US2318559A - Material for and process of pickling copper or its alloys - Google Patents
Material for and process of pickling copper or its alloys Download PDFInfo
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- US2318559A US2318559A US391127A US39112741A US2318559A US 2318559 A US2318559 A US 2318559A US 391127 A US391127 A US 391127A US 39112741 A US39112741 A US 39112741A US 2318559 A US2318559 A US 2318559A
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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
- 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
- C23G1/02—Cleaning or pickling metallic material with solutions or molten salts with acid solutions
- C23G1/10—Other heavy metals
- C23G1/103—Other heavy metals copper or alloys of copper
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- This invention relates. to the pickling of metal articles and has particular application to the acid pickling of copper and copper-containing alloys for the purpose of removing scale and producing a bright finish. 5,. 1
- ferric. salts such. as ferric sulfat and ferric chloride; either aloneor in combination with mineralacids, such as; sulfuric or muriatic acid.
- solutions containing such saltsare not only capable of removing scale in 3.1-: satisfactory manner, but they tend to avoid the, production of fa reddish or copper rich surface and to remove any surface areas predominantly red in color result-- 5- ingiromthe annealing or other heat treatment to which the metal is generally. subjected. -I-Iow-. ever, these baths also areobjectionable; in that.- they tend to produce surfaces of;a dull ordirty appearance, and atv best do notform .a smooth; 40
- a further object of the invention is to provide a bath for pickling copper or its alloys which-is capable of removing the dull or dirty appearance obtained as a result of preliminary pickling of, the metal in other pickling baths.
- the invention relates in general to the pickling of copper or its alloys with acid reacting aqueousbaths containing ferric salts, to which there has been added a substance capable of supplying organic anions, particularly aliphatic anions, either directly or by interaction with other ingredients of the bath. More specifically the invention is directed to the pickling of copper or its alloys withaqueous solutions of ferric salts, such as ferriosulfate or ferric chloride, containing relatively small amounts of organic acids. salts or esters, which act in combination with the ferric salts not only to remove scale, but to remove or prevent discoloration and produce a smooth and bright, natural appearing surface onthe metal; j
- The-copper. alloys which may be successfully treated in accordance with the invention include such;- alloys as cartridge brass, high brass, lowbrass, leaded brass, red brass, rich low brass, the bronzes, gilding metal and nickel silver.
- High nickel alloys such as constantan, cupro-nickel, and Monel metal, and-.alloyscontaining silicon orjberyllium, such as silicon brass, silicon bronze, and beryllium copper, may also be treated, but require somewhat larger amounts of pickling agents than the other copper alloys.
- the organic agents which may be used for the purposes of this invention include a wide variety of acids, or theirsalts or.esters.
- acids or theirsalts or.esters.
- substances which have been found to be most suitable'may be'mentioned such organic acids as citric, tartaric, acetic,- adipic, lactic, glycollic, gluconic, succinic, malonid, d1 malic, formic and benzoic acids, and their equivalent salts or esters.
- These substances are. readily soluble in water, and in some instances are capable of producing the desired results when used in exceedingly small amounts.
- the amountof ferric salt employed in the pickling operations may be widely varied. For example, it is possible to use anywhere from 1 to 50%. However, it. is preferable frolff't'h'e standpoint of economy to use solutions containing not more than 10% of the ferric salt, ex-
- This preliminary pickle may consist of an aqueous solution of either mineral acid, preferably sulfuric or muriatic acid, or a combination of such an acid with a ferric salt, preferably ferric sulfate or chloride.
- the reagents used in the preliminary pickle may be present in quantities varying from about 1 to 50%. However, it is preferable to use. the mineral acid in amountsvarying from to and the ferric salt in amounts varying from 5 to In the case of certain alloys, particularly those having silicon oxide scales, it is necessary to use hydrofluoric acid in the pre-pickle, which may be present in amounts varying from .1 to 5% together with a suitable amount of ferric salt.
- Example I A low brass containing 85 parts of copper and 15 parts of zinc and having a scale which was unusually hard to remove was subjected for about 2 minutes to an aqueous pre-pickle containing 10% sulfuric acid at a temperature of 125 F. It was then pickled for about 5 minutes in an aqueous solution containing 9% of ferric sulfate and 0.1% of cream of tartar at 160 F. The metal, following the above treatment, "had all of its scale removed and at the same time had a smooth and bright surface and an appearance entirely natural to brass.
