US3260619A - Methods and compositions for cleaning metal - Google Patents
Methods and compositions for cleaning metal Download PDFInfo
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- US3260619A US3260619A US430465A US43046565A US3260619A US 3260619 A US3260619 A US 3260619A US 430465 A US430465 A US 430465A US 43046565 A US43046565 A US 43046565A US 3260619 A US3260619 A US 3260619A
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- potassium hydroxide
- cleaning
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- 238000000034 method Methods 0.000 title claims description 45
- 239000000203 mixture Substances 0.000 title description 41
- 238000004140 cleaning Methods 0.000 title description 24
- 229910052751 metal Inorganic materials 0.000 title description 23
- 239000002184 metal Substances 0.000 title description 23
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 73
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 61
- 239000000463 material Substances 0.000 claims description 35
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 26
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 claims description 24
- 239000011780 sodium chloride Substances 0.000 claims description 13
- 235000010344 sodium nitrate Nutrition 0.000 claims description 12
- 239000004317 sodium nitrate Substances 0.000 claims description 12
- 239000010935 stainless steel Substances 0.000 claims description 11
- 229910001220 stainless steel Inorganic materials 0.000 claims description 11
- 238000011282 treatment Methods 0.000 claims description 9
- 238000007654 immersion Methods 0.000 claims description 8
- 238000002844 melting Methods 0.000 claims description 6
- 230000008018 melting Effects 0.000 claims description 6
- 238000005554 pickling Methods 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 3
- 230000001050 lubricating effect Effects 0.000 claims description 2
- XLYOFNOQVPJJNP-PWCQTSIFSA-N Tritiated water Chemical compound [3H]O[3H] XLYOFNOQVPJJNP-PWCQTSIFSA-N 0.000 claims 1
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 14
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 14
- 239000010936 titanium Substances 0.000 description 14
- 229910052719 titanium Inorganic materials 0.000 description 14
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 239000000047 product Substances 0.000 description 9
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 8
- 239000011521 glass Substances 0.000 description 8
- 239000001257 hydrogen Substances 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 8
- 229910045601 alloy Inorganic materials 0.000 description 7
- 239000000956 alloy Substances 0.000 description 7
- 229910052759 nickel Inorganic materials 0.000 description 7
- 229910000601 superalloy Inorganic materials 0.000 description 7
- 229910052742 iron Inorganic materials 0.000 description 6
- 229910052750 molybdenum Inorganic materials 0.000 description 6
- 239000011733 molybdenum Substances 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 6
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 5
- 229910052804 chromium Inorganic materials 0.000 description 5
- 239000011651 chromium Substances 0.000 description 5
- 238000000576 coating method Methods 0.000 description 5
- 150000002739 metals Chemical class 0.000 description 5
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 5
- 229910052721 tungsten Inorganic materials 0.000 description 5
- 239000010937 tungsten Substances 0.000 description 5
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 229910001069 Ti alloy Inorganic materials 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 239000010941 cobalt Substances 0.000 description 4
- 229910017052 cobalt Inorganic materials 0.000 description 4
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000003483 aging Methods 0.000 description 3
- 238000000137 annealing Methods 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910000856 hastalloy Inorganic materials 0.000 description 3
- 239000000314 lubricant Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 229910000851 Alloy steel Inorganic materials 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 150000001447 alkali salts Chemical class 0.000 description 2
- 239000011538 cleaning material Substances 0.000 description 2
- 230000002939 deleterious effect Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000009877 rendering Methods 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 229910052720 vanadium Inorganic materials 0.000 description 2
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 229910001200 Ferrotitanium Inorganic materials 0.000 description 1
- 241000775881 Haematopota pluvialis Species 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 239000001996 bearing alloy Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 229940000425 combination drug Drugs 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000005098 hot rolling Methods 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 239000010955 niobium Substances 0.000 description 1
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000011833 salt mixture Substances 0.000 description 1
- 238000005488 sandblasting Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
Classifications
-
- 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
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/28—Cleaning or pickling metallic material with solutions or molten salts with molten salts
Definitions
- This application relates to methods and compositions for cleaning metal and relates more particularly to the cleaning of a large variety of normally difficult metal surfaces.
- Many mechanical means such as sandblasting and the like are used industrially for the removal of this coating, but it will be readily seen that, in addition to the inherent difficulties of such a procedure, the stainless steel surface resulting therefrom may well be pitted or otherwise marred.
- molten alkali baths such as K-l are useful in the cleaning of surfaces subjected to this type of treatment, it may be necessary to immerse the metallic product from six to eight times before all of the glass and oxide is removed. This thus-formed glass coating has been found more difficult to clean than siliceous materials resulting from casting molds or other investment procedures.
- Another object of this invention is the provision of fused, substantially anhydrous, molten alkali salt mixture which is particularly adapted for exceptionally difficult cleaning processes.
- a further objective of the instant invention is to provide a material of the type described having a composition uniquely capable of use in a large variety of different procedures without modification.
- a particularly. important object of this invention is the provision of a composition having the ability to efficiently clean particularly sensitive metallic surfaces at relatively low temperatures, for example, below 900 F., and preferably below 800 F., without becoming undesirably viscous and difiicult to desludge.
- Yet another object of the instant invention is to provide a method for both descaling and deglassing materials manufactured utilizing a vitreous lubricant at high temperatures.
