US3415692A - Method of passivating metal surfaces - Google Patents

Method of passivating metal surfaces Download PDF

Info

Publication number
US3415692A
US3415692A US439457A US43945765A US3415692A US 3415692 A US3415692 A US 3415692A US 439457 A US439457 A US 439457A US 43945765 A US43945765 A US 43945765A US 3415692 A US3415692 A US 3415692A
Authority
US
United States
Prior art keywords
solution
passivating
cleaning
hydrazine
acid
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
US439457A
Inventor
Joseph A Armentano
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.)
Combustion Engineering Inc
Original Assignee
Combustion Engineering Inc
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 Combustion Engineering Inc filed Critical Combustion Engineering Inc
Priority to US439457A priority Critical patent/US3415692A/en
Priority to NL6602847A priority patent/NL6602847A/xx
Priority to ES0323833A priority patent/ES323833A1/en
Priority to FR52375A priority patent/FR1470805A/en
Priority to BE677475D priority patent/BE677475A/xx
Application granted granted Critical
Publication of US3415692A publication Critical patent/US3415692A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • 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
    • C23C22/60Chemical 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 alkaline aqueous solutions with pH greater than 8
    • 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
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions

Definitions

  • ABSTRACT OF THE DISCLOSURE The water and steam containing portions of a steam generator are cleaned and passivated by cleaning with an acid cleaning solution followed by neutralization and then filling the portions with a passivating solution containing 25-l000 p.p.m. hydrogen peroxide or in excess of 300 p.p.m. hydrozine at a pH in excess of 7.0.
  • the passivating solution is drained from the portions and the metal surfaces exposed to the atmosphere.
  • This invention relates to the prevention of corrosion and more particularly to the passivation of metal surfaces to reduce the possibility of corrosion.
  • the present invention is principally concerned with the passivation of oxide-free metal surfaces prior to exposure to the atmosphere to prevent oxidation upon such exposure.
  • the invention will be described with particular reference to the cleaning and passivation of the water-side heat transfer surfaces in steam generating units.
  • Chemical cleaning is normally accomplished with an acid solution. Freshly cleaned surfaces are free of protective films and thus quite active and more susceptible to oxidation than scaled surfaces. This active metal surface rusts rapidly in the presence of moisture and oxygen thereby causing corrosion problems particularly if the unit is to be out of service for a period of time. If the unit is to be kept in wet storage, i.e., filled with water, an inhibitor is normally placed in the water so as to inhibit corrosion. On the other hand, if the unit must be drained so as to expose the metal surfaces to the atmosphere, it is quite important that the surfaces be passivated prior to draining. It is this latter passivation to which this invention is directed.
  • An object of the present invention is, therefore, to provide a novel technique for passivating metal surfaces to prevent oxidation and corrosion.
  • A- specific object of the present invention is to provide a technique for chemically cleaning a steam generating unit and passivating the cleaned metal surfaces to reduce corrosion upon exposure to the atmosphere.
  • Another object of the invention is to provide a passivating technique utilizing materials which contain no dissolved solids.
  • Chemical cleaning procedures generally involve four steps which are: (l) pre-boiling with alkaline materials, (2) contacting of the surfaces with an acidic solvent or a solvent containing a chelate, (3) neutralizing and postboiling with a strong alkaline solution, and (4) passivating the freshly cleaned surfaces if an extended lay-up period is anticipated.
  • the alkaline pre-boil is not a necessary procedure and is usually only carried out in preoperational cleaning to remove organics.
  • a suitable material for this pre-boil would be a solution of Na CO and Na PO
  • the conventional material utilized for the acid cleaning step is a solution of inhibited hydrochloricacid, usually a 5 percent by weight solution.
  • the acid be inhibited so that once the mill scale and deposits have been removed, the acid attack on the base metal will be minimized.
  • Many inhibitors are commercially available and they vary depending upon the acid with which they are to be used. Polyamines are used in many of these products. Dow Chemical Co., for example, has an inhibitor for hydrochloric acid designated as A-120. This solution is admitted to the boiler and the temperature of the solvent and metal is maintained at about ISO- F.
  • suitable acid cleaning materials include organic solvents such as citric acid, formic acid, hydroxy-acetic acid and ethylenediarnine tetraacetic acid.