- Emmple II The same kind of brass as in Example I was pre-pickled for about 2 minutes in an aqueous solution containing 10% sulfuric acid and 9% ferric sulfate at 125 F., and then pickled for about 2 minutes in-an aqueous solution containing 9% of ferric sulfate and 3% of acetic acid at room temperature. Substantially the same beneficial results as in Example I were noted.
- Example III cept in the case of high nickel or silicon alloys Example IV A high brass of the kind described in Example III was subjected for about 2 minutes to a preliminary pickle in an aqueous bath containing 10% of sulfuric acid at F. and then pickled for about 3 minutes at room temperature in an aqueous solution containing 9% of ferric sulfate and 3% of acetic acid. The resulting brass was entirely free of scale and had a smooth, bright and natural appearance.
- Example V I A sample of nickel silver was pre-pickled for about 2 minutes in an aqueous solution containing 10% of sulfuric acid and 9% of ferric sulfate at a temperature of about 140 F., and then immersed for about 4 minutes in an aqueous pickling bath containing 9% of ferric sulfate and .5% of adipic acid at room temperature. After treatment in the above manner the alloy was free of scale and had a smooth bright and natural appearance.
- Eaxample VI A sample of silicon bronze was subjected for about 1 minute to the action of an aqueous prepickle containing 18% of ferric sulfate and 2% of hydrofluoric acid at F., and then pickled for about 3 minutes in an aqueous solution containing 9% of ferric sulfate and 1% of cream of tartar at 160 F.
- the alloy treated in the above manner was smooth and bright and had an appearance natural to bronze.
- a preliminary pickle is not always necessary, as frequently satisfactory results may be obtained with a single immersion in baths containing ferric salts and organic acid or like brightening agents.
- a preliminary descaling bath it is usually not necessary to employ more than about 10% of the mineral acid and/or the ferric salt, except in the case of silicon-containing alloys and high nickel alloys, which require somewhat larger amounts of ferric salts and, in the case of silicon alloys, a small amount of hydrofluoric acid.
- the temperature of the bath maybe varied between its freezing and boiling points, i. e., maintained at any intermediate point therebetween. Although in general more marked results are obtained by increasing the temperature of the bath, and also the time of immersion, it is usually not necessary to employ a temperature much above about 160 F., and in the case of high brasses and other easily pickled copper alloys it is sufficient to employ room or only slightly elevated temperatures. Moreover, baths 252. COMPOSITIONS.
- the time of immersion of the copper or alloy in the baths may be varied from a few seconds, in the case of easily pickled stock, to minutes or more, as required. In general, however, it is not necessary to immerse the stock for more than about 4 or 5 minutes, and when agitation of the bath is resorted to, even less time is usually suflicient.
- pickling baths such as those described herein in the pickling of copper or its alloys, it is possible not only to thoroughly remove oxide scale, but to remove predominately reddish areas resulting 'from preferential volatilization during annealing and to prevent general red coloration resulting from preferential dissolution during pickling. Moreover, the baths or solutions of this invention tend to pro cute smooth and shiny surfaces which have an appearance natural to the particular alloy being treated.
- An aqueous acid reacting bath for pickling copper or its alloys containing water-soluble ferric ions and organic anions.
- An aqueous acid reacting bath for pickling copper or its alloys containing ferric ions and organic aliphatic anions.
- An aqueous bath for pickling copper or its alloys containing a ferric salt and an organic aliphatic acid 3.
- An aqueous acid reacting bath for pickling copper or its alloys containing a ferric salt and a salt of an organic aliphatic acid.
- An aqueous bath for pickling copper or its alloys containing ferric sulfate and citric acid 6.
- An aqueous acid reacting bath for pickling copper or its alloys containing ferric sulfate and cream of tartar.
- An aqueous bath for pickling copper or its alloys containing ferric sulfate and acetic acid 8.
- the method of pickling copper or its alloys which comprises subjecting the same to the action of an aqueous acid reacting bath containing ferric sulfate and organic aliphatic anions.
- the method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing a mineral acid, and then subjecting it to the action of an aqueous acid reacting bath containing water-soluble ferric ions and organic anions.
- the method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing a ferric salt and a mineral acid, and then subjecting it to the action of an aqueous acid reacting bath containing water soluble ferric ions and organic anions.
