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US1488553A - Process of coating sheet steel with aluminum - Google Patents

Process of coating sheet steel with aluminum Download PDF

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Publication number
US1488553A
US1488553A US614965A US61496523A US1488553A US 1488553 A US1488553 A US 1488553A US 614965 A US614965 A US 614965A US 61496523 A US61496523 A US 61496523A US 1488553 A US1488553 A US 1488553A
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Prior art keywords
aluminum
bath
sheets
rollers
coating
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US614965A
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Peacock Samuel
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WILLIS G WALDO
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WILLIS G WALDO
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/66Electroplating: Baths therefor from melts

Definitions

  • This invention relates to a process of coating sheet steel with aluminum, and has for its object to provide a procedure which will be more efiicient in action and less costly in practice than those which have been heretofore proposed.
  • the invention consists in the novel steps and combinations of steps constituting the process, all as will be more fully hereinafter disclosed and particularly pointed outin the claims.
  • Figure 1 is a diagrammatic plan View ,of an apparatus suitable for carrying out this invention
  • Figure 2 is a sectional view of the parts shown in Figure 1;
  • Figure 3 is an enlarged sectional detailed view of a pair of rollers between which the sheets to be coated pass.
  • concentration of the aluminum in the bath is maintained in any wellknown and suitable manner as by the addition of the solid alkali metal fluoride in such a way as to keep the bath saturated and in substantially the same manner as commonly employed in commercial practice in recovering the metal itself.
  • a carbon cathode I employ a cathode of sheet steel.
  • the bath is maintained at somewhat below the usual temperature of 900 C. but above the temperature of 7 00 C., by making the bath consist of a mixture of sodium and potassium aluminum fluorides in suitable pro portions. But nevertheless, the working temperature of the bath is still well above the melting point of aluminum.
  • the properties of the molten bath alone seem to be sufiicient to maintain an even coating of aluminum on the sheet steel even when vertical cathodes are used,but it is found thatwhen rather thick,
  • rollers such as 2 and 3 submerged in the molten alkali metal-aluminum fluoride bath 4, and some times it is found desirable to pass them through such a bath one or more times; That is, I prefer to provide a suitable container 5 in which is mounted a plurality of rollers 2 and 3, as illustrated, and which accommodates the molten bath 4 by any suitable means, as for example acurved inclined bottom 6.
  • the upper rollers 2 are preferably provided with a plurality of conductors 7 and suitably insulated from the rollers 2, and the axes'8 of which are all joined to the negative lead 9 of the circuit.
  • the positive lead-l0 ot' the circuit is conveniently joined to a.
  • pair of carbon anodes dipping is provided with an extension or stand pipe 15 in which is placed an additional set of rollers 2 and 3 as shown, and these rollers are submerged in some suitable molten cooling liquid 16, such for example as a mix-- ture of sodium and potassium nitrates or other low melting point bath which will not injuriously act upon the coated sheets 1.
  • suitable molten cooling liquid 16 such for example as a mix-- ture of sodium and potassium nitrates or other low melting point bath which will not injuriously act upon the coated sheets 1.
  • Each set of rollers 2 and 3 are so disposed that they form a continuous curved path for the sheets 1, as plainly shown in Figure 2, and they are so spaced apart that the positively driven lower rollers 3 will feed the sheets successively from one pair of rollers to the next, so that the said sheets never get out of control of the said rollers 2 and 3 until they emerge at the point 17 from the top of the stand pipe 15.
  • the sheets 1 are preferably fed by hand or in any other suitable manner between the first pair of rollers 2 and 3, whereupon the positively driven rollers 3 soon force the sheets forward to the next pair, and thus are the sheets propelled underneath the surface of the molten bath 4 and out through the stand pipe 15 at the point 17.
  • current being fed into the bath through the anodes 11 aluminum is deposited on the surfaces of the sheets 1 as they pass through the bath and especially on the under surfaces of said sheets.
  • the current having reached the said sheets 1 it passes along and through said sheets to the conductor 7 with which each of the rollers 2 are provided, and out of theaxes 8 of said rollers 2 through the' lead- 9 and back 7 to the source of supply, all as will be clear from Figures 1 and 3.
  • any defects that inay be found in the coating after passing through the first two or three pairs of rollers are mechanically pressed down and spread out over the'sur: face of the sheet by the succeeding rollers so that before the sheet has emerged from the bath the mechanical smoothing and compressing of the coating has made it so uniform that the last rollers find a smooth and coherent surface for deposition, and they therefore give the sheet a pleasing and finished appearance.

