US2576680A - Method for increasing the resistance to corrosion of stainless steel - Google Patents
Method for increasing the resistance to corrosion of stainless steel Download PDFInfo
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- US2576680A US2576680A US690829A US69082946A US2576680A US 2576680 A US2576680 A US 2576680A US 690829 A US690829 A US 690829A US 69082946 A US69082946 A US 69082946A US 2576680 A US2576680 A US 2576680A
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- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23C—COATING 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
- C23C22/00—Chemical 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
- C23C22/05—Chemical 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
- C23C22/06—Chemical 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 aqueous acidic solutions with pH less than 6
- C23C22/48—Chemical 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 aqueous acidic solutions with pH less than 6 not containing phosphates, hexavalent chromium compounds, fluorides or complex fluorides, molybdates, tungstates, vanadates or oxalates
- C23C22/50—Treatment of iron or alloys based thereon
Definitions
- the present invention relates to amethod for. increasing the resistance of steel devices'to acids.
- the present invention provides for a method to increase in a very large measure the resistance of stainless steels with respect toa certain num-- ber of acids, particularly sulfuric acid, and which makes itpossible toobtain with such steelsvats or other apparatus showing a perfect resistance to-sul'f'uric acid in all concentrations and at temperatures as high as in the neighborhood of C. and a considerably increased resistance to' nitric acid, phosphoric acid, organic acids andother corrosive mediums such as sea water, J avelwater, etc.
- the combined treatment according to the in-- vention may be applied either to separate elements such as, for instance, sheet metal, intended to be used for the manufacture .of vats or other apparatus or to already finished devices.
- Nitric acid of 36 B. 10% by volume
- Said mixture may be used cold or hot. It acts much more rapidly when heated.
- the pickling may be realized very simply by cleaning the welded parts with a cloth impregnated with the mixture by passing said cloth repeatedly over said parts and then allowing to dry during 24 hours in a moist atmosphere.
- mixture constitutes, generally speaking, an excellent pickling reactive for stainless steel coming out of thermic treatment. 7 y In most cases, however, it is necessary to effect the corrosion and the passivation on the finished apparatus; in such a case it is not necessary to proceed with a particular pickling of the weldings said pickling being eifected automatically' in the course of both the above mentioned operations.
- the corrosion and the passivation may be effected simultaneously or successively.
- the corrosion treatment must be effected preferably by means of a reducing acid such as a diluted sulphuric r hydrochloric solution.
- the duration of the attack is controlled so as to lead to a loss of weight of the steel of about 150 grams per square meter, for instance. It generally varies, according to the nature of the steel and of the acid which are used, between ten minutes and one hour in the cold.
- the attack may be efiected with a loss of weight which is less than that which has just been indicated if the metalhas already been submitted to an attack either in the course of a prior operation before the manufacture of the apparatus or, in the case of sheet metal, in the course of its pickling process at the end of its manufacture. The effect of this corrosion must not, however, have been destroyed by a later preheating or cold rolling.
- Thefpassivation treatment consecutive to this first treatment may be effected, for instance, through action, on the surfaces to be treated, of an oxidizing non-corrosive bath such as a 10% solution of nitric acid, the treatment being extended from one to 48 hours until a markedly electro-positive and preferably high potential with respect to the calomel electrode is obtained for the treated metal.
- an oxidizing non-corrosive bath such as a 10% solution of nitric acid
- the treatment of apparatus encounters no difficulties when they are of relatively small dimensions.
- the said apparatus may be totally immersed in the passivation liquid, passivation thusbeing ensured both inside and outside.
- the best passivation method consists in filling the vessel with sulphuric acid the concentration of which is substantially equal to that of the acid which is intended to be contained therein and in applying to said vessel during said filling operation a D. C.
- a first method consists inrusing both the passivating and corrosive action of certain mixtures such as the above mentioned mixture of sodium fluoride and nitric acid.
- This mixture is rather delicate; due to the fact that it is no longer passivating when its content in iron and chromium salts exceeds a certainrvalue, whichrequires its frequent renewal.
- certain steel grades such as the 18/8 molybdenum steel require its use in a heated state (60 C.) In this case the corrosion is comparatively small, of the order of 50 grams per square meter on previously sand blasted surfaces.
- aqua regia is to be proscribed in an absolute manner.
- the apparatus is filled in the above mentioned manner but while raising the intensity of the current to a higher value up to 100 amp. per; square meter in case of previously sand blasted surfaces showing, owing to this fact, a maximum aptitude to corrosion.