  • Hydrochloric acid is a much more rapid cleaning agent than the organic solvents and the organics are, therefore, used for applications where the chloride ion is objectionable such as with austenitic stainless steels.
  • the acid solution is drained from the boiler under a positive pressure of nitrogen.
  • the boiler is then rinsed with demineralized water to remove any residual acid and filled with a neutralizing solution consisting of 0.5 percent by weight soda ash.
  • the passivating technique of the present invention is carried out.
  • This technique is directed to the use of passivating materials which will effectively prepare a boiler for exposure to the atmosphere and which will be volatile and leave behind no solids.
  • the invention is particularly directed to the use of hydrazine and hydrogen peroxide as passivating materials.
  • Hydrazine has been employed in the past in low concentrations as an oxygen scavenger to remove dissolved oxygen from boiler water during wet storage.
  • the present invention is directed to the use of this material in greater concentrations prior to the draining of the cleaning and rinse solutions from the boiler to passivate the metal surface.
  • hydrazine should be present in solution at concentrations in excess of 300 p.p.m., although slightly lower concentrations will provide some degree of passivation.
  • the upper limit to the concentration of hydrazine in the passivating solution will be determined by economic factors since at a certain level the cost of adding more hydrazine to the solution could not be justified by the small increase in passivating capacity.
  • a solution of perhaps 1 percent hydrazine would be a practical upper limit.
  • a desirable pH for the hydrazine passivating solution is in the range of 9.5 or 10. The pH is adjusted to the desirable value with ammonia or some other amine which will itself add no solids to the system such as morpholine or cyclohexylamine. Test specimens passivated with hydrazine have, upon exposure, retained their luster for periods of at least two months under various adverse atmospheric conditions.
  • the hydrogen peroxide passivating solution of the present invention has a hydrogen peroxide concentration of preferably less than 1000 ppm. and perhaps down to 50 or 25 p.p.m. although such low concentrations would not be very effective.
  • the pH of the hydrogen peroxide solution is also adjusted with ammonia or other amines to a value somewhere around 10. Although this pH adjustment is not necessary, the fastest and best passivation can be obtained if the pH is elevated to a valve in excess of 7.0.
  • the upper concentration limit of 1000 ppm. was selected since an increase in the concentration would not greatly increase the effectiveness and higher concentrations might be slightly hazardous in the presence of oxidizable materials, such as organics.
  • the products of the hydrogen peroxide passivation of pickled steel are the unobjectionable materials of water and oxygen.
  • the byproducts of the use of hydrazine as a passivator are also unobjectionable, consisting of nitrogen, hydrogen, ammonia and hydrogen peroxide which, in turn, produces water and oxygen. It can be seen that these materials will leave behind no harmful deposits as would the passivators employing dissolved solids.
  • the amount of time that it is necessary to subject the metal surfaces to the passivating solution will, of course, vary depending upon many factors. Some of these factors include the concentration of the passivating material in the solution, the pH of the solution, the temperature and particular metal being treated. The amount of time required is also dependent upon the degree of passivation desired. The longer the treatment period, the more complete will be the passivation up to a certain point beyond which no further action will take place. A period of perhaps 24 hours would yield at least some significant passivation. One factor involved in determining the period necessary will be the amount of time the metal is to be exposed to the atmosphere; the longer the expected exposure, the longer should be the passivation treatment.
  • a method of cleaning and passivating the metal surfaces of the water and steam containing portions of a steam generator comprising the steps of filling said portions with an acid cleaning solution, draining said acid cleaning solution from said portions, filling said portions with a neutralizing solution, draining said neutralizing solution, from said portions, filling said portions with a passivating solution having a pH in excess of 7.0 and comprising at least in part a compound selected from the group consisting of hydrogen peroxide and hydrazine wherein the concentration of said hydrogen peroxide is from 25 to 1000 ppm. and the concentration of said hydrazine is in excess of 300 ppm. and then draining said passivating solution from said portions and exposing said metal surfaces to the atmosphere.

