NO771743L - PROCEDURES FOR PHOSPHATING METALS - Google Patents

PROCEDURES FOR PHOSPHATING METALS

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Publication number
NO771743L
NO771743L NO771743A NO771743A NO771743L NO 771743 L NO771743 L NO 771743L NO 771743 A NO771743 A NO 771743A NO 771743 A NO771743 A NO 771743A NO 771743 L NO771743 L NO 771743L
Authority
NO
Norway
Prior art keywords
phosphating
poly
solution
litre
oxyacrylate
Prior art date
Application number
NO771743A
Other languages
Norwegian (no)
Inventor
Claus Christ
Joachim Kandler
Original Assignee
Hoechst Ag
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hoechst Ag filed Critical Hoechst Ag
Publication of NO771743L publication Critical patent/NO771743L/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C22/00Chemical 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
    • C23C22/05Chemical 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 using aqueous solutions
    • C23C22/06Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/07Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
    • C23C22/08Orthophosphates

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Treatment Of Metals (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Description

Det er- kjent å fosfatene metalloverflater, idet It is known that the phosphates metal surfaces, as

de behandles med et surt fosfateringsmiddel. Herved bringes metalloverflaten i kontakt med en-vandig oppløsning, som vanligvis inneholder tungmetallioner og fosfationer. Det kan imidlertid også anvendes sure alkalifosfatoppløsninger. Vanligvis arbeides her etter dyppe- eller sprøytefremgangsmåten. they are treated with an acid phosphating agent. This brings the metal surface into contact with an aqueous solution, which usually contains heavy metal ions and phosphate ions. However, acidic alkali phosphate solutions can also be used. This is usually done using the dipping or spraying method.

Under f osf ateringsreaks j orien kommer det nå til en anrikning av fosfatoppløsningen med tungmetallioner, som ut-løses fra metalloverflaten. Disse tungmetallioner fører vanligvis til en fast vedhengende skorpe i fosfateringsanlegget. Spesielt uheldig er denne skorpedannelse på sprøyteinnretninger, dyser og varmeaggregater. Skorpedannelsen fører endelig såvidt at fosfateringsoppløsningens ytelse senkes i dysesystemet således at det ikke mer er sikret en jevn tilførsel av fosfater-ingsoppløsning etter noen tid. Det kommer da til forstyrrelser i dannelsen av fosfatovertrekket. Dessuten bevirker skorpedannelse på varmeelementene en utilstrekkelig varmeovergang, hvorved det vanskeliggjøres en jevn temperaturføring. Fosfat-eringsanlegg er derfor bare å holde i en god driftstilstand med høyt oppbud av personell. During the phosphate reaction, the phosphate solution is now enriched with heavy metal ions, which are released from the metal surface. These heavy metal ions usually lead to a solid adherent crust in the phosphating plant. This crust formation on spray devices, nozzles and heating units is particularly unfortunate. The crust formation finally leads to the extent that the performance of the phosphating solution is lowered in the nozzle system so that a steady supply of phosphating solution is no longer ensured after some time. There will then be disturbances in the formation of the phosphate coating. In addition, crust formation on the heating elements causes an insufficient heat transfer, which makes it difficult to maintain an even temperature. Phosphating plants must therefore only be kept in good operating condition with a high level of staffing.

Det har selvs.agt ikke manglet på forsøk til å beherske disse vanskeligheter. Således er det fra DOS 2.402. 702 kjent en fremgangsmåte til fosfatering av metaller, hvor skorpedannelsen skal nedsettes ved tilsetning av en oppløsning av et naftalinsulfonsyre-formaldehyd-kondensasjonsprodukt eller dets salter. Også i DOS 2.240.867 behandles problemet med nedsettelse av skorpedannelse ved fosfatering av metaller og der foreslås for behandlingen av metaller med en sinkfosfatoppløs-ning tilsetning av kullhydrater. There has certainly not been a lack of attempts to master these difficulties. Thus it is from DOS 2.402. 702 known a method for the phosphating of metals, where crust formation is to be reduced by the addition of a solution of a naphthalene sulfonic acid-formaldehyde condensation product or its salts. Also in DOS 2,240,867 the problem of reduction of crust formation by phosphating of metals is treated and there the addition of carbohydrates is proposed for the treatment of metals with a zinc phosphate solution.

