US2378002A - Electrolytic apparatus - Google Patents
Electrolytic apparatus Download PDFInfo
- Publication number
- US2378002A US2378002A US422900A US42290041A US2378002A US 2378002 A US2378002 A US 2378002A US 422900 A US422900 A US 422900A US 42290041 A US42290041 A US 42290041A US 2378002 A US2378002 A US 2378002A
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- strip
- electrolyte
- anode
- electropolishing
- stainless steel
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- 239000003792 electrolyte Substances 0.000 description 16
- 229910001220 stainless steel Inorganic materials 0.000 description 13
- 239000010935 stainless steel Substances 0.000 description 12
- 238000005498 polishing Methods 0.000 description 11
- 238000000034 method Methods 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 239000000956 alloy Substances 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 4
- 230000009471 action Effects 0.000 description 4
- 229910045601 alloy Inorganic materials 0.000 description 4
- 229920001971 elastomer Polymers 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- KMUONIBRACKNSN-UHFFFAOYSA-N potassium dichromate Chemical compound [K+].[K+].[O-][Cr](=O)(=O)O[Cr]([O-])(=O)=O KMUONIBRACKNSN-UHFFFAOYSA-N 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000002932 luster Substances 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 229910021653 sulphate ion Inorganic materials 0.000 description 3
- 229910001369 Brass Inorganic materials 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 229910002065 alloy metal Inorganic materials 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000010951 brass Substances 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- 239000011651 chromium Substances 0.000 description 2
- 238000005530 etching Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- GLDOVTGHNKAZLK-UHFFFAOYSA-N octadecan-1-ol Chemical compound CCCCCCCCCCCCCCCCCCO GLDOVTGHNKAZLK-UHFFFAOYSA-N 0.000 description 2
- 239000012047 saturated solution Substances 0.000 description 2
- 238000007493 shaping process Methods 0.000 description 2
- 238000000638 solvent extraction Methods 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- 239000001117 sulphuric acid Substances 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 229910000792 Monel Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- VSYMNDBTCKIDLT-UHFFFAOYSA-N [2-(carbamoyloxymethyl)-2-ethylbutyl] carbamate Chemical compound NC(=O)OCC(CC)(CC)COC(N)=O VSYMNDBTCKIDLT-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000010406 cathode material Substances 0.000 description 1
- 229960000541 cetyl alcohol Drugs 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 125000003438 dodecyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 150000002191 fatty alcohols Chemical class 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- GOQYKNQRPGWPLP-UHFFFAOYSA-N n-heptadecyl alcohol Natural products CCCCCCCCCCCCCCCCCO GOQYKNQRPGWPLP-UHFFFAOYSA-N 0.000 description 1
- BXWNKGSJHAJOGX-UHFFFAOYSA-N n-hexadecyl alcohol Natural products CCCCCCCCCCCCCCCCO BXWNKGSJHAJOGX-UHFFFAOYSA-N 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 125000000913 palmityl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 238000007517 polishing process Methods 0.000 description 1
- 239000008237 rinsing water Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003460 sulfonic acids Chemical class 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F7/00—Constructional parts, or assemblies thereof, of cells for electrolytic removal of material from objects; Servicing or operating
Definitions
- This invention relates to improvements in treating metal articles, and more particularly to apparatus for electropolishing fabricated structural members.
- the invention is especially adapted for finishing moulding strip material having an outer covering surface made of stainless steel or similar stainless alloy metal containing iron and chromium, or iron, chromium and nickel.
- Another object is to devise an improved .method and apparatus for manufacturing a composite sheet metal article having a surface member of light gauge or thickness which is highly polished electrolytically and presents an attractive appearance.
- Another object is to provide an improved method and apparatus for producing a bright finish or structural moulding strips electrochemically and without the use of mechanical polishing devices and wherein the article may be treated while it is maintained stationary and the electrolytic polishing means passed thereover.
