US2380284A - Method of cleaning ferrous metal articles - Google Patents

Method of cleaning ferrous metal articles Download PDF

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Publication number
US2380284A
US2380284A US469703A US46970342A US2380284A US 2380284 A US2380284 A US 2380284A US 469703 A US469703 A US 469703A US 46970342 A US46970342 A US 46970342A US 2380284 A US2380284 A US 2380284A
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Prior art keywords
alkali metal
cleaning
bath
cyanide
metal
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Expired - Lifetime
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US469703A
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James H Young
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EIDP Inc
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EI Du Pont de Nemours and Co
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Priority to US469703A priority Critical patent/US2380284A/en
Priority to GB21312/43A priority patent/GB575103A/en
Application granted granted Critical
Publication of US2380284A publication Critical patent/US2380284A/en
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    • 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
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/28Cleaning or pickling metallic material with solutions or molten salts with molten salts

Definitions

  • This invention relates to metal cleaning, for example removal of oxides and other foreign material from the surface of iron, steel and other metal articles by treatment in certain novel fused baths.
  • Oxide coatings are commonly removed from iron and steel by acid pickling operations. This method of deoxidizing steel surfaces has the disadvantage that the acid tends to etch the metal after the oxide is removed and also tends to corrode steel equipment. After the pickling operations the pickled metal usually has to be subjected to an alkaline treatment to remove the last traces of acid. Aqueous alkaline solutions are also used in metal cleaning but with the exception of electrolytic methods these are useful only for the purpose of removing greasy impurities and are not effective for removing oxides.
  • An object of the present invention is an emclent method and composition for cleaning metals which is especially adapted for removal of oxide scale from iron or steel articles but which is also effective in removing other types of impurities from metal surfaces, including oils, greases and other organic impurities.
  • the above objects may be attained in accordance with the present invention by contacting the metal surface to be cleaned with a molten mixture of alkali metal cyanide and alkali metal hydroxide at an elevated temperature.
  • the treatment of ferrous metals in a fused bath containing alkali metal cyanide results in carburizing or nitrlding, or both.
  • fused alkali metal hydroxides containing relatively large amounts of alkali metal cyanide may be utilized as herein described substantially without any carburizing or nitriding effect.
  • the cyanide acts as an active reducing agent to reduce and thereby remove oxide scale from the article to be cleaned while the fused alkali metal hydroxide component of the bath effectively removes organic impurities.
  • a metal cleaning bath may be prepared according to my invention by dissolving alkali metal cyanide, for example, in concentrations of about -80% by weight in fused alkali metal hydroxid preferably anhydrous.
  • the melting point of such compositions will vary from slightly above 200 C. up to between 400 and 500 C., de-
  • alkali metal hydroxides and cyanides pending upon the particular alkali metal hydroxides and cyanides utilized.
  • Such a mixture will have an eutectic point generally ranging Ordinarily from about 40 to by weight of alkali metal cyanide, depending on the ingredients chosen.
  • the eutectic mixture of sodium cyanide and sodium hydroxide contains about 40% by weight of sodium cyanide and melts at about 220 C.