Description

United States Patent 3,415,692 METHOD OF PASSIVATING METAL SURFACES Joseph A. Armentano, Manchester, Conn., assignor to Combustion Engineering, Inc., Windsor, Conn., a corporation of Delaware No Drawing. Filed Mar. 12, 1965, Ser. No. 439,457 1 Claim. (Cl. 1486.14)
ABSTRACT OF THE DISCLOSURE The water and steam containing portions of a steam generator are cleaned and passivated by cleaning with an acid cleaning solution followed by neutralization and then filling the portions with a passivating solution containing 25-l000 p.p.m. hydrogen peroxide or in excess of 300 p.p.m. hydrozine at a pH in excess of 7.0. The passivating solution is drained from the portions and the metal surfaces exposed to the atmosphere.
This invention relates to the prevention of corrosion and more particularly to the passivation of metal surfaces to reduce the possibility of corrosion.
The present invention is principally concerned with the passivation of oxide-free metal surfaces prior to exposure to the atmosphere to prevent oxidation upon such exposure. The invention will be described with particular reference to the cleaning and passivation of the water-side heat transfer surfaces in steam generating units.
The importance of maintaining clean heat transfer surfaces in boilers has been recognized for many years. Tube cleanliness becomes increasingly more important as higher and higher pressures are maintained in such boilers. Because of the size of modern utility boilers and the large number of long inaccessible circuits, mechanical cleaning of an entire unit is virtually impossible. For this reason, the practice of chemically cleaning boilers has progressed in recent years to the point of becoming a routine maintenance procedure. Chemical techniques are used for both pre-operational and post-operational cleaning. The pre-operational cleaning is utilized to remove mill scale and oxidation products which have been formed as a result of heat treatment, hot working and welding as well as ordinary atmospheric rusting. Post-operational cleaning is utilized to remove deposits which have accumulated during operation of the boiler such as iron, copper, nickel, zinc, calcium and magnesium. The copper and iron are the most prevalent and troublesome deposits in utility boilers.
Chemical cleaning is normally accomplished with an acid solution. Freshly cleaned surfaces are free of protective films and thus quite active and more susceptible to oxidation than scaled surfaces. This active metal surface rusts rapidly in the presence of moisture and oxygen thereby causing corrosion problems particularly if the unit is to be out of service for a period of time. If the unit is to be kept in wet storage, i.e., filled with water, an inhibitor is normally placed in the water so as to inhibit corrosion. On the other hand, if the unit must be drained so as to expose the metal surfaces to the atmosphere, it is quite important that the surfaces be passivated prior to draining. It is this latter passivation to which this invention is directed. The atmospheric rusting of ferritic materials proceeds rapidly in the presence of oxygen and moisture and it is difficult or impossible to keep and a drained unit free from moisture. The pits formed during storage seldom penetrate the tube surface but these discontinuities represent sites for future operational corrosion, Likewise, the oxides formed are objectionable and they may become loose and move to critical areas of the boiler.
Passivation has been carried out in the past by the use 3,415,692 Patented Dec. 10, 1968 ice of buffered sodium nitrite solutions as well as with other soluble salts. These passivating solutions may contain on the order of 10,000 p.p.m. of dissolved solids. Such solu' tions, although they have proved to be effective, all present one significant problem. This is the fact that some of the dissolved solids invariably remain behind in the boiler and may cause problems when the boiler is eventually put back into service.
An object of the present invention is, therefore, to provide a novel technique for passivating metal surfaces to prevent oxidation and corrosion.
A- specific object of the present invention is to provide a technique for chemically cleaning a steam generating unit and passivating the cleaned metal surfaces to reduce corrosion upon exposure to the atmosphere.
Another object of the invention is to provide a passivating technique utilizing materials which contain no dissolved solids.
Other objects and advantages will become apparent from the description of the invention which follows.
Chemical cleaning procedures generally involve four steps which are: (l) pre-boiling with alkaline materials, (2) contacting of the surfaces with an acidic solvent or a solvent containing a chelate, (3) neutralizing and postboiling with a strong alkaline solution, and (4) passivating the freshly cleaned surfaces if an extended lay-up period is anticipated. The alkaline pre-boil is not a necessary procedure and is usually only carried out in preoperational cleaning to remove organics. A suitable material for this pre-boil would be a solution of Na CO and Na PO The conventional material utilized for the acid cleaning step is a solution of inhibited hydrochloricacid, usually a 5 percent by weight solution. It is imperative that the acid be inhibited so that once the mill scale and deposits have been removed, the acid attack on the base metal will be minimized. Many inhibitors are commercially available and they vary depending upon the acid with which they are to be used. Polyamines are used in many of these products. Dow Chemical Co., for example, has an inhibitor for hydrochloric acid designated as A-120. This solution is admitted to the boiler and the temperature of the solvent and metal is maintained at about ISO- F. Other suitable acid cleaning materials include organic solvents such as citric acid, formic acid, hydroxy-acetic acid and ethylenediarnine tetraacetic acid. Hydrochloric acid is a much more rapid cleaning agent than the organic solvents and the organics are, therefore, used for applications where the chloride ion is objectionable such as with austenitic stainless steels. At the conclusion of the acid cleaning period, the acid solution is drained from the boiler under a positive pressure of nitrogen. The boiler is then rinsed with demineralized water to remove any residual acid and filled with a neutralizing solution consisting of 0.5 percent by weight soda ash.