Oppfinnelsen vedrører nå en fremgangsmåte til nedsettelse av skorpedannelse ved fosfatering av metaller med en metallionholdig vandig fosfateringsoppløsning som har en pH-verdi mellom 3,0 og 6,0, idet fremgangsmåten erkarakterisertved at det til oppløsningen settes et alkali- eller ammoniumsalt av poly-a-oksyakrylsyre med formel The invention now relates to a method for reducing crust formation when phosphating metals with a metal ion-containing aqueous phosphating solution which has a pH value between 3.0 and 6.0, the method being characterized by adding an alkali or ammonium salt of poly-a to the solution -oxyacrylic acid with formula

hvori R-^ og betyr et hydrogenatom eller en alkylgruppe eller et karbontall mellom 1 og 3, M betyr' et alkalimetall eller en ammoniumgruppe og n betyr et helt tall mellom 3 og en" høyere verdi, inntil forbindelsen ennu er oppløselig i vann. wherein R-^ and means a hydrogen atom or an alkyl group or a carbon number between 1 and 3, M means' an alkali metal or an ammonium group and n means an integer between 3 and a' higher value, until the compound is still soluble in water.

Vanligvis er det ikke tilstrekkelig når mengden av poly-a-oksyakrylat i fosfateringsoppløsrdngen utgjør mindre enn 0,005 g/liter. På den annen side er det imidlertid heller ikke nødvendig å tilsette mer enn 1 g/liter. Meget gode resultater fåes alltid når det anvendes mengder mellom 0,01 til 0,2 g/liter. Molekylvekten av den anvendte polymere, bestemt etter forholdet av Flory (sammenlign L. Manderkern og P.J. Flory, J. Chem. Physik, 1952, 20, side 212 til 214) bør vanligvis ligge mellom 5000 og 140.000. Dette betyr at i tilfellet av natrium-poly-a-hydroksyakrylat skal n ha. en verdi i forannevnte formel mellom 45 og 1275- Fortrinnsvis utgjør molekylvekten ikke mindre enn 10.000 (n = 90). Generally, it is not sufficient when the amount of poly-α-oxyacrylate in the phosphating solution amounts to less than 0.005 g/liter. On the other hand, however, it is also not necessary to add more than 1 g/litre. Very good results are always obtained when amounts between 0.01 to 0.2 g/litre are used. The molecular weight of the polymer used, as determined by the ratio of Flory (compare L. Manderkern and P.J. Flory, J. Chem. Physik, 1952, 20, pages 212 to 214) should generally be between 5,000 and 140,000. This means that in the case of sodium poly-α-hydroxyacrylate, n should have. a value in the aforementioned formula between 45 and 1275- Preferably the molecular weight is not less than 10,000 (n = 90).

Ved tilsetningen av poly-a-oksyakrylater hindres avleiringen av metallskorper riktignok ikkejfullstendig, det viser seg imidlertid en bemerkelsesverdig endring av skorpedannelsen. Avleiringen dannes nemlig nå ikke mere som fast skorpe, men i form av en lett fjernbar utfelling eller slam. Riktignok er også nå fra tid til annen fjerning av slammet nød-vendig, imidlertid- gjennomføres denne rensning på meget enkel måte, eksempelvis ved enkel spyling av overflatene som har av-leiringene ved hjelp av en slange. The addition of poly-α-oxyacrylates does not completely prevent the deposition of metal crusts, however, a remarkable change in crust formation is evident. The deposit is now no longer formed as a solid crust, but in the form of an easily removable precipitate or sludge. Admittedly, even now from time to time removal of the sludge is necessary, however, this cleaning is carried out in a very simple way, for example by simply rinsing the surfaces that have the deposits with the help of a hose.

Fra de tyske Offenlegungsschrifter 2.161.727, 2.136.672 og 2.34 6.500 er det kjent anvendelsen av poly-a-oksyakrylater som kompleksdannende tilsetning for metallioner i vaske- og rensemidlet. Det kunne imidlertid ikke forutsees From the German Offenlegungsschrifter 2,161,727, 2,136,672 and 2,346,500, the use of poly-a-oxyacrylates as a complexing additive for metal ions in the detergent and cleaning agent is known. However, it could not be predicted

1 1

at evnen av poly-a-oksyakrylater til å danne komplekser med metallioner i sure fosfateringsoppløsninger istedenfor hårde skorper ville danne et lett avspylbart slam. that the ability of poly-α-oxyacrylates to form complexes with metal ions in acid phosphating solutions instead of hard crusts would form an easily rinseable sludge.