- a further object of this invention is the provision of methods for descaling titanium and alloys containing a predominant portion of titanium which preclude hydrogen pickup thereby avoiding the necessity of relatively expensive protective treatments such as vacuum annealing.
- a still further object of this invention is the provision of methods for cleaning the surfaces of wrought heatresisting steel alloys in such a manner as to preclude deleterious effect on the characteristics of the Product.
- compositions to be utilized according to the methods of the instant invention are weight ratio of potassium hydroxide to sodium hydroxide. While many prior art patents generally suggest the use of one or both materials, it has not been recognized heretofore that the potassium hydroxide provides unique advantages to the composition. Potassium hydroxide is more aggressive and dissolves the iron in iron oxide scales more readily than sodium hydroxide baths. Similar compositions without the potassium hydroxide have been found to be particularly inefficient and undesirable in that they fail to provide the excellent descaling and deglassing properties of the material of the instant invention and further in that they are found to sometimes even oxidize the metallic surface being treated rather than remove the oxides.
- a weight ratio between these constituents of at least 0.1 has been ascertained to be necessary to render the composition effective as a multipurpose cleaning material and particularly with regard to its efl iciency in the descaling of titanium and certain ditficult titanium alloys.
- the presence of the potassium hydroxide in at least this quantitative ratio has provided the unique descaling-deglassing properties for cleaning metal surfaces manufactured utilizing a vitreous lubricant.
- the maintenance of this potassium hydroxide level renders the material especially effective for cleaning other normally difiicu-lt metallic surfaces such as those of wrought heat-resisting steel superalloys.
- the upper level of the weight ratio between potassium hydroxide and sodium hydroxide in the composition may be somewhat varied, but it has been found that a value of substantially in excess of 0.4 is undesirable from a commercial viewpoint.
- the advantageous cleaning properties provided by the presence of the potassium hydroxide must be balanced against its increased cost as compared with sodium hydroxide and its corrosive effect on both the equipment being utilized and the material being treated.
- the presence of the sodium nitrate in the molten alkali bath has also been found to be critical to the production of an efiicient descaling and/ or deglassing technique.
- This material in the specific mixture defined hereinabove contributes to the unique properties of the bath and its capability of use for many varied cleaning purposes.
- the sodium'chloride is included in a relatively high percentage as compared to the one or two percent sodium chloride remaining in commercially produced caustic from its manufacturing process.
- This material assists in providing a molten bath which remains relatively thin or of low viscosity even at somewhat reduced treating temperatures such as below 900 F. or even below 800 F.
- this property of the molten bath of this invention is extremely important in order to provide a commercially acceptable method of continuously desludging the same thereby extending its effective life and precluding undesirable contamination of the product.
- the metal to be cleaned is immersed in a molten bath of the above composition for a period of time which may be as little as 30 seconds while the bath is maintained at an elevated temperature.
- time of the treatment will depend upon the size of the work-piece as well as the type and thickness of the material to be removed and the temperature of the bath. While the temperature may vary over a substantial range of from above its melting point to in excess of 1000 F., the specific composition of the bath of this invention allows the same to be utilized at relatively low temperatures, below 900 F. and even below 800 F. in those instances where higher temperatures would be undesirable such as in the treatment of titanium, titanium alloys, and steel superalloys. This ability avoids aging of the material and various other disadvantageous phenomenona such as hydrogen pickup, pitting, oxidation and the like as explained hereinabove.
- the metal is withdrawn from the alkali bath, preferably washed in water to remove any of the bath clinging to its surfaces, and pickled in a conventional manner in a dilute acidic material such as sulfuric acid, hydrochloric acid which may be in the form of sodium chloride added to the sulfuric acid, nitric acid, hydrofluoric acid and the like, alone or in admixtures, maintained at elevated temperatures, for example, in excess of about F. to provide a clean bright surface.
- the pickling treatments may vary substantially in accordance with well known techniques.
- the bath of this invention maintains its efiiciency over extended periods, small quantities of additional material being added from time to time to replace losses occurring from dragout of the workpieces and their carriers, these intermittent additions maintaining both the volume and equilibrium of the bath.
- Example 1 A 2600 pound charge of a material having the preferred formulation set forth above was added to a salt pot and heated to a temperature of approximately 900 F. Sections of glass-coated, scaled tubing inches long by 3 /2 inches diameter having nonuniform vitreous bonded and fused coatings on their surfaces as much as inch thick in places resulting from a Sejournet-type extrusion process, were immersed in the bath for periods of times ranging from 30 seconds to several hours. The treated tubes were then withdrawn from the bath, quenched in water and pickled in a dilute acidic material in a conventional manner. Substantially all of the scale and glass were removed inmost instances in a single immersion. In extremely difiicult cases, a single reimmersion functioned to completely clean the surfaces, the final product having a bright, unmarred finish. Sludge was readily removed during the processing.
- Example 2 The procedure of Example 1 was repeated immersing titanium workpieces having scaled surfaces formed by high temperature annealing processes in excess of 1200 C. and as high as 1450 C. The bath temperature was maintained between 800 F. and 900 F. The resulting products were completely descaled with no hydrogen pickup. Even reducing the temperature to from 700 to 800 F. resulted in excellent descaling while the bath viscosity remained sufiiciently low to permit satisfactory desludging.