- the method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing not more than about 20% of a ferric salt and not more than about 15% of a mineral acid, and then subjecting it to the action of an aqueous acid reacting bath containing not more than about 20% of a ferric salt and not more than about 3% of organic aliphatic anions.
- the method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing ferric sulfate and sulfuric acid, and then subjecting it to the action of an aqueous bath containing ferric sulfate and citric acid.
- the method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing ferric sulfate and sulfuric acid, and then subjecting it to the action of an aqueous acid reacting bath containing ferric sulfate and cream of tartar.
- the method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing ferric sulfate and sulfuric acid, and then subjecting it to the action of an aqueous bath containing ferric sulfate and acetic acid.
- An aqueous acid reacting bath for pickling copper or its alloys containing a ferric salt and an ester of an organic aliphatic acid for pickling copper or its alloys containing a ferric salt and an ester of an organic aliphatic acid.
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Description
252.cMP0sm0Ns. CROSS REFERENQE Exam.
Patented May 4, 1943 MATERIAL FOR AND PROCESS OF PICKLING COPPER on ITS ALLOYS John O. Percival, Somerville, Mass., assignor .to Monsanto Chemical Company, St. Louis, Mo., a
corporation of Delaware No Drawing. Application April 30, 1941,
- Serial No. 391,127
(crux-8) 18 Claims.
This invention relates. to the pickling of metal articles and has particular application to the acid pickling of copper and copper-containing alloys for the purpose of removing scale and producing a bright finish. 5,. 1
It is common practice to. remove the oxide scale from articles composed essentially of copper and copper alloys, such" as brass and bronze compositions, by dipping them in aqueous solutions of sulfuric or muriatic acid. Although these acids are adapted to remove certain scales, such as black cupric oxide scale and the oxides of alloying elements such as zinc and tin, they do not adequately remove any cuprous oxide scale, which is red and tendsto leave the surface with an undesirable red coloration. More over, they do not act on copper richsurface areas,-
which are frequently formed as a result of preferential volatilization of the alloying element during annealing, and in general they tend to preferentially dissolvethe alloying elements .ofthe alloy instead of the copper, which further: contributes ,to the poor, or .unsatisfactorycolorof the alloy.. a
To overcome. the objectionable-features of acidickling bathsof the above type, resort has been made to the useof aqueousv solutionsof ferric. salts, such. as ferric sulfat and ferric chloride; either aloneor in combination with mineralacids, such as; sulfuric or muriatic acid. Thus,
solutions containing such=saltsare not only capable of removing scale in 3.1-: satisfactory manner, but they tend to avoid the, production of fa reddish or copper rich surface and to remove any surface areas predominantly red in color result-- 5- ingiromthe annealing or other heat treatment to which the metal is generally. subjected. -I-Iow-. ever, these baths also areobjectionable; in that.- they tend to produce surfaces of;a dull ordirty appearance, and atv best do notform .a smooth; 40
shiny, natural appearing surface: such as is required in the trade.
. It is accordingly an important objectof the invention to provide a pickling bath. for copper or its alloys which not only removes oxide scales satisfactorily, but avoidsthe. formation of red colorations and produces-bright and smooth surfaces having an appearance which is more natural to the copper or alloy than that produced by mineral acids and/or ferric salts,
A further object of the invention is to provide a bath for pickling copper or its alloys which-is capable of removing the dull or dirty appearance obtained as a result of preliminary pickling of, the metal in other pickling baths.
Still further objects and advantages of the invention will appear from the following description and appended claims.