En spesiell fordel ved fremgangsmåten ifølge oppfinnelsen er å se deri at poly-a-bks<y>akr<y>latene kan tilsettes til ønskede fosfateringsoppløsninger i OH-området mellom 3,0 og 6,0 .som inneholder metallioner og fosfationer og er anvendbare for fosfatsj iktdannelse.n. Poly-a-oksyakrylatene kan også anvendes i konaentrater, som før bruk fortynnes til fremstilling av en arbeidsoppløsning. Slike konsentrater kan såvel være vandige oppløsninger som også pulverformede produkter. Dessuten 'kan det nevnte polymerisat imidlertid også direkte' tilsettes til fosfateringsbadet. Mengden av poly-a-oksyakrylatet som skal tilsettes refererer seg .der hver gang til volumet av arbeidsoppløsningen. Fosfateringsoppløsningen kan foruten metall- og fosfationer dessuten også inneholde forskjellige andre tilsetninger. Deres utvalg og konsentrasjon i oppløs-ningen retter seg etter det foreskrevne anvendelsesformål og er vanlig for fagfolk. En typisk "fosfateringsoppløsning inneholder imidlertid minst følgende ioner i de nedenfor angitte konsentrasj oner: A particular advantage of the method according to the invention is that the poly-a-bks<y>acrylates can be added to desired phosphating solutions in the OH range between 3.0 and 6.0, which contain metal ions and phosphate ions and are applicable for phosphate layer formation.n. The poly-a-oxyacrylates can also be used in single concentrations, which are diluted before use to produce a working solution. Such concentrates can be aqueous solutions as well as powdered products. In addition, however, the aforementioned polymerizate can also be added directly to the phosphating bath. The quantity of the poly-α-oxyacrylate to be added refers each time to the volume of the working solution. In addition to metal and phosphate ions, the phosphating solution can also contain various other additives. Their selection and concentration in the solution is based on the prescribed purpose of use and is common for professionals. However, a typical phosphating solution contains at least the following ions in the concentrations indicated below:

Som modifiseringsmiddél kommer!det f.eks. i betraktning molybdationer (ca. 0,001 til 1 g/liter), p-nitro-benzoat (ca. 0,1 - 0,6 g/liter) eller også anioniske. eller ikke ioniske tensider (ca. 0,05 - 5 g/liter). As a modifying agent, there is e.g. taking into account molybdenum cations (approx. 0.001 to 1 g/litre), p-nitro-benzoate (approx. 0.1 - 0.6 g/litre) or also anionic ones. or non-ionic surfactants (approx. 0.05 - 5 g/litre).

Denne arbeidsoppløsning, bringes normalt ved tempe-raturer mellom 40 til 90°C, fortrinnsvis ved 55 til 75°C i be-røring med metalloverflåtene. Som metalloverflater som skal fosfateres kommer det fremfor alt i betraktning aluminium-, jern- eller ståloverflater . This working solution is normally brought into contact with the metal surfaces at temperatures between 40 to 90°C, preferably at 55 to 75°C. Aluminum, iron or steel surfaces are primarily considered as metal surfaces to be phosphated.

Eksempel 1. Example 1.

Følgende fosfateringsoppløsninger ble sammenlignet med hverandre: The following phosphating solutions were compared to each other:

Oppløsningene (hver gang 1 liter) ble med fosforsyre innstillet på en pH = 4,0 og hensatt ved 60°C i 2 timer med hver gang 7,0 g fin stålull. The solutions (each time 1 litre) were adjusted with phosphoric acid to a pH = 4.0 and left at 60°C for 2 hours with 7.0 g of fine steel wool each time.

Deretter ble det av hver oppløsning i begerglass langsomt avdampet 200 cm^ i tørkeskap ved l40°C lufttemperatur og deretter ved begerglassets, indre' vegger vurdert med hensyn til avleiringen. Med en slik forsøksanordning er det mulig å fremstille de i praksis foreliggende forhold. Next, 200 cm^ of each solution in a beaker was slowly evaporated in a drying cabinet at 140°C air temperature and then the inner walls of the beaker were assessed with regard to the deposit. With such an experimental device, it is possible to produce the conditions present in practice.

Herved fremkom følgende' resultater : This resulted in the following results:

Oppløsning 1: Det avleiret seg mange punktformede hårde par- tikler. Resolution 1: Many point-shaped hard par- tickles.

Oppløsning 2: Det .dannet seg en tynn, hård- avleiringsfilm. Oppløsning 3: Det opptrådte ingen avleiringer. Resolution 2: A thin, hard deposit film formed. Solution 3: No deposits appeared.

Herav viser det seg at ved tilsetning av et poly-a-oksyakrylat inntrer en betraktelig reduksjon av skorpedannelsen., også sammenlignet med en fosfateringsoppløsning som inneholder natriumkarboksymetylcellulose. From this it appears that when a poly-a-oxyacrylate is added, there is a considerable reduction in crust formation, also compared to a phosphating solution containing sodium carboxymethyl cellulose.

Eksempel 2. Example 2.

I hårdt vann (25° dH) ble det fremstillet en f osf ateringsoppløsning som .inneholdt 8 g/liter NaH2POi|, 0,1 g/ In hard water (25° dH) a phosphate solution was prepared which contained 8 g/litre NaH2POi|, 0.1 g/

liter molybdat, 1 g/liter ikke ioniske tensider og innstillet med fosforsyre til pH = 4,0. Med denne oppløsning ble det i liter of molybdate, 1 g/litre of non-ionic surfactants and adjusted with phosphoric acid to pH = 4.0. With this resolution, it became i

■. sprøytefremgangsmåten behandlet ved 65 o C et '! stålblikk. Derved opptrådte under bruk slamdannels.e og det dannet seg fast vedhengende skorpedannelser. ■. the spray process treated at 65 o C et '! sheet steel. As a result, sludge formation occurred during use and firmly attached crust formations formed.