- the action of the current is extended with the same intensity during about fifteen minutes after the end of the filling; vthen it is reduced to a much smaller value, of. the order of 3 amp. per square meter, and maintained at this valueduring two to four days. It is also'possibleto render the treatment much more rapid by, maintaining the current at the initial filling intensity but the consumption of current and the loss of metal aremuch higher.
- the initial physical condition of the metal is of minor importance if said treatments are effected on the finished apparatus however, the chemical treatmentrwith a fluoride bathas well asthe electric treatment,aftercorrosion or simultaneously with the corrosion-are facilitated when the metal which constitutes, the apparatus has, ,already been submitted to a corrosion,even if the latter has been followed by a deformationsuch "7%, ment ofthe finished apparatus,-thesheetmetal used in its construction must "have already been rendered passive to acid and said 'passiv'i'ty must not have "been destroyeddurin'g the ro1ling"or conformation operations.
- a chemically or electrically treated stainless chromium manganese steel containing, for example; 18% chromium, manganese, 2% nickel and 0.5% titanium resists up to about 100 C. the acid concentration which is the most corrosive for this steel: 19 B. Under the same conditions the 18/8 molybdenum steel resists acid showing a concentration of 40 131%. which is the most corrosive for it.
- the corrosion operation is preferably realized by means of a uniform attack by a corrosive solution such as a reducing acid (diluted hydrochloric or sulphuric acid or their mixtures) or of mixtures of reducing and of oxidizing substances (solutions of hydrochloric and nitric acids, hydrofluoric and nitric acids or sodium fluoride and nitric acid).
- a corrosive solution such as a reducing acid (diluted hydrochloric or sulphuric acid or their mixtures) or of mixtures of reducing and of oxidizing substances (solutions of hydrochloric and nitric acids, hydrofluoric and nitric acids or sodium fluoride and nitric acid).
- the passivation is then operated by means of an oxidizing non-corrosive liquid such as nitric acid.
- nitric passivation treatment consecutive to the ccrros'ion'treatment isrealized with a10% solution of nitric acid.
- the operation requires two to three days if the'operation is realized'at 30 C. and 'oneweek'ifrealized at10" C.
- -A stainlesssteel device which'has been-so treated offers a "bright silver -white surface of very characteristic aspect.
- the sheet metal used for the constitution of-th'eeipparatus' was commercial "sheet metal -having been submitted to-a pickling operation at'theend of the manufacture. -It was '-attackable by s'ulphuric acid of 40 B, v
- the corrosive attack treatment was effected chemically on the-finished'apparatus. To this end, the vat wasfilled up tothe edge with cold sulphuric acid of "4:0 B. the attack was allowed to 'go' onduring one hour'whereafterthe vat was emptied and the apparatus left in a moist place during several days.
- Example II -Pickling vat made of steel with 18% of chromium, 10% of manganese, 2% of nickel and 0.5% of titanium, intended for containing hot sulphuric solutions of 20
- B. Meas uring 1 m. x 2 m. and 1 m. height; containing a coil of wound and welded pipe of the same metal as the vat helically wound in a heated state and secured to the vat by rolled up supports.
- the sheet metal used for the construction of the apparatus and the coil was commercial sheet metal which had been submitted to a pickling operation at the end of the manufacture.
- the finished apparatus was submitted to the electric passivating treatment.
- a vertical sheet metal band measuring about 20 x cm. extending down to a few millimetres from the bottom was arranged inside the vat.
- a potential difference of 1.5 to 2 volts was established between the vat and the sheet metal by means of a source of electric energy capable of yielding 3 amp. during three days.
- the vat was then filled with sulphuric acid of 20 Be. while causing a current of 3 amp. to pass and said current was maintained during three days.
- vat was then emptied. After said treatment, it was able to'contain sulphuric solutions up to temperatures nearing 100 C. without any attack of its walls.
- Example III -Cylindrical vat similar to that of ExampleI but made of nickel-chromiummolybdenum steel intended for containing cold commercial sulphuric acid.
- the apparatus being comparatively simple and the corrosion resistance requirements less high it was possible to form the vat of assembled commercial sheet metal of nickel-chromium-molybdenum steel previously passivated by a chemical treatment, thus avoiding a treatment of the finished apparatus.
- the inner weldings were merely pickled by means of a cloth impregnated with the above mentioned fiuonitric mixture once the apparatus was finished. The vat wasthen rinsed and it was found able to resist the attack of cold commercial sulfuric acid.
- the method for increasing the resistance to corrosion of stainless steel which comprises treating at least the part of said stainless steel which is to be contacted with the corroding medium by the following steps: (1) an attack treatment with a solution of sodium fluoride and nitricacid until there is a loss of weight amounting to about 150 grams per square meter, (2) a non-corrosive passivation treatment with solution of nitric acid until said part has a high electro-positive potential with respect to a calomel electrode.