The invention relates in general to the pickling of copper or its alloys with acid reacting aqueousbaths containing ferric salts, to which there has been added a substance capable of supplying organic anions, particularly aliphatic anions, either directly or by interaction with other ingredients of the bath. More specifically the invention is directed to the pickling of copper or its alloys withaqueous solutions of ferric salts, such as ferriosulfate or ferric chloride, containing relatively small amounts of organic acids. salts or esters, which act in combination with the ferric salts not only to remove scale, but to remove or prevent discoloration and produce a smooth and bright, natural appearing surface onthe metal; j
The-copper. alloys which may be successfully treated in accordance with the invention include such;- alloys as cartridge brass, high brass, lowbrass, leaded brass, red brass, rich low brass, the bronzes, gilding metal and nickel silver. High nickel alloys, such as constantan, cupro-nickel, and Monel metal, and-.alloyscontaining silicon orjberyllium, such as silicon brass, silicon bronze, and beryllium copper, may also be treated, but require somewhat larger amounts of pickling agents than the other copper alloys. 1
The organic agents which may be used for the purposes of this invention include a wide variety of acids, or theirsalts or.esters. Among the substances which have been found to be most suitable'may be'mentioned such organic acids as citric, tartaric, acetic,- adipic, lactic, glycollic, gluconic, succinic, malonid, d1 malic, formic and benzoic acids, and their equivalent salts or esters. These substances are. readily soluble in water, and in some instances are capable of producing the desired results when used in exceedingly small amounts. In general they are employed in amounts varying from about .1 to 10%, although in special instances, such as when cream of tar- ,tar is employed, it is possible touse as little as .001%. Preferably, however, they are used in amounts varying from .1 to 3%, as larger amounts do not show any appreciable increase in efiectiveness. i
The amountof ferric salt employed in the pickling operations may be widely varied. For example, it is possible to use anywhere from 1 to 50%. However, it. is preferable frolff't'h'e standpoint of economy to use solutions containing not more than 10% of the ferric salt, ex-
of copper, when amounts as high as 20% may be required. Solutions which are appreciably stronger than this are too viscous for quick drainage. Exceedingly weak solutions on the other hand require constant replenishment.
Although it is possible to obtain highly satisfactory results by pickling the metal in a single bath containing a ferric salt and one or more of the above organic addition agents, it is frequently desirable to employ a preliminary pickle, particularly when the surface of the metal being treated is covered with a relatively heavy scale. This preliminary pickle, commonly called a prepickle, may consist of an aqueous solution of either mineral acid, preferably sulfuric or muriatic acid, or a combination of such an acid with a ferric salt, preferably ferric sulfate or chloride. By using a pre-pickle such as the above the descaling action is enhanced, and it is possible to employ a reduced quantity of the primary pickling or brightening agent.
The reagents used in the preliminary pickle may be present in quantities varying from about 1 to 50%. However, it is preferable to use. the mineral acid in amountsvarying from to and the ferric salt in amounts varying from 5 to In the case of certain alloys, particularly those having silicon oxide scales, it is necessary to use hydrofluoric acid in the pre-pickle, which may be present in amounts varying from .1 to 5% together with a suitable amount of ferric salt.
A further understanding of the invention will be obtained from the following examples of baths suitable for the treatment of different a1- loys:
Example I A low brass containing 85 parts of copper and 15 parts of zinc and having a scale which was unusually hard to remove was subjected for about 2 minutes to an aqueous pre-pickle containing 10% sulfuric acid at a temperature of 125 F. It was then pickled for about 5 minutes in an aqueous solution containing 9% of ferric sulfate and 0.1% of cream of tartar at 160 F. The metal, following the above treatment, "had all of its scale removed and at the same time had a smooth and bright surface and an appearance entirely natural to brass.
Emmple II The same kind of brass as in Example I was pre-pickled for about 2 minutes in an aqueous solution containing 10% sulfuric acid and 9% ferric sulfate at 125 F., and then pickled for about 2 minutes in-an aqueous solution containing 9% of ferric sulfate and 3% of acetic acid at room temperature. Substantially the same beneficial results as in Example I were noted.
Example III cept in the case of high nickel or silicon alloys Example IV A high brass of the kind described in Example III was subjected for about 2 minutes to a preliminary pickle in an aqueous bath containing 10% of sulfuric acid at F. and then pickled for about 3 minutes at room temperature in an aqueous solution containing 9% of ferric sulfate and 3% of acetic acid. The resulting brass was entirely free of scale and had a smooth, bright and natural appearance.
Example V I A sample of nickel silver was pre-pickled for about 2 minutes in an aqueous solution containing 10% of sulfuric acid and 9% of ferric sulfate at a temperature of about 140 F., and then immersed for about 4 minutes in an aqueous pickling bath containing 9% of ferric sulfate and .5% of adipic acid at room temperature. After treatment in the above manner the alloy was free of scale and had a smooth bright and natural appearance.
Eaxample VI A sample of silicon bronze was subjected for about 1 minute to the action of an aqueous prepickle containing 18% of ferric sulfate and 2% of hydrofluoric acid at F., and then pickled for about 3 minutes in an aqueous solution containing 9% of ferric sulfate and 1% of cream of tartar at 160 F. The alloy treated in the above manner was smooth and bright and had an appearance natural to bronze.
