|Publication number||US3620934 A|
|Publication date||Nov 16, 1971|
|Filing date||Jul 19, 1967|
|Priority date||Aug 8, 1966|
|Also published as||DE1621046A1, DE1621046B2|
|Publication number||US 3620934 A, US 3620934A, US-A-3620934, US3620934 A, US3620934A|
|Original Assignee||Fer Blanc Sarl Centre Rech Du|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (12), Referenced by (40), Classifications (25)|
|External Links: USPTO, USPTO Assignment, Espacenet|
United States Patent  Inventor Joseph Endle Thionville, France  Appl. No. 654,433  Filed July 19, 1967  Patented Nov. 16, 1971  Assignee Societe A Responsahilite Limitee Centre de Recherches du Fer Blane Thionville, France  Priority Aug. 8, 1966 [3 3] France [31 72,432
 METHOD OF ELECTROLYTIC TINNING SHEET STEEL 12 Claims, 1 Drawing Fig.
 US. Cl 204/34, 204/37 T, 204/54  Int. Cl C23b1/00  Field of Search t 204/34, 37.5, 40, 54
[5 6] References Cited UNITED STATES PATENTS 2,266,330 12/1941 Nachtman 204/37.5
2,407,579 9/1946 Schweikher 204/54 3,260,580 7/1966 Kamm or al. 204/37 3,445,351 5/1969 Swalheim 204/37 1,417.896 5/1922 Fletcher 204/34 1.898,765 211933 Dunn 204/34 1,972,835 9/1934 Tainton 204/34 1,979,996 1 1/1934 Phillips et al. 204/34 2,3 63,973 1 1/1944 Kenedy et a1 204/34 2,381 ,778 8/1945 Schoonmaker ct al. 204/37 2,673,836 3/1954 Vonada 204/28 2,915,444 l2/l959 Meyer 204/l45 Primary ExaminerT. Tung Assistant Examiner-Williarn Solomon AttorneyMason, Fenwick & Lawrence ABSTRACT: A method of electrolytic tinning sheet steel in which a sheet of steel is subjected to degreasing in an alkaline bath, pickling in an acid bath in which the sheet steel is polarized as the cathode, preliminary coating with metal, tinmng in an acid bath and treating to obtain the fusion and cooling of the tin deposited on the sheet. The method makes it possible to produce tinplate that has a layer of FeSn, which is continuous by virtue of very dense seeding and which thus has improved corrosion resistance.
METHOD OF ELECTROLYTIC TINNING SHEET STEEL The present invention relates to a method of electrolytically tin-plating sheet steel, whereby tin-plated sheet steel of improved corrosion resistance can be produced.
One proposed method of electrolytically tin plating comprises the steps of electrolytically degreasing the sheet steel in an alkaline bath; rinsing the sheet material in water and then electrolytically pickling it in an acid bath, first cathodically and then anodically; rinsing the sheet material in water again and then subjecting the scaled and soaked material to preliminary tinning in an alkaline bath; rerinsing the pretinned sheet and then putting it into an acid-tinning bath; and finally subjecting the tinned sheet to treatment for fusing and cooling the deposited tin.
This proposed method necessitates careful rinsing between pickling, pretinning and tinning, not only to avoid neutralizing one bath by carry over from another, but also to avoid the precipitation of tin compounds in the acid-tinning bath, these tin compounds arising from alkaline stannates carried by the sheet when it leaves the pretinning section. This method also entails modifying an existing tinning installation by the provision of extra vats for the alkaline pretinning, which makes the conversion of existing plant costly.
It is known that the corrosion resistance of tin plate depends mainly on the continuity of the layer of crystalline FeSn,alloy formed between the steel sheet and the coating of tin during the fusion of the deposited tin. This continuity of the crystalline layer depends onthe surface condition of the steel/tin interface, this surface condition determining the density and growth of the Fesn grains.
The present invention at least partially eliminates the drawbacks mentioned above, one object thereof being to provide a method of electrolytic tinning whereby a sheet of steel is subjected to degreasing in an alkaline bath; pickling in an acid bath in which the sheet of steel is polarized as the cathode, preliminary coating with metal, tinning in an acid bath and treating to obtain the fusion and. cooling of the tin on the sheet. This method makes it possible to produce tinplate that has a layer of Fesn which is continuous by virtue of very dense seeding and which thus has improved corrosion resistance, while enabling certain steps in the process to be simplified.
