SK5932002A3 - Coating an aluminum alloy substrate - Google Patents
Coating an aluminum alloy substrate Download PDFInfo
- Publication number
- SK5932002A3 SK5932002A3 SK593-2002A SK5932002A SK5932002A3 SK 5932002 A3 SK5932002 A3 SK 5932002A3 SK 5932002 A SK5932002 A SK 5932002A SK 5932002 A3 SK5932002 A3 SK 5932002A3
- Authority
- SK
- Slovakia
- Prior art keywords
- aluminum
- solution
- copolymer
- tank
- coating
- Prior art date
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- 238000000576 coating method Methods 0.000 title claims abstract description 28
- 239000011248 coating agent Substances 0.000 title claims abstract description 25
- 239000000758 substrate Substances 0.000 title claims abstract description 22
- 229910000838 Al alloy Inorganic materials 0.000 title claims description 32
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 32
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 28
- 229920001577 copolymer Polymers 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 229920000642 polymer Polymers 0.000 claims abstract description 22
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000003729 cation exchange resin Substances 0.000 claims abstract description 12
- 150000002903 organophosphorus compounds Chemical class 0.000 claims abstract description 11
- 229920002126 Acrylic acid copolymer Polymers 0.000 claims abstract description 6
- 125000001273 sulfonato group Chemical group [O-]S(*)(=O)=O 0.000 claims abstract 2
- 238000000034 method Methods 0.000 claims description 38
- 239000011347 resin Substances 0.000 claims description 16
- 229920005989 resin Polymers 0.000 claims description 16
- 150000002118 epoxides Chemical class 0.000 claims description 11
- -1 aluminum ions Chemical class 0.000 claims description 8
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 claims description 6
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 6
- 150000001875 compounds Chemical class 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 5
- 229920000915 polyvinyl chloride Polymers 0.000 claims description 5
- 239000004800 polyvinyl chloride Substances 0.000 claims description 5
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims description 4
- 239000007795 chemical reaction product Substances 0.000 claims description 4
- 229910021645 metal ion Inorganic materials 0.000 claims description 4
- ZTWTYVWXUKTLCP-UHFFFAOYSA-N vinylphosphonic acid Chemical compound OP(O)(=O)C=C ZTWTYVWXUKTLCP-UHFFFAOYSA-N 0.000 claims description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- 229920000728 polyester Polymers 0.000 claims description 3
- 238000002203 pretreatment Methods 0.000 claims description 3
- 239000008237 rinsing water Substances 0.000 claims description 3
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 2
- 239000008199 coating composition Substances 0.000 claims 2
- 238000007743 anodising Methods 0.000 claims 1
- 238000011010 flushing procedure Methods 0.000 claims 1
- 239000000243 solution Substances 0.000 abstract description 28
- 229910045601 alloy Inorganic materials 0.000 abstract description 5
- 239000000956 alloy Substances 0.000 abstract description 5
- 239000007864 aqueous solution Substances 0.000 abstract description 4
- JOUOJMIHRPQLAA-UHFFFAOYSA-N ethenylphosphonic acid;prop-2-enoic acid Chemical compound OC(=O)C=C.OP(O)(=O)C=C JOUOJMIHRPQLAA-UHFFFAOYSA-N 0.000 abstract description 4
- 238000001223 reverse osmosis Methods 0.000 abstract description 3
- 239000012528 membrane Substances 0.000 abstract description 2
- 238000000108 ultra-filtration Methods 0.000 abstract description 2
- 230000003716 rejuvenation Effects 0.000 abstract 1
- 239000000203 mixture Substances 0.000 description 7
- 239000002245 particle Substances 0.000 description 7
- 238000005260 corrosion Methods 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 238000007739 conversion coating Methods 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- 229920000620 organic polymer Polymers 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 238000011282 treatment Methods 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 229910001430 chromium ion Inorganic materials 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 239000000314 lubricant Substances 0.000 description 3
- 239000000049 pigment Substances 0.000 description 3
- 229920001467 poly(styrenesulfonates) Polymers 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910000861 Mg alloy Inorganic materials 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 2
- 239000011651 chromium Substances 0.000 description 2
- JOPOVCBBYLSVDA-UHFFFAOYSA-N chromium(6+) Chemical compound [Cr+6] JOPOVCBBYLSVDA-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 238000005098 hot rolling Methods 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 239000004408 titanium dioxide Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- DJHGAFSJWGLOIV-UHFFFAOYSA-N Arsenic acid Chemical compound O[As](O)(O)=O DJHGAFSJWGLOIV-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- ABLZXFCXXLZCGV-UHFFFAOYSA-N Phosphorous acid Chemical compound OP(O)=O ABLZXFCXXLZCGV-UHFFFAOYSA-N 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- 229920000180 alkyd Polymers 0.000 description 1
- 229940000488 arsenic acid Drugs 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical class [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 229910000151 chromium(III) phosphate Inorganic materials 0.000 description 1
- IKZBVTPSNGOVRJ-UHFFFAOYSA-K chromium(iii) phosphate Chemical compound [Cr+3].[O-]P([O-])([O-])=O IKZBVTPSNGOVRJ-UHFFFAOYSA-K 0.000 description 1
- 229920001688 coating polymer Polymers 0.000 description 1
- 238000005097 cold rolling Methods 0.000 description 1
- 210000003298 dental enamel Anatomy 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000007765 extrusion coating Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 150000002222 fluorine compounds Chemical class 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052735 hafnium Inorganic materials 0.000 description 1