- the method for increasing the resistance to corrosion of stainless steel which comprises treating at least the part of said stainless steel which is to be contacted with the corroding medium by the following steps:' (1) an attack treatment with a solution of sodium fluoride and nitric acid until there is a loss of weight amounting to about grams per square meter, (2) a non-corrosive passivation treatment with an approximately 10% solution of nitric acid'at 30 0.; for at least 48 hours and until said part has a high electro-positive potential with respect to a calomel electrode.
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Description
Patented Nov. 27, 1951 METHOD FOR INCREASING THE RESIST- ANCE T CORROS STEEL ION OF STAINLESS Louis Guit'ton, Ugine, -France, assignor to Societe WEle'ctro-Chimi'e, d?ElectroMetallurgie et des- Acieries Electriques dUgine,- Paris, France, a corporation of France No Drawing. Application August '15,, 1946, Serial No. 690,829. In France September 15, 1.9 15
The present invention relates to amethod for. increasing the resistance of steel devices'to acids.
It is well known that commercial-stainless steels such as steels with 15 to 18% chromium, 18/8 chromium-nickel steels (18% chromium and 8% nickel), 18/8 chromium-nickel steels with-molybdenum and copper do not shown an industrial re sistance to certain acids, whatever the degree of dilution of the latter may be. Thus, the said steels resist sulphuric acid only when the latter. is in theform of it most concentrated solutions (60 to- 65 B.) or, on the contrary, in thetorm of its most diluted solutions (less than 6%.) and, in both cases, only when the said solutions are: cold.
The resistance to concentrated solutions is not even total; moreover, it is practically rather precarious owing to the fact that since these latter solutions are hygroscopic the concentrated liquid which creeps along the Walls above the level of the solution absorbs the moistness of the air so that it is diluted and can then cause strong local corrosion.
Likewise, if the above mentioned steels 'sho'w a certain passivity to sulfuric acid solutions of high dilutions the observed resistance remains atle'ast very unstable. 1 1
Thus, an 18/8. chromium-nickel steel test-piece when immersed during 48 hours an acid-of '40 B.-has lost 1800 grams persquare meter at 30 glazed or polished. 18/8 steel with molybdenum and copper resists better in the cold -but--atest piece of said steel when immersedinsulphuric acid of 40 B. at 30 C. during-48 hours has still lost 350 grams per square meter while it had lost only 3 grams per square metre in'acid of '65 B.-
The above mentioned steels are also seldom: apt to resist long enough in other corrosivemediums such as, phosphoric acid and organicacids when used at certain concentrations.-
This lack: offr'esistance appears in a still more: marked manner in the case of. apparatus made ofv such stainless steels and comprising welded joints and parts which have been distorted or hammered in a cold or hot-state. The zones adjacent the weldings always undergouadeeper attack than the rest of themetalowing to the preheating to which they have-beensubmitted. The danger'is considerably increased when a roddiffer'ent from that which forms the sheet metal to be welded (case of chromium-manganese steel) is used for supplying metal for the weld- The foregoing results in that for many applications, the chemical industry has no other means than to resort to ceramic materials, glass. Wood, lead and other like materials, Unfortunately said materials off a quite insuflicient mechanical strength and a high difiiculty of application.
The present invention provides for a method to increase in a very large measure the resistance of stainless steels with respect toa certain num-- ber of acids, particularly sulfuric acid, and which makes itpossible toobtain with such steelsvats or other apparatus showing a perfect resistance to-sul'f'uric acid in all concentrations and at temperatures as high as in the neighborhood of C. and a considerably increased resistance to' nitric acid, phosphoric acid, organic acids andother corrosive mediums such as sea water, J avelwater, etc.
Said "method fundamentally consists in the whole of the following measures applied simultaneously or successively:
(a) The steel surfaces which are later to comeinto contact with the corrosive medium are submitted to a uniformattackbyan acid, attack limited to a small loss of weight, of the order of grams per square meter for instance;
(b) The same surfaces are submitted, simultaneously with the above mentionedcorros'iorr treatment or after said treatment,- to a passivation treatment capable of conferringto a metal an electro-positive potential with respect to the cal'omel electrode such as, for instance, attack by moist air, by means of an acid or, preferably, by an electrolytic anodic' treatment.
The combined treatment according to the in-- vention may be applied either to separate elements such as, for instance, sheet metal, intended to be used for the manufacture .of vats or other apparatus or to already finished devices.
