US2377876A - Metal cleaning process and composition - Google Patents

Metal cleaning process and composition Download PDF

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Publication number
US2377876A
US2377876A US389919A US38991941A US2377876A US 2377876 A US2377876 A US 2377876A US 389919 A US389919 A US 389919A US 38991941 A US38991941 A US 38991941A US 2377876 A US2377876 A US 2377876A
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US
United States
Prior art keywords
hydride
alkali metal
bath
metal
sodium
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Lifetime
Application number
US389919A
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English (en)
Inventor
Harvey N Gilbert
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
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
Priority to NL62044D priority Critical patent/NL62044C/xx
Priority to BE463149D priority patent/BE463149A/xx
Priority to LU28268D priority patent/LU28268A1/xx
Priority to US389919A priority patent/US2377876A/en
Application filed by EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to GB6836/42A priority patent/GB557530A/en
Application granted granted Critical
Publication of US2377876A publication Critical patent/US2377876A/en
Priority to FR924482D priority patent/FR924482A/fr
Priority to CH278603D priority patent/CH278603A/fr
Priority to DEP38218A priority patent/DE849789C/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • 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 the art of cleaning metals and more particularly to a method for cleaning metals in fused baths.
  • Oxide scale and other surface impurities are commonly removed from steel and other metal articles by treatments in aqueous solutions of acids or alkalies, with and without the utilization of electric current.
  • a great variety of such cleaning solutions and processes are known and used for treating different kinds of metal articles and for different purposes.
  • difliculties are encountered because of the chemically resistant nature of the surface impurities to be removed and in such case it is often necessary to use drastic chemical treatments which not only remove the surface impurities but also dissolve a considerable portion of the underlying metal. This difficulty is encountered for example in the treatment of certain chrome alloy steels. In order to properly clean such steels for certain purposes and to remove mill scale, and the like therefrom.
  • An object of the present invention is to provide 3 an improved method for cleaning metal surfaces. particularly a method which will adequately remove surface impurities without substantial attack on the underlying metal.
  • a further object is to provide a fused alkali bath which is suitable for cleaning steel articles without substantial attack on the steel. Further object will be apparent from the following description of my invention.
  • I may first provide a fused bath comprising an alkali metal hydroxide containing in solution an appreciable quantity of an alkali metal hydride.
  • I may for example utilize a bath consisting of 55 molten caustic soda having dissolved therein from 1-20% of sodium hydride (NaH).
  • the bath is protected from oxidizing influences so as to prevent the formation of alkali metal oxide in the bath, although in some cases small amounts of alkali metal oxide are not detrimental.
  • a preferred method of preventing oxidation of the active ingredient of the bath is to continuously pass a stream of hydrogen gas into the bath.
  • the hydrogen may or may not be preheated, as desired.
  • a convenient and preferred method of operating my process consists in floating a layer of molten sodium on the surface of a fused caustic soda bath and passing in hydrogen so that it comes into contact with the sodium at the interface between the sodium and caustic layers, for example by passing the hydrogen in below the surface of the caustic so that, it rises through the caustic and thence into the layer of sodium.
  • the sodium hydride which is 'formed in the presence of the molten caustic soda immediately dissolves therein, forming a solution of the hydride in the caustic soda.
  • the layer of sodium metal protects the hydride in the bath from oxidation with the air and the sodium layer may in turn be protected from oxidation if desired. for example. by maintaining over it an atmosphere of non-oxidizing gas such as hydrogen. hydrocarbon, or nitrogen.
  • a small portion of the bath wherein work is to be introduced may be kept free from the sodium layer and if desired, this portion of the bath may be protected from the air by means of a non-oxidizing gas atmosphere or by the use of a floating layer of solid material insoluble in the bath, for example finely divided carbon such as charcoal or graphite.
  • a floating layer of solid material insoluble in the bath for example finely divided carbon such as charcoal or graphite.
  • I may react h.v drogen with a fused mixture of alkali metal oxide and alkali metal hydroxide. for example, a mixture of sodium monoxide and sodium hydroxide.
  • alkali metal oxide readily dissolves in alkali metal hydroxide and in that solution it readily reacts with hydrogen to form the hydride.
  • the alkali metal hydride content becomes depleted some of the bath may be regenerated by adding more alkali metal oxide and again treating the bath with hydrogen.
  • the treatment with hydrogen may be continued while the bath is being utilized to clean metal articles, in order to insure complete reduction of oxides at all times.
  • Baths suitable for my cleaning process also may be made by dissolving preformed solid sodium hydride or other alkali metal hydride in the alkali metal hydroxide fused bath.
  • the invention is not restricted to baths which contain only-alkali metal hydroxide and hydride, as various fusible diluents may be added without departing from the spirit and scope of my invention.
  • alkali metal halides, carbonates or other fusible inorganic compounds suitable article converting the'hydride to alkali metal oxide and alkali metal peroxide, which latter compound tends to cause reoxidation of the cleaned for addition to fused salt heat treating baths may be added, including fusible compounds of metals other than the alkali metals. Addition of such compounds may be made in order to obtain baths having various melting points.
  • compositions may be made having low melting points, so that the baths may be operated at temperatures as low as about 250 C.
  • Similar low melting compositions may be made by dissolving the alkali metal hydride in fused mixtures of sodium and potassium hydroxides.