- VBJZVLUMGGDVMO-UHFFFAOYSA-N hafnium atom Chemical compound [Hf] VBJZVLUMGGDVMO-UHFFFAOYSA-N 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 238000010335 hydrothermal treatment Methods 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 238000007746 phosphate conversion coating Methods 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate group Chemical group S(=O)(=O)([O-])[O-] QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 125000001174 sulfone group Chemical group 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/18—Pretreatment of the material to be coated
- C23C18/20—Pretreatment of the material to be coated of organic surfaces, e.g. resins
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/86—Regeneration of coating baths
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
- B05D7/14—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to metal, e.g. car bodies
- B05D7/16—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials to metal, e.g. car bodies using synthetic lacquers or varnishes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
- B05D7/50—Multilayers
- B05D7/51—One specific pretreatment, e.g. phosphatation, chromatation, in combination with one specific coating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D2202/00—Metallic substrate
- B05D2202/20—Metallic substrate based on light metals
- B05D2202/25—Metallic substrate based on light metals based on Al
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
- B05D7/50—Multilayers
- B05D7/52—Two layers
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Treatment Of Metals (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Laminated Bodies (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Other Surface Treatments For Metallic Materials (AREA)
- Paints Or Removers (AREA)
Abstract
Description
SPÔSOB POVLIEKANIA SUBSTRÁTU Z HLINÍKOVEJ ZLIATINYMETHOD OF COATING THE ALUMINUM ALLOY SUBSTRATE
Oblasť technikyTechnical field
Predložený vynález sa týka spôsobu povliekania substrátu z hliníkovej zliatiny polymérom. Vynález sa zvlášť týka spôsobu predbežnej úpravy substrátu hliníkovej zliatiny kopolymérom vinylfosfónovej kyseliny s akrylovou kyselinou pred povliekaním substrátu polymérom.The present invention relates to a method of coating an aluminum alloy substrate with a polymer. In particular, the invention relates to a process for pretreating an aluminum alloy substrate with a vinylphosphonic acid-acrylic acid copolymer prior to coating the substrate with a polymer.
Doterajší stav technikyBACKGROUND OF THE INVENTION
Hoci sa hliník sám chráni proti korózii vytváraním prírodného oxidačného povlaku, ochrana nie je úplná. Pri výskyte vlhkosti a elektrolytov, hliníkové zliatiny korodujú omnoho rýchlejšie ako čistý hliník.Although aluminum protects itself against corrosion by forming a natural oxidation coating, protection is not complete. When moisture and electrolytes occur, aluminum alloys corrode much faster than pure aluminum.
Preto je potreba upraviť substráty z hliníkovej zliatiny predbežnou úpravou alebo inými chemikáliami, ktoré poskytnú zlepšenú odolnosť voči korózii, rovnako ako prospešnú priľnavosť pre polyméry.Therefore, there is a need to treat aluminum alloy substrates with pretreatment or other chemicals that provide improved corrosion resistance as well as beneficial adhesion to polymers.
Doposiaľ boli v odbore chemické konverzné povlaky tvorené na hliníkových zliatinách konvertovaním povrchu kovu na pevne priľnavý povlak, ktorého časť sa skladala z oxidovanej formy hliníka. Chemické konverzné povlaky poskytujú vysokú odolnosť voči korózii a zlepšenú priľnavosť polymérových povlakov. Konverzný povlak z chrómu a fosforečnanu je obyčajne zaisťovaný stykom hliníka s vodným roztokom obsahujúcim ióny šesťmocného chrómu, ióny fosforečnanu a ióny fluoridu. V posledných rokoch vzrastajú záujmy ohľadne znečisťovania životného prostredia účinkami chrómanov a fosforečnanov vypustenými do vodných tokov pri takýchto spôsoboch. Vzhľadom k vysokej rozpustnosti a silnej oxidačnej vlastnosti iónov šesťmocného chrómu, musia byť na nakladanie s odpadom použité drahé postupy likvidácie odpadu na redukciu iónov šesťmocného chrómu na ióny trojmocného chrómu.To date, chemical conversion coatings have been formed on aluminum alloys by converting the metal surface into a firmly adherent coating, some of which consisted of an oxidized form of aluminum. Chemical conversion coatings provide high corrosion resistance and improved adhesion of polymer coatings. The chromium-phosphate conversion coating is usually provided by contacting aluminum with an aqueous solution containing hexavalent ions, phosphate ions and fluoride ions. In recent years, concerns have been increasing regarding the pollution of the environment by the effects of chromates and phosphates discharged into watercourses in such processes. Due to the high solubility and strong oxidizing properties of hexavalent chromium ions, expensive waste disposal procedures must be used to reduce hexavalent chromium ions to trivalent chromium ions.
922/B922 / B
V doterajšom stave techniky boli v tejto oblasti urobené pokusy vyrobiť prijateľné konverzné povlaky pre hliník bez chrómanov. Napríklad niektoré konverzné povlaky bez chrómanov obsahujú zirkón, titán, hafnium a/alebo kremík, niekedy kombinované s fluoridmi, povrchovo aktívnymi látkami a polymérmi, ako je kyselina polyakrylová. Napriek rozsiahlemu úsiliu, ktoré bolo v minulosti vykonané, dosiaľ nie je úplne uspokojivo vyriešené konverzné povliekanie bez chrómanov alebo základ pre zdokonalenie priľnavosti a odolnosti polymérov, ktoré povliekajú substráty z hliníkovej zliatiny, voči korózii. Priľnavosť polyméru a odolnosť voči korózii sú dôležité vlastnosti povlakov listov z hliníkovej zliatiny, používaných na výrobu telies a ukončenie zásobníkov na potraviny a koncov zásobníkov na nápoje.Attempts have been made in the art to produce acceptable conversion coatings for chromate-free aluminum. For example, some chromate-free conversion coatings contain zirconium, titanium, hafnium and / or silicon, sometimes combined with fluorides, surfactants and polymers such as polyacrylic acid. Despite extensive efforts in the past, chromium-free conversion coating or the basis for improving the corrosion-resistant adhesion and resistance of polymers that coat aluminum alloy substrates has not been satisfactorily solved yet. Adhesion of the polymer and corrosion resistance are important properties of the aluminum alloy sheet coatings used to make the bodies and end of the food containers and the ends of the beverage containers.