- Example 3 A procedure similar to Example 2 was utilized to descale particularly diflicult alloys of titanium such as the following:
- Type 461 containing 5 percent aluminum and 2.5 percent tin
- Type 464 containing 6 .percent aluminum and 4 percent vanadium
- Type 120 VCA containing 13 percent vanadium, 11 percent chromium and 3 percent aluminum.
- Example 4 Utilizing a procedure similar to Example 2, various samples of steel superalloys conditioned by heat treating and hot rolling thereby forming oxide coatings, were descaled, such as the following:
- compositions and methods for the cleaning of metals specifically a large variety of normally difficult materials at relatively low temperatures, which satisfy all of the objectives of the instant application, and others, including many advantages of great practical utility and commercial importance.
- a composition for the cleaning of metals consisting essentially of a fused, substantially anhydrous, mixture of from 9-15 weight percent sodium nitrate, from 5-15 weight percent sodium chloride, from 8-20 weight percent potassium hydroxide and from 50-78 weight percent sodium hydroxide, the weight ratio of potassium hydroxide to sodium hydroxide being at least 0.1 and not substantially in excess of 0.4.
- composition in accordance with claim 1 wherein said mixture consists essentially of 12 weight percent sodium nitrate, '10 weight percent sodium chloride, 15 weight percent potassium hydroxide and 63 weight percent sodium hydroxide.
- a method for cleaning stainless steel and titanium base metals comprising immersing the metal to be treated in a molten bath consisting essentially of a mixture of from 9-15 weight percent sodium nitrate, from 5-15 weight percent sodium chloride, from 8-20 weight percent potassium hydroxide and from 50-78 weight percent sodium hydroxide, the weight ratio of potassium hydroxide to sodium hydroxide being at least 0.1 and not substantially in excess of 0.4, for at least 30 seconds, maintaining said bath at an elevated temperature above its melting point during the immersion, and removing the metal from said bath.
- a method in accordance with claim 3 further including the steps of washing the metal removed from said bath in water, and subjecting the same to a pickling treatment in a dilute acid solution.
- a method of removing scale and glass from a stainless steel product manufactured by a high temperature process utilizing glass as a lubricating material comprising immersing the stainless steel product in a molten bath consisting essentially of from 9-15 weight percent sodium nitrate, from v5-15 weight percent sodium chloride, from 8-20 weight percent potassium hydroxide and from 50-78 weight percent sodium hydroxide, the weight ratio of potassium hydroxide to sodium hydroxide being at least 0.1 and not substantially in excess of 0.4 for at least 30 seconds, maintaining said bath at a temperature above its melting point during the immersion, and removing the stainless steel product from the bath.
- a method in accordance with claim 6 further including the steps of washing the stainless steel product in water, and subjecting the same to a pickling treatment in a dilute acid solution.
- a method of descaling a metal selected from the group consisting of titanium and alloys containing a predominant portion of titanium comprising immersing the metal to be treated in a molten bath consisting essentially of a mixture of from 9- 15 weight percent sodium nitrate, from 515 weight percent sodium chloride, from 8-20 weight percent potassium hydroxide and from 50-78 weight percent sodium hydroxide, the weight ratio of potassium hydroxide to sodium hydroxide being at least 0.1 and not substantially in excess of 0.4 for at least 30 seconds, maintaining said bath at a temperature above its melting point and below about 900 F. during the immersion, and removing the metal from said bath.
- a method of descaling a wrought heat-resisting steel alloy comprising immersing the alloy to be treated in a molten bath consisting essentially of a mixture of from 9-1'5 weight percent sodium nitrate, from 5-15 weight percent sodium chloride, from 8-20 weight percent potassium hydroxide and from 5078 weight percent sodium hyroxide, the weight ratio of potassium hyroxide to sodium hydroxide being at least 0.1 and not substantially in excess of 0.4 for at least 30 seconds, maintaining said bath at a temperature above its melting point and below about 900 F. during the immersion, and removing the alloy from said bath.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
United States Patent 3,260,619 METHODS AND CUMPOSITIONS FOR CLEG METAL Robert H. Shoemaker and Harold Geschwender, Detroit, Mich, assignors to Kolene Corporation, Detroit, Mich. No Drawing. Filed Feb. 4, 1965, Ser. No. 430,465 14 (Claims. (Cl. 134-4)) This is a continuation-in-part of our earlier application of the same title, Serial No. 241,169, filed November 30, 1962, now abandoned.
This application relates to methods and compositions for cleaning metal and relates more particularly to the cleaning of a large variety of normally difficult metal surfaces.
As conducive to a better understanding of the instant inventive concept, it should be recognized that various materials in the form of fused molten alkali salts have been used heretofore for removing oxide scale and the like from metal surfaces, such as the well known mixture disclosed in Webster et al. US. Patent No. 2,458,661 known in the trade as Kolene Kl. While such materials are extremely efiicient for many applications, it has been found that, with certain particularly difficult problems, prior art compositions and methods are somewhat lacking. For example, stainless steel tubing and the like is frequently manufactured by an extrusion or drawing process utilizing glass of various forms as a lubricant. Such procedures are described in detail in Sejournet et al. Patent No. 2,538,917 among others. The resulting prodnot not only has an oxide scale formed on its surface from the high temperatures utilized, both on its interior and exterior in the case of tubing, but further includes a tenaciously bonded, fused, vitreous coating which is frequently uneven, ranging in thickness from a few thousandths of an inch to as much as A inch in places. Many mechanical means such as sandblasting and the like are used industrially for the removal of this coating, but it will be readily seen that, in addition to the inherent difficulties of such a procedure, the stainless steel surface resulting therefrom may well be pitted or otherwise marred. Although certain molten alkali baths such as K-l are useful in the cleaning of surfaces subjected to this type of treatment, it may be necessary to immerse the metallic product from six to eight times before all of the glass and oxide is removed. This thus-formed glass coating has been found more difficult to clean than siliceous materials resulting from casting molds or other investment procedures.