- Figure 1 illustrates diagrammatically in cross section an apparatus for electropolishing a mould ing strip of material such as commonly used for ornamental purposes;
- Figure 2 is a fragmentary detail sectional view taken on the line 2-2 of Figure 1 and looking in the direction of the arrows;
- Figure 3 is a similar view as in Figure 2 illustrating the treatment of a differently shaped two-ply structural member
- Figure 4 is an enlarged fragmentary detail sectional view illustrating diagrammatically the electropolishing action
- Figure 5 is a View illustrating schematically a modified arrangement wherein the article being electropolished is maintained substantially stationary while the electropolishing device is moved thereover;
- Figure 6 is a fragmentary detail sectional view taken on the line 6li of Figure 5.
- the backing strip also provides a support for the paper-thin thickness stainless steel sheet used and permits shaping and workingof the structural member into the desired form without having to contend with warping, buckling, 0r kinking, such as would be encountered when shaping and polishing the I In Figure 1 a composite strip such as a mould-.
- Compartment I3 is a rubber or glass lined chamber in which the electrolyte is placed for treating the strip. As illustrated in Figure 1, the strip is guided into this compartment between the rolls 11, through the rubber dam l8 and into the electrolyte. The strip is anodically treated by being passed over the closely spaced anode contact rolls 20 which are arranged longitudinally along the path of the strip.
- Suitable heating means may be provided for maintaining the electrolyte at the optimum temperature for efiecting the electrolytic treatment.
- the temperature of the electrolyte is held at approximately degrees F.
- a cathode member 22 has an inner surface shape to correspond to the contour of the surface of the moulding to be polished and is placed as near to the work as possible in order to increase the efflciency of the polishing.
- the cathode comprises an elongated hollow rod which is provided with an opening 23 through which the strip material passes while in contact with the anode rolls 20.
- the cathode member is suitably supported on the axle shafts 25 of the anode rolls 2
- the anode roller supporting contact members 20 may be made of stainless steel or other suitable alloy metal which does not become passive in the electrolyte. Copper or brass may be utilized if de sired.
- the anode and cathode members are connected to a source of electric current and the proper current density maintained as required for treating the particular structural member which is to be electropolished.
- the proportions and concentrations of the electrolyte and the temperature of operation, as well as current densities, may vary over a relatively wide range according to the particular metal or alloy strip material being treated.
- a current density of 200 to 500 amperes per square foot may be used in the treatment of stainless steel.
- a voltage of six to twelve volts may be employed.
- the electrolytic bath may comprise a mixture of a saturated solution of potassium dichromate in strong sulphuric acid to which has been added from to 25 per cent by volume of sulphonated high molecular weight alcohol, such as lauryl, cetyl and stearyl alcohol.
- sulphonated high molecular weight alcohol such as lauryl, cetyl and stearyl alcohol.
- These sulfonic acid salts have the general formula CH3(CH:) sOSQsNa where n is ten or more.
- the electrolyte may consist of a concentrated aqueous solution of a sulphated fatty alcohol or as an alternativemay be employed as a separate treatment step, depending upon the particular article being processed.
- an electropolishing electrolyte for cold and hot rolled stainless steel sheet or strip of the 18-8 type use may be made of an aqueous solution of ferric sulphate and hydrofluoric acid.
- Ferric sulphate functions as an oxidizing agent controlling the action of the hydrofluoric to prevent etching of the surface resulting in a matte finish.
- concentration of ferric sulphate and hydrofluoric acid maybe varied to suit the conditions but generally a range between 5 to per cent parts ferric sulphate and 1 to 5 per cent parts of concentrated hydrofluoric acid in water are preferable.
- the strip material After the strip material has been anodically electropolished by subjecting it to the electrolytic treatment in compartment is, it is drawn through the rubber dam 28 in the partitioning wall 29 and advanced through the rinsing water 30 of the compartment l4. Suitable supporting rolls 32 are provided for supporting the strip while it passes through the rinse water. Thereafter the strip is conveyed outward through the rubber dam aperture u in the partitioning wall 35 and passes over a hot air drier blower means 38 suitably arranged in the compartment l5. Finally the strip is conveyed between the rolls 39 and cut to the desired length or otherwise stored for shipment.
- the electropolishing treatment is similar to electroplating except that the flow of current is in the reverse direction.