In case the constituent parts of an apparatus are treated before the assembly of the latter, it is necessary, after the assembly, to pickle the weldings which may have been effected.
Only the combination of' the above mentioned. means makes it possible to obtainfor the treated apparatus a stability with respect to corrosive mediums which was never obtained hitherto. In fact. if the surfaces under considerationare sub-:- mitted to one oi' said treatments only, no appre ciable result isobtained. U y r composition:
Sodium fluoride: 0.4 to 2% by weight Nitric acid of 36 B.: 10% by volume Said mixture may be used cold or hot. It acts much more rapidly when heated. The pickling may be realized very simply by cleaning the welded parts with a cloth impregnated with the mixture by passing said cloth repeatedly over said parts and then allowing to dry during 24 hours in a moist atmosphere. mixture constitutes, generally speaking, an excellent pickling reactive for stainless steel coming out of thermic treatment. 7 y In most cases, however, it is necessary to effect the corrosion and the passivation on the finished apparatus; in such a case it is not necessary to proceed with a particular pickling of the weldings said pickling being eifected automatically' in the course of both the above mentioned operations.
. As explained above, the corrosion and the passivation may be effected simultaneously or successively.
If said operations take place successively the corrosion treatment must be effected preferably by means of a reducing acid such as a diluted sulphuric r hydrochloric solution. The duration of the attack is controlled so as to lead to a loss of weight of the steel of about 150 grams per square meter, for instance. It generally varies, according to the nature of the steel and of the acid which are used, between ten minutes and one hour in the cold. The attack may be efiected with a loss of weight which is less than that which has just been indicated if the metalhas already been submitted to an attack either in the course of a prior operation before the manufacture of the apparatus or, in the case of sheet metal, in the course of its pickling process at the end of its manufacture. The effect of this corrosion must not, however, have been destroyed by a later preheating or cold rolling. Y a
Thefpassivation treatment consecutive to this first treatment may be effected, for instance, through action, on the surfaces to be treated, of an oxidizing non-corrosive bath such as a 10% solution of nitric acid, the treatment being extended from one to 48 hours until a markedly electro-positive and preferably high potential with respect to the calomel electrode is obtained for the treated metal.
. The treatment of apparatus encounters no difficulties when they are of relatively small dimensions. In this case, the said apparatus may be totally immersed in the passivation liquid, passivation thusbeing ensured both inside and outside.
It is to be noted that this I the assembly, for instance through thermic treatment, hammering. etc.
As regards resistance to sulfuric acid, the best passivation method consists in filling the vessel with sulphuric acid the concentration of which is substantially equal to that of the acid which is intended to be contained therein and in applying to said vessel during said filling operation a D. C.
voltage of 1.5 to 2 volts, whereby the inner part of the vessel serves as positive pole and receives an intensity of the order of 5 amp. per square meter. This is obtained in practice by connecting the body of the vessel itself to the positive pole of the source of current and by arranging inside said vessel an 18/8 molybdenum steel cathode having its lower end located only a few millimetres short from the bottom in order that in the beginning of the filling the corrosion has no time to start. in the lower part of the vessel. The current is interrupted a few moments after the filling is ended.
In case the corrosion and passivation are realised simultaneously in order to obtain a good resistance towards sulfuric acid, a first method consists inrusing both the passivating and corrosive action of certain mixtures such as the above mentioned mixture of sodium fluoride and nitric acid. The use of this mixture is rather delicate; due to the fact that it is no longer passivating when its content in iron and chromium salts exceeds a certainrvalue, whichrequires its frequent renewal. On theother hand, certain steel grades such as the 18/8 molybdenum steel require its use in a heated state (60 C.) In this case the corrosion is comparatively small, of the order of 50 grams per square meter on previously sand blasted surfaces. For passivation, aqua regia is to be proscribed in an absolute manner.
It is also possible, and this is the most eflicacious and most reliable method, to use the above mentioned electric treatment but while extending it after the filling so as to determine a loss of weight of the order of 50 to 250 grams per square meter.
For example, the apparatus is filled in the above mentioned manner but while raising the intensity of the current to a higher value up to 100 amp. per; square meter in case of previously sand blasted surfaces showing, owing to this fact, a maximum aptitude to corrosion. The action of the current is extended with the same intensity during about fifteen minutes after the end of the filling; vthen it is reduced to a much smaller value, of. the order of 3 amp. per square meter, and maintained at this valueduring two to four days. It is also'possibleto render the treatment much more rapid by, maintaining the current at the initial filling intensity but the consumption of current and the loss of metal aremuch higher.
