METAL CONNECTOR OR ADAPTOR FOR HYDRAULIC OR OIL DYNAMIC APPLICATION AT HIGH PRESSURE AND RELATIVE GALVANIC TREATMENT FOR CORROSION PROTECTION

Abstract

The metal connector or adaptor for hydraulic or oil dynamic application at high pressure, comprises electrolytic passivated zinc plating free from hexavalent chromium, the zinc plating comprising an external trivalent chromium passivation layer, said passivation layer having a distinctive unique coloration among high corrosion resistance processes.

Claims

1. A metal connector or adaptor for hydraulic or oil dynamic application at high pressure, comprising electrolytic passivated zinc plating free from hexavalent chromium, wherein said zinc plating comprises an external trivalent chromium passivation layer sealed with at least one silicon compound, said passivation layer having a distinctive unique coloration among high corrosion resistance processes.

2. The metal connector or adaptor for hydraulic or oil dynamic application at high pressure according to claim 1, wherein said coloration is slightly iridescent grey-violet.

3. The metal connector or adaptor for hydraulic or oil dynamic application at high pressure according to claim 1, wherein said passivation layer comprises an azo complex of chromium that gives said passivation layer said coloration.

4. The metal connector or adaptor for hydraulic or oil dynamic application at high pressure according to claim 1, wherein said passivation layer is covered in a further zinc chromate sealing layer.

5. A galvanic treatment for the corrosion protection of metal connectors and/or adaptors for hydraulic or oil dynamic application at high pressure, comprising in sequence at least one electrolytic zinc plating step, at least one rinsing step and at least one passivation step in an electrolytic passivation solution comprising trivalent chromium, a dye in turn comprising at least one azo complex of chromium, and at least one silicon sealant.

6. The galvanic treatment for the corrosion protection of metal connectors and/or adaptors for hydraulic or oil dynamic application at high pressure according to claim 5, wherein said passivation step is performed with said electrolytic solution having a temperature comprised between 20 and 40° C., a pH comprised between 1.4 and 3.4, an immersion time of pieces comprised between 25 and 120 seconds, and the pieces to be treated subject to mechanical agitation.

7. The galvanic treatment for the corrosion protection of metal connectors and/or adaptors for hydraulic or oil dynamic application at high pressure according to claim 5, wherein said passivation step is performed with said electrolytic solution having a temperature of 30° C., a pH comprised between 2.0 and 2.5 and an immersion time of pieces of 60 seconds.

8. The galvanic treatment for the corrosion protection of metal connectors and/or adaptors for hydraulic or oil dynamic application according to claim 6, after said passivation step it comprises comprising a sealing step in an electrolytic solution based on zinc chromate.

9. The galvanic treatment for the corrosion protection of metal connectors and/or adaptors for hydraulic or oil dynamic application at high pressure according to claim 8, after said sealing step comprising a hot drying step.

10. The galvanic treatment for the corrosion protection of metal connectors and/or adaptors for hydraulic or oil dynamic application at high pressure according to claim 6, wherein the pH is regulated with a 50% nitric acid solution.

Description

DETAILED DESCRIPTION

[0015] The galvanic treatment for the corrosion protection of metal connectors and/or adaptors for hydraulic or oil dynamic application at high pressure, comprises in sequence at least one electrolytic zinc plating step, at least one rinsing step and at least one passivation step in an electrolytic passivation solution comprising trivalent chromium, a dye in turn comprising at least one azo complex of chromium, and at least one silicon sealant.

[0016] The passivation step is performed with the electrolytic solution having a temperature comprised between 20 and 40° C., a pH comprised between 1.4 and 3.4, immersion time of pieces comprised between 25 and 120 seconds, and the pieces to be treated subject to mechanical agitation.

[0017] Preferably the passivation step is performed with the electrolytic solution having a temperature of 30° C., a pH comprised between 2.0 and 2.5 and an immersion time of pieces of 60 seconds.

[0018] Preferably the pH is regulated with a 50% nitric acid solution.

[0019] After the passivation step a sealing step is envisaged in an electrolytic solution based on zinc chromate.

[0020] After the sealing step a hot drying step is envisaged.

[0021] The metal connector or adaptor for hydraulic or oil dynamic application at high pressure that is obtained with this galvanic treatment has an electrolytic passivated zinc plating free from hexavalent chromium, comprising an external trivalent chromium passivation layer sealed with at least one silicon compound.

[0022] Advantageously the passivation layer has a distinctive unique coloration among high corrosion resistance processes.

[0023] In particular the coloration is slightly iridescent grey-violet.

[0024] The passivation layer comprises an azo complex of chromium that gives it this unique coloration.

[0025] Advantageously the passivation layer is covered in a further zinc chromate sealing layer.

[0026] An example of a galvanic treatment in compliance with the invention is reported below.

[0027] The metal pieces, in particular ferrous, are first prepared for the zinc plating.

[0028] The piece preparation step envisages degreasing with solvents (trieline or perchloroethylene), or hot degreasing with alkaline solutions. This is followed by a wash in hot and cold water. Subsequently, pickling in a 75% volume hydrochloric acid solution at room temperature in a tank coated in Vipla or hard rubber, then washing in running water, then hot pre-degreasing in alkaline solutions, then cathodic and anodic electrolytic degreasing, or only anodic, then washing in running water, then neutralisation in 25% volume hydrochloric acid solution, then washing in running water, then neutralisation in 5-10% sodium cyanide solution, at room temperature. The tank may be made of iron, bare, or coated in Vipla.