  • the bath may be diluted with various other fusible inorganic compounds which are substantially non-reactive towards alkali metal hydroxides and cyanides.
  • alkali metal hydroxide may be replaced by an alkali metal carbonate, such as soda ash.
  • alkali metal carbonate such as soda ash.
  • my cleaning baths invariably will contain more or less alkali metal carbonate caused by absorption of carbon dioxide from the atmosphere.
  • terials may be added to the bath in concentrations up to 20 to 50% by weight of the bath, for example alkali and alkaline earth metal halides, borates, phosphates, and the like. amples of such diluents are: barium chloride, so-
  • hydroxide and cyanide be derived from the same alkali metal and if desired mixtures of one or more diiferent alkali metal hydroxides with one or more difierent alkali metal cyanides may be utilized in any desired combination.
  • I have obtained excellent results with baths made by fusing together equal parts of sodium and potassium cyanide with various amounts of'caustic soda.
  • the eutectic point corresponds to an alkali metal cyanide concentration of about 60% by weight and a melting point of about 240 C.
  • the cleaning bath In order to clean ironor steel articles without carburization or nitriding, the cleaning bath must be operated at a temperature below 600 0., preferably at 300 to 500 C. For this reason and in order that the bath may have a suitable degree of fluidity I prefer to utilize a bath having a melting point not higher than about 400 C. Best results are usually obtained by using a substantially eutectic composition having a melting point between 200 and 300 C. Such baths will have more or less cleaning action at temperatures as low as the melting point, but effective cleaning action usually does not occur until the temperature has risen to around 300 C. Within the range of 300 to 500 C., the herein described baths effectively clean iron and steel by reduction of oxides and by decomposition and removal of or- Other diluent maare also case hardened.
  • the herein described process is also eflective for cleaning non-ferrous articles as well as ferrous metals.
  • it may be used for cleaning nickel, brass, copper, bronze, monel metal, and the like. This method, of course, is
  • ot suitable for treating metals such as, zinc, which are highly reactive with molten alkali metal hydroxides.
  • the metal articles may be contacted with the molten cleaning composition in any desired manner, it is ordinarily preferable to simply immerse the article to be cleaned in the fused bath for a sufficient time to effect the desired cleaning.
  • the time of treatment will vary depending on the nature and amount of the oxide present. Usual- 1y, 2. treating time may vary from 1 to 30 minutes.
  • the cleaned article After removal from the cleaning bath, the cleaned article may be cooled and washed with water or directly quenched in a water bath.
  • the cleaned article After washing to remove the alkaline cleaning composition, the cleaned article is ready for other operations, such as electroplating, galvanizing, painting or the like.
  • the method of removing impurities in the form of oxides from a ferrous metal article which comprises subjecting said article to the cleaning action of a fused bath consisting essentially of a substantially homogeneous, anhydrous, eutectic mixture of alkali metal hydroxide and alkali metal cyanide, while maintaining said bath at a temperature below 600 C.
  • the method of removing impurities in the form of oxides from a ferrous metal article which comprises subjecting said article to the cleaning action of a fused bath consisting essentially 01' a substantially homogeneous, anhydrous, eutectic mixture of sodium hydroxide and sodium cyanide, in approximately 60-40 weight ratio, while maintaining said bath at a temperature substantially within the range of 300 to 500 C.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Description