  • the various diluents which can thus be added to vary the melting point of the bath will be apparent to those skilled in compounding fused baths for metal treatment. Obviously, any
  • ingredient added to the baths must be substantially chemically inert to the alkali metal hydroxide and hydride or at least if it combines with the hydroxide must form a fusible compound which likewise will dissolve the alkali metal hydride. Also, all bath ingredients must be substantially non-oxidizing in character.
  • the hydrides and hydroxides of the other alkali metals e. g., potassium, and lithium, may be used with substantially equal effectiveness.
  • the alkali metal hydride be dissolved in .the fused bath.
  • alkali metal hydrides in the free state readily decompose when heated at temperatures in the range of 300- 600 0.
  • a molten composition such as one containing alkali metal hydroxide
  • the hydrides have a remarkably high thermal stability and undergo little or no decomposition at these temperatures in the absence of oxides or other oxidizing agents.
  • the dissolved hydride is chemically very reactive and readily attacks metal oxides to cause their reduction.
  • the hydride bath treatment alone does not completely remove mill scale but reduces it to form a. slightly adherent coating on the steel.
  • the quenching with water may be accomplished either by dipping the article in a bath of water or by spraying or otherwise flowing a stream of water on to the article as desired. The water quenching also serves to prevent remetal surface.
  • the bath temperature for the metal cleaning operations may be varied as desired over a wide range above the melting point of the molten bath.
  • using solutions of sodium hydride in fused caustic soda excellent; cleaning of various metals may be accomplished at temperatures from 320 to around 600 C.
  • the temperature to be used will depend to some extent on the concentration of hydride, as high concentrations of hydride tend to increase the melting point of the bath.
  • a caustic soda bath having around 15 to 20% by weight of sodium hydride must be operated at around 380 to 400 C. or higher, whereas at a hydride concentration of 1 to 5%, this bath may be operated at about 320 to 350 C.
  • the hydride concentration of the cleaning bath may vary from 1 to 20% by weight, or even higher. For most purposes, I prefer to maintain a concentration of around 2 to 5% by weight. At the higher concentrations, e. g., around 15%, the possibility of hydride loss due to oxidation is increased and there is some tendency for volatilization of the hydride, indicated by a slight fuming of the bath, especially at the higher temperatures. Because of the reactive nature of the hydride, ordinarily there is no necessity to exceed a hydride concentration of about 5% by weight, nor to operate at temperatures above 350 to 400 C. I prefer to operate at temperatures below 400 C. because at 400 C. or higher the hydride tends to vaporize from the bath.
  • the cleaning bath does not deteriorate with use and may be used practically indefinitely, so long as the required quantity of hydride is added to, or formed in, the bath.
  • the bath does not acmulate compounds of the metals treated, because the surface oxides are reduced to the metallic state.
  • the hydride is converted to'alkali metal hydroxide, a bath constituent. Hence substantially no foreign material accumulates in the bath.
  • the herein described alkali metal hydride solutions may conveniently be prepared at a distance from the place of utilization, cooled and stored and shipped in sealed containers. On cooling the composition becomes a solid solution of the alkali metal hydride.
  • my invention includes such compositions and is not restricted to the production of those compositions at the time and place of utilization.
  • such compositions are potentially useful for various operations other than cleaning metal surfaces.
  • the alkali hydride is an active reducing agent
  • these compositions may be used in various operations where a highly active reducing agent is required, for example, to reduce metal oxides in order to obtain pure metal therefrom.
  • these compositions are suitable as a source of hydrogen, since they readily react with water to form hydrogen gas.
  • the solid solution of alkali metal hydride may be reacted with cold water in conventional generating apparatus, to obtain substantially complete conversion of the hydride to hydrogen gas and alkali metal hydroxide.
  • my hydride compositions often are more suitable and more convenient to use than other previously known compositions used for generating hydrogen.
  • compositions may be used for numerous purposes in place of free alkali metals, for example in chemical reactions and syntheses where sodium and other alkali metals are commonly employed, and various reduction reactions, including reduction of metal oxides.
  • the alkali metal hydrides have been found to react with replaceable hydrogen atoms in organic compounds, for example, with hydroxy compounds. Thus, sodium hydride readily reacts with alcohols to form sodium alcoholates.
  • My hydride compositions may be advantageously employed in place of alkali metals for such purposes, so long as the presence of the alkali metal hydroxide is not disadvantageous.
  • tion comprising at least one alkali metal hydroxide containing about 1 to 20% by weight of dissolved alkali metal hydride and then quenching said articles with water.
  • the process for cleaning ferrous metal ar- 5 ticles to remove metal oxides which comprises immersing said articles in a molten composition comprising sodium hydroxide containing about 1 to by weight of dissolved sodium hydride and then quenching said articles with water.
  • the process for producing a solution of alkali metal hydride in fused alkali metal hydroxide which comprises introducing hydrogen into a fused mass comprising alkali metal monoxide and at least one alkali metal hydroxide, the amount of said monoxide in said mass and the amount of hydrogen introduced therein being sufficient to produce therein a solution of 1 to 20 per cent by weight of said hydride in said hydroxide.
  • a fused bath for removing metal oxide from metal articles composed of metals substantially non-reactive with molten alkali metal hydroxides which'comprises molten alkali metal hydroxide 30 having about 1 to 20% by weight of alkali metal hydride dissolved therein.
  • a fused bath for removing metal oxide from metal articles composed of metals substantially non-reactive with molten alkali metal hydroxides G5 which comprises molten sodium hydroxide having about 1 to 20% by weight of sodium hydrlde dissolved therein.