Deretter ble fremgangsmåten gjentatt, imidlertid ble det til oppløsningen satt 0,2 g/liter natrium-poly-a-oksyakrylat. Det viste seg at nå ved samme fremgangsmåtevarighet dannet det seg riktignok også avleiringer, som imidlertid meget lett lot seg fjerne ved bare spyling ved hjelp av en slange. The procedure was then repeated, however, 0.2 g/litre of sodium poly-α-oxyacrylate was added to the solution. It turned out that now with the same duration of the procedure deposits also formed, which, however, could be very easily removed by simply flushing with a hose.

Claims (3)

1. Fremgangsmåte til nedsettelse av skorpedannelse ved fosfatering av metaller med en metallionholdig vandig fosfateringsoppløsning, som har en pH-verdi mellom 3,0 og 6,0, karaktérisert ved at det til oppløsningen settes et alkali- eller ammoniumsalt av poly-a-oksyakrylsyre med formel 1. Method for reducing crust formation when phosphating metals with a metal ion-containing aqueous phosphating solution, which has a pH value between 3.0 and 6.0, characterized by adding an alkali or ammonium salt of poly-a-oxyacrylic acid to the solution with formula hvori Rj og betyr et hydrogenatom eller en alkylgruppe,med et ■ karbonatall mellom 1 og 3, M betyr et' alkalimetall eller en ammoniumgruppe og n betyr et helt tall mellom 3-og en høyere verdi, inntil forbindelsen ennu er oppløselig i vann.in which Rj and means a hydrogen atom or an alkyl group with a carbon number between 1 and 3, M means an alkali metal or an ammonium group and n means an integer between 3 and a higher value, until the compound is still soluble in water. 2. Fremgangsmåte ifølge krav 1,karakterisert vedat poly-a-oksyakrylatet tilsettes i en mengde fra 0,005 til 1 g/liter....2. Method according to claim 1, characterized in that the poly-a-oxyacrylate is added in an amount from 0.005 to 1 g/litre.... 3. Fremgangsmåte ifølge krav 1,karakterisert vedat molekylvekten av poly-a-oksyakrylatet ifølge Flory ligger mellom 5000 og 140.000.3. Method according to claim 1, characterized in that the molecular weight of the poly-α-oxyacrylate according to Flory is between 5,000 and 140,000.
NO771743A 1976-05-19 1977-05-18 PROCEDURES FOR PHOSPHATING METALS NO771743L (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19762622276 DE2622276A1 (en) 1976-05-19 1976-05-19 METAL PHOSPHATING METHOD

Publications (1)

Publication Number Publication Date
NO771743L true NO771743L (en) 1977-11-22

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ID=5978389

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Application Number Title Priority Date Filing Date
NO771743A NO771743L (en) 1976-05-19 1977-05-18 PROCEDURES FOR PHOSPHATING METALS

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AR (1) AR212770A1 (en)
BR (1) BR7703193A (en)
CH (1) CH629539A5 (en)
DE (1) DE2622276A1 (en)
DK (1) DK217377A (en)
ES (1) ES458765A1 (en)
FR (1) FR2352069A1 (en)
IT (1) IT1084699B (en)
NL (1) NL7705325A (en)
NO (1) NO771743L (en)
PT (1) PT66563B (en)
SE (1) SE7705874L (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4417965A1 (en) * 1994-05-21 1995-11-23 Henkel Kgaa Iron phosphating using substituted monocarboxylic acids

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3136663A (en) * 1960-10-24 1964-06-09 Kelite Corp Compositions and methods for preservation of metals
DE2211256C2 (en) * 1972-03-09 1982-12-02 Hoechst Ag, 6000 Frankfurt Process for the preparation of poly-α-oxy-acrylic acid
GB1549856A (en) * 1975-06-20 1979-08-08 Ici Ltd Phosphating process

Also Published As

Publication number Publication date
FR2352069B1 (en) 1981-07-24
DE2622276A1 (en) 1977-12-08
FR2352069A1 (en) 1977-12-16
ES458765A1 (en) 1978-03-16
CH629539A5 (en) 1982-04-30
SE7705874L (en) 1977-11-20
NL7705325A (en) 1977-11-22
PT66563A (en) 1977-06-01
BR7703193A (en) 1978-01-31
PT66563B (en) 1979-01-22
AR212770A1 (en) 1978-09-29
DK217377A (en) 1977-11-20
IT1084699B (en) 1985-05-28

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