V doterajšom stave techniky boli taktiež urobené pokusy upraviť predbežné substráty rôznymi organofosforečnými zlúčeninami pred ich povliekaním polymérom. Tu použitý termín „organofosforečné zlúčeniny“ zahrňuje organofosforečné zlúčeniny, organofosfínové zlúčeniny, organofosfónové zlúčeniny, rovnako ako rôzne soli, estery, parciálne soli a parciálne estery takýchto kyselín. Napríklad holandský patent č. 263 668 zoAttempts have also been made in the prior art to treat pre-substrates with various organophosphorus compounds prior to coating them with polymer. As used herein, the term "organophosphorus compounds" includes organophosphorus compounds, organophosphine compounds, organophosphonic compounds, as well as various salts, esters, partial salts, and partial esters of such acids. For example, Dutch patent no. 263 668 zo
14. apríla 1961 popisuje spôsob, pri ktorom sú oceľové listy upravované kopolymérom vinylfosfónovej kyseliny s akrylovou kyselinou pred povliekaním alkydovým živicovým smaltom. Hoci niektoré organofosforečné predbežné úpravy môžu účinkovať obdobne, je finančne náročné ich zavádzať. Stále teda zostáva potreba poskytnúť účinný a hospodárny spôsob na predbežnú úpravu substrátu hliníkovej zliatiny organofosforečnou zlúčeninou pred aplikáciou povliekania polymérom.April 14, 1961 discloses a process wherein steel sheets are treated with a vinylphosphonic acid-acrylic acid copolymer prior to coating with alkyd resin enamel. Although some organophosphorus pre-treatments may have a similar effect, it is costly to implement them. Thus, there remains a need to provide an efficient and economical process for pretreating an aluminum alloy substrate with an organophosphorus compound prior to applying the polymer coating.
Podstata vynálezuSUMMARY OF THE INVENTION
Základným predmetom predloženého vynálezu je poskytnúť účinný a hospodárny spôsob na predbežnú úpravu substrátu hliníkovej zliatiny organofosforečnou zlúčeninou pred aplikáciou povliekania polymérom.It is an object of the present invention to provide an efficient and economical process for pretreating an aluminum alloy substrate with an organophosphorus compound prior to applying the polymer coating.
922/B922 / B
Aby sa vyhovelo tomuto základnému predmetu, spôsob podľa vynálezu zaisťuje opatrenia na odstránenia hliníka a iných katiónov z roztokov na predbežnú úpravu, a tým sa vyhýba nákladnej likvidácii takýchto roztokov.In order to satisfy this essential object, the process of the invention provides for measures to remove aluminum and other cations from the pretreatment solutions, thereby avoiding the costly disposal of such solutions.
Ďalšie predmety a výhody vynálezu budú zrejmé odborníkovi v odbore z nasledujúceho podrobného popisu.Other objects and advantages of the invention will be apparent to those skilled in the art from the following detailed description.
Prehľad obrázkov na výkreseOverview of the figures in the drawing
Jediný obrázok znázorňuje prietokový diagram spôsobu podľa tohto vynálezu.A single figure shows a flow diagram of a method according to the invention.
Podrobný popis vynálezuDETAILED DESCRIPTION OF THE INVENTION
V súlade s vynálezom je tu poskytnutý spôsob na povliekanie substrátu z hliníkovej zliatiny organickým polymérom. Substrát z hliníkovej zliatiny môže byť vyhotovený vo forme tabuľového listu, výlisku alebo odliatku a výhodne je v tvare listu.According to the invention there is provided a method for coating an aluminum alloy substrate with an organic polymer. The aluminum alloy substrate may be in the form of a sheet, molded or cast, and is preferably sheet-shaped.
Na uskutočnenie tohto vynálezu v praxi sú výhodné rôzne hliníkové zliatiny dosiahnuteľné v tvare listu, vrátane zliatin patriacich do radu AA2000, 3000, 5000, 6000 a 7000. Zliatiny hliníka a horčíka radu AA5000 a zvlášť zliatiny AA5042 a AA5182 sú preferované. List je vyrobený z týchto zliatin je použiteľný na tvarovanie do telies a ukončenie zásobníkov na potraviny a koncov zásobníkov na nápoje.In practice, the various sheet-like aluminum alloys achievable in the practice of the present invention, including AA2000, 3000, 5000, 6000 and 7000 series alloys, are preferred. Aluminum and magnesium alloys of the AA5000 series and especially AA5042 and AA5182 alloys are preferred. The sheet made of these alloys is useful for shaping into bodies and finishing food containers and beverage container ends.