- the work piece II is made the anode and the cathode 22 is of such a shape and area that it can be placed relatively close to the surface of the work and a concentrated anodic treatment eilected so as to produce high luster finish 0n the work without pitting or discoloring the work.
- the time required for electropolishing the work varies with the condition of the anode surface, shape and degree of polish desired, as well as the current densities employed.
- the peaks or raised portions ll forming the rough surface of the work are dissolved and removed, as illustrated by the arrows in Figure 4, without undue etching or pitting of the surface.
- the final surface plane of the article after the electrolytic treatment would conform to the dotted line shown at H in Figure 4. In this way, a high anodic luster" is produced.
- FIG 3 there is illustrated a differently shaped composite structural strip 45 wherein the cathode member I! is shaped to provide an inner contour surface II which coincides with the shape of the strip 45.
- in this instance are of a width to properly support the strip 45 and a sufficient number of these anode contact rolls are provided to give the required anode area in order to efi'ect efficient electrolytic polishing of the surface of the stainless steel.
- FIG. 5 and 6 a modification is shown wherein a movable anodic electropolishing unit, generally designated I2, is provided.
- I2 a movable anodic electropolishing unit
- the article is placed in the electrolyte as in a tank or suitable compartment it and the anode electrode treating unit I! moved over the strip so as to electrolytically polish the surface as desired;
- the unit 52 comprises an anode contact roller 60 mounted on the axle member 62 which is fixed to the insulated supporting member 64.
- likewise supports the cathode member 65 which is .iuxtapositioned relative to the anode roller 5. and comprises a surface contour 66 which corresponds with the surface 68 of the structural material which is to be polished.
- the anode electrode unit 52 is moved along over the strip being treated while maintaining the anode contact roller 60 against the side of the strip which is not to be polished, or backing member in the case of a two-ply structural article, and the surface anodically treated to produce a bright surface.
- Suitable means may be provided for automatically advancing the electrolytic treating unit over the article to be polished and the bath may be heated by conventional means so as to maintain the same at a temperature of about to 250 degrees F.
- This modification is adapted for producing a high polish on strips or the like articles of complicated shapes.
- this invention is adapted for treating structural members having a stainless steel surface covering which has been previously treated to remove scale and other foreign substances
- our method may be used in treating articles which have not been pretreated, since the electrolytic polishing action simultaneously removes particles of scale and similar surface contamination.
- the scale is of such a thickness that it cannot be removed during the electropolishing treatment, it is more economical to remove this by the usual acid pickling treatment prior toelectropolishing.
- this invention is also adapted for use as a supplement to mechanical polishing, bufling and burnishing when desired. Further, this improved method of polishing may be utilized in treating stainless steel wire, band, sheet and spun shapes, or castings and the like, as well as multl-ply structural strip material, as illustrated in the drawing. Also various types of metals and alloys may be electropolished by our method and apparatus. Other metals than stainless steel, such as copper, brass, nickel, Monel, cobalt, zinc, tin, lead, aluminum, iron and their alloy may be electropolished by utilizing the method and apparatus of this invention.
- An apparatus of the class described having a compartment containing an electrolyte, means for conducting and guiding a preformed structural member through said electrolyte and for making anodic contact, said guiding and contacting means comprising a plurality of rolls having axle shafts in said compartment arranged to support the preformed structural member as it passes through said compartment, a cathode member of elongated form shaped to surround said structural member and supported upon said axle shafts, and insulating means comprising a spacer block between said cathode member and said axle shafts.
- An apparatus or the class described having a compartment containing an electrolyte, means for conducting and guiding a preformed structural member through said electrolyte and for making anodic contact, said guiding and contacting means comprising a plurality of rolls having axle shafts in said compartment arranged to support the preformed structural member as it passes through said compartment, a cathode member of elongated form having an inner surface shaped to correspond to the contour of the surface of said structural member, said cathode member supported upon said axle shafts and formed to partially surround said structural member and the upper portions of said anode rolls, and insulating material between the cathode member and said axle shafts.