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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)
  • Coating With Molten Metal (AREA)

Description

April 1, 1924.
S. PEACOCK PROCESS OF COATING SHEET STEEL WITH ALUMINUM Filed Jan. 26. 1923 Jana/ml Peacock Invantaz' Attorney Patented; Apr. 1 1924.
UNITED STATES PATENT! OFFICE. Y
SAMUEL PEA-COCK, OF WHEELING, WEST VIRGINIA, ASSIGNOR T0 WILLIS G. WALD O,
OF WASHINGTON, DISTRICT OF COLUMBIA.
PROCESS OF COATING SHEET STEEL WITH ALUMINUM.
Application filed January 26, 1923. Serial No. 614,965.
To all whom it may concern:
Be it known that I, SAMUEL PEAcooK, a
citizen of the United States, residing at \(Vheeling, in the county of Ohio and State of lVest Vir inia, have invented certain new and useful mprovements in Processes of Coating Sheet Steel with Aluminum; and I do hereby declare the following to be a full, clear, and exact description of the invention, such as will enable others skilled in the art to which it appertains to make vand use the same.
This invention relates to a process of coating sheet steel with aluminum, and has for its object to provide a procedure which will be more efiicient in action and less costly in practice than those which have been heretofore proposed.
With these and other objects in view, the invention consists in the novel steps and combinations of steps constituting the process, all as will be more fully hereinafter disclosed and particularly pointed outin the claims.
Referring to the accompanying drawings forming a part of this specification, in which like numerals designate like parts in all the views:
Figure 1 is a diagrammatic plan View ,of an apparatus suitable for carrying out this invention;
Figure 2 is a sectional view of the parts shown in Figure 1; and
Figure 3 is an enlarged sectional detailed view of a pair of rollers between which the sheets to be coated pass.
In order to more clearly explain the invention, it issaid: Light age sheet steel for automobile bodies and ot er purposes when coated with aluminum possesses through the medium of the steel core, the strength'of steel, while the surface is protected from excessive corrosion by the aluminum coating, and therefore it has a much longer life in use than would otherwise be the case. But as is also well known, it is exceedingly difficult and expensive to electrolytically deposit aluminum from aqueous solutions on sheet steel and at the same time get asatisfactory, smooth reguline deposit.
of an alkali metal aluminum fluoride. The
concentration of the aluminum in the bath is maintained in any wellknown and suitable manner as by the addition of the solid alkali metal fluoride in such a way as to keep the bath saturated and in substantially the same manner as commonly employed in commercial practice in recovering the metal itself. Instead of a carbon cathode I employ a cathode of sheet steel. Further, the bath is maintained at somewhat below the usual temperature of 900 C. but above the temperature of 7 00 C., by making the bath consist of a mixture of sodium and potassium aluminum fluorides in suitable pro portions. But nevertheless, the working temperature of the bath is still well above the melting point of aluminum. For very thin coatings, which have little or no industrial application, the properties of the molten bath alone seem to be sufiicient to maintain an even coating of aluminum on the sheet steel even when vertical cathodes are used,but it is found thatwhen rather thick,
found necessary to pass the sheet steel cathode sheets 1 between rollers such as 2 and 3 submerged in the molten alkali metal-aluminum fluoride bath 4, and some times it is found desirable to pass them through such a bath one or more times; That is, I prefer to provide a suitable container 5 in which is mounted a plurality of rollers 2 and 3, as illustrated, and which accommodates the molten bath 4 by any suitable means, as for example acurved inclined bottom 6. The upper rollers 2 are preferably provided with a plurality of conductors 7 and suitably insulated from the rollers 2, and the axes'8 of which are all joined to the negative lead 9 of the circuit. The positive lead-l0 ot' the circuit is conveniently joined to a. pair of carbon anodes dipping is provided with an extension or stand pipe 15 in which is placed an additional set of rollers 2 and 3 as shown, and these rollers are submerged in some suitable molten cooling liquid 16, such for example as a mix-- ture of sodium and potassium nitrates or other low melting point bath which will not injuriously act upon the coated sheets 1. Each set of rollers 2 and 3 are so disposed that they form a continuous curved path for the sheets 1, as plainly shown in Figure 2, and they are so spaced apart that the positively driven lower rollers 3 will feed the sheets successively from one pair of rollers to the next, so that the said sheets never get out of control of the said rollers 2 and 3 until they emerge at the point 17 from the top of the stand pipe 15.
The operation of this apparatus will be clear from the foregoing, but may bebriefly summarized as follows:
The sheets 1 are preferably fed by hand or in any other suitable manner between the first pair of rollers 2 and 3, whereupon the positively driven rollers 3 soon force the sheets forward to the next pair, and thus are the sheets propelled underneath the surface of the molten bath 4 and out through the stand pipe 15 at the point 17. In the meantime, current being fed into the bath through the anodes 11, aluminum is deposited on the surfaces of the sheets 1 as they pass through the bath and especially on the under surfaces of said sheets. The current having reached the said sheets 1 it passes along and through said sheets to the conductor 7 with which each of the rollers 2 are provided, and out of theaxes 8 of said rollers 2 through the' lead- 9 and back 7 to the source of supply, all as will be clear from Figures 1 and 3. As the conductors 7 and the surfaces of the rollers 2 and 5, themselves are aptto somewhat mar the coating on the sheets when especially thick and coherent coatings are desired, I find it convenient to take the sheets 1 after they have. emerged from the point 17 'of the stand pipe 15 and turn them upside down,
-v whereupon the coatingis found to be very satisfactory. It is very probable that the mechanical action of the spring pressed rollers 2 con'lpressing the sheets onto the rollers 3 serves to compact the coating and to render it more smooth andeven than would otherwise be the case. Especially is this found to be the fact when a compare-- tively large number of rollers 2 and 3 are provided, as is the case here. That is to say, any defects that inay be found in the coating after passing through the first two or three pairs of rollers are mechanically pressed down and spread out over the'sur: face of the sheet by the succeeding rollers so that before the sheet has emerged from the bath the mechanical smoothing and compressing of the coating has made it so uniform that the last rollers find a smooth and coherent surface for deposition, and they therefore give the sheet a pleasing and finished appearance.
It is obvious that those skilled in the art may vary the details of the process without departing from the spirt thereof, and therefore it is not desired to be limited to the above disclosure except as may be required by the claims. What-is claimed is:
1. The process of coating sheet steel with aluminum which consists in providing a molten bath consisting of a mixture of sodium and potassium aluminum fluorides at a temperature above 700 0.; passing said sheet steel beneath the surface of said bath while passing a current from said bath to said sheet steel and compacting the coating produced in the bath; and gradually cooling said coating out of contact with the atmosphere.
2. The process of coating steel sheets with aluminum which consists in passing said sheets through a molten'bath contai'nlng an alkali metal-aluminum fluoride; plating out the aluminum from said bath onto said sheets; compacting the coating during the plating action; and passing said sheets through a cooling bath out of contact with the atmosphere.v
3. The process of'co'ating steel sheets with aluminum which consists in passing said sheet-s beneath the surface of a molten-bath containing an aluminunr fluoride admixed with an alkali-metal fluoride; passing a current of electricity into said bath with said sheets forming cathodes, While compactin the coatings thus produced; and cooling sai sheets out of contact with the atmosphere.
4.- The process of coating a steel sheet with aluminum which consists in passing said sheet through a molten bath of alkali metalaluminum fluoride at "a temperatuieabove themelting point of aluminum; passin an electric current to said sheet as a cathode to coat the same with aluminum; compacting the coating thus formed at a plurality of pointsin the-path of travel of said sheet;
and eooling the coated sheet.
ture above the melting point of aluminum, out said aluminum onto said sheet; and said bath containing aluminum in chemical mechanically compressing the coating thus combination and being of suchacomposition obtained at a plurality of points in the 10 that metallic aluminum may be readily path of travel of said sheet.
5 plated out of the same; making said sheet In testimony whereof I affix my signature.
serve as a cathode in said bath; passing an electric current through said bath to plate SAMUEL PEACOCK.
US614965A 1923-01-26 1923-01-26 Process of coating sheet steel with aluminum Expired - Lifetime US1488553A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2709154A (en) * 1948-04-05 1955-05-24 Josephine Maria Hansgirg Corrosion resisting coatings
US2762764A (en) * 1955-01-11 1956-09-11 United States Steel Corp Method of electroplating aluminum and electrolyte therefor
US3007854A (en) * 1957-06-14 1961-11-07 Nat Steel Corp Method of electrodepositing aluminum on a metal base
US3154085A (en) * 1960-09-02 1964-10-27 Continental Can Co Sheet or coil cooling tank
US3226315A (en) * 1960-06-09 1965-12-28 Nat Steel Corp Continuous electroplating apparatus
US3226111A (en) * 1964-02-26 1965-12-28 Klondex Inc Machine for passing sheet material through a liquid
US3267008A (en) * 1962-10-04 1966-08-16 Nat Steel Corp Method of recovering aluminum halide from metal strip electrodeposited with an aluminum-containing coating from a fused salt bath
US3468782A (en) * 1965-02-05 1969-09-23 Luigi Bovone Machine for having glass plates electrochemically copper plated by means of soluble electrodes,in the making of mirrors
FR2004968A1 (en) * 1968-03-28 1969-12-05 Yawata Iron & Steel Co
US3570504A (en) * 1968-10-01 1971-03-16 Buckbee Mears Co Washing and drying apparatus