A method of electrolytic tinning in accordance with the invention is characterized by the fact that the metallic precoating of the sheet material is carried out in an acid pickling bath containing bivalent metal ions, the concentration of which is low in relation to that of hydrogen ions.
Hence, the previously degreased sheeting, when rendered cathodic in relation to two parallel counterelectrodes of which it constitutes the plane of symmetry, becomes the seat of abundant evolution of hydrogen and a slight adherent deposit of metal. The hydrogen liberated reduces the oxides and mechanically removes impurities from the surface of the sheeting, while the slight deposit of metal preserves it from any subsequent contamination.
Since the clectrodeposition pickling bath is substituted directly for the conventional pickling bath, the operations of pickling and precoating can take place in one and the same working vat. However, the electrodeposition pickling may be preceded by conventional pickling when the strip is particularly heavily oxidized.
By means of the invention, an extremely thin initial coating of adherent metal can be deposited in the pickling bath on the steel sheet as soon as this is clean. This coating or deposit then protects the steel/tin interface from any contamination likely to occur between emergence from the electrodeposition pickling bath and entry into the first tinning bath proper. Despite the abundant evolution of hydrogen, the slight deposit of metal resulting from the electrodepositon pickling is not spongy, as might have been expected, but adherent and uniform.
Further features will become apparent from the following description of various ways of putting the invention into practice from the accompanying drawings, in which:
FIG. I is a micrograph of the alloy coating of tinplate obtained by the conventional method;
FIG. 2 is a micrograph of the alloy coating on tinplate obtained by a method in accordance with the invention, employing a stage of tinning and pickling in an acid medium;
FIG. 3 is a micrograph of the alloy coating on tinplate obtained by a method in accordance with the invention, employing a stage of cathode nickel plating and pickling in an acid medium; and
FIG. 4 is a micrograph of the alloy coating on tinplate obtained by a method in accordance with the invention, employing a stage of cathode tinning, nickel plating and pickling in an acid medium.
All these micrographs are enlarged l6,000 times.
A method of electrolytic tinning in accordance with the invention should preferably comprise the following steps:
A steel strip or sheet is first subjected to conventional degreasing; then, after drying and rinsing in water, the degreased sheet is put into an acid electrodeposition pickling bath consisting of an aqueous solution of acid containing bivalent metal ions (tin or nickel, alone or mixed, these metals preferably being used in the form of bivalent ions). The sheet is polarized as the cathode, the anode consisting of a material possessing good resistance to anodic dissolution.
Having undergone the treatment of electrodeposition pickling (pickling and precoating with metal), the sheet is dried and rinsed in water before being put into the tinning bath or baths, in which it receives an additional coating of tin by conventional electrodeposition. The tinned sheet is then subjected to a treatment for fusing the tin coating in the usual way, for example, Joule effect, induction, radiation and so forth, and is then cooled with water. This procedure is economical and does not necessitate technical alterations to existing plant, the electrodeposition pickling taking place in the section provided for the conventional pickling. When the constituents of the electrodeposition pickling baths are chemically compatible with those of the tinning bath that follows the electrodeposition pickling, the rinsing stage between the electrodeposition pickling and the conventional tinning can be reduced to the strict minimum or even dispensed with altogether.
The electrodeposition pickling bath may have an acidity of [0 to 200 gram equivalents of sulfuric acid per liter of bath.
This means that the electrodeposition pickling bath may be made with sulfuric acid or some acid other than sulfuric or from a mixture of acids from which sulfuric acid may be absent.
The content of bivalent metal or metals in the electrodeposition pickling bath may range from 0.1 to 300 grams per liter of bath. Within the limits just quoted, however, it is important not to associate any random concentration of acid with any random concentration of metal. To obtain effective electrodeposition pickling leaving an adherent homogeneous deposit of metal, it is important that the concentration of hydrogen ions should be high-enough, in relation to the concentration of metal ions, to ensure that the cathode current output in deposited metal is low, being less than 50 percent and preferably between 5 percent and 25 percent.
There is thus always an abundant evolution of hydrogen on the cathode-polarized sheet metal, and this evolution contributes essentially to the elimination of oxides on the faces of the sheeting.
In this method, the metal coating forms on the steel sheet or strip as soon as the steel has been stripped by reduction. There is therefore no risk of oxidation of the sheet, which, once it emerges from the electrodeposition pickling bath, can no longer oxidize during the subsequent rinsing in an atmospheric medium, because it is already protected by a very thin coating of metal.