, In all; the above described treatments the initial physical condition of the metal is of minor importance if said treatments are effected on the finished apparatus however, the chemical treatmentrwith a fluoride bathas well asthe electric treatment,aftercorrosion or simultaneously with the corrosion-are facilitated when the metal which constitutes, the apparatus has, ,already been submitted to a corrosion,even if the latter has been followed by a deformationsuch "7%, ment ofthe finished apparatus,-thesheetmetal used in its construction must "have already been rendered passive to acid and said 'passiv'i'ty must not have "been destroyeddurin'g the ro1ling"or conformation operations. Anyhow, the treatment of the finished apparatu's which, by the way, isalways to be recommended, cannot'be avoided when the 'apparatusis to"resist'hot"acid'-or when thesheet'metal is to be submitted to conformations in a heated'state or to severe conformations in "a cold state or furthermore when the weldings cannot be pickled. I
On the other hand, the various treatments indicatedabove as well for the case ofthesuccessive corrosion and passivation as for thefc'ase when'both said operations are 'efiected simultan'e cusly' have not all'the same efiicaciousnessa'ccording to the natureof the steel constituting the walls of the'apparatus andaccordingto theconcentration and the temperature of thesul'ph'uric acid which is to come into contact with the treated surfaces.
Thus, for instance, with a steel containing 15% chromium, without nickel, a satisfactory resistance of the apparatus can be obtained only towards cold solutions of sulphuric acid and on condition that the passivating treatment is effected electrically.
On the contrary, stainless steels "with 18% chromium and 8% nickeLhaving been submitted tonne of the abovementioned chemical treatments, satisfactorily resist sulphuric acid solutions of any concentration attemperatures under 50 0.. In order to be able to resist higher temperaturesthe apparatus made of such steels must necessarily b8 submitted to 'an" electric passivating'treatment. I
"A chemically or electrically treated stainless chromium manganese steel containing, for example; 18% chromium, manganese, 2% nickel and 0.5% titanium resists up to about 100 C. the acid concentration which is the most corrosive for this steel: 19 B. Under the same conditions the 18/8 molybdenum steel resists acid showing a concentration of 40 131%. which is the most corrosive for it.
It does not seem to be possible whatever may be the treatment employed and the steel which is used, to obtain a stable passivity of stainless steels to concentrated or fairly diluted sulphuric acid at boiling temperature. However, the application of a very weak permanent anodic current of the order of 3 amp. per square meter makes it possible to maintain in a passive condition the surfaces in contact with the acid so long as the current passes while limiting the corrosion to a small value.
If, instead of essentially endeavoring to obtain the resistance to sulphuric acid it is desired to obtain a considerably better resistance to other corrosive mediums such as nitric acid, phos phoric acid, organic acids, more particularly acetic acid and oxalic acid, sea water, Javel water and the like, the corrosion operation is preferably realized by means of a uniform attack by a corrosive solution such as a reducing acid (diluted hydrochloric or sulphuric acid or their mixtures) or of mixtures of reducing and of oxidizing substances (solutions of hydrochloric and nitric acids, hydrofluoric and nitric acids or sodium fluoride and nitric acid). The passivation is then operated by means of an oxidizing non-corrosive liquid such as nitric acid.
The best results have been obtained by adopting for the corrosion treatment either a mixture of hydrofluoric and nitric acids or the above mentioned mixture of *sodium fluorideand nitric acid, used between 30 and 80 The duration of the treatment 'depends upon thetemperature'andthe'surface conditions of'the metal. For usual surfaces (commercial surfaces which are pickled, brightened or not, rolled in acoldstate) the attack'may last 3 -to 24hoursa-t the temperatureof 30 C.'-and'30minutes'to two hours at'the'temperatureof 60 C.
The nitric passivation treatment consecutive to the ccrros'ion'treatment isrealized with a10% solution of nitric acid. The operation requires two to three days if the'operation is realized'at 30 C. and 'oneweek'ifrealized at10" C. -A stainlesssteel device which'has been-so treated offers a "bright silver -white surface of very characteristic aspect.
"Results; which are i still appreciable though less satisfactory than thosewhich are obtained with twoconsecutive-operations can'also be obtaine'dfas regards resistance tovarious' corrosive liquids, by means of a single operation combining the corrosion and passivatio'n, for instanceby means of mixture of sodium-fluorid'e-nitric acid.