After the acid cleaning and neutralization, the passivating technique of the present invention is carried out. This technique, as has been pointed out, is directed to the use of passivating materials which will effectively prepare a boiler for exposure to the atmosphere and which will be volatile and leave behind no solids. The invention is particularly directed to the use of hydrazine and hydrogen peroxide as passivating materials.
Hydrazine has been employed in the past in low concentrations as an oxygen scavenger to remove dissolved oxygen from boiler water during wet storage. The present invention, however, is directed to the use of this material in greater concentrations prior to the draining of the cleaning and rinse solutions from the boiler to passivate the metal surface. To be effective as a passivator hydrazine should be present in solution at concentrations in excess of 300 p.p.m., although slightly lower concentrations will provide some degree of passivation. The upper limit to the concentration of hydrazine in the passivating solution will be determined by economic factors since at a certain level the cost of adding more hydrazine to the solution could not be justified by the small increase in passivating capacity. A solution of perhaps 1 percent hydrazine would be a practical upper limit. A desirable pH for the hydrazine passivating solution is in the range of 9.5 or 10. The pH is adjusted to the desirable value with ammonia or some other amine which will itself add no solids to the system such as morpholine or cyclohexylamine. Test specimens passivated with hydrazine have, upon exposure, retained their luster for periods of at least two months under various adverse atmospheric conditions.
The hydrogen peroxide passivating solution of the present invention has a hydrogen peroxide concentration of preferably less than 1000 ppm. and perhaps down to 50 or 25 p.p.m. although such low concentrations would not be very effective. The pH of the hydrogen peroxide solution is also adjusted with ammonia or other amines to a value somewhere around 10. Although this pH adjustment is not necessary, the fastest and best passivation can be obtained if the pH is elevated to a valve in excess of 7.0.
The upper concentration limit of 1000 ppm. was selected since an increase in the concentration would not greatly increase the effectiveness and higher concentrations might be slightly hazardous in the presence of oxidizable materials, such as organics. The products of the hydrogen peroxide passivation of pickled steel are the unobjectionable materials of water and oxygen. The byproducts of the use of hydrazine as a passivator are also unobjectionable, consisting of nitrogen, hydrogen, ammonia and hydrogen peroxide which, in turn, produces water and oxygen. It can be seen that these materials will leave behind no harmful deposits as would the passivators employing dissolved solids.
Although the mechanism of the passivation of the metal surfaces by the hydrazine is not known, it is thought that the passivation by both the hydrazine and the hydrogen peroxide are related. In studies of the decomposition of dilute aqueous solutions of hydrazine, hydrogen peroxide has been identified as one of the by-products. The amount of hydrogen peroxide formed is inversely proportional to the rate of oxidation of the hydrazine. It is thought that this formation of hydrogen peroxide oxidizes the metal and forms a protective film to render the surface passive to corrosion. The invention, however, is not to be limited by any particular theory with respect to either the hydrazine or the hydrogen peroxide.
The amount of time that it is necessary to subject the metal surfaces to the passivating solution will, of course, vary depending upon many factors. Some of these factors include the concentration of the passivating material in the solution, the pH of the solution, the temperature and particular metal being treated. The amount of time required is also dependent upon the degree of passivation desired. The longer the treatment period, the more complete will be the passivation up to a certain point beyond which no further action will take place. A period of perhaps 24 hours would yield at least some significant passivation. One factor involved in determining the period necessary will be the amount of time the metal is to be exposed to the atmosphere; the longer the expected exposure, the longer should be the passivation treatment.
While the invention has been described with reference to a particular application and with reference to particular materials and procedures, it will be understood that this description is illustrative only and that changes may be made within the scope of the claim without departing from the invention.
I claim:
1. A method of cleaning and passivating the metal surfaces of the water and steam containing portions of a steam generator comprising the steps of filling said portions with an acid cleaning solution, draining said acid cleaning solution from said portions, filling said portions with a neutralizing solution, draining said neutralizing solution, from said portions, filling said portions with a passivating solution having a pH in excess of 7.0 and comprising at least in part a compound selected from the group consisting of hydrogen peroxide and hydrazine wherein the concentration of said hydrogen peroxide is from 25 to 1000 ppm. and the concentration of said hydrazine is in excess of 300 ppm. and then draining said passivating solution from said portions and exposing said metal surfaces to the atmosphere.
References Cited UNITED STATES PATENTS 2,077,450 4/1937 Weisberg et a1 1486.14 2,473,456 6/1949 Thurber 148-6.]4 2,890,974 6/1959 Carrigan 1486.14
FOREIGN PATENTS 103,593 4/1938 Australia. 614,352 6/1935 Germany. 200,892 7/ 1923 Great Britain.
OTHER REFERENCES Combustion, November 1961, pp. 51-53. Hess et al.: Power Engineering, vol. 59, No. 9, pp. 81, 82, 83, September 1955.
RALPH S. KENDALL, Primary Examiner.
U.S. Cl. X.R. 122379
US439457A 1965-03-12 1965-03-12 Method of passivating metal surfaces Expired - Lifetime US3415692A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
US439457A US3415692A (en) 1965-03-12 1965-03-12 Method of passivating metal surfaces
NL6602847A NL6602847A (en) 1965-03-12 1966-03-04
ES0323833A ES323833A1 (en) 1965-03-12 1966-03-05 A method of passivating a metal surface, to reduce the possibility of corrosión of such surfaces when they are exposed to the atmosphere. (Machine-translation by Google Translate, not legally binding)
FR52375A FR1470805A (en) 1965-03-12 1966-03-07 Process of passivation of a metal surface
BE677475D BE677475A (en) 1965-03-12 1966-03-07