To illustrate the present invention, tinning pickling, nickelplating pickling and tinning and nickel-plating pickling are described hereunder in greater detail. No limitation on the scope of the invention is implied by these examples.
lTINNING PICKLING The tinning pickling bath is an acid hath made with sulfuric acid, for example, containing stannous salts. The tin content of such a bath may vary between 0.3 and 1.5 g. per liter of bath and the content of sulfuric acid between 15 and 100 g. per liter of bath, without the results varying appreciably. These figures naturally do not represent a limitation.
To effect an appreciable slowing down of oxidation of the stannous ions to stannic ions and of the ferrous ions to ferric ions (the iron coming mainly from the reduction of the iron oxides on the sheet), it is preferable to use a hath made with acids belonging to the phenosulfonic acid family, such as, for example, phenolsulfonic or cresolsulfonic acid, or from a mixture of sulfuric and phenolsulfonic acids. in that case, the tin deposited will be still more adherent than in a sulfuric medium alone. The contents of stannous tin and acid given for the sulfuric bath are equally applicable to baths modified with phenolsulfide acids, the acidity then being expressed in gram equivalents of sulfuric acid per liter of bath. The anodes employed are acid proof, being made of graphite, for example, or of stainless steel or an iron-silicon alloy containing 13 percent of Si.
The present invention is not limited, as regards the tinning pickling bath, to the acid or acid mixture solutions quoted as examples. it should be emphasized that the use of other acids, alone or in the form of mixtures, mineral or organic, comes within the scope of the invention.
The stannous ions are introduced into the tinning pickling bath in the form of stannous salts, such as stannous sulfates or else by the dissolution of one or more soluble tin anodes placed among the acid proof anodes, or again in the form of used or excess tinning bath containing stannous ions. This last method is particularly advantageous on grounds of economy, acid-tinning baths tending to become rich in stannous ions. This procedure also enables the acidity of the tinning pickling bath to be kept constant. The introduction of fresh stannous ions to the bath is carried out, of course, as the stannous ions in the bath are consumed by the deposition of tin and in such a way that the concentration of stannous ions remains within a definite range, for the baths mentioned above, for example, within the range of 0.3 to 1.5 g. per liter of bath.
The time taken by the sheet metal to pass through the tinning pickling bath may amount to up to 5 seconds. The current-density values vary, being and 60 a./sq.dm., and the bath temperature lies between C. and 80 C.
Tests of the A.T.C. (Alloy Tin Couple) type made with sheets of tinplate manufactured in accordance with the invention have given values of between 0.5 and 0.12 p. a./sq.cm.
The values obtained by tests of l.S.T. (Iron Solution Test) type, though usually below 20 g. of iron, have shown considerable improvement.
The adhesion of solder to tinplate prepared by a method in accordance with the invention is in general improved on average by l5 to percent in relation to adhesion to tinplate obtained by traditional methods.
In general, tinplate manufactured in accordance with the invention has a better surface shine than tinplate obtained without tinning pickling.
The A.T.C. test consists in determining in microamperes per square centimeter the electric current arising in a cell consisting of an electrode of pure tin and a specimen of tinplate from which the coating of tin has been dissolved and of which the FeSn, alloy coating has remained adhered to the steel sheet. The two electrodes are immersed on short circuit in deaerated grapefruit juice at a temperature of 26 C. The short-circuit current is measured after a 20-hour output of the cell. It is considered that the sheet of tinplate has good corrosion resistance when this current is less than 0.12 a./sq.cm.
, and very good resistance if it is less than 0.085 a./sq.cm.
EXAMPLE [-1 The tinning pickling bath contained 100 g. of sulfuric acid and 1.5 g. of tin per liter of bath, the tin being introduced into the bath in the form of stannous sulfate. The bath temperature 15 was C., the current density was 17 a./sq.dm., the duration of treatment was 2 seconds and the mass of the tin deposit obtained by the pickling operation was 0.7 g./sq.rn.
The current density is the current applied per face of unit surface area (sq.dm.). 2 The mass deposited per unit surface area is the sum of the masses deposited on each side of this unit surface area. This method of calculation is usual in the tinplate industry. The actual mass depos'ited per face of unit surface area is thus 1 one-half of that given.
in accordance with the invention, the degreased and rinsed sheeting was passed to the tinning pickling section. On emerging from the tinning pickling, it underwent further tinning, to bring the total amount of tin deposited up to 16.8 g./sq.m.
The coating of tin was then fused by Joule effect and dipped into water.
Solder Tests on the l.S.T. A.T.C. adhesion steel sheeting 6. Fe pA./sq.cm. ltgJcm.