[0029] This is followed by the electrolytic zinc plating of the metal pieces. The zinc plating is performed with a zinc plating bath commercially known as Cromozink or Olozink.

[0030] In general the electrolytic zinc plating consists of placing the items to be zinc plated (well cleaned with mechanical brushing or washing in alkaline solutions for degreasing and then acid solutions for pickling them) as a cathode in an electrolytic bath. The items to be zinc plated are placed on suitable frames and then immersed in the zinc plating bath. Some metal bars of the metal to be deposited, connected to the anode, and soluble metal salts to be deposited are immersed in the same bath (respecting some geometric principles). When the current is supplied the positive ions of the metal to be deposited migrate towards the negative pole, where they are discharged becoming deposited in the form of a continuous metal layer. Instead, at the positive pole, the metal is dissolved with the formation of ions in solution, which reintegrate the ions discharged at the cathode. The overall reaction is a redox reaction, as a result of the anodic oxidation of the metal which dissolves loosing electrons and the cathodic reduction of the ions deposited as a metal gaining electrons. Two important zinc plating groups can be distinguished according to the chemical composition of the zing plating baths. Zinc forms many soluble salts and, under certain conditions, can be electrodeposited from acid solutions (to sulphate, fluoborate, chloride, sulphamate, etc.) and from alkaline solutions (to cyanide, pyrosulphate, zincate, ethanolamine, etc.). According to the production requirements and the zinc plating type, automatic program systems can be provided for various processes. It is important to obtain pure zinc deposits, since the presence therein of extraneous metals (nickel, lead, tin and copper) may greatly accelerate atmospheric corrosion. From this point of view acidic sulphate solutions are preferable to cyanide ones, since there is a lower tendency for metal impurities to pass from the anodes to the deposits in sulphate baths compared to cyanide ones—in the latter of which the potentials to discharge many of the extraneous metals are very close. It follows that it is more important in zinc plating to use pure zinc anodes in cyanide baths than in sulphate ones. The reason why zinc, not a very noble metal, separates well from acidic solutions with very high current efficiencies, is that hydrogen on zinc has a very high overvoltage. However, to prevent the simultaneous separation of hydrogen with zinc, there must be no impurities in the bath, which would lower the overvoltage, or no carbon or graphite particles on the surface of the cathode. Cyanalkaline baths have the disadvantage of a lower current efficiency and above all dependent on the electrodeposition conditions. As well as the current efficiency, the solubility of the anodes is also usually better in acidic solutions than in alkaline ones. Furthermore, acidic baths have higher conductivity, which leads to reductions in electrical energy consumption.

[0031] After the electrolytic zinc plating, which provides corrosion resistance, the pieces are washed in running water and a pre-passivation is performed in nitric acid (0.25-0.5% vol.), and then rinsing.

[0032] Hence the passivation is performed using the following operating parameters.

TABLE-US-00001 OPERATING PARAMETERS OF THE WORK SOLUTION Range Optimal Component A 80-120 cc/1 100 cc/1 of the work solution Component B 80-120 cc/1 100 cc/1 of the work solution Temperature 20-40° C. 30° C. Immersion time  45″-120″ 60″ pH 1.4-3.4 2.0-2.5 Tanks Polypropylene, coated steel Movement necessary, mechanical or with insufflated air, in plating barrels slow, intermittent rotation is recommended Heating recommended, with Teflon or pyrex

[0033] The immersion times may vary according to the concentration and aging status of the work solution.

[0034] The concentration of the work solution must be maintained through regular additions of components A and B, in a 1:1 ratio.

[0035] To regulate the pH of the work tank, a 50% nitric acid solution is used, and a calibrated pH meter to control the values.

[0036] To ensure the correct supply, the work solution is periodically titrated.

[0037] Component A comprises a solution based on: [0038] cobalt salt <10% [0039] organic acids <10% [0040] ammonium bifluoride <5% [0041] trivalent chromium 30% [0042] dye in the form of a chromium azo complex [0043] sealant in the form of silicon compounds

[0044] Component B is a solution based on chromium compounds commercially known as Spectramate 25.

[0045] Passivation with such a work solution therefore represents a process based on trivalent chromium formulated to fulfil the requirement for deposits with high corrosion resistance. It enables a thick conversion layer to be obtained with self-healing properties similar to those obtained with hexavalent chromium passivations and, above all, a slightly iridescent grey-violet finish is produced, a unique color among high corrosion resistance processes. This work solution enables work to be performed with great operating flexibility, at very wide pH and temperature ranges (also at room temperature, eliminating heating costs), and is ideal for acid zinc or cyanide-free zinc static or barrel plating systems.

[0046] After passivation the pieces are rinsed to be prepared for the subsequent sealing step which is performed through immersion in a bath of a solution commercially known as Zinc-Chro-Shield.

[0047] The last operation after sealing consists of hot drying (60° C.).

[0048] The galvanic treatment method as conceived herein is susceptible to many modifications and variations, all falling within the scope of the inventive concept; furthermore, all the details are replaceable by technically equivalent elements.

[0049] The materials used, as well as the dimensions, may in practice be of any type, according to needs and the state of the art.