- a tank containing an electrolyte containing an electrolyte
- a plurality of rollers in said tank for carryin said structural members for carryin said structural members
- insulating supportingmembers carried by said axle shafts insulating supportingmembers carried by said axle shafts
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
Description
June 1945- F. E. DRUMMOND ET AL 2,373,002
ELECTROLYTIC APPARATUS Original Filed Dec. 20, 1940 64 Jmu nvfflm FaLsoM EDnvmmuo,
Dawn f-BENCH,
Patented June 12, 1945 ELECTROLYTIC APPARATUS Folsom E. Drummond, Metuchen, N. J., and David E. Bench, Dayton, Ohio, asslgnors to The Himmel Brothers Company, Hamden, Conn., a corporation of Connecticut Original application December 20, 1940, Serial No.
370,971. Divided and this application December 13. 1941. Serial No. 422.900
3 Claims.
This invention relates to improvements in treating metal articles, and more particularly to apparatus for electropolishing fabricated structural members. The invention is especially adapted for finishing moulding strip material having an outer covering surface made of stainless steel or similar stainless alloy metal containing iron and chromium, or iron, chromium and nickel.
This application is a division of our copending application, Serial No. 370,971, filed December 20, 1940, which is directed particularly to the method hereinafter described. This application deals particularly with the apparatus herein described and illustrated.
It is the principal object of this invention to provide an improved method and apparatus for polishing metal electrolytically so as to produce an article having a high polish or luster without the use of mechanical polishing devices such as has been the common practice heretofore.
Another object is to devise an improved .method and apparatus for manufacturing a composite sheet metal article having a surface member of light gauge or thickness which is highly polished electrolytically and presents an attractive appearance.
Another object is to provide an improved method and apparatus for producing a bright finish or structural moulding strips electrochemically and without the use of mechanical polishing devices and wherein the article may be treated while it is maintained stationary and the electrolytic polishing means passed thereover.
These and other objects and advantages will be apparent from the following description taken in connection with the drawing.
Figure 1 illustrates diagrammatically in cross section an apparatus for electropolishing a mould ing strip of material such as commonly used for ornamental purposes;
Figure 2 is a fragmentary detail sectional view taken on the line 2-2 of Figure 1 and looking in the direction of the arrows;
Figure 3 is a similar view as in Figure 2 illustrating the treatment of a differently shaped two-ply structural member;
Figure 4 is an enlarged fragmentary detail sectional view illustrating diagrammatically the electropolishing action;
Figure 5 is a View illustrating schematically a modified arrangement wherein the article being electropolished is maintained substantially stationary while the electropolishing device is moved thereover;
Figure 6 is a fragmentary detail sectional view taken on the line 6li of Figure 5.
In general, it has been found difiicult to polish stainless steel strip and similar alloy steels inasmuch as the stainless alloy material has a very low heat conductivity so that high temperatures are developed during the polishing operation which are not dissipated rapidly causing discoloration and buckling of the stainless steel strip. This diliiculty has been overcome by providing the stainless steel strip with a backing member of relatively high heat conductivity whereby the heat developed during polishing is conducted away fast enough to prevent overheating the metal strip. The backing strip also provides a support for the paper-thin thickness stainless steel sheet used and permits shaping and workingof the structural member into the desired form without having to contend with warping, buckling, 0r kinking, such as would be encountered when shaping and polishing the I In Figure 1 a composite strip such as a mould-.
ing, designated 10, and preformed having a stainless steel shell H is advanced through the electropolishing unit l2. This unit preferably com -v prises three compartments l3, l4 and 15 arranged for electropolishing, rinsing and drying of the strip. Compartment I3 is a rubber or glass lined chamber in which the electrolyte is placed for treating the strip. As illustrated in Figure 1, the strip is guided into this compartment between the rolls 11, through the rubber dam l8 and into the electrolyte. The strip is anodically treated by being passed over the closely spaced anode contact rolls 20 which are arranged longitudinally along the path of the strip.
