Classifications

• • C—CHEMISTRY; METALLURGY
  • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
  • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
  • C25D3/00—Electroplating: Baths therefor
  • C25D3/66—Electroplating: Baths therefor from melts
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10S204/00—Chemistry: electrical and wave energy
  • Y10S204/08—AC plus DC

Definitions

• the object of the invention is to use a molten mass for the separation or precipitation of any metals or alloys, more particularly of metals which have hardening and improving properties, such. more particularly chromium, nickel. molybdenum, tungsten, mangz nese, etc, which are deposited alone, or simultaneously with one or more other metals, on other metals, more particularly on iron.
• this problem is 1 solved. by choosing as the electrolyte a composition whose point of fusion diiiers by at 100 (1, preferably by several hundred de s, from the point of fusion of the metal or lioy to be deposited.
• the metals or alloys to be deposited are introduced into the melt in any desired form, ior instance in the form of one of their salts.
• suitable materials for the iiuxing composition can be chiefly used boron compounds, and sulphates, bisulphates, silicates or cyanides.
• Suitable boron compounds are for instance metaborates and borates of the alkalis, oi the alkaline earths, of magnesium, and in certain cases also of zinc and of manganese. As a rule it is preferable to use a mixture of several of the substances mentioned.
• chromium some other metal is to be deposited or precipitated, the separation potential of which is close to that of chromium, for instance, nickel, in the above mentioned mass of boron compounds, there are dissolved for instance 8 parts of chromium oxide and 8 parts of nickel compound, such as nickel oxide, and the electrolysis is again effected with a current density of about 1000 amperes per square meter.
• the new process it is also possible to deposit metals, the separation potential of which is higher than that of chromium, for instance the boron contained in the mass, by imrreasing the current density to a sufiicient extent.
• chromium is also separated in addition to boron.
• the composition of the mass need not be modified in this case.
• the current density amounts in this case to about 4000 ampcres per square meter. The temperature remains the same as that stated above. If the molten mass does not contain any heavy metal, for instance if it contains only sodium borate, it will be possible, with the current density mentioned to separate on the cathode boron alone.
• a still better technical effect is obtained with the new process by using direct current of a non-uniform or irregular strength. This ensures a finer grain in the metal deposits. The reason for this result is that the process of crystallization during the depositing of the metal is disturbed. In most cases the metal coating deposited on a polished cathode surface will be therefore still smooth and bright even with a great thickness of deposit. This is an advantage as it saves the cost of polishing, which is of special importance in the case of hard metals such as chromium. The action could be still further improved, for instance by reversing the direction of the current in the intervals between two current impulses depositing metal.
• the new process oli'ers substantial advantages for instance in the manufacture of boron-containing chromium coating by electrolysis of a molten mass containing boron compounds.
• the best density of cur rent for the precipitation of metallic chromium is materially smaller than the density of current at which boron chromide is obtained. If the current density is increased to such an extent as to separate boron chromide, it will be difficult to obtain the deposit in a compact form, as a powdery deposit is easily produced. This difiiculty is overcome by electrolyzing with a uniform current density which gives an irreproachable metallic chromium deposit, and by increasing the current density at regular intervals and for a short period of time to such an extent as to produce separation of boron chromide which is embedded in the subsequently precipitated deposit of metallic chromium.
• an iron surface is to be hardened merely by an electrolytic borating in the molten mass, it is preferable to work with a non-uniform direct current, in order to give time for the boron separated by one current impulse, to diffuse into the iron surface before the next current impulse is sent.
• the current is either sent in the same direction, reversed or broken between two precipitating current impulses.
• the non-uniform electric current for the purpose in question can be generated in various ways, to suit the special requirements.
• into the direct current circuit can be switched in a source of alternating current, for instance the secondary winding of a transformer, or the armature of the current generator can be provided with two separate windings, one of which supplies alternating current, and the other one direct current, these two windings being connected together in series.
• the separate excitation of the direct current generator could also be periodically modified in the required manner.
• Furt er, the electrolytic bath can be switched in and out at regular intervals, or two different sources of currents could be connected to the bath, or an auxiliary resistance could be short circuited.
• the molten bath is thereupon brought to a temperature of about 590 C., and the object to be coated for instance a sheet or plate of iron, is dipped into the bath and connected as the cathode.