With tinning pickling 8 012 I0 Without tinning pickling 15 0.50 I
EXAMPLE [-2 Solder Tests on the same l.S.T. A.T.C. adhesion steel sheeting p0. Fe nAJlqxm. ltgJcm.
With tinning pickling 7 010 9.5 Without tinning pickling l4 0.40 l
When the tinning pickling was preceded by conventional cathode pickling in a sulfuric medium containing 30 g. of sulfuric acid per liter of bath, at ambient temperature, at 14 a./sq.dm. for 1.2 seconds, the A.T.C. value was 0.095 to 0.10 p. a./sq.cm. This example shows that it is not necessary for the tinning pickling to be preceded by conventional pickling.
EXAMPLE l-3 The tinning pickling bath contained 53 g. of phenolsulfonic acid (equivalent to 15 g. of sulfuric acid) and 0.6 g. of stannous tin per liter of bath. The stannous ions were introduced into the bath in the form of excess tinning electrolyte. The bath temperature was C. The current density was l6 a./sq.dm. The time taken by the degreased sheeting to pass through the bath was 1.8 seconds. The sheeting emerging from this bath was lightly tinned (0.8 g. of tin per sq.m.).
The sheeting was subject to the same series of operations as in example I.
It should be noted that in the three foregoing examples, the shine on the tinplate obtained with tinning pickling was clearly better than that of tinplate obtained without tinning pickling.
In FIGS. 1 and 2, the micrographs (enlarged sixteen thousand times) show the appearance of the crystalline FeSn layer on one and the same kind of steel, according to whether or not the tinning pickling here proposed is used.
FIG. I shows the appearance of the alloy layer of the tin plate obtained with conventional cathodic acid pickling, while FIG. 2 shows the appearance of the alloy layer of tinplate obtained with tinning cathodic acid pickling. The distribution of alloy tin in FIG. 1 is 2.5 g./sq.m. and that in FIG. 2 is L9 g./sq.m.
The operations of degreasing, tinning after pickling, fusion and cooling were identical in both cases. The two drawings clearly show that the tinplate obtained by a method in accordance with the invention has, in general, the advantage, over tinplate of traditional type, of having a distinctly higher grain density. This results in an alloy layer of more compact structure and hence in an appreciably better A.T.C. test value, which is changed from 0.32 a a./sq.cm. (tinplate obtained by conventional method) to 0.08 a./sq.cm. (tinplate obtained by a method in accordance with the invention).
II NICKEL-PLATING PICKLING Solder Tests on the same I.S.T. A.T.C. adhesion steel sheeting 40. Fe A./sq.cm. kgjcm.
With nickle-plating pickling 8 0.10 9 Without nickel-plating pickling 14 0.37 7.5
The improvement in surface shine obtained on tinplate by nickel-plating pickling was less marked than with tinning pickling. The appearance of the alloy coating on the tinplate obtained by this application of the invention is shown in FIG. 3. The proportion of alloy tin in FIG. 3 is 1.8 g./sq.m. and the A.T.C. value 0.10 pa./sq.cm.
Ill TINNING AND NICKEL-PLATING PICKLING Example I l The electrodeposition pickling bath contained 15 g. of sulfuric acid, I g. ofnickel in sulfate form (NiSO -7H 0) and 0.5 g. of stannous tin in the form of used or excess acid tinning bath per liter of bath. The bath temperature was 60 C., the current density 14 a./sq.dm. and the duration of treatment 2 seconds. The mass of the metal clectrodeposited during pickling was 0.2 g. of tin and 0.02 of nickel per sq.m.
The sequence of operations was the same as in example H, the only difference being that the tinning pickling was replaced by tinning and nickel-plating pickling.
Solder Tests on the same I.S.T. A.T.C. Solder adhesion steel sheeting .tG. Fe A./sq.cm. KgJcm.
With tinning and nickelpllting pickling 7 0.05 9 Without tinning and nickel-plating pickling l4 0.37 7.5
This example showed a noteworthy improvement in the A.T.C. in relation to the examples I-land II-l, this improvement having been obtained by the addition of a little tin to the nickel-plating pickling bath. It should be noted that the improvement in surface shine thus obtained on the tinplate was as marked as with tinning pickling, as compared to that of the traditional tinplate.
The appearance of the alloy layer on tinplate obtained by this form of application of the invention is shown in FIG. 4. Here the relatively dense structure is clearly brought out. The distribution of alloy tin in FIG. 4 is 1.6 g.lsq.m. and the A.T.C. value is 0.05 a a./sq.cm.