The following are'examples of some forms'of execution of the invention:
Example I .Cylindrical vat of stainless steel with 18% chromium, 8% nickel intended for containing cold sulphuric acid of40"B.; the body of the vat is welded-alonga=generatr-ix; the bottom is formed 'ofadis'c the edges of which are hammered back 'at 'aright angleandwhich is welded onto the cylindrical body a 1 few centimetres above the lower part of the vat. "The sheet metal used for the constitution of-th'eeipparatus' was commercial "sheet metal -having been submitted to-a pickling operation at'theend of the manufacture. -It was '-attackable by s'ulphuric acid of 40 B, v
The corrosive attack treatment was effected chemically on the-finished'apparatus. To this end, the vat wasfilled up tothe edge with cold sulphuric acid of "4:0 B. the attack was allowed to 'go' onduring one hour'whereafterthe vat was emptied and the apparatus left in a moist place during several days.
At the end of this time the inside of the vat had become perfectly resisting to cold sulphuric acid of 40 B., which is the most corrosive concentration.
Example II.-Pickling vat made of steel with 18% of chromium, 10% of manganese, 2% of nickel and 0.5% of titanium, intended for containing hot sulphuric solutions of 20 B. Meas uring 1 m. x 2 m. and 1 m. height; containing a coil of wound and welded pipe of the same metal as the vat helically wound in a heated state and secured to the vat by rolled up supports. The sheet metal used for the construction of the apparatus and the coil was commercial sheet metal which had been submitted to a pickling operation at the end of the manufacture.
The finished apparatus was submitted to the electric passivating treatment. To this end, a vertical sheet metal band measuring about 20 x cm. extending down to a few millimetres from the bottom was arranged inside the vat. A potential difference of 1.5 to 2 volts was established between the vat and the sheet metal by means of a source of electric energy capable of yielding 3 amp. during three days. The vat was then filled with sulphuric acid of 20 Be. while causing a current of 3 amp. to pass and said current was maintained during three days.
The vat was then emptied. After said treatment, it was able to'contain sulphuric solutions up to temperatures nearing 100 C. without any attack of its walls.
Example III.-Cylindrical vat similar to that of ExampleI but made of nickel-chromiummolybdenum steel intended for containing cold commercial sulphuric acid. The apparatus being comparatively simple and the corrosion resistance requirements less high it was possible to form the vat of assembled commercial sheet metal of nickel-chromium-molybdenum steel previously passivated by a chemical treatment, thus avoiding a treatment of the finished apparatus. The inner weldings were merely pickled by means of a cloth impregnated with the above mentioned fiuonitric mixture once the apparatus was finished. The vat wasthen rinsed and it was found able to resist the attack of cold commercial sulfuric acid.
A similar result could have been obtained by pickling the weldings with a cloth impregnated with aqua regia. 2
What I claim is:
1. The method for increasing the resistance to corrosion of stainless steel, which comprises treating at least the part of said stainless steel which is to be contacted with the corroding medium by the following steps: (1) an attack treatment with a solution of sodium fluoride and nitricacid until there is a loss of weight amounting to about 150 grams per square meter, (2) a non-corrosive passivation treatment with solution of nitric acid until said part has a high electro-positive potential with respect to a calomel electrode.
2. The method for increasing the resistance to corrosion of stainless steel, which comprises treating at least the part of said stainless steel which is to be contacted with the corroding medium by the following steps:' (1) an attack treatment with a solution of sodium fluoride and nitric acid until there is a loss of weight amounting to about grams per square meter, (2) a non-corrosive passivation treatment with an approximately 10% solution of nitric acid'at 30 0.; for at least 48 hours and until said part has a high electro-positive potential with respect to a calomel electrode.
3. The method for increasing the resistance to corrosion of stainless steel apparatus, which com-v prises treating stainless steel sheets by the following steps:v (1) an attack treatment with a solution of sodium fluoride and nitric acid until there is a loss ofweight amounting to about 150 grams per square meter, (2) a non-corrosive passivation treatment with a solution of nitric acid until said part has a high electro-positive potential with respect to a calomel electrode, fabricating the sheets into an apparatus by welding such as to destroyat'least partially the effects of the passivation treatment, thereafter pickling the welds there produced with a solution of sodium fluoride and nitric acid, and allowing said parts to dry during at least twentyfour hours in a moist atmosphere.
LOUIS GUITTON.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,279,101 Gravell Sept. 17, 1918 1,549,022 Otte Aug. 11, 1925 1,562,710 Madsen Nov. 24, 1925 1,793,936 Knauss Feb. 24, 1931 1,961,752 Fink et a1. June 5, 1934 2,175,771 Giles Oct. 10, 1939 2,209,924 Leiter et a1. July 30, 1940 2,357,219 Mott Aug. 29, 1944 2,357,554 Sears Sept. 5, 1944 2,377,792 Lawrence et al a- June 5, 1945 2,390,402 Uhlig Dec. 4, 1945 OTHER REFERENCES Pollitt, The Causes and Prevention of Corrosion, VanNostrand Co., New York, 1923, page 139.