It should be understood that the above ex-' amples are illustrative only, and that wide variations may be made not only in the amount and kind of pickling or brightening agents used, but in the time of treatment and temperature of the bath. Different alloys require different amounts of pickling or brightening agents, and different immersion periods and bath temperatures, depending on the nature of the alloy and the kind of annealing or other treatment to which it has previously been subjected. In general, however, it is not necessary to employ more than about 20% of the ferric salt and about 3% of the organic acid or other brightening agent in the primary pickling bath, as larger amounts do not appreciably. increase the effectiveness of the baths and in the case of the ferric salts they frequently result in solutions which are too viscous for efficient drainage.
The use of a preliminary pickle is not always necessary, as frequently satisfactory results may be obtained with a single immersion in baths containing ferric salts and organic acid or like brightening agents. When a preliminary descaling bath is employed, however, it is usually not necessary to employ more than about 10% of the mineral acid and/or the ferric salt, except in the case of silicon-containing alloys and high nickel alloys, which require somewhat larger amounts of ferric salts and, in the case of silicon alloys, a small amount of hydrofluoric acid.
The temperature of the bath maybe varied between its freezing and boiling points, i. e., maintained at any intermediate point therebetween. Although in general more marked results are obtained by increasing the temperature of the bath, and also the time of immersion, it is usually not necessary to employ a temperature much above about 160 F., and in the case of high brasses and other easily pickled copper alloys it is sufficient to employ room or only slightly elevated temperatures. Moreover, baths 252. COMPOSITIONS.
containing certain of the agents, such as acetic acid, should not be heated in any case.
The time of immersion of the copper or alloy in the baths may be varied from a few seconds, in the case of easily pickled stock, to minutes or more, as required. In general, however, it is not necessary to immerse the stock for more than about 4 or 5 minutes, and when agitation of the bath is resorted to, even less time is usually suflicient.
By using pickling baths such as those described herein in the pickling of copper or its alloys, it is possible not only to thoroughly remove oxide scale, but to remove predominately reddish areas resulting 'from preferential volatilization during annealing and to prevent general red coloration resulting from preferential dissolution during pickling. Moreover, the baths or solutions of this invention tend to pro duce smooth and shiny surfaces which have an appearance natural to the particular alloy being treated.
It is believed that the beneficial brightening effects resulting from the addition of the organic acids, esters or salts is related to the ability-of these substances to form complexes with metallic ions. The exact cause of the effectiveness of the organic addition agents in improving the action of pickling baths containing ferric salts is unknown, however, and it is not intended to predicate the invention on any theory or belief such as the above.
Where reference is made herein to the per centof substance or agent employed in the bath, this.
is intended to mean the number of grams present or added per 100 cc. of solution. Also, where use is made of the term primary pickling bath, it is to be understood that this refers to the bathscontaining ferric salts and organic addition agents of the type described, 1, e. to those baths which may be used either alone or subsequent to a preliminary pickle to obtain the objects and advantages of the invention.
It is also to be understood that the invention is not limited in its application to the details described herein, since the invention is capable of other embodiments and of being practiced or carried out in various ways. Also it is to be understood that the phraseology or terminology employed herein is for the purpose of description and not of limitation, and it is not intended to: limit the invention claimed herein beyond the requirements of the prior art.
I claim:
1. An aqueous acid reacting bath for pickling copper or its alloys containing water-soluble ferric ions and organic anions.
2. An aqueous acid reacting bath for pickling copper or its alloys containing ferric ions and organic aliphatic anions.
3. An aqueous bath for pickling copper or its alloys containing a ferric salt and an organic aliphatic acid.
4. An aqueous acid reacting bath for pickling copper or its alloys containing a ferric salt and a salt of an organic aliphatic acid.
'cRoss REFERENCWEW 5. An aqueous acid reacting bath for pickling copper or its alloys containing ferric sulfate and organic anions.
6. An aqueous bath for pickling copper or its alloys containing ferric sulfate and citric acid.
7. An aqueous acid reacting bath for pickling copper or its alloys containing ferric sulfate and cream of tartar.
8. An aqueous bath for pickling copper or its alloys containing ferric sulfate and acetic acid.
9. The method of pickling copper or its alloys which comprises subjecting the same to the action of an aqueous acid reacting bath containing water-soluble ferric ions and organic anions.
10. The method of pickling copper or its alloys which comprises subjecting the same to the action of an aqueous acid reacting bath containing a ferric salt and organic aliphatic anions.