Patented July 10, 1945 METHOD OF CLEANING FERROUS METAL ARTICLES James H. Young, Niagara Falls, N. Y., assignor to E. I. du Pont de Nemours & Company, Wilmington, DeL; a corporation of Delaware No Drawing. Application December 21, 1942, Serial No. 469,703
2 Claims.
This invention relates to metal cleaning, for example removal of oxides and other foreign material from the surface of iron, steel and other metal articles by treatment in certain novel fused baths.
Oxide coatings are commonly removed from iron and steel by acid pickling operations. This method of deoxidizing steel surfaces has the disadvantage that the acid tends to etch the metal after the oxide is removed and also tends to corrode steel equipment. After the pickling operations the pickled metal usually has to be subjected to an alkaline treatment to remove the last traces of acid. Aqueous alkaline solutions are also used in metal cleaning but with the exception of electrolytic methods these are useful only for the purpose of removing greasy impurities and are not effective for removing oxides.
An object of the present invention is an emclent method and composition for cleaning metals which is especially adapted for removal of oxide scale from iron or steel articles but which is also effective in removing other types of impurities from metal surfaces, including oils, greases and other organic impurities. Other objects will be apparent from the ensuing description of the invention.
The above objects may be attained in accordance with the present invention by contacting the metal surface to be cleaned with a molten mixture of alkali metal cyanide and alkali metal hydroxide at an elevated temperature. the treatment of ferrous metals in a fused bath containing alkali metal cyanide results in carburizing or nitrlding, or both. However, I have discovered that fused alkali metal hydroxides containing relatively large amounts of alkali metal cyanide may be utilized as herein described substantially without any carburizing or nitriding effect. Under the conditions in my herein described process the cyanide acts as an active reducing agent to reduce and thereby remove oxide scale from the article to be cleaned while the fused alkali metal hydroxide component of the bath effectively removes organic impurities.
A metal cleaning bath may be prepared according to my invention by dissolving alkali metal cyanide, for example, in concentrations of about -80% by weight in fused alkali metal hydroxid preferably anhydrous. The melting point of such compositions will vary from slightly above 200 C. up to between 400 and 500 C., de-
pending upon the particular alkali metal hydroxides and cyanides utilized. Such a mixture will have an eutectic point generally ranging Ordinarily from about 40 to by weight of alkali metal cyanide, depending on the ingredients chosen. For example, the eutectic mixture of sodium cyanide and sodium hydroxide contains about 40% by weight of sodium cyanide and melts at about 220 C.
If desired, for the purpose of adjusting the melting point of the bath or for other reasons, the bath may be diluted with various other fusible inorganic compounds which are substantially non-reactive towards alkali metal hydroxides and cyanides. For example, up to about 50% by weight of the alkali metal hydroxide may be replaced by an alkali metal carbonate, such as soda ash. After extended periods of use my cleaning baths invariably will contain more or less alkali metal carbonate caused by absorption of carbon dioxide from the atmosphere. terials may be added to the bath in concentrations up to 20 to 50% by weight of the bath, for example alkali and alkaline earth metal halides, borates, phosphates, and the like. amples of such diluents are: barium chloride, so-
.dium chloride, potassium chloride, calcium chloride, and strontium chloride.
, It is not necessary that the hydroxide and cyanide be derived from the same alkali metal and if desired mixtures of one or more diiferent alkali metal hydroxides with one or more difierent alkali metal cyanides may be utilized in any desired combination. For example I have obtained excellent results with baths made by fusing together equal parts of sodium and potassium cyanide with various amounts of'caustic soda. In this combination, the eutectic point corresponds to an alkali metal cyanide concentration of about 60% by weight and a melting point of about 240 C.
In order to clean ironor steel articles without carburization or nitriding, the cleaning bath must be operated at a temperature below 600 0., preferably at 300 to 500 C. For this reason and in order that the bath may have a suitable degree of fluidity I prefer to utilize a bath having a melting point not higher than about 400 C. Best results are usually obtained by using a substantially eutectic composition having a melting point between 200 and 300 C. Such baths will have more or less cleaning action at temperatures as low as the melting point, but effective cleaning action usually does not occur until the temperature has risen to around 300 C. Within the range of 300 to 500 C., the herein described baths effectively clean iron and steel by reduction of oxides and by decomposition and removal of or- Other diluent maare also case hardened.
The herein described process is also eflective for cleaning non-ferrous articles as well as ferrous metals. For example, it may be used for cleaning nickel, brass, copper, bronze, monel metal, and the like. This method, of course, is
ot suitable for treating metalssuch as, zinc, which are highly reactive with molten alkali metal hydroxides.
While the metal articles may be contacted with the molten cleaning composition in any desired manner, it is ordinarily preferable to simply immerse the article to be cleaned in the fused bath for a sufficient time to effect the desired cleaning. For complete removal of oxide impurities, the time of treatment will vary depending on the nature and amount of the oxide present. Usual- 1y, 2. treating time may vary from 1 to 30 minutes.
After removal from the cleaning bath, the cleaned article may be cooled and washed with water or directly quenched in a water bath.
After washing to remove the alkaline cleaning composition, the cleaned article is ready for other operations, such as electroplating, galvanizing, painting or the like.
I claim:
1. The method of removing impurities in the form of oxides from a ferrous metal article which comprises subjecting said article to the cleaning action of a fused bath consisting essentially of a substantially homogeneous, anhydrous, eutectic mixture of alkali metal hydroxide and alkali metal cyanide, while maintaining said bath at a temperature below 600 C.
2. The method of removing impurities in the form of oxides from a ferrous metal article which comprises subjecting said article to the cleaning action of a fused bath consisting essentially 01' a substantially homogeneous, anhydrous, eutectic mixture of sodium hydroxide and sodium cyanide, in approximately 60-40 weight ratio, while maintaining said bath at a temperature substantially within the range of 300 to 500 C.
JAMES H. YOUNG.
US469703A 1942-12-21 1942-12-21 Method of cleaning ferrous metal articles Expired - Lifetime US2380284A (en)