In addition to the cleaning of glass-coated metals resulting from Sejournet and other like processes, various other difficult problems have been encountered utilizing prior art materials. For example, the removal of scale from titanium, while possible with compositions currently in use, presents unique problems in that at the elevated temperatures of 900 F. and above necessary for efficient cleaning heretofore, the metallic surface has a tendency to pick up hydrogen resulting in a phenomenon known as hydrogen embrittlement which detrimentally affects the properties of the metal thereby necessitating the use of a vacuum annealing. Prior art materials have been tried at temperatures below 900 F., but at these relatively low treating temperatures, in addition to a sub stantial decrease in the cleaning effectiveness of the salts, the molten bath has become extremely viscous rendering the same particularly difficult to desludge. In order to provide a commercially feasible metal cleaning procedure, it is desirable to utilize a molten salt bath of a relatively low viscosity which is capable of having the sludge, in the form of oxides and the like removed from the metal surfaces, continuously displaced by agitation or the like 3,260,619 Patented July 12, 1966 "ice in a manner such as disclosed, for example, in Shoemaker et al. US. Patent No. 2,863,465 whereby the effectiveness of the bath will be realized for an extended period of time whether the cleaning operation is of the batch, or continuous, type. Prior art materials have been particularly ineflicient, both from a cleaning and from a desludging standpoint, unless the relatively high temperatures mentioned hereinabove were utilized. These problems are somewhat magnified with the use of various alloys of titanium which are more difiicult to descale than pure titanium and with which it has been necessary to use temperatures substantially in excess of 900 F., and sometimes even above 1000 F. in order to provide complete descaling.
Similarly, many of the highly sophisticated alloys known generally in the trade as superalloys or wrought heatresisting alloys are particularly difiicult to clean utilizing prior art materials. Such alloys have high oxidative resistance and tensile strength at temperatures up to about 2500 F. and contain additives such as chromium to combat oxidation, nickel, manganese, nitrogen, molybdenum or tungsten to render the same austenitic and cobalt, titanium, aluminum and silicon to further provide superstrength and other desirable characteristics for use in high pressure industrial equipment, jet-engines, missiles and the like. Once again, the use of normal temperature ranges in excess of 900 F. necessary with prior art materials produces a product having many deficiencies. For example, superalloys descaled in this manner are subject to pitting, possible galvanic attack in the salt, particularly with molybdenum-bearing alloys, and possible age hardening. Further, prior art compositions at these high temperatures have a tendency to form more oxides on the metallic surfaces than they remove as contrasted with the reverse in the instant case. Attempts to use lower temperatures with these superalloys result in inefficient descaling and undue viscosity of the molten bath rendering the same difiicult to desludge.
It is a primary object of the instant invention to provide compositions and methods for the cleaning of various metals which are free from the foregoing, and other, disadvantages.
Another object of this invention is the provision of fused, substantially anhydrous, molten alkali salt mixture which is particularly adapted for exceptionally difficult cleaning processes.
A further objective of the instant invention is to provide a material of the type described having a composition uniquely capable of use in a large variety of different procedures without modification.
A particularly. important object of this invention is the provision of a composition having the ability to efficiently clean particularly sensitive metallic surfaces at relatively low temperatures, for example, below 900 F., and preferably below 800 F., without becoming undesirably viscous and difiicult to desludge.
Yet another object of the instant invention is to provide a method for both descaling and deglassing materials manufactured utilizing a vitreous lubricant at high temperatures.
A further object of this invention is the provision of methods for descaling titanium and alloys containing a predominant portion of titanium which preclude hydrogen pickup thereby avoiding the necessity of relatively expensive protective treatments such as vacuum annealing.
A still further object of this invention is the provision of methods for cleaning the surfaces of wrought heatresisting steel alloys in such a manner as to preclude deleterious effect on the characteristics of the Product.
Additionally, it is an important object of this invention to provide a composition and methods for the cleaning of metals which are highly efiicient and reliable in operation,
relatively inexpensive and simple in practice, and particularly noncorrosive to the equipment being utilized.
Other and further objects reside in the particular com bination and quantitative ratios of the component parts of the compositions and the specific arrangement of the manipulative steps of the methods.