Suitable heating means may be provided for maintaining the electrolyte at the optimum temperature for efiecting the electrolytic treatment. In general, the temperature of the electrolyte is held at approximately degrees F. A cathode member 22 has an inner surface shape to correspond to the contour of the surface of the moulding to be polished and is placed as near to the work as possible in order to increase the efflciency of the polishing. As illustrated, the cathode comprises an elongated hollow rod which is provided with an opening 23 through which the strip material passes while in contact with the anode rolls 20. The cathode member is suitably supported on the axle shafts 25 of the anode rolls 2| and is insulated therefrom by means of the spacer block means 21. Either copper or lead may be used as the cathode material. The anode roller supporting contact members 20 may be made of stainless steel or other suitable alloy metal which does not become passive in the electrolyte. Copper or brass may be utilized if de sired.
The anode and cathode members are connected to a source of electric current and the proper current density maintained as required for treating the particular structural member which is to be electropolished. The proportions and concentrations of the electrolyte and the temperature of operation, as well as current densities, may vary over a relatively wide range according to the particular metal or alloy strip material being treated. A current density of 200 to 500 amperes per square foot may be used in the treatment of stainless steel. A voltage of six to twelve volts may be employed.
The electrolytic bath may comprise a mixture of a saturated solution of potassium dichromate in strong sulphuric acid to which has been added from to 25 per cent by volume of sulphonated high molecular weight alcohol, such as lauryl, cetyl and stearyl alcohol. These sulfonic acid salts have the general formula CH3(CH:) sOSQsNa where n is ten or more. In some instances the electrolyte may consist of a concentrated aqueous solution of a sulphated fatty alcohol or as an alternativemay be employed as a separate treatment step, depending upon the particular article being processed.
Another example of electrolyte which may be used comprises a saturated solution of potassium dichromate in sulphuric acid containing 50% by volume of phosphoric acid.
Further, as an electropolishing electrolyte for cold and hot rolled stainless steel sheet or strip of the 18-8 type use may be made of an aqueous solution of ferric sulphate and hydrofluoric acid. Ferric sulphate functions as an oxidizing agent controlling the action of the hydrofluoric to prevent etching of the surface resulting in a matte finish. The concentration of ferric sulphate and hydrofluoric acid maybe varied to suit the conditions but generally a range between 5 to per cent parts ferric sulphate and 1 to 5 per cent parts of concentrated hydrofluoric acid in water are preferable.
After the strip material has been anodically electropolished by subjecting it to the electrolytic treatment in compartment is, it is drawn through the rubber dam 28 in the partitioning wall 29 and advanced through the rinsing water 30 of the compartment l4. Suitable supporting rolls 32 are provided for supporting the strip while it passes through the rinse water. Thereafter the strip is conveyed outward through the rubber dam aperture u in the partitioning wall 35 and passes over a hot air drier blower means 38 suitably arranged in the compartment l5. Finally the strip is conveyed between the rolls 39 and cut to the desired length or otherwise stored for shipment.
The electropolishing treatment, as diagrammatically illustrated in Figure 4, is similar to electroplating except that the flow of current is in the reverse direction. As shown, the work piece II is made the anode and the cathode 22 is of such a shape and area that it can be placed relatively close to the surface of the work and a concentrated anodic treatment eilected so as to produce high luster finish 0n the work without pitting or discoloring the work. The time required for electropolishing the work varies with the condition of the anode surface, shape and degree of polish desired, as well as the current densities employed.
During the concentrated electrolytic action on the surface of the strip being treated the peaks or raised portions ll forming the rough surface of the work are dissolved and removed, as illustrated by the arrows in Figure 4, without undue etching or pitting of the surface. For example, the final surface plane of the article after the electrolytic treatment would conform to the dotted line shown at H in Figure 4. In this way, a high anodic luster" is produced.
In Figure 3 there is illustrated a differently shaped composite structural strip 45 wherein the cathode member I! is shaped to provide an inner contour surface II which coincides with the shape of the strip 45. The anode contact roll members 5| in this instance are of a width to properly support the strip 45 and a sufficient number of these anode contact rolls are provided to give the required anode area in order to efi'ect efficient electrolytic polishing of the surface of the stainless steel.