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US439457A US3415692A (en) 1965-03-12 1965-03-12 Method of passivating metal surfaces

Publications (1)

Publication Number Publication Date
US3415692A true US3415692A (en) 1968-12-10

Family

ID=23744775

Family Applications (1)

Application Number Title Priority Date Filing Date
US439457A Expired - Lifetime US3415692A (en) 1965-03-12 1965-03-12 Method of passivating metal surfaces

Country Status (4)

Country Link
US (1) US3415692A (en)
BE (1) BE677475A (en)
ES (1) ES323833A1 (en)
NL (1) NL6602847A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3888702A (en) * 1973-11-19 1975-06-10 Gen Motors Corp Hydrogen peroxide treatment of nickel surfaces for silicone rubber bonding
US4045253A (en) * 1976-03-15 1977-08-30 Halliburton Company Passivating metal surfaces
EP0744475A1 (en) * 1995-05-23 1996-11-27 Bethlehem Steel Corporation Process for improving the formability and weldability properties of zinc coated sheet steel
DE19544224A1 (en) * 1995-11-28 1997-06-05 Asea Brown Boveri Chemical operation of a water / steam cycle
US20040129295A1 (en) * 2002-11-22 2004-07-08 Lovetro David C. Chemical composition and method
US20040207122A1 (en) * 2002-02-22 2004-10-21 Massidda Joseph F. Anti-corrosive package
WO2017109641A1 (en) * 2015-12-22 2017-06-29 Sabic Global Technologies B.V. Method of steel passivation

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB200892A (en) * 1922-04-19 1923-07-19 Alfred Mai Process for treating iron, steel and the like to produce a protective surface layer thereon
DE614352C (en) * 1933-07-29 1935-06-07 Ver Fuer Die Probier Und Forsc Process for removing an unpleasant smell and taste from metal surfaces
US2077450A (en) * 1935-01-08 1937-04-20 Alrose Chemical Company Method and composition for coating iron and steel articles
US2473456A (en) * 1943-12-23 1949-06-14 Bell Telephone Labor Inc Passivation of ferrous metals
US2890974A (en) * 1957-12-02 1959-06-16 Fairchild Engine & Airplane Passivation of stainless steel alloys