Consistent with the above objectives, it has been found that a fused, substantially anhydrous cleaning material formed of the following mixture has all of the desired properties and characteristics:
Of particular importance in the formation of the compositions to be utilized according to the methods of the instant invention is the weight ratio of potassium hydroxide to sodium hydroxide. While many prior art patents generally suggest the use of one or both materials, it has not been recognized heretofore that the potassium hydroxide provides unique advantages to the composition. Potassium hydroxide is more aggressive and dissolves the iron in iron oxide scales more readily than sodium hydroxide baths. Similar compositions without the potassium hydroxide have been found to be particularly inefficient and undesirable in that they fail to provide the excellent descaling and deglassing properties of the material of the instant invention and further in that they are found to sometimes even oxidize the metallic surface being treated rather than remove the oxides. A weight ratio between these constituents of at least 0.1 has been ascertained to be necessary to render the composition effective as a multipurpose cleaning material and particularly with regard to its efl iciency in the descaling of titanium and certain ditficult titanium alloys. Further, the presence of the potassium hydroxide in at least this quantitative ratio has provided the unique descaling-deglassing properties for cleaning metal surfaces manufactured utilizing a vitreous lubricant. Also, the maintenance of this potassium hydroxide level renders the material especially effective for cleaning other normally difiicu-lt metallic surfaces such as those of wrought heat-resisting steel superalloys. The upper level of the weight ratio between potassium hydroxide and sodium hydroxide in the composition may be somewhat varied, but it has been found that a value of substantially in excess of 0.4 is undesirable from a commercial viewpoint. The advantageous cleaning properties provided by the presence of the potassium hydroxide must be balanced against its increased cost as compared with sodium hydroxide and its corrosive effect on both the equipment being utilized and the material being treated.
The presence of the sodium nitrate in the molten alkali bath has also been found to be critical to the production of an efiicient descaling and/ or deglassing technique. This material in the specific mixture defined hereinabove contributes to the unique properties of the bath and its capability of use for many varied cleaning purposes.
It will be noted that the sodium'chloride is included in a relatively high percentage as compared to the one or two percent sodium chloride remaining in commercially produced caustic from its manufacturing process. This material assists in providing a molten bath which remains relatively thin or of low viscosity even at somewhat reduced treating temperatures such as below 900 F. or even below 800 F. As pointed out hereinabove, this property of the molten bath of this invention is extremely important in order to provide a commercially acceptable method of continuously desludging the same thereby extending its effective life and precluding undesirable contamination of the product.
Although each of the materials forming part of the bath of this invention are known in and of themselves for use in the cleaning of metallic surfaces, the particular combination defined hereby and the specific quantitative relationship between the components of the mixture, provide a synergi tic result not realizable from the individual materials or other combinations of the same. Specifical- 1y, this particular composition has the advantage of being useful without modification for cleaning in an efficient manner various metallic surfaces which have caused difiiculty in the past.
While it is particularly important to include all of the materials in the quantitative ratios set forth hereinabove, it is also of great importance to exclude various materials found in previously known compositions. For example, certain baths suggested by the prior art have required the presence of additional components such as alkali carbonates. However, it has been found that baths of this composition must be frequently replaced because their eifectiveness has deteriorated below a point of minimum usefulness. This relatively rapid decrease in efficiency of the bath is a direct result of the presence of the carbonate. Similarly, the inclusion of various other materials has been found to produce deleterious effects on the bath in many instances. Hydrogen-containing compounds, such as hydrides and the like, render the bath undesirable for titanium cleaning in that the effects of hydrogen embrittlement are increased. Thus, the specific composition defined by this invention, and this composition alone, can provide the unique multipurpose characteristics desired.
With regard to the treating methods, the metal to be cleaned is immersed in a molten bath of the above composition for a period of time which may be as little as 30 seconds while the bath is maintained at an elevated temperature. It will be understood that the time of the treatment will depend upon the size of the work-piece as well as the type and thickness of the material to be removed and the temperature of the bath. While the temperature may vary over a substantial range of from above its melting point to in excess of 1000 F., the specific composition of the bath of this invention allows the same to be utilized at relatively low temperatures, below 900 F. and even below 800 F. in those instances where higher temperatures would be undesirable such as in the treatment of titanium, titanium alloys, and steel superalloys. This ability avoids aging of the material and various other disadvantageous phenomenona such as hydrogen pickup, pitting, oxidation and the like as explained hereinabove.
Following the immersion, the metal is withdrawn from the alkali bath, preferably washed in water to remove any of the bath clinging to its surfaces, and pickled in a conventional manner in a dilute acidic material such as sulfuric acid, hydrochloric acid which may be in the form of sodium chloride added to the sulfuric acid, nitric acid, hydrofluoric acid and the like, alone or in admixtures, maintained at elevated temperatures, for example, in excess of about F. to provide a clean bright surface. The pickling treatments may vary substantially in accordance with well known techniques.
The bath of this invention maintains its efiiciency over extended periods, small quantities of additional material being added from time to time to replace losses occurring from dragout of the workpieces and their carriers, these intermittent additions maintaining both the volume and equilibrium of the bath.
Having now described the instant inventive concept in more general terms, the following specific examples will serve to illustrate the same although, it is to be understood that these examples are not to be interpreted as limiting.
Example 1 A 2600 pound charge of a material having the preferred formulation set forth above was added to a salt pot and heated to a temperature of approximately 900 F. Sections of glass-coated, scaled tubing inches long by 3 /2 inches diameter having nonuniform vitreous bonded and fused coatings on their surfaces as much as inch thick in places resulting from a Sejournet-type extrusion process, were immersed in the bath for periods of times ranging from 30 seconds to several hours. The treated tubes were then withdrawn from the bath, quenched in water and pickled in a dilute acidic material in a conventional manner. Substantially all of the scale and glass were removed inmost instances in a single immersion. In extremely difiicult cases, a single reimmersion functioned to completely clean the surfaces, the final product having a bright, unmarred finish. Sludge was readily removed during the processing.