In Figures 5 and 6 a modification is shown wherein a movable anodic electropolishing unit, generally designated I2, is provided. In this instance, where it is desired to maintain a preshaped strip or structural article It stationary while electropolishing the same, the article is placed in the electrolyte as in a tank or suitable compartment it and the anode electrode treating unit I! moved over the strip so as to electrolytically polish the surface as desired;
The unit 52 comprises an anode contact roller 60 mounted on the axle member 62 which is fixed to the insulated supporting member 64. The member 6| likewise supports the cathode member 65 which is .iuxtapositioned relative to the anode roller 5. and comprises a surface contour 66 which corresponds with the surface 68 of the structural material which is to be polished. In this method the anode electrode unit 52 is moved along over the strip being treated while maintaining the anode contact roller 60 against the side of the strip which is not to be polished, or backing member in the case of a two-ply structural article, and the surface anodically treated to produce a bright surface. Suitable means may be provided for automatically advancing the electrolytic treating unit over the article to be polished and the bath may be heated by conventional means so as to maintain the same at a temperature of about to 250 degrees F. This modification is adapted for producing a high polish on strips or the like articles of complicated shapes.
Although this invention is adapted for treating structural members having a stainless steel surface covering which has been previously treated to remove scale and other foreign substances, our method may be used in treating articles which have not been pretreated, since the electrolytic polishing action simultaneously removes particles of scale and similar surface contamination. However, when the scale is of such a thickness that it cannot be removed during the electropolishing treatment, it is more economical to remove this by the usual acid pickling treatment prior toelectropolishing.
It will be understood that this invention is also adapted for use as a supplement to mechanical polishing, bufling and burnishing when desired. Further, this improved method of polishing may be utilized in treating stainless steel wire, band, sheet and spun shapes, or castings and the like, as well as multl-ply structural strip material, as illustrated in the drawing. Also various types of metals and alloys may be electropolished by our method and apparatus. Other metals than stainless steel, such as copper, brass, nickel, Monel, cobalt, zinc, tin, lead, aluminum, iron and their alloy may be electropolished by utilizing the method and apparatus of this invention.
It will be understood further that this invention is not limited to the particular electrolyte and apparatus illustrated in the drawing and that various modifications can be made by those skilled in the art without departing from the spirit and scope of this invention.
We claim:
1. An apparatus of the class described having a compartment containing an electrolyte, means for conducting and guiding a preformed structural member through said electrolyte and for making anodic contact, said guiding and contacting means comprising a plurality of rolls having axle shafts in said compartment arranged to support the preformed structural member as it passes through said compartment, a cathode member of elongated form shaped to surround said structural member and supported upon said axle shafts, and insulating means comprising a spacer block between said cathode member and said axle shafts.
2. An apparatus or the class described having a compartment containing an electrolyte, means for conducting and guiding a preformed structural member through said electrolyte and for making anodic contact, said guiding and contacting means comprising a plurality of rolls having axle shafts in said compartment arranged to support the preformed structural member as it passes through said compartment, a cathode member of elongated form having an inner surface shaped to correspond to the contour of the surface of said structural member, said cathode member supported upon said axle shafts and formed to partially surround said structural member and the upper portions of said anode rolls, and insulating material between the cathode member and said axle shafts.
3. In an apparatus for electropolishing preformed structural members: a tank containing an electrolyte; a plurality of rollers in said tank for carryin said structural members; anodically connected axle shafts carrying said rollers and being in electric conductive connection with said rollers; insulating supportingmembers carried by said axle shafts; cathode means supported and spaced from said anodic rollers by said insulating members, said cathode member being of elongated Shape n ving an inner surface shaped to correspond with the contour of said structural members.