Hliníkové zliatiny vhodné pre listy na konce zásobníkov, napríklad AA5182, sú poskytované ako ingot alebo predvalok alebo doska v odbore známymi technikami odlievania. Pred spracovaním je ingot alebo predvalok podrobený homogenizácii pri zvýšenej teplote. Zliatinový predvalok je potom za horúca valcovaný na získanie kalibrovaného listu ako medzíproduktu. Napríklad materiál môže byť za horúca valcovaný pri vstupnej teplote kovu asi 371 až 524 °C na získanie medzíproduktu majúceho hrúbku asi 2,54 až 3,81 mm. Tento materiál je za studená valcovaný na získanie listu o hrúbke y rozmedzíAluminum alloys suitable for container end sheets, for example AA5182, are provided as an ingot or billet or slab by known casting techniques in the art. Prior to processing, the ingot or billet is subjected to homogenization at elevated temperature. The alloy billet is then hot rolled to obtain a calibrated sheet as an intermediate product. For example, the material may be hot rolled at a metal inlet temperature of about 371 to 524 ° C to obtain an intermediate having a thickness of about 2.54 to 3.81 mm. This material is cold rolled to obtain a sheet having a thickness y range
922/B asi od 1,52 do 3,81 mm. Uprednostňuje sa list z hliníkovej zliatiny AA5182 so stupňom tvrdosti (temper) H19. List z hliníkovej zliatiny 5042 na čelné konce je výhodne so stupňom tvrdosti H9.922 / B from about 1.52 to 3.81 mm. Preferred is an aluminum alloy sheet AA5182 with a H19 temper. The aluminum alloy sheet 5042 at the front ends is preferably of a hardness grade H9.
Hliníkové zliatiny, ako je AA5042, sú poskytované ako ingot, ktorý je homogenizovaný. Nasleduje valcovanie za horúca na intermediárny kaliber asi 2,54 až 3,81 mm. Typicky je intermediárny kalibrovaný produkt vyžíhaný, nasleduje valcovanie za horúca a potom valcovanie za studená na získanie finálneho kalibrovaného produktu, ktorý má hrúbku asi 1,52 až 3,81 mm. List je povliekaný polymérom a potom ťahaný a znova ťahaný do telesa zásobníka na potraviny. Uprednostňujú sa listy hliníkovej zliatiny AA5042 so stupňom tvrdosti H2x.Aluminum alloys such as AA5042 are provided as an ingot that is homogenized. This is followed by hot rolling to an intermediate gauge of about 2.54 to 3.81 mm. Typically, the intermediate calibrated product is annealed, followed by hot rolling and then cold rolling to obtain a final calibrated product having a thickness of about 1.52 to 3.81 mm. The sheet is coated with polymer and then drawn and re-drawn into the food container body. Preference is given to AA5042 aluminum alloy sheets having a hardness grade of H2x.
Prírodný oxidový povlak povrchu listu z hliníkovej zliatiny je všeobecne dostatočný na uskutočnenie nášho vynálezu. Prírodný oxidový povlak má obyčajne hrúbku približne 3 až 5 nm. Kvôli lepšej ochrane proti korózii môže oxidový povlak vzrastať spracovaním, ako je anodická oxidácia alebo hydrotermálne spracovanie vo vode, vodnej pare alebo vodných roztokoch.The natural oxide coating of the surface of the aluminum alloy sheet is generally sufficient to carry out our invention. The natural oxide coating usually has a thickness of about 3 to 5 nm. For better corrosion protection, the oxide coating can be increased by treatment such as anodic oxidation or hydrothermal treatment in water, water vapor or aqueous solutions.
List hliníkovej zliatiny podľa tohto vynálezu je obyčajne vyčistený alkalickým povrchovým čistiacim prostriedkom na odstránenie akýchkoľvek zvyškových mazadiel, ktoré prilipli k povrchu, a potom sa opláchne vodou. Čisteniu sa však dá vyhnúť v prípade, ak obsah zvyškových mazadiel je zanedbateľný.The aluminum alloy sheet of the present invention is typically cleaned with an alkaline surface cleaner to remove any residual lubricants adhered to the surface and then rinsed with water. However, cleaning can be avoided if the residual lubricant content is negligible.
Vyčistený povrch listu je potom predbežne upravený v prvej nádrži s kompozíciou obsahujúcou vodný roztok organofosforečnej zlúčeniny. Roztok výhodne obsahuje asi 1 až 20 g/l kopolyméru vinylfosfónovej kyseliny s akrylovou kyselinou (VPAA-AA kopolymér). Uprednostňujú sa roztoky obsahujúce asi 4 až 10 g/l kopolyméru. Kopolymér obyčajne obsahuje asi 5 až 50 % molárnych kyseliny vinylfosfónovej, výhodne asi 20 až 40 % molárnych. VPA-AA kopolymér môže mať molekulárnu hmotnosť asi 20 000 až 100 000, výhodne asi 50 000 až 80 000. Zvlášť výhodný VPA-AA kopolymér obsahuje asi 30 % molárnych VPA a asi 70 % molárnych AA. Roztok má teplotu asi 38The cleaned leaf surface is then pretreated in a first tank with a composition comprising an aqueous solution of an organophosphorus compound. The solution preferably contains about 1 to 20 g / l of a vinylphosphonic acid-acrylic acid copolymer (VPAA-AA copolymer). Solutions containing about 4 to 10 g / l of copolymer are preferred. The copolymer usually contains about 5 to 50 mole% vinylphosphonic acid, preferably about 20 to 40 mole%. The VPA-AA copolymer may have a molecular weight of about 20,000 to 100,000, preferably about 50,000 to 80,000. A particularly preferred VPA-AA copolymer contains about 30 mole% VPA and about 70 mole% AA. The temperature is about 38
922/B až 93 °C, výhodnejšie asi 49 až 82 °C. Zvlášť výhodný roztok má teplotu asi 77 °C.922 / B to 93 ° C, more preferably about 49 to 82 ° C. A particularly preferred solution has a temperature of about 77 ° C.