It was found that similar workpieces treated with prior art com-positions required six to eight immersions before the surfaces were rendered substantially clean.
Example 2 The procedure of Example 1 was repeated immersing titanium workpieces having scaled surfaces formed by high temperature annealing processes in excess of 1200 C. and as high as 1450 C. The bath temperature was maintained between 800 F. and 900 F. The resulting products were completely descaled with no hydrogen pickup. Even reducing the temperature to from 700 to 800 F. resulted in excellent descaling while the bath viscosity remained sufiiciently low to permit satisfactory desludging.
Similar titanium samples processed utilizing prior art materials required temperatures in excess of 900 F. to produce satisfactory descaling with the material picking up hydrogen resulting in detrimental effects from the standpoint of the physical characteristics of the titanium metal in subsequent operations.
Example 3 A procedure similar to Example 2 was utilized to descale particularly diflicult alloys of titanium such as the following:
Type 48-1 containing 8 percent manganese;
Type 461 containing 5 percent aluminum and 2.5 percent tin;
Type 464 containing 6 .percent aluminum and 4 percent vanadium; and
Type 120 VCA containing 13 percent vanadium, 11 percent chromium and 3 percent aluminum.
Completely satisfactory descaling of the above materials was realized at temperatures below 900 F. and even below 800 F.
Subjection of these same materials to prior art descaling techniques resulted in age hardening and other undesirable effects.
Example 4 Utilizing a procedure similar to Example 2, various samples of steel superalloys conditioned by heat treating and hot rolling thereby forming oxide coatings, were descaled, such as the following:
Multimelt (M)chromium 18-22 percent, nickel 18-22 percent, molybdenum 2.75-3.75 percent, tungsten 2-3 percent, cobalt 18-22 percent, columbium .75-l.5 percent, the rest essentially iron;
Hastelloy X-chromium 20-23 percent, nickel 46 percent, molybdenum 8-10 percent, tungsten .2-1 percent, cobalt .5-2.5 percent, iron 17-20 percent;
Hastelloy B-molybdenum 26-30 percent, iron 4-6 percent, the rest essentially nickel;
Hastelloy Cchromium 13-17 percent, molybdenum 16-18 percent, tungsten 3.7-5.3 percent, iron 4.5-7 percent, the rest essentially nickel;
Haynes Alloy chromium 19-21 percent, nickel 9-11 percent, tungsten 14-16 percent, iron 2 percent maximum, the rest essentially cobalt; and
Ren 4lchromium 11.5 percent, nickel 76 percent, silicon 4 percent, other elements 5 percent.
Complete descaling of these materials at temperatures below 900 F. and even below 800 F. has been effected with the salt remaining thin and fluid thereby facilitating desludging of the same.
Similar treatments of these and comparable superalloys with prior art compositions necessitated the use of temperatures in excess of 900 F. resulting in pitting, age hardening, galvanic attack and oxidation by the salt.
It will now be seen that there are herein provided compositions and methods for the cleaning of metals, specifically a large variety of normally difficult materials at relatively low temperatures, which satisfy all of the objectives of the instant application, and others, including many advantages of great practical utility and commercial importance.
Since many embodiments may be made of the instant inventive concept, and since many modifications may be made of the embodiments hereinbefore described, it is to be understood that all matter herein is to be interpreted merely as illustrative and not in a limiting sense. Accordingly what is claimed is:
1. A composition for the cleaning of metals consisting essentially of a fused, substantially anhydrous, mixture of from 9-15 weight percent sodium nitrate, from 5-15 weight percent sodium chloride, from 8-20 weight percent potassium hydroxide and from 50-78 weight percent sodium hydroxide, the weight ratio of potassium hydroxide to sodium hydroxide being at least 0.1 and not substantially in excess of 0.4.
2. A composition in accordance with claim 1 wherein said mixture consists essentially of 12 weight percent sodium nitrate, '10 weight percent sodium chloride, 15 weight percent potassium hydroxide and 63 weight percent sodium hydroxide.
3. A method for cleaning stainless steel and titanium base metals comprising immersing the metal to be treated in a molten bath consisting essentially of a mixture of from 9-15 weight percent sodium nitrate, from 5-15 weight percent sodium chloride, from 8-20 weight percent potassium hydroxide and from 50-78 weight percent sodium hydroxide, the weight ratio of potassium hydroxide to sodium hydroxide being at least 0.1 and not substantially in excess of 0.4, for at least 30 seconds, maintaining said bath at an elevated temperature above its melting point during the immersion, and removing the metal from said bath.
4. A method in accordance with claim 3 wherein said mixture consist-s essentially of 12 weight percent sodium nitrate, 10 weight percent sodium chloride, 15 weight percent potassium hydroxide and 63 weight percent sodium hydroxide.
5. A method in accordance with claim 3 further including the steps of washing the metal removed from said bath in water, and subjecting the same to a pickling treatment in a dilute acid solution.