11. The method of pickling copper or its alloys which comprises subjecting the same to the action of an aqueous acid reacting bath containing ferric sulfate and organic aliphatic anions.
12. The method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing a mineral acid, and then subjecting it to the action of an aqueous acid reacting bath containing water-soluble ferric ions and organic anions.
13. The method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing a ferric salt and a mineral acid, and then subjecting it to the action of an aqueous acid reacting bath containing water soluble ferric ions and organic anions.
14. The method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing not more than about 20% of a ferric salt and not more than about 15% of a mineral acid, and then subjecting it to the action of an aqueous acid reacting bath containing not more than about 20% of a ferric salt and not more than about 3% of organic aliphatic anions.
15. The method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing ferric sulfate and sulfuric acid, and then subjecting it to the action of an aqueous bath containing ferric sulfate and citric acid.
16. The method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing ferric sulfate and sulfuric acid, and then subjecting it to the action of an aqueous acid reacting bath containing ferric sulfate and cream of tartar.
17. The method of pickling copper or its alloys which comprises immersing the same in an aqueous bath containing ferric sulfate and sulfuric acid, and then subjecting it to the action of an aqueous bath containing ferric sulfate and acetic acid.
18. An aqueous acid reacting bath for pickling copper or its alloys containing a ferric salt and an ester of an organic aliphatic acid.
JOHN O. PERCIVAL.
i i a
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US3317340A (en) * | 1963-01-29 | 1967-05-02 | Henkel & Cie Gmbh | Preparation of metal surfaces for enameling |
US3320171A (en) * | 1964-08-27 | 1967-05-16 | Dow Chemical Co | Powderless etching bath and method for etching curved segments |
US3341384A (en) * | 1964-05-04 | 1967-09-12 | Allied Chem | Dissolution of metal with acidified hydrogen peroxide containing dibasic acid |
US3411938A (en) * | 1964-08-07 | 1968-11-19 | Sperry Rand Corp | Copper substrate cleaning and vapor coating method |
US3510351A (en) * | 1964-11-27 | 1970-05-05 | Paul Van Dillen | Method for etching and cleaning of objects and plants,particularly tube systems and boiler plants,consisting of iron or steel |
US3646946A (en) * | 1969-01-06 | 1972-03-07 | Olin Mathieson | Copper alloy cleaning process |
US3728155A (en) * | 1969-01-06 | 1973-04-17 | Olin Corp | Copper alloy cleaning process |
US3754969A (en) * | 1971-06-18 | 1973-08-28 | Dow Corning | Method of adhering room temperature vulcanizable silicone rubber to metal surfaces |
US3986970A (en) * | 1973-05-02 | 1976-10-19 | The Furukawa Electric Co., Ltd. | Solution for chemical dissolution treatment of tin or alloys thereof |
US4014715A (en) * | 1975-12-08 | 1977-03-29 | General Electric Company | Solder cleaning and coating composition |
US4051057A (en) * | 1974-12-13 | 1977-09-27 | Harry Ericson | Solutions for cleaning surfaces of copper and its alloys |
FR2436193A1 (en) * | 1978-09-13 | 1980-04-11 | Olin Corp | PROCESS FOR CLEANING A COPPER-BASED ALLOY SURFACE HAVING A THERMALLY FORMED METAL OXIDE SURFACE LAYER |
US4298404A (en) * | 1979-09-06 | 1981-11-03 | Richardson Chemical Company | Chromium-free or low-chromium metal surface passivation |
US4299640A (en) * | 1980-07-25 | 1981-11-10 | The General Tire & Rubber Company | Rubber-brass adhesion improved through treatment of the metal with amino carboxylic acid or salt thereof |
US4333785A (en) * | 1980-05-15 | 1982-06-08 | The General Tire & Rubber Company | Adhesion of brass to rubber |