Povrch listu môže byť ponorený do kompozície alebo kompozícia môže byť valcovaním povliekaná alebo rozstrekovaná na povrch listu. Výhodná linka nepretržitého čistenia a predbežnej úpravy je prevádzkovaná pri asi 158 až 474 m za minútu. Kontaktná doba, asi 6 sekúnd medzi povrchom listu a kompozíciou, je dostatočná, pokiaľ je linka prevádzkovaná pri 316 m za minútu. VPA-AA kopolymér reaguje s oxidovým alebo hydroxidovým povlakom a vytvorí vrstvu na povrchu listu.The sheet surface may be immersed in the composition or the composition may be rolled or sprayed onto the sheet surface. A preferred continuous cleaning and pretreatment line is operated at about 158 to 474 m per minute. A contact time of about 6 seconds between the sheet surface and the composition is sufficient when the line is operated at 316m per minute. The VPA-AA copolymer reacts with an oxide or hydroxide coating to form a layer on the sheet surface.
List hliníkovej zliatiny prechádzajúci cez roztok na predbežnú úpravu kontaminuje roztok iónmi rôznych prvkov, vrátane hliníka, horčíka, železa, chrómu, a mangánu. Roztok na predbežnú úpravu stráca účinnosť, keď koncentrácia hliníka vzrastie na asi 150 až 200 ppm. Preto sa teda poskytuje spôsob na odstránenie iónov hliníka a iných kovov z roztoku na predbežnú úpravu.The aluminum alloy sheet passing through the pretreatment solution contaminates the solution with ions of various elements, including aluminum, magnesium, iron, chromium, and manganese. The pretreatment solution loses effectiveness when the aluminum concentration rises to about 150 to 200 ppm. Thus, a method is provided for removing aluminum and other metal ions from a pretreatment solution.
Aspoň časť roztoku na predbežnú úpravu je premiestnená do druhej nádrže obsahujúcej katiónovomeničovú živicu. Živica teda môže byť realizovaná ako pelety, guľôčky, vlákna alebo čiastočky a výhodne je typu guľôčiek z tvrdého guľatého gélu. Živica má minimálnu celkovú kapacitu vo vodíkovej forme 1,9 mekv./ml vlhkosti. Výhodne živica má priemernú veľkosť čiastočiek asi 650 pm, špecifickú hmotnosť asi 1,22 až 1,23 a objemovú hustotu asi 2,994 g/cm3.At least a portion of the pretreatment solution is transferred to a second tank containing the cation exchange resin. Thus, the resin may be in the form of pellets, beads, fibers or particles, and is preferably of the round ball gel type. The resin has a minimum total hydrogen capacity of 1.9 meq / ml moisture. Preferably, the resin has an average particle size of about 650 µm, a specific gravity of about 1.22 to 1.23, and a bulk density of about 2.994 g / cm 3 .
Živica je výhodne gél obsahujúci kopolymér styrénu a divinylbenzénu s funkčnými kyslými skupinami, výhodne sulfónovými skupinami. Alternatívne môže kopolymér obsahovať funkčné kyslé skupiny kyseliny fosfónovej a kyseliny arzénovej. Zvlášť výhodná kaniónovomeničová živica je predávaná firmou Dow Chemical Company z Midland, Michigan pod ochrannou známkou DOWEX G-26 (H).The resin is preferably a gel comprising a copolymer of styrene and divinylbenzene with acidic functional groups, preferably sulfone groups. Alternatively, the copolymer may contain functional acid groups of phosphonic acid and arsenic acid. A particularly preferred cation exchange resin is sold by the Dow Chemical Company of Midland, Michigan under the trademark DOWEX G-26 (H).
922/B922 / B
Menej výhodne môže kaniónovomeničová živica obsahovať etylén kopolymerizovaný s nenasýtenou kyselinou karboxylovou ako je kyselina akrylová.Less preferably, the cation exchange resin may comprise ethylene copolymerized with an unsaturated carboxylic acid such as acrylic acid.
Potom roztok na predbežnú úpravu prejde cez druhý zásobník, ktorý obsahuje zníženú koncentráciu hliníka. Koncentrácia hliníka v roztoku na úpravu je menšia ako asi 75 ppm, výhodnejšie menšia ako 25 ppm a optimálne okolo asi 10 ppm alebo aj menej. Roztok na úpravu obsahujúci organofosforečnú zlúčeninu a zníženú koncentráciu hliníka je vrátený späť do prvého zásobníka.Then the pretreatment solution passes through a second container containing a reduced aluminum concentration. The concentration of aluminum in the treatment solution is less than about 75 ppm, more preferably less than 25 ppm and optimally about 10 ppm or less. The treatment solution containing the organophosphorus compound and the reduced aluminum concentration is returned to the first container.
List predbežne upravený môže byť prípadne opláchnutý vodou na odstránenie nadbytočného VPA-AA kopolyméru. Voda na opláchnutie má výhodne teplotu asi 77 až 82 °C. Voda na opláchnutie je koncentrovaná odstraňovaním prebytočnej vody tak, že VPA-AA kopolymér môže byť recyklovaný. Niektoré výhodné techniky koncentrácie zahrňujú reverznú osmózu a filtráciu membránou. Po koncentrácii môže byť voda na opláchnutie premiestnená do prvého zásobníka, aby sa obnovila hodnota VPA-AA kopolyméru.The pretreated sheet may optionally be rinsed with water to remove excess VPA-AA copolymer. The rinse water preferably has a temperature of about 77-82 ° C. The rinse water is concentrated by removing excess water so that the VPA-AA copolymer can be recycled. Some preferred concentration techniques include reverse osmosis and membrane filtration. After concentration, the rinse water may be transferred to the first container to restore the VPA-AA copolymer value.