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB200892A (en) * 1922-04-19 1923-07-19 Alfred Mai Process for treating iron, steel and the like to produce a protective surface layer thereon
DE614352C (en) * 1933-07-29 1935-06-07 Ver Fuer Die Probier Und Forsc Process for removing an unpleasant smell and taste from metal surfaces
US2077450A (en) * 1935-01-08 1937-04-20 Alrose Chemical Company Method and composition for coating iron and steel articles
US2473456A (en) * 1943-12-23 1949-06-14 Bell Telephone Labor Inc Passivation of ferrous metals
US2890974A (en) * 1957-12-02 1959-06-16 Fairchild Engine & Airplane Passivation of stainless steel alloys

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3888702A (en) * 1973-11-19 1975-06-10 Gen Motors Corp Hydrogen peroxide treatment of nickel surfaces for silicone rubber bonding
US4045253A (en) * 1976-03-15 1977-08-30 Halliburton Company Passivating metal surfaces
EP0744475A1 (en) * 1995-05-23 1996-11-27 Bethlehem Steel Corporation Process for improving the formability and weldability properties of zinc coated sheet steel
KR100292229B1 (en) * 1995-05-23 2001-06-01 더블류. 엔. 바즈론 Improvement of Formability and Weldability of Zinc Coated Steel Sheet
US5660707A (en) * 1995-05-23 1997-08-26 Bethlehem Steel Corporation Process for improving the formability and weldability properties of zinc coated sheet steel
US5714049A (en) * 1995-05-23 1998-02-03 Bethlehem Steel Corporation Process for improving the formability and weldability properties of zinc coated sheet steel
US5776413A (en) * 1995-11-28 1998-07-07 Asea Brown Boveri Ag Chemical mode of operation of a water/steam cycle
DE19544224A1 (en) * 1995-11-28 1997-06-05 Asea Brown Boveri Chemical operation of a water / steam cycle
DE19544224B4 (en) * 1995-11-28 2004-10-14 Alstom Chemical operation of a water / steam cycle
US20040207122A1 (en) * 2002-02-22 2004-10-21 Massidda Joseph F. Anti-corrosive package
US8048216B2 (en) * 2002-02-22 2011-11-01 Massidda Joseph F Anti-corrosive package
US8551238B2 (en) 2002-02-22 2013-10-08 Joseph F. Massidda Anti-corrosive package
US20040129295A1 (en) * 2002-11-22 2004-07-08 Lovetro David C. Chemical composition and method
US7459005B2 (en) 2002-11-22 2008-12-02 Akzo Nobel N.V. Chemical composition and method
WO2017109641A1 (en) * 2015-12-22 2017-06-29 Sabic Global Technologies B.V. Method of steel passivation

Also Published As

Publication number Publication date
BE677475A (en) 1966-09-07
NL6602847A (en) 1966-09-13
ES323833A1 (en) 1967-01-16

Similar Documents

Publication Publication Date Title
US3522093A (en) Processes of cleaning and passivating reactor equipment
EP0086245B1 (en) Aqueous acid metal cleaning composition and method of use
US3308065A (en) Scale removal, ferrous metal passivation and compositions therefor
US3072502A (en) Process for removing copper-containing iron oxide scale from metal surfaces
US4452643A (en) Method of removing copper and copper oxide from a ferrous metal surface
US3996062A (en) Method for removing scale from metallic substrates
US3447965A (en) Removal of copper containing scale from ferrous surfaces
USRE30796E (en) Scale removal, ferrous metal passivation and compositions therefor
US3413160A (en) Passivation of ferrous metal surface
US2567835A (en) Removing copper-containing incrustations from steam generators
US3460989A (en) Method of treating ferrous metal surfaces
US4045253A (en) Passivating metal surfaces
US3248269A (en) Scale removal
CA1267827A (en) Solvent for removing iron oxide deposits
US5849220A (en) Corrosion inhibitor
US3415692A (en) Method of passivating metal surfaces
JPS6320305B2 (en)
US3067070A (en) Cleaning method for industrial systems
US4636327A (en) Aqueous acid composition and method of use
EP2455514A1 (en) Method for treating iron-based metal surface which is exposed to superheated steam
US4861386A (en) Enhanced cleaning procedure for copper alloy equipment
US2847384A (en) Descalant composition and use
US3642641A (en) Corrosion inhibition
US5589107A (en) Method and composition for inhibiting corrosion
US3579447A (en) Method of removing copper deposits from ferrous metal surfaces using hydroxyalkyl thiourea