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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)
US389919A 1941-04-23 1941-04-23 Metal cleaning process and composition Expired - Lifetime US2377876A (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
NL62044D NL62044C (fr) 1941-04-23
BE463149D BE463149A (fr) 1941-04-23
LU28268D LU28268A1 (fr) 1941-04-23
US389919A US2377876A (en) 1941-04-23 1941-04-23 Metal cleaning process and composition
GB6836/42A GB557530A (en) 1941-04-23 1942-05-20 Improvements in or relating to materials or compositions suitable for cleaning metalarticles and for other purposes
FR924482D FR924482A (fr) 1941-04-23 1946-03-26 Procédé de nettoyage des métaux et composition pour la mise en ceuvre de ce procédé
CH278603D CH278603A (fr) 1941-04-23 1947-03-29 Procédé pour éliminer les oxydes métalliques souillant des surfaces métalliques.
DEP38218A DE849789C (de) 1941-04-23 1949-03-30 Verfahren zum Reinigen metallischer Gegenstaende

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US389919A US2377876A (en) 1941-04-23 1941-04-23 Metal cleaning process and composition

Publications (1)

Publication Number Publication Date
US2377876A true US2377876A (en) 1945-06-12

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US389919A Expired - Lifetime US2377876A (en) 1941-04-23 1941-04-23 Metal cleaning process and composition

Country Status (8)

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US (1) US2377876A (fr)
BE (1) BE463149A (fr)
CH (1) CH278603A (fr)
DE (1) DE849789C (fr)
FR (1) FR924482A (fr)
GB (1) GB557530A (fr)
LU (1) LU28268A1 (fr)
NL (1) NL62044C (fr)