Pripravený list je povliekaný kompozíciou polyméru, ktorý výhodne obsahuje organický polymér dispergovaný v organickom rozpúšťadle. Tri výhodné polyméry na povliekanie sú epoxidy, polyvinylchlorid a polyestery. Vhodné epoxidy zahrňujú fenolom modifikované epoxidy, polyesterom modifikované epoxidy, epoxy-modifikovaný polyvinylchlorid a epoxidy so zosieťovanými väzbami. Polymérové kompozície môžu byť čisté alebo môžu obsahovať čiastočky pigmentu. Čiastočky pigmentu sú výhodne oxid titaničitý, hlinitý alebo kremičitý. Preferujú sa čiastočky oxidu titaničitého o strednom rozmedzí veľkosti čiastočiek 0,5 až 10 mikrometrov.The prepared sheet is coated with a polymer composition, which preferably comprises an organic polymer dispersed in an organic solvent. Three preferred coating polymers are epoxides, polyvinyl chloride and polyesters. Suitable epoxides include phenol-modified epoxides, polyester-modified epoxides, epoxy-modified polyvinyl chloride, and crosslinked epoxides. The polymer compositions may be pure or may contain pigment particles. The pigment particles are preferably titanium dioxide, alumina or silica. Titanium dioxide particles having a mean particle size range of 0.5 to 10 microns are preferred.
Alternatívne môže byť pripravený list povliekaný elektrolyticky, štrbinovým povliekaním, prietlačným povliekaním, povliekaním nanášaním, povliekaním rozprašovaním alebo inými spôsobmi trvalého povliekania.Alternatively, the prepared sheet may be electrolytically coated, slit coating, extrusion coating, coating coating, spray coating or other permanent coating methods.
922/B922 / B
Polymérom povlečený list je sušený, stočený a nakoniec vytvarovaný do telies zásobníkov alebo čelných dosiek zásobníkov.The polymer-coated sheet is dried, coiled and finally formed into container bodies or container front plates.
Príklady uskutočnenia vynálezuDETAILED DESCRIPTION OF THE INVENTION
Ako schematický ukazuje obrázok, je tu poskytnutá rola listu 10 z AA5182-H19 z hliníkovej a horčíkovej zliatiny majúcej hrúbku asi 224 mikrometrov. List 10 je očistený alkalickým povrchovo aktívnym čistiacim prostriedkom v kadi 20 na odstránenie akýchkoľvek zvyškových mazadiel z povrchu listu. Očistený list je potom oplachovaný v deionizovanom vodnom kúpeli 30.As schematically shown in the figure, there is provided a roll of sheet 10 of AA5182-H19 of aluminum and magnesium alloy having a thickness of about 224 microns. The sheet 10 is cleaned with an alkaline surfactant cleaner in the vat 20 to remove any residual lubricants from the sheet surface. The cleaned sheet is then rinsed in a deionized water bath 30.
Očistený a opláchnutý list je predbežne upravený v prvej nádrži 40 roztokom obsahujúcim asi 10 g/l VPA-AA kopolyméru pozostávajúceho z asi 30 % molárnych skupín VPA a asi 70 % molárnych skupín AA, rozpustených vo vode. Roztok má teplotu asi 77 °C a spočiatku obsahuje asi 10 ppm hliníka. VPA-AA kopolymér reaguje s povlakom na povrchu listu z oxidu hlinitého alebo hydroxidu hlinitého, aby vytvoril vrstvu obsahujúcu reakčný produkt kopolyméru a oxid alebo hydroxid.The cleaned and rinsed sheet is pretreated in the first tank 40 with a solution containing about 10 g / l VPA-AA copolymer consisting of about 30 mole% VPA and about 70 mole% AA dissolved in water. The solution has a temperature of about 77 ° C and initially contains about 10 ppm aluminum. The VPA-AA copolymer reacts with a coating on the surface of an aluminum oxide or aluminum hydroxide sheet to form a layer containing the reaction product of the copolymer and an oxide or hydroxide.
Predbežne upravený list je potom opláchnutý vodou 50, aby sa odstránili prebytky VPA-AA kopolyméru. Opláchnutá voda 50 má výhodne teplotu asi 77 až 82 °C.The pretreated sheet is then rinsed with water 50 to remove excess VPA-AA copolymer. The rinsed water 50 preferably has a temperature of about 77-82 ° C.
Opláchnutý list je povliekaný valcovaním s kompozíciou polyméru 60, ktorý výhodne obsahuje organický polymér a čiastočky pigmentu dispergované v organickom rozpúšťadle. Organickým polymérom je výhodne epoxidová živica. Niektoré vhodné epoxidy obsahujú fenolom modifikované epoxidy, polyesterom modifikované epoxidy, epoxy-modifikovaný polyvinylchlorid a epoxidy so zosieťovanými väzbami.The rinsed sheet is rolled with a polymer composition 60, which preferably comprises an organic polymer and pigment particles dispersed in an organic solvent. Preferably, the organic polymer is an epoxy resin. Some suitable epoxides include phenol-modified epoxides, polyester-modified epoxides, epoxy-modified polyvinyl chloride, and cross-linked epoxides.
922/B922 / B
Polymérom povlečený list je sušený v teplovzdušnej sušiarni 70 a je potom zrolovaný ako povlečený listový produkt 80.The polymer-coated sheet is dried in a hot air dryer 70 and is then rolled up as a coated sheet product 80.