6. A method of removing scale and glass from a stainless steel product manufactured by a high temperature process utilizing glass as a lubricating material comprising immersing the stainless steel product in a molten bath consisting essentially of from 9-15 weight percent sodium nitrate, from v5-15 weight percent sodium chloride, from 8-20 weight percent potassium hydroxide and from 50-78 weight percent sodium hydroxide, the weight ratio of potassium hydroxide to sodium hydroxide being at least 0.1 and not substantially in excess of 0.4 for at least 30 seconds, maintaining said bath at a temperature above its melting point during the immersion, and removing the stainless steel product from the bath.
7. A method in accordance with claim 6 wherein said mixture consists essentially of 12 weight percent sodium nitrate, 10 weight percent sodium chloride, 15 weight percent potassium hydroxide and 63 weight percent sodium hydroxide.
8. A method in accordance with claim 6 further including the steps of washing the stainless steel product in water, and subjecting the same to a pickling treatment in a dilute acid solution.
9. A method of descaling a metal selected from the group consisting of titanium and alloys containing a predominant portion of titanium comprising immersing the metal to be treated in a molten bath consisting essentially of a mixture of from 9- 15 weight percent sodium nitrate, from 515 weight percent sodium chloride, from 8-20 weight percent potassium hydroxide and from 50-78 weight percent sodium hydroxide, the weight ratio of potassium hydroxide to sodium hydroxide being at least 0.1 and not substantially in excess of 0.4 for at least 30 seconds, maintaining said bath at a temperature above its melting point and below about 900 F. during the immersion, and removing the metal from said bath.
10. A method in accordance with claim 9 wherein said mixture consists essentially of 12 Weight percent sodium nitrate, 10 weigh-t percent sodium chloride, 15 weight percent potassium hydroxide and 63 weight percent sodium hydroxide.
11. A method in accordance with claim 9 wherein said temperature is maintained at from 700800 F.
12. A method of descaling a wrought heat-resisting steel alloy comprising immersing the alloy to be treated in a molten bath consisting essentially of a mixture of from 9-1'5 weight percent sodium nitrate, from 5-15 weight percent sodium chloride, from 8-20 weight percent potassium hydroxide and from 5078 weight percent sodium hyroxide, the weight ratio of potassium hyroxide to sodium hydroxide being at least 0.1 and not substantially in excess of 0.4 for at least 30 seconds, maintaining said bath at a temperature above its melting point and below about 900 F. during the immersion, and removing the alloy from said bath.
13. A method in accordance with claim 12 wherein said mixture consists essentially of 12 weight percent sodium nitrate, 10 weight percent sodium chloride, 15 weight percent potassium hydroxide and 63 weight percent sodium hydroxide.
14. A method in accordance with claim 12 wherein said temperature is maintained at from 700800 F.
References Cited by the Examiner UNITED STATES PATENTS 2,655,481 10/1953 Clingan 252-156 XR 2,931,778 4/1960 Ilenda et a1 252156 3,030,239 4/1962 Mekjean et al. 252 156 XR FOREIGN PATENTS Y 490,861 2/1953 Canada.
JULIUS GREENWALD, Primary Examiner.
J. T. FEDIGAN, Assistant Examiner.
Claims (2)
- 6. A METHOD OF REMOVING SCALE AND GLASS FROM A STAINLESS STEEL PRODUCT MANUFACTURED BY A HIGH TEMPERATURE PROCESS UTILIZING GLASS AS A LUBRICATING MATERIAL COMPRISING IMMERSING THE STAINLESS STEEL PRODUCT IN A MOLTEN BATH CONSISTING ESSENTIALLY OF FROM 9-15 WEIGHT PERCENT SODIUM NITRATE, FROM 5-15 WEIGHT PERCENT SODIUM CHLORIDE, FROM 8-20 WEIGHT PERCENT POTASSIUM HYDROXIDE AND FROM 50-78 WEIGHT PERCENT SODIUM HYDROXIDE, THE WEIGHT RATIO OF POTASSIUM HYDROXIDE TO SODIUM HYDROXIDE BEING AT LEAST 0.1 AND NOT SUBSTANTIALLY IN EXCESS OF 0.4 FOR AT LEAST 30 SECONDS, MAINTAINING SAID BATH AT A TEMPERATURE ABOVE ITS MELTING POINT DURING THE IMMERSION, AND REMOVING THE STAINLESS STEEL PRODUCT FROM THE BATH.