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2448262A (en) * 1943-07-19 1948-08-31 Du Pont Metal cleaning
US2499764A (en) * 1945-11-24 1950-03-07 Armco Steel Corp Processing stainless steel
US2569158A (en) * 1946-02-21 1951-09-25 United States Steel Corp Method of removing scale from ferrous articles
US2601864A (en) * 1947-07-02 1952-07-01 Artemas F Holden Composition for and method of descaling metal parts
US2678290A (en) * 1946-09-05 1954-05-11 Pottberg Rolfe Process of removing surface oxide films on metal
US2734036A (en) * 1956-02-07 Preventing the formation of carbon
US2790738A (en) * 1955-04-14 1957-04-30 Du Pont Titanium descaling bath and process
US2794001A (en) * 1954-10-13 1957-05-28 Du Pont Descaling metals
US2796366A (en) * 1955-10-31 1957-06-18 Du Pont Process and bath for descaling metals
US2880855A (en) * 1955-11-29 1959-04-07 Lasalle Steel Co Method of processing steel
US2891848A (en) * 1956-10-25 1959-06-23 Albert L Jaffe Separation of metals
US2935419A (en) * 1956-08-27 1960-05-03 American Mollerizing Corp Method of aluminization and pretreating medium therefor
US2935428A (en) * 1954-03-30 1960-05-03 Callery Chemical Co Method and composition for subjecting metals to reducing conditions
US2936286A (en) * 1955-07-25 1960-05-10 Dictaphone Corp Production of acicular iron particles
US3424614A (en) * 1963-02-28 1969-01-28 Schloemann Ag Cleaning,particularly de-scaling,of metal articles
US3494793A (en) * 1965-05-12 1970-02-10 Dynamit Nobel Ag Reduction of hydride losses from molten baths containing hydrides
US3506487A (en) * 1966-12-13 1970-04-14 Dynamit Nobel Ag Process for the removal of scale from very scaly metal surfaces
US3625900A (en) * 1968-01-22 1971-12-07 Kolene Corp Prefused descaling bath constituent and method of maintaining a constant chemical composition of a bath
WO2005064042A1 (fr) * 2003-12-29 2005-07-14 Bochemie, S.R.O. Bain reducteur pour le decalaminage de metaux et son procede de preparation
US20230002912A1 (en) * 2020-06-18 2023-01-05 Jiangsu Xcmg Construction Machinery Research Institute Ltd. Workpiece cleaning apparatus and cleaning method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE961634C (de) * 1952-02-05 1957-04-11 Ver Deutsche Metallwerke Ag Verfahren zum Erzielen blanker Oberflaechen von metallischen Werkstoffen und deren Legierungen, vorzugsweise von chromhaltigen Staehlen

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2734036A (en) * 1956-02-07 Preventing the formation of carbon
US2448262A (en) * 1943-07-19 1948-08-31 Du Pont Metal cleaning
US2499764A (en) * 1945-11-24 1950-03-07 Armco Steel Corp Processing stainless steel
US2569158A (en) * 1946-02-21 1951-09-25 United States Steel Corp Method of removing scale from ferrous articles
US2678290A (en) * 1946-09-05 1954-05-11 Pottberg Rolfe Process of removing surface oxide films on metal
US2601864A (en) * 1947-07-02 1952-07-01 Artemas F Holden Composition for and method of descaling metal parts
US2935428A (en) * 1954-03-30 1960-05-03 Callery Chemical Co Method and composition for subjecting metals to reducing conditions
US2794001A (en) * 1954-10-13 1957-05-28 Du Pont Descaling metals
US2790738A (en) * 1955-04-14 1957-04-30 Du Pont Titanium descaling bath and process
US2936286A (en) * 1955-07-25 1960-05-10 Dictaphone Corp Production of acicular iron particles
US2796366A (en) * 1955-10-31 1957-06-18 Du Pont Process and bath for descaling metals
US2880855A (en) * 1955-11-29 1959-04-07 Lasalle Steel Co Method of processing steel
US2935419A (en) * 1956-08-27 1960-05-03 American Mollerizing Corp Method of aluminization and pretreating medium therefor
US2891848A (en) * 1956-10-25 1959-06-23 Albert L Jaffe Separation of metals
US3424614A (en) * 1963-02-28 1969-01-28 Schloemann Ag Cleaning,particularly de-scaling,of metal articles
US3494793A (en) * 1965-05-12 1970-02-10 Dynamit Nobel Ag Reduction of hydride losses from molten baths containing hydrides
US3506487A (en) * 1966-12-13 1970-04-14 Dynamit Nobel Ag Process for the removal of scale from very scaly metal surfaces
US3625900A (en) * 1968-01-22 1971-12-07 Kolene Corp Prefused descaling bath constituent and method of maintaining a constant chemical composition of a bath
WO2005064042A1 (fr) * 2003-12-29 2005-07-14 Bochemie, S.R.O. Bain reducteur pour le decalaminage de metaux et son procede de preparation
US20230002912A1 (en) * 2020-06-18 2023-01-05 Jiangsu Xcmg Construction Machinery Research Institute Ltd. Workpiece cleaning apparatus and cleaning method

Also Published As

Publication number Publication date
FR924482A (fr) 1947-08-06
LU28268A1 (fr)
CH278603A (fr) 1951-10-31
GB557530A (en) 1943-11-24
BE463149A (fr)
DE849789C (de) 1952-09-18
NL62044C (fr)

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