Aby bola udržaná nízka koncentrácia kovových iónov v roztoku na predbežnú úpravu, sú časti roztoku periodicky premiestňované z prvej nádrže 40 do druhej nádrže 100, ktorá obsahuje katiónovomeničovú živicu. Zvlášť preferovaná živica je pevná katiónovomeničová živica predávaná firmou Dow Chemical Company Midland, Michigan, pod ochrannou známkou DOWEX G26 (H). Táto pevná katiónovomeničová živica je predávaná ako tvrdé guľaté guľôčky o veľkosti 650 mikrometrov (suchá okatosť). Pevnou katiónovomeničovou živicou je gél obsahujúci kopolymér styrénu s divinylbenzénom so sulfátovými funkčnými skupinami. Spracovanie so živicou produkuje spracovaný roztok majúci koncentráciu hliníka, ktorá je optimálne menšia ako asi 10 ppm. Spracovaný roztok je vrátený cez potrubie 110 z druhého zásobníka 100 do prvej nádrže 40.In order to maintain a low concentration of metal ions in the pretreatment solution, portions of the solution are periodically transferred from the first reservoir 40 to the second reservoir 100 which contains the cation exchange resin. A particularly preferred resin is a solid cation exchange resin sold by Dow Chemical Company of Midland, Michigan under the trademark DOWEX G26 (H). This solid cation exchange resin is sold as hard spherical beads of 650 microns (dry mesh). The solid cation exchange resin is a gel comprising a styrene-divinylbenzene copolymer with sulfate functional groups. The resin treatment produces a treated solution having an aluminum concentration that is optimally less than about 10 ppm. The treated solution is returned via line 110 from the second container 100 to the first tank 40.
Katiónovomeničová živica sa eventuálne stáva nasýtenou kovovými soľami. Živica je regenerovaná prepraním so silným roztokom 120 kyseliny, ako je 6 až 10 % HCI alebo objemovo 6 až 12 % kyselina sírová vo vode. Soli kovov 130 vymyté z druhého zásobníka 100 sa odkladajú.The cation exchange resin eventually becomes saturated with metal salts. The resin is regenerated by washing with a strong solution of acid 120, such as 6 to 10% HCl or 6 to 12% sulfuric acid in water by volume. The metal salts 130 washed out of the second container 100 are discarded.
Použitá preplachovacia voda z vodného preplachovania 50 je taktiež recyklovaná na obnovenie hodnôt VPA-AA kopolyméru. Použitá preplachová voda je najskôr zavedená do koncentračného zariadenia 140, kde sa odstraňuje voda, napríklad reverznou osmózou a membránovou ultrafiltráciou. Koncentrovaná voda z prepláchnutia je potom vrátená do prvej nádrže 40.The rinse water used from the water rinse 50 is also recycled to recover VPA-AA copolymer values. The rinsing water used is first introduced into a concentration device 140 where water is removed, for example by reverse osmosis and membrane ultrafiltration. The concentrated rinse water is then returned to the first tank 40.
Spôsob katiónovej výmeny podľa predkladaného vynálezu udržiava koncentráciu hliníka na prijateľných úrovniach v roztoku na predbežnú úpravu. 200 ml alikvót roztoku na predbežnú úpravu pri 60 °C obsahujúci 10 g/l VPA-AA kopolyméru, 350 ppm hliníka a iné kovy, sa umiestni do 250 ml Erlenmeyerovej banky obsahujúcej 40 ml vlhkého objemu živice DOWEX G-26 (H) vo vodíkovom cykle. Banka sa umiestni na vodnom kúpeli a udržiava sa pri teplote 60 °C po dobu 16 až 20 hodín. Živica je pripravená premytím 400 až 600 mlThe cation exchange process of the present invention maintains the aluminum concentration at acceptable levels in the pretreatment solution. A 200 ml aliquot of the 60 ° C pre-treatment solution containing 10 g / l VPA-AA copolymer, 350 ppm aluminum and other metals was placed in a 250 ml Erlenmeyer flask containing 40 ml wet volume of DOWEX G-26 (H) resin in hydrogen cycle. The flask was placed in a water bath and kept at 60 ° C for 16-20 hours. The resin is prepared by washing 400 to 600 ml
922/B objemovo 6% HCI, nasleduje prepláchnutie so 600 až 800 ml. deionizovanej vody.922 / B by volume 6% HCl, followed by rinsing with 600 to 800 mL. deionized water.
Po 16 až 20 hodinách doby styku sa roztok na predbežnú úpravu filtruje a živica sa prepláchne 25 ml deionizovanej vody. Roztok sa analyzuje a výsledky sú ukázané v nasledujúcej tabuľke. Všetky koncentrácie sú korigované na porovnanie s ohľadom na objem 200 ml.After a contact time of 16 to 20 hours, the pretreatment solution is filtered and the resin is rinsed with 25 ml of deionized water. The solution is analyzed and the results are shown in the following table. All concentrations are corrected for comparison with a 200 ml volume.
Tabuľka - analýza roztoku na predbežnú úpravuTable - analysis of pretreatment solution
Látka Počiatočná koncentrácia (ppm) Po G-26 (H) (ppm)Substance Initial Concentration (ppm) After G-26 (H) (ppm)
n.d nezistiteľnýn.d undetectable
Odborník v odbore pochopí, pokiaľ má popísaný vynález s odkazmi na niektoré v súčasnosti preferované uskutočnenia, že predkladaný vynález môže byť uskutočnený i inak, bez toho, aby došlo k odchýleniu sa od ducha a rámca pripojených patentových nárokov.It will be understood by one of ordinary skill in the art that, with reference to some of the presently preferred embodiments, the present invention may be practiced otherwise without departing from the spirit and scope of the appended claims.