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US469703A US2380284A (en) 1942-12-21 1942-12-21 Method of cleaning ferrous metal articles
GB21312/43A GB575103A (en) 1942-12-21 1943-12-20 Improvements in and relating to the cleaning of metals and metal articles

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Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2425907A (en) * 1947-08-19 Method of washing glass surfaces
US2440837A (en) * 1943-07-28 1948-05-04 J H Shoemaker Metal cleaning composition
US2442802A (en) * 1945-09-07 1948-06-08 Ici Ltd Cleaning of metals
US2567456A (en) * 1947-04-07 1951-09-11 J H Shoemaker Metal cleaning composition and process
US2619436A (en) * 1946-08-06 1952-11-25 Taylor H Beech Method of cleaning glass forming molds
US2632718A (en) * 1946-08-21 1953-03-24 William Isler Method of descaling ferrous metals
US2678290A (en) * 1946-09-05 1954-05-11 Pottberg Rolfe Process of removing surface oxide films on metal
US2738294A (en) * 1951-09-13 1956-03-13 Diamond Alkali Co Salt bath system and method for treating metals
US3030239A (en) * 1957-10-24 1962-04-17 Hooker Chemical Corp Process and salt for descaling of metals
US3069296A (en) * 1961-06-23 1962-12-18 Bell Aerospace Method for removal of iron nitride
US3153602A (en) * 1961-07-11 1964-10-20 Foseco Int Treatment of vessels used for holding molten aluminum metal
US3506487A (en) * 1966-12-13 1970-04-14 Dynamit Nobel Ag Process for the removal of scale from very scaly metal surfaces
US3698467A (en) * 1971-01-04 1972-10-17 United Aircraft Corp Method of removing silaceous cores from nickel and cobalt superalloy castings
US4756846A (en) * 1984-12-28 1988-07-12 Amchem Products, Inc. Alkaline tin-plate degreasing detergent
US20130316192A1 (en) * 2011-01-05 2013-11-28 Voestalpine Stahl Gmbh Method for surface treatment of a protectively coated substrate

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111041501A (en) * 2019-12-02 2020-04-21 河南航天精工制造有限公司 Mixed alkali for removing titanium alloy surface oxide and method for removing titanium alloy surface oxide

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2425907A (en) * 1947-08-19 Method of washing glass surfaces
US2440837A (en) * 1943-07-28 1948-05-04 J H Shoemaker Metal cleaning composition
US2442802A (en) * 1945-09-07 1948-06-08 Ici Ltd Cleaning of metals
US2619436A (en) * 1946-08-06 1952-11-25 Taylor H Beech Method of cleaning glass forming molds
US2632718A (en) * 1946-08-21 1953-03-24 William Isler Method of descaling ferrous metals
US2678290A (en) * 1946-09-05 1954-05-11 Pottberg Rolfe Process of removing surface oxide films on metal
US2567456A (en) * 1947-04-07 1951-09-11 J H Shoemaker Metal cleaning composition and process
US2738294A (en) * 1951-09-13 1956-03-13 Diamond Alkali Co Salt bath system and method for treating metals
US3030239A (en) * 1957-10-24 1962-04-17 Hooker Chemical Corp Process and salt for descaling of metals
US3069296A (en) * 1961-06-23 1962-12-18 Bell Aerospace Method for removal of iron nitride
US3153602A (en) * 1961-07-11 1964-10-20 Foseco Int Treatment of vessels used for holding molten aluminum metal
US3506487A (en) * 1966-12-13 1970-04-14 Dynamit Nobel Ag Process for the removal of scale from very scaly metal surfaces
US3698467A (en) * 1971-01-04 1972-10-17 United Aircraft Corp Method of removing silaceous cores from nickel and cobalt superalloy castings
US4756846A (en) * 1984-12-28 1988-07-12 Amchem Products, Inc. Alkaline tin-plate degreasing detergent
US20130316192A1 (en) * 2011-01-05 2013-11-28 Voestalpine Stahl Gmbh Method for surface treatment of a protectively coated substrate

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GB575103A (en) 1946-02-04

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