Claims (1)
1. A NON-CORROSIVE CHOLINE CHLORIDE COMPOSITION COMPRISING AQUEOUS CHOLINE CHLORIDE SOLUTION OF A CONCENTRATION OF AT LEAST 50% CHLORINE CHLORIDE, AN INHIBITOR SELECTED FROM THE GROUP CONSISTING OF TETRAALKALI METAL PYROPHOSPHATES, ALKALI METAL PHYTATES, ALKALI METAL HEXAMETAPHOSPHATES, AND ALKALI METAL TRIPOLYPHOSPHATES, AND A COMPOUND SELECTED FROM THE GROUP CONSISTING OF TARTARIC ACID, CITRIC ACID, ALKALI METAL ACID TARTRATES, AND ALKALI METAL ACID CITRATES THE PH OF SAID COMPOSITION BEING ADJUSTED TO BETWEEN 7.0 AND 8.5.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR2576680X | 1945-09-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2576680A true US2576680A (en) | 1951-11-27 |
Family
ID=9686687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US690829A Expired - Lifetime US2576680A (en) | 1945-09-15 | 1946-08-15 | Method for increasing the resistance to corrosion of stainless steel |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2576680A (en) |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2943954A (en) * | 1958-02-10 | 1960-07-05 | Mead Corp | Casting surface for producing castsurfaced mineral coated paper |
| US3009865A (en) * | 1958-06-02 | 1961-11-21 | Mueller Walter Adolf | Anodic protection of kraft digesters |
| US3049479A (en) * | 1958-11-10 | 1962-08-14 | Chemionics Engineering Lab Inc | Corrosion-erosion-cavitation protection for marine propellers |
| US3126328A (en) * | 1958-12-01 | 1964-03-24 | Electrolytic bridge assembly for | |
| US3147204A (en) * | 1960-02-25 | 1964-09-01 | Chemical Construction Corp | Anodic prevention of hydrogen embrittlement of metals |
| US3162550A (en) * | 1961-05-08 | 1964-12-22 | Union Oil Co | Process of preventing corrosion of ferrous metal by an aqua ammonia solution |
| US3182007A (en) * | 1958-12-01 | 1965-05-04 | Continental Oil Co | Electrode assembly for the anodic passivation of metals |
| US3198724A (en) * | 1960-08-17 | 1965-08-03 | Whirlpool Co | Hot water heater with electrical scale control |
| US3208925A (en) * | 1960-01-07 | 1965-09-28 | Continental Oil Co | Anodic protection against corrosion |
| US3249524A (en) * | 1961-11-01 | 1966-05-03 | Sinclair Research Inc | Method of reducing corrosion |
| US3287237A (en) * | 1962-03-28 | 1966-11-22 | Allegheny Ludlum Steel | Surface treatment of bright annealed strip |
| US3720548A (en) * | 1970-04-02 | 1973-03-13 | Stamicarbon | Process for increasing the corrosion resistance of austenitic stainless steels |
| US3839096A (en) * | 1971-01-22 | 1974-10-01 | Int Nickel Co | Reproducibility of color in coloring stainless steel |
| US4026737A (en) * | 1974-10-22 | 1977-05-31 | Nippon Steel Corporation | Method for coloring a stainless steel |
| EP0776256A4 (en) * | 1994-09-26 | 1998-05-20 | Squibb & Sons Inc | Stainless steel acid treatment |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1279101A (en) * | 1918-04-30 | 1918-09-17 | James H Gravell | Method of preparing pickled iron and steel for painting. |
| US1549022A (en) * | 1924-12-27 | 1925-08-11 | Valley Holding Corp | Method of treating the surfaces of cold-worked iron chromium alloys |
| US1562710A (en) * | 1920-07-27 | 1925-11-24 | Madsenell Corp | Method of treating metallic objects and resulting products |
| US1793936A (en) * | 1925-01-31 | 1931-02-24 | Madsenell Corp | Method of fabricating metal-coated articles |
| US1961752A (en) * | 1931-07-23 | 1934-06-05 | Colin G Fink | Process of treating metal and alloy articles to improve the resistivity thereof to corrosion and to the product thereof |
| US2175771A (en) * | 1936-01-30 | 1939-10-10 | American Sheet & Tin Plate | Chromium-bearing metal |
| US2209924A (en) * | 1939-04-25 | 1940-07-30 | Budd Edward G Mfg Co | Passivation of stainless steel |
| US2357219A (en) * | 1942-01-10 | 1944-08-29 | Joseph P Moran | Corrosion-resistant ferrous alloys |