US4361445A (en) * | 1978-09-13 | 1982-11-30 | Olin Corporation | Copper alloy cleaning process |
US4386992A (en) * | 1979-05-11 | 1983-06-07 | Sunstar Chemical Ind. Co., Ltd. | Two-part adhesive and bonding method employing same |
US4444601A (en) * | 1979-09-06 | 1984-04-24 | Richardson Chemical Company | Metal article passivated by a bath having an organic activator and a film-forming element |
US4479840A (en) * | 1979-05-11 | 1984-10-30 | Sunstar Giken Kabushiki | Two-part adhesive and bonding method employing same |
US4600443A (en) * | 1984-10-01 | 1986-07-15 | Kennecott Corporation | Process for removing surface oxides from a copper-base alloy |
FR2582676A1 (en) * | 1985-06-03 | 1986-12-05 | Nat Semiconductor Corp | METHOD FOR TINNING THE EXTERNAL CONNECTIONS OF AN ENCAPSULATED SEMICONDUCTOR DEVICE |
US4713144A (en) * | 1986-08-01 | 1987-12-15 | Ardrox Inc. | Composition and method for stripping films from printed circuit boards |
US4714517A (en) * | 1986-05-08 | 1987-12-22 | National Semiconductor Corporation | Copper cleaning and passivating for tape automated bonding |
US5468303A (en) * | 1994-02-25 | 1995-11-21 | Zt Corporation | Rust, corrosion, and scale remover |
WO2000026440A2 (en) * | 1998-11-03 | 2000-05-11 | Eilenburger Elektrolyse- Und Umwelttechnik Gmbh | Circular method for pickling copper and copper alloys |
US10377968B2 (en) | 2017-06-12 | 2019-08-13 | General Electric Company | Cleaning compositions and methods for removing oxides from superalloy substrates |
-
1941
- 1941-04-30 US US391127A patent/US2318559A/en not_active Expired - Lifetime
Cited By (48)
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US2435239A (en) * | 1945-02-05 | 1948-02-03 | Joe A Stone | Process for removing resin coating from copper wire |
US2631950A (en) * | 1949-09-27 | 1953-03-17 | Rosenfeld Myer | Method of and composition for removing rust and scale |
US2982702A (en) * | 1950-05-09 | 1961-05-02 | Ralph F Wehrmann | Pretreating uranium for metal plating |
US2650875A (en) * | 1950-12-09 | 1953-09-01 | Diversey Corp | Method of etching aluminum and aluminum base alloys |
US2710792A (en) * | 1953-03-30 | 1955-06-14 | Kelite Products Inc | Composition and process for treating aluminum and aluminum alloys preparatory to spot welding |
US3041285A (en) * | 1955-05-27 | 1962-06-26 | Purex Corp Ltd | Composition for cleaning and polishing aluminum and aluminum alloys |
US2959555A (en) * | 1956-09-28 | 1960-11-08 | Dow Chemical Co | Copper and iron containing scale removal from ferrous metal |
US3091526A (en) * | 1957-01-08 | 1963-05-28 | Union Carbide Corp | High-purity titanium production |
US3019194A (en) * | 1957-02-18 | 1962-01-30 | Alan D Brite | Cleaning composition and method |
US3003899A (en) * | 1957-05-17 | 1961-10-10 | Dow Chemical Co | Removal of scale deposits |
US2872302A (en) * | 1957-09-12 | 1959-02-03 | Sylvania Electric Prod | Etchant |
US2980559A (en) * | 1958-02-06 | 1961-04-18 | Dow Chemical Co | Pickling of magnesium alloys |
US2947703A (en) * | 1958-07-16 | 1960-08-02 | Nalco Chemical Co | Process of inhibiting corrosion of ferrous metals in contact with aqueous solutions of acids |
US2981634A (en) * | 1958-10-20 | 1961-04-25 | Pfizer & Co C | Process for treating ferrous metals |
US3053719A (en) * | 1958-12-08 | 1962-09-11 | Purex Corp Ltd | Composition and process for etching magnesium |
US3025189A (en) * | 1958-12-10 | 1962-03-13 | Purex Corp Ltd | Composition and process for removing heat scale from metal parts |
US3011906A (en) * | 1960-08-24 | 1961-12-05 | Pfizer & Co C | Process for treating ferrous metals |
US3266934A (en) * | 1962-12-04 | 1966-08-16 | John R Alexander | Removal of contaminants from interiors of enclosures |
US3317340A (en) * | 1963-01-29 | 1967-05-02 | Henkel & Cie Gmbh | Preparation of metal surfaces for enameling |
US3231425A (en) * | 1963-04-24 | 1966-01-25 | Olin Mathieson | Process for treating metal surfaces |