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2709154A (en) * 1948-04-05 1955-05-24 Josephine Maria Hansgirg Corrosion resisting coatings
US2762764A (en) * 1955-01-11 1956-09-11 United States Steel Corp Method of electroplating aluminum and electrolyte therefor
US3007854A (en) * 1957-06-14 1961-11-07 Nat Steel Corp Method of electrodepositing aluminum on a metal base
US3226315A (en) * 1960-06-09 1965-12-28 Nat Steel Corp Continuous electroplating apparatus
US3154085A (en) * 1960-09-02 1964-10-27 Continental Can Co Sheet or coil cooling tank
US3267008A (en) * 1962-10-04 1966-08-16 Nat Steel Corp Method of recovering aluminum halide from metal strip electrodeposited with an aluminum-containing coating from a fused salt bath
US3226111A (en) * 1964-02-26 1965-12-28 Klondex Inc Machine for passing sheet material through a liquid
US3468782A (en) * 1965-02-05 1969-09-23 Luigi Bovone Machine for having glass plates electrochemically copper plated by means of soluble electrodes,in the making of mirrors
FR2004968A1 (en) * 1968-03-28 1969-12-05 Yawata Iron & Steel Co
US3570504A (en) * 1968-10-01 1971-03-16 Buckbee Mears Co Washing and drying apparatus

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