| US2357554A (en) * | 1942-07-20 | 1944-09-05 | Schlage Lock Co | Anodic treatment of ferrous metals |
| US2377792A (en) * | 1941-02-28 | 1945-06-05 | Solvay Process Co | Preventing corrosion of ferrous metals by solutions of electrolytes |
| US2390402A (en) * | 1942-09-02 | 1945-12-04 | Gen Electric | Method of passivating stainless steels |
-
1946
- 1946-08-15 US US690829A patent/US2576680A/en not_active Expired - Lifetime
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1279101A (en) * | 1918-04-30 | 1918-09-17 | James H Gravell | Method of preparing pickled iron and steel for painting. |
| US1562710A (en) * | 1920-07-27 | 1925-11-24 | Madsenell Corp | Method of treating metallic objects and resulting products |
| US1549022A (en) * | 1924-12-27 | 1925-08-11 | Valley Holding Corp | Method of treating the surfaces of cold-worked iron chromium alloys |
| US1793936A (en) * | 1925-01-31 | 1931-02-24 | Madsenell Corp | Method of fabricating metal-coated articles |
| US1961752A (en) * | 1931-07-23 | 1934-06-05 | Colin G Fink | Process of treating metal and alloy articles to improve the resistivity thereof to corrosion and to the product thereof |
| US2175771A (en) * | 1936-01-30 | 1939-10-10 | American Sheet & Tin Plate | Chromium-bearing metal |
| US2209924A (en) * | 1939-04-25 | 1940-07-30 | Budd Edward G Mfg Co | Passivation of stainless steel |
| US2377792A (en) * | 1941-02-28 | 1945-06-05 | Solvay Process Co | Preventing corrosion of ferrous metals by solutions of electrolytes |
| US2357219A (en) * | 1942-01-10 | 1944-08-29 | Joseph P Moran | Corrosion-resistant ferrous alloys |
| US2357554A (en) * | 1942-07-20 | 1944-09-05 | Schlage Lock Co | Anodic treatment of ferrous metals |
| US2390402A (en) * | 1942-09-02 | 1945-12-04 | Gen Electric | Method of passivating stainless steels |
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2943954A (en) * | 1958-02-10 | 1960-07-05 | Mead Corp | Casting surface for producing castsurfaced mineral coated paper |
| US3009865A (en) * | 1958-06-02 | 1961-11-21 | Mueller Walter Adolf | Anodic protection of kraft digesters |
| US3049479A (en) * | 1958-11-10 | 1962-08-14 | Chemionics Engineering Lab Inc | Corrosion-erosion-cavitation protection for marine propellers |
| US3126328A (en) * | 1958-12-01 | 1964-03-24 | Electrolytic bridge assembly for | |
| US3127337A (en) * | 1958-12-01 | 1964-03-31 | Anodic passivation system | |
| US3182007A (en) * | 1958-12-01 | 1965-05-04 | Continental Oil Co | Electrode assembly for the anodic passivation of metals |
| US3208925A (en) * | 1960-01-07 | 1965-09-28 | Continental Oil Co | Anodic protection against corrosion |
| US3147204A (en) * | 1960-02-25 | 1964-09-01 | Chemical Construction Corp | Anodic prevention of hydrogen embrittlement of metals |
| US3198724A (en) * | 1960-08-17 | 1965-08-03 | Whirlpool Co | Hot water heater with electrical scale control |
| US3162550A (en) * | 1961-05-08 | 1964-12-22 | Union Oil Co | Process of preventing corrosion of ferrous metal by an aqua ammonia solution |
| US3249524A (en) * | 1961-11-01 | 1966-05-03 | Sinclair Research Inc | Method of reducing corrosion |
| US3287237A (en) * | 1962-03-28 | 1966-11-22 | Allegheny Ludlum Steel | Surface treatment of bright annealed strip |
| US3720548A (en) * | 1970-04-02 | 1973-03-13 | Stamicarbon | Process for increasing the corrosion resistance of austenitic stainless steels |
| US3839096A (en) * | 1971-01-22 | 1974-10-01 | Int Nickel Co | Reproducibility of color in coloring stainless steel |
| US4026737A (en) * | 1974-10-22 | 1977-05-31 | Nippon Steel Corporation | Method for coloring a stainless steel |
| EP0776256A4 (en) * | 1994-09-26 | 1998-05-20 | Squibb & Sons Inc | Stainless steel acid treatment |
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