US3269881A (en) * | 1963-12-30 | 1966-08-30 | Allied Chem | Hydrogen peroxide etching of copper in manufacture of printed circuits |
US3293093A (en) * | 1963-12-30 | 1966-12-20 | Allied Chem | Dissolution of metal with acidified hydrogen peroxide and use as copper etchant in manufacture of printed circuits |
US3341384A (en) * | 1964-05-04 | 1967-09-12 | Allied Chem | Dissolution of metal with acidified hydrogen peroxide containing dibasic acid |
US3411938A (en) * | 1964-08-07 | 1968-11-19 | Sperry Rand Corp | Copper substrate cleaning and vapor coating method |
US3320171A (en) * | 1964-08-27 | 1967-05-16 | Dow Chemical Co | Powderless etching bath and method for etching curved segments |
US3510351A (en) * | 1964-11-27 | 1970-05-05 | Paul Van Dillen | Method for etching and cleaning of objects and plants,particularly tube systems and boiler plants,consisting of iron or steel |
US3646946A (en) * | 1969-01-06 | 1972-03-07 | Olin Mathieson | Copper alloy cleaning process |
US3728155A (en) * | 1969-01-06 | 1973-04-17 | Olin Corp | Copper alloy cleaning process |
US3754969A (en) * | 1971-06-18 | 1973-08-28 | Dow Corning | Method of adhering room temperature vulcanizable silicone rubber to metal surfaces |
US3986970A (en) * | 1973-05-02 | 1976-10-19 | The Furukawa Electric Co., Ltd. | Solution for chemical dissolution treatment of tin or alloys thereof |
US4051057A (en) * | 1974-12-13 | 1977-09-27 | Harry Ericson | Solutions for cleaning surfaces of copper and its alloys |
US4014715A (en) * | 1975-12-08 | 1977-03-29 | General Electric Company | Solder cleaning and coating composition |
US4361445A (en) * | 1978-09-13 | 1982-11-30 | Olin Corporation | Copper alloy cleaning process |
FR2436193A1 (en) * | 1978-09-13 | 1980-04-11 | Olin Corp | PROCESS FOR CLEANING A COPPER-BASED ALLOY SURFACE HAVING A THERMALLY FORMED METAL OXIDE SURFACE LAYER |
US4479840A (en) * | 1979-05-11 | 1984-10-30 | Sunstar Giken Kabushiki | Two-part adhesive and bonding method employing same |
US4386992A (en) * | 1979-05-11 | 1983-06-07 | Sunstar Chemical Ind. Co., Ltd. | Two-part adhesive and bonding method employing same |
US4444601A (en) * | 1979-09-06 | 1984-04-24 | Richardson Chemical Company | Metal article passivated by a bath having an organic activator and a film-forming element |
US4298404A (en) * | 1979-09-06 | 1981-11-03 | Richardson Chemical Company | Chromium-free or low-chromium metal surface passivation |
US4333785A (en) * | 1980-05-15 | 1982-06-08 | The General Tire & Rubber Company | Adhesion of brass to rubber |
US4299640A (en) * | 1980-07-25 | 1981-11-10 | The General Tire & Rubber Company | Rubber-brass adhesion improved through treatment of the metal with amino carboxylic acid or salt thereof |
US4600443A (en) * | 1984-10-01 | 1986-07-15 | Kennecott Corporation | Process for removing surface oxides from a copper-base alloy |
FR2582676A1 (en) * | 1985-06-03 | 1986-12-05 | Nat Semiconductor Corp | METHOD FOR TINNING THE EXTERNAL CONNECTIONS OF AN ENCAPSULATED SEMICONDUCTOR DEVICE |
US4714517A (en) * | 1986-05-08 | 1987-12-22 | National Semiconductor Corporation | Copper cleaning and passivating for tape automated bonding |
US4713144A (en) * | 1986-08-01 | 1987-12-15 | Ardrox Inc. | Composition and method for stripping films from printed circuit boards |
US5468303A (en) * | 1994-02-25 | 1995-11-21 | Zt Corporation | Rust, corrosion, and scale remover |
WO2000026440A2 (en) * | 1998-11-03 | 2000-05-11 | Eilenburger Elektrolyse- Und Umwelttechnik Gmbh | Circular method for pickling copper and copper alloys |
WO2000026440A3 (en) * | 1998-11-03 | 2002-10-03 | Eilenburger Elektrolyse & Umwelttechnik Gmbh | Circular method for pickling copper and copper alloys |
US10377968B2 (en) | 2017-06-12 | 2019-08-13 | General Electric Company | Cleaning compositions and methods for removing oxides from superalloy substrates |
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