- 8. A METHOD IN ACCORDANCE WTH CLAIM 6 FURTHER INCLUDING THE STEPS OF WASHING THE STAINLESS STEEL PRODUCT IN WATER, AND SUBJECTING THE SAME TO A PICKLING TREATMENT IN A DILUTE ACID SOLUTION.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US430465A US3260619A (en) | 1965-02-04 | 1965-02-04 | Methods and compositions for cleaning metal |
| BE680347D BE680347A (en) | 1965-02-04 | 1966-04-29 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US430465A US3260619A (en) | 1965-02-04 | 1965-02-04 | Methods and compositions for cleaning metal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3260619A true US3260619A (en) | 1966-07-12 |
Family
ID=23707668
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US430465A Expired - Lifetime US3260619A (en) | 1965-02-04 | 1965-02-04 | Methods and compositions for cleaning metal |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3260619A (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3873280A (en) * | 1972-08-22 | 1975-03-25 | Merit Abrasive Prod | Descaling of steel strip |
| US4026777A (en) * | 1976-04-01 | 1977-05-31 | Allegheny Ludlum Industries, Inc. | Metallic descaling system |
| JPS5278631A (en) * | 1975-12-26 | 1977-07-02 | Nisshin Steel Co Ltd | Method of pickling extremely thin stainless strip |
| DE2714136A1 (en) * | 1976-04-01 | 1977-10-20 | Allegheny Ludlum Ind Inc | METAL BODY DESCALE METHOD |
| US4066521A (en) * | 1977-02-09 | 1978-01-03 | Allegheny Ludlum Industries, Inc. | Metallic descaling system |
| US4140821A (en) * | 1976-03-05 | 1979-02-20 | International Lead Zinc Research Organization, Inc. | Process for preheating and preparing ferrous metal for galvanizing |
| US4415415A (en) * | 1982-11-24 | 1983-11-15 | Allegheny Ludlum Steel Corporation | Method of controlling oxide scale formation and descaling thereof from metal articles |
| US5221358A (en) * | 1991-08-16 | 1993-06-22 | Kolene Corporation | Descaling/deglassing salt composition and method |
| US5348628A (en) * | 1991-04-02 | 1994-09-20 | Unitika Ltd. | Method of treating salt bath liquid |
| US5542981A (en) * | 1994-06-22 | 1996-08-06 | Lee, Sr.; Clel E. | Process for removing mineral deposits from lagoon recycle lines |
| US5830291A (en) * | 1996-04-19 | 1998-11-03 | J&L Specialty Steel, Inc. | Method for producing bright stainless steel |
| WO2011085172A2 (en) | 2010-01-11 | 2011-07-14 | Kolene Corporation | Metal surface scale conditioning |
| CN102677140A (en) * | 2012-05-04 | 2012-09-19 | 大连理工大学 | Process for cleaning surfaces of stainless steel castings |
| US20190047094A1 (en) * | 2017-08-11 | 2019-02-14 | General Electric Company | Method of repairing superalloys |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA490861A (en) * | 1953-02-24 | H. Vaughn Thomas | Inhibiting alkali dissolution of glass | |
| US2655481A (en) * | 1949-04-04 | 1953-10-13 | Eastern Stainless Steel Corp | Oxide removing bath |
| US2931778A (en) * | 1954-09-28 | 1960-04-05 | Diamond Alkali Co | Alkaline composition |
| US3030239A (en) * | 1957-10-24 | 1962-04-17 | Hooker Chemical Corp | Process and salt for descaling of metals |
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1965
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA490861A (en) * | 1953-02-24 | H. Vaughn Thomas | Inhibiting alkali dissolution of glass | |
| US2655481A (en) * | 1949-04-04 | 1953-10-13 | Eastern Stainless Steel Corp | Oxide removing bath |
| US2931778A (en) * | 1954-09-28 | 1960-04-05 | Diamond Alkali Co | Alkaline composition |
| US3030239A (en) * | 1957-10-24 | 1962-04-17 | Hooker Chemical Corp | Process and salt for descaling of metals |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3873280A (en) * | 1972-08-22 | 1975-03-25 | Merit Abrasive Prod | Descaling of steel strip |
| JPS5278631A (en) * | 1975-12-26 | 1977-07-02 | Nisshin Steel Co Ltd | Method of pickling extremely thin stainless strip |
| US4140821A (en) * | 1976-03-05 | 1979-02-20 | International Lead Zinc Research Organization, Inc. | Process for preheating and preparing ferrous metal for galvanizing |
| US4026777A (en) * | 1976-04-01 | 1977-05-31 | Allegheny Ludlum Industries, Inc. | Metallic descaling system |
| DE2714136A1 (en) * | 1976-04-01 | 1977-10-20 | Allegheny Ludlum Ind Inc | METAL BODY DESCALE METHOD |
| US4066521A (en) * | 1977-02-09 | 1978-01-03 | Allegheny Ludlum Industries, Inc. | Metallic descaling system |
| US4415415A (en) * | 1982-11-24 | 1983-11-15 | Allegheny Ludlum Steel Corporation | Method of controlling oxide scale formation and descaling thereof from metal articles |
| US5348628A (en) * | 1991-04-02 | 1994-09-20 | Unitika Ltd. | Method of treating salt bath liquid |
| US5221358A (en) * | 1991-08-16 | 1993-06-22 | Kolene Corporation | Descaling/deglassing salt composition and method |
| US5542981A (en) * | 1994-06-22 | 1996-08-06 | Lee, Sr.; Clel E. | Process for removing mineral deposits from lagoon recycle lines |
| US5830291A (en) * | 1996-04-19 | 1998-11-03 | J&L Specialty Steel, Inc. | Method for producing bright stainless steel |
| WO2011085172A2 (en) | 2010-01-11 | 2011-07-14 | Kolene Corporation | Metal surface scale conditioning |
| CN102677140A (en) * | 2012-05-04 | 2012-09-19 | 大连理工大学 | Process for cleaning surfaces of stainless steel castings |
| US20190047094A1 (en) * | 2017-08-11 | 2019-02-14 | General Electric Company | Method of repairing superalloys |
| US11207751B2 (en) * | 2017-08-11 | 2021-12-28 | General Electric Company | Method of repairing superalloys |
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