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US7416831B2 (en) * | 2004-08-20 | 2008-08-26 | Eastman Kodak Company | Substrate for lithographic printing plate precursor |
WO2011145594A1 (en) * | 2010-05-21 | 2011-11-24 | 貴和化学薬品株式会社 | Chromium-free metal surface treatment agent, and metal surface treatment method using same |
CN107532308A (en) * | 2015-05-01 | 2018-01-02 | 诺维尔里斯公司 | Continuous coiled material preprocess method |
KR20230169412A (en) | 2019-01-02 | 2023-12-15 | 노벨리스 인크. | Systems and methods for laminating can end stock |
KR102273220B1 (en) * | 2019-12-10 | 2021-07-05 | 김준수 | Aluminum alloy for enamel coating and method for manufacturing die casted aluminum alloy frying pan |
KR20230019951A (en) * | 2020-06-10 | 2023-02-09 | 노벨리스 인크. | Pretreatment composition bonded to a metal substrate and method for preparing the same |
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NL228877A (en) * | 1957-08-19 | 1900-01-01 | ||
US2909455A (en) * | 1958-09-24 | 1959-10-20 | Amchem Prod | Method of coating a succession of aluminum surfaces |
NL129564C (en) * | 1960-04-16 | 1900-01-01 | ||
ZA728674B (en) * | 1972-05-26 | 1973-09-26 | Amchem Prod | Stabilization of acidic aqueous coating compositions containing an organic coating-forming material |
US4012351A (en) * | 1972-11-20 | 1977-03-15 | Amchem Products, Inc. | Stabilization of acidic aqueous coating compositions containing an organic coating-forming material |
JPS53125238A (en) * | 1977-04-09 | 1978-11-01 | Nippon Paint Co Ltd | Regenerating method for surface treating liquid for aluminum and its alloy |
US5103550A (en) * | 1989-12-26 | 1992-04-14 | Aluminum Company Of America | Method of making a food or beverage container |
US5277788A (en) * | 1990-10-01 | 1994-01-11 | Aluminum Company Of America | Twice-anodized aluminum article having an organo-phosphorus monolayer and process for making the article |
US5368974A (en) * | 1993-05-25 | 1994-11-29 | Eastman Kodak Company | Lithographic printing plates having a hydrophilic barrier layer comprised of a copolymer of vinylphosphonic acid and acrylamide overlying an aluminum support |
JP3620893B2 (en) * | 1995-07-21 | 2005-02-16 | 日本パーカライジング株式会社 | Surface treatment composition for aluminum-containing metal and surface treatment method |
US6020030A (en) * | 1998-05-07 | 2000-02-01 | Aluminum Company Of America | Coating an aluminum alloy substrate |
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1999
- 1999-11-03 AT AT99964956T patent/ATE263853T1/en not_active IP Right Cessation
- 1999-11-03 JP JP2001535632A patent/JP2003513773A/en active Pending
- 1999-11-03 WO PCT/US1999/025894 patent/WO2001032955A1/en active IP Right Grant
- 1999-11-03 DE DE69916339T patent/DE69916339T2/en not_active Expired - Fee Related
- 1999-11-03 SK SK593-2002A patent/SK286005B6/en not_active IP Right Cessation
- 1999-11-03 TR TR2002/01197T patent/TR200201197T2/en unknown
- 1999-11-03 ES ES99964956T patent/ES2219101T3/en not_active Expired - Lifetime
- 1999-11-03 CA CA002397674A patent/CA2397674C/en not_active Expired - Fee Related
- 1999-11-03 CN CNB998169935A patent/CN1187473C/en not_active Expired - Fee Related
- 1999-11-03 PT PT99964956T patent/PT1228263E/en unknown
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- 1999-11-03 EP EP99964956A patent/EP1228263B1/en not_active Expired - Lifetime
- 1999-11-03 CZ CZ20021422A patent/CZ299666B6/en not_active IP Right Cessation
- 1999-11-03 KR KR1020027005773A patent/KR100610579B1/en active IP Right Grant
- 1999-11-03 DK DK99964956T patent/DK1228263T3/en active
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- 1999-11-03 AU AU30976/00A patent/AU3097600A/en not_active Abandoned
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KR100610579B1 (en) | 2006-08-09 |
CN1375018A (en) | 2002-10-16 |
HUP0203608A3 (en) | 2005-05-30 |
CZ20021422A3 (en) | 2003-01-15 |
PT1228263E (en) | 2004-07-30 |
DE69916339T2 (en) | 2005-03-17 |
EP1228263B1 (en) | 2004-04-07 |
CA2397674C (en) | 2006-07-04 |
CA2397674A1 (en) | 2001-05-10 |
WO2001032955A1 (en) | 2001-05-10 |
CZ299666B6 (en) | 2008-10-08 |
AU3097600A (en) | 2001-05-14 |
NO20022089L (en) | 2002-05-08 |
NO20022089D0 (en) | 2002-05-02 |
PL354493A1 (en) | 2004-01-26 |
DK1228263T3 (en) | 2004-08-09 |
BR9917547A (en) | 2002-06-25 |
DE69916339D1 (en) | 2004-05-13 |
JP2003513773A (en) | 2003-04-15 |
TR200201197T2 (en) | 2002-08-21 |
ES2219101T3 (en) | 2004-11-16 |
SK286005B6 (en) | 2008-01-07 |
CN1187473C (en) | 2005-02-02 |
ATE263853T1 (en) | 2004-04-15 |
HUP0203608A2 (en) | 2003-03-28 |
KR20020068531A (en) | 2002-08-27 |
EP1228263A1 (en) | 2002-08-07 |
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MM4A | Patent lapsed due to non-payment of maintenance fees |
Effective date: 20101103 |