FOLSOM E. DRUMMOND. DAVID E. BENCH.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US422900A US2378002A (en) | 1940-12-20 | 1941-12-13 | Electrolytic apparatus |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US37097140A | 1940-12-20 | 1940-12-20 | |
| US422900A US2378002A (en) | 1940-12-20 | 1941-12-13 | Electrolytic apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2378002A true US2378002A (en) | 1945-06-12 |
Family
ID=27005179
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US422900A Expired - Lifetime US2378002A (en) | 1940-12-20 | 1941-12-13 | Electrolytic apparatus |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2378002A (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2454935A (en) * | 1945-06-27 | 1948-11-30 | Meaker Company | Continuous wire and strip electroprocessing machine |
| US2506582A (en) * | 1945-06-20 | 1950-05-09 | Mateosian Edward Der | Electrolytic polishing of metals |
| US2516105A (en) * | 1945-06-20 | 1950-07-25 | Mateosian Edward Der | Electrolytic polishing of metals |
| US2522071A (en) * | 1943-04-06 | 1950-09-12 | Tait William Henry | Valve structure for passage of strip material through the wall of liquid treatment baths |
| US2539455A (en) * | 1944-01-27 | 1951-01-30 | Mazia Joseph | Electrolytic polishing of metals |
| US2686859A (en) * | 1950-10-11 | 1954-08-17 | Western Electric Co | Electroplating |
| US2725355A (en) * | 1950-07-21 | 1955-11-29 | Western Electric Co | Apparatus for electropolishing metallic articles |
| US2725352A (en) * | 1950-07-21 | 1955-11-29 | Western Electric Co | Methods of and apparatus for dissolving surface projections, electropolishing and passivating metallic tapes |
| US2725353A (en) * | 1950-07-21 | 1955-11-29 | Western Electric Co | Electropolishing metallic articles |
| US2751344A (en) * | 1949-06-21 | 1956-06-19 | Charles A Kienberger | Electropolisher |
| US3974056A (en) * | 1975-05-23 | 1976-08-10 | Ann Arbor Circuits, Inc. | Electroplating selected portions of a strip |
| US4421623A (en) * | 1981-11-26 | 1983-12-20 | Dr. C. Otto & Comp. G.M.B.H. | Apparatus for guiding material in strip form |
| US20080289970A1 (en) * | 2006-09-25 | 2008-11-27 | Poligrat Gmbh | Electropolishing process for cobalt and cobalt alloys |
-
1941
- 1941-12-13 US US422900A patent/US2378002A/en not_active Expired - Lifetime
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2522071A (en) * | 1943-04-06 | 1950-09-12 | Tait William Henry | Valve structure for passage of strip material through the wall of liquid treatment baths |
| US2539455A (en) * | 1944-01-27 | 1951-01-30 | Mazia Joseph | Electrolytic polishing of metals |
| US2506582A (en) * | 1945-06-20 | 1950-05-09 | Mateosian Edward Der | Electrolytic polishing of metals |
| US2516105A (en) * | 1945-06-20 | 1950-07-25 | Mateosian Edward Der | Electrolytic polishing of metals |
| US2454935A (en) * | 1945-06-27 | 1948-11-30 | Meaker Company | Continuous wire and strip electroprocessing machine |
| US2751344A (en) * | 1949-06-21 | 1956-06-19 | Charles A Kienberger | Electropolisher |
| US2725355A (en) * | 1950-07-21 | 1955-11-29 | Western Electric Co | Apparatus for electropolishing metallic articles |
| US2725352A (en) * | 1950-07-21 | 1955-11-29 | Western Electric Co | Methods of and apparatus for dissolving surface projections, electropolishing and passivating metallic tapes |
| US2725353A (en) * | 1950-07-21 | 1955-11-29 | Western Electric Co | Electropolishing metallic articles |
| US2686859A (en) * | 1950-10-11 | 1954-08-17 | Western Electric Co | Electroplating |
| US3974056A (en) * | 1975-05-23 | 1976-08-10 | Ann Arbor Circuits, Inc. | Electroplating selected portions of a strip |
| US4421623A (en) * | 1981-11-26 | 1983-12-20 | Dr. C. Otto & Comp. G.M.B.H. | Apparatus for guiding material in strip form |
| US20080289970A1 (en) * | 2006-09-25 | 2008-11-27 | Poligrat Gmbh | Electropolishing process for cobalt and cobalt alloys |
| US8080148B2 (en) * | 2006-09-25 | 2011-12-20 | Poligrat Gmbh | Electropolishing process for cobalt and cobalt alloys |
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