion is added (application example 3), a particularly good so-called lacquer holding capacity is achieved, i.e. that a coat of varnish on the foil does not sink in.
Claims (8)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3814292A DE3814292A1 (en) | 1988-04-28 | 1988-04-28 | AGENT FOR DRINKING FIBER FABRICS CONTAINING CELLULOSE |
Publications (4)
Publication Number | Publication Date |
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NO891708D0 NO891708D0 (en) | 1989-04-25 |
NO891708L NO891708L (en) | 1989-10-30 |
NO179752B true NO179752B (en) | 1996-09-02 |
NO179752C NO179752C (en) | 1996-12-11 |
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Family Applications (1)
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NO891708A NO179752C (en) | 1988-04-28 | 1989-04-25 | Means for impregnating cellulosic fibrous materials |
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EP (1) | EP0342386B1 (en) |
AT (1) | ATE103618T1 (en) |
DE (2) | DE3814292A1 (en) |
ES (1) | ES2061767T3 (en) |
NO (1) | NO179752C (en) |
Families Citing this family (8)
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DE3905913A1 (en) * | 1989-02-25 | 1990-09-13 | Basf Ag | AMINO SOLVENT SOLUTIONS WITH LOW ELECTRICAL CAPACITY |
AT398768B (en) * | 1991-08-05 | 1995-01-25 | Chemie Linz Gmbh | MODIFIED MELAMINE RESINS AND PREPREGS AND LAMINATES BASED ON THIS MELAMINE RESINS |
DE4420013A1 (en) | 1994-06-08 | 1995-12-14 | Basf Ag | Melamine resin mixtures |
DE4439156A1 (en) | 1994-11-04 | 1996-05-09 | Cassella Ag | Impregnating resins for foils and edges |
AR040209A1 (en) * | 2002-06-14 | 2005-03-16 | Agrolinz Melamin Gmbh | RESIN AMINO MOLDING MATERIAL FOR PRODUCTS WITH IMPROVED FLEXIBILITY AND RESIN AMINO PRODUCTS WITH IMPROVED FLEXIBILITY |
DE10333893A1 (en) * | 2003-07-22 | 2005-02-10 | Kompetenzzentrum Holz Gmbh | Plastics and wood composites |
DE102004015737B3 (en) * | 2004-03-29 | 2005-12-22 | Basf Ag | Aqueous melamine resin mixture, useful for impregnating absorbent paper and absorbent support materials, comprises a resin content comprising polyvalent alcohols, caprolactam, 2-(2-phenoxy-ethoxy)-ethanol and/or polyethylene glycol |
EP2407513A1 (en) | 2010-06-23 | 2012-01-18 | Basf Se | Aqueous modified urea resin mixture, method for producing and use of same to saturate absorbent carriers and compound material produced using the urea resin material |
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NL131745C (en) * | 1967-05-23 | |||
DE2005166C3 (en) * | 1970-02-05 | 1975-05-15 | Chemische Fabrik Pfersee Gmbh, 8900 Augsburg | Process for the production of water-soluble, etherified methylolmelamines |
DE3632588A1 (en) * | 1986-09-25 | 1988-04-07 | Cassella Ag | METHOD FOR PRODUCING MELAMINE FORMALDEHYDE RESINS |
-
1988
- 1988-04-28 DE DE3814292A patent/DE3814292A1/en not_active Withdrawn
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1989
- 1989-04-22 DE DE89107284T patent/DE58907322D1/en not_active Expired - Lifetime
- 1989-04-22 EP EP89107284A patent/EP0342386B1/en not_active Expired - Lifetime
- 1989-04-22 AT AT89107284T patent/ATE103618T1/en not_active IP Right Cessation
- 1989-04-22 ES ES89107284T patent/ES2061767T3/en not_active Expired - Lifetime
- 1989-04-25 NO NO891708A patent/NO179752C/en unknown
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NO891708D0 (en) | 1989-04-25 |
ES2061767T3 (en) | 1994-12-16 |
DE3814292A1 (en) | 1989-11-09 |
DE58907322D1 (en) | 1994-05-05 |
NO179752C (en) | 1996-12-11 |
NO891708L (en) | 1989-10-30 |
EP0342386A1 (en) | 1989-11-23 |
ATE103618T1 (en) | 1994-04-15 |
EP0342386B1 (en) | 1994-03-30 |
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