The details given above for tinning pickling, namely the bath temperature, cathode current density, duration of treatment, nature of counterelectrodes, form in which the metal ions are introduced into the bath and the protection of oxidizable metal ions against oxidation, are valid for the other electrodeposition pickling methods.
The results described above are thus obtained by the use of relatively modest means in conventional acid tinning plant, by merely modifying the composition of the bath as well as the counterelectrodes of the existing electrolytic pickling section.
A method in accordance with the invention offers the important advantage of relative simplicity over other proposed methods based on the use of baths that are chemically not very compatible with the preceding and following baths, which entails thorough drying and rinsing. Before these known methods can be put into practice, too, existing acid tinning plant requires extensive modification.
Another not inconsiderable advantage of a method in accordance with the invention is that the recovery of excess acid tinning bath liquid is permitted.
The invention is naturally not limited to the forms described, but includes all variants thereof.
Thus, one variant of the invention consists in subjecting the sheet steel, after degreasing, to conventional acid electrolytic pickling, followed by the electrodeposition pickling described above..This procedure may be found useful when the sheeting is heavily oxidized, but the preliminary pickling is not necessary in everyday practice.
1. In a method of electrolytically tin-plating sheet steel comprising subjecting the sheet steel to the steps of:
pickling in an acid bath;
preliminary coating with a metal;
acid tinning; and
fusing and cooling the tin deposited on the sheet steel;
the improvement comprising carrying out the preliminary coating of the sheet steel, polarized as the cathode, in an acid bath having a temperature between 20 and C. containing bivalent ions of a metal selected from the group consisting of tin and nickel in an amount between 0.1 and L5 g. per liter of bath and an acid content between 10 and I00 grams equivalent of sulfuric acid per liter of bath, thereby removing oxides from the steel strip surfaces and simultaneously depositing a thin coating of tin or nickel on the steel, said strip being passed through said acid bath for a time of about I to 5 seconds, and supplying to said steel strip an electric current of about l0 to 30a./sq.dm., thereby ensu fing a cathode efficiency in deposited metal of about to 25 percent.
2. A method according to claim I, in which the metal ions contained in the acid pickling bath are stann'ous ions.
3. A method according to claim 2, in which the stannous ions are introduced into the acid pickling bath in the form of used or excess tinning bath.
4. A method according to claim I, in which the metal ions contained in the acid pickling bath are bivalent nickel ions.
5. A method according to claim 1 in which the metal ions contained in the acid pickling bath are a mixture of stannous and nickel ions.
6. A method according to claim 1, in which the metal ions are introduced to the acid pickling bath in the form of bivalent salts.
7. A method in accordance with claim 1, in which an antioxidant additive is added to slow down the oxidation of the readily oxidizable metal ions in the pickling bath, which additive is compatible with the acid content in the acid pickling bath.
8. A method according to claim! in which the step of pickling in an acid bath is preceded by a conventional acid pickling.
9. The process of claim 1 wherein the bath contains bivalent tin and nickel ions, and includes the step of simultaneously depositing a thin coating of tin and nickel on the steel strip surfaces.
10. A method according to claim I, in which the bivalent metal ions of tin are introduced to the acid pickling bath in the form of used or excess tinning bath.
11. A method according to claim 1, in which an antioxidant additive is added to the pickling bath to slow down the oxidation of the readily oxidizable metal ions in the pickling bath, which additive is compatible with the acid content in the acid pickling bath.
[2. A method according to claim I, in which the electrodepositing pickling step in an acid bath is preceded by a conventional acid pickling.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US1417896 *||Jan 17, 1921||May 30, 1922||Fletcher Electro Salvage Compa||Electrodeposition of metals upon iron and alloys of iron|
|US1898765 *||Jun 20, 1932||Feb 21, 1933||Bullard Co||Electrocleaning process|
|US1972835 *||Mar 8, 1932||Sep 4, 1934||Tainton Urlyn Clifton||Coating ferrous articles with zinc|
|US1979996 *||Apr 3, 1931||Nov 6, 1934||Gen Motors Corp||Electroplating process|
|US2266330 *||Feb 25, 1937||Dec 16, 1941||John S Nachtman||Process for electroplating strip steel|
|US2363973 *||Jul 8, 1939||Nov 28, 1944||Revere Copper & Brass Inc||Method of copper plating stainless steel cooking vessels|
|US2381778 *||Dec 13, 1940||Aug 7, 1945||Standard