• the anode could be formed for instance by the melting crucible of graphite.
• a silicon containing metal coating it is desired to obtain a silicon containing metal coating, suitable quantities of silicates are also introduced into the mass.
• the composition of the mass is made for instance as above, of 1000 parts by weight of potassium cyanide and 120 parts by weight of chromium oxide, and as addition parts by weight of sodium silicate.
• the electrolysis of the molten mass is carried out preferably at a temperature of about 540 C. and with a current density of 3000- 4:000 amperes per square meter at the cathode.
• a silicon containing chromium coatin which has a still greater. resistance to oxidizing influences and to acids as well as a greater hardness than a pure chromium coating.
• any desired other metals or their alloys can be deposited in a similar manner in the form of practically useful coating.
• alkali metal compounds as solvents
• hydroxides or carbonates could also be introduced as addition into the above mentioned masses forming solvents.
• auxiliary anode becomes necessary as in many aqueous galvanic processes.
• the supply electrodes for such holes there are preferably used, as auxiliary anodes, rods or wires of some other metal, such as for instance copper, covered with a thick deposit of chromium by strongly aqueous electrolysis or by molten mass electrolysis. Carbon or solid chromium is too brittle to be used as anode material for the purpose in question.
• the carbon (or graphite ⁇ used as the crucihle and eventually at the same time also as an electrode, is liable to wear, and is protected from burning and other chemical action.
• a thin and strongly adhering layer of boron carbide or silicium carbide This coating is obtained by exposing the carbon as cathode to the action of electric current in the molten boric acid or silicic acid which contains an addition of suitable metals for the purpose of increasing its conductivity.
• EmampZe The carbon crucible to be protected, connected as cathode, is filled wit from a fused bath the molten boric acid to which has been added 10% borax, whilst a carbon rod, connected as anode, is introduced into the centre of the crucible.
• the temperature is about 950 C.
• the electrolysis is continued for a short time, about 10 minutes, with a current density of 5000 amperes per square meter.
• the boron separated combines in nascent state, owing to the heat, with the carbon and forms boron carbide.
• a process for the production of solid, adherent coatings of metals which comprises electrolytically depositing the metals at a temperature below the melting point thereof point of fusion of which is at least 100 C. lower than the melting point of the metals to be deposited, said hath containing a borate and a compound of the metal to be deposited.
• adherent metallic coatings containing chromium which comprises electrically de ositing the chromium at a temperature below the melting point thereof from a fused bath the point of 'fusion of which is at least 100 C.
• said bath containing a borate and a compound of chromium.
• a process for the production of solid, adherent metallic coatings containing chromium and boron which comprises electrically depositing the chromium at a temperature below the melting point thereof from a fused bath the point of fusion of which is at least 100 C. lower than the melting point of the chromium, said bath containing a borate and a compound of chromium.
• a process for the production of solid, adherent metallic coatings containing chromium which comprises electrolytically depositing the chromium at a temperature below the melting point thereof from a fused bath comprising a borateand a compound of chromium.
• adherent metallic coatings containing chromium which comprises electrolytically depositing the chromium at a temperature beow the melting point thereof from a fused bath comprising a borate, an alkaline earth metal salt, and a com ound of chromium.
• A. process for t e production of solid, adherent metallic coatings'containin chromium which comprises electrolytica ly depositing the chromium from a fused bath comprising a b'orate and a compound of chromium and during said deposition periodi cally varying the current density.
• a process for the production of solid, adherent metallic coatings containing chro-' mium which comprises electrolytically depositing the chromium from a fused bath comprising a borate and a compound of chromium and during said deposition periodically varying the current density by the superposition of an alternating. current.
• a process for the productionof solid, adherent metallic coatings containing chromium which comprises electrolytically depositing the chromium at a temperature below the melting point thereof from a fused bath containing at least one borate, and chromium oxide.

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Electrochemistry (AREA)
• Materials Engineering (AREA)
• Metallurgy (AREA)
• Organic Chemistry (AREA)
• Electroplating Methods And Accessories (AREA)
• Electrolytic Production Of Metals (AREA)

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Publications (1)

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Cited By (10)

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• 0
  • BE BE340393D patent/BE340393A/xx unknown
• 1927
  • 1927-03-08 GB GB6441/27A patent/GB286457A/en not_active Expired
  • 1927-03-21 FR FR631193D patent/FR631193A/fr not_active Expired
  • 1927-03-23 US US177831A patent/US1795512A/en not_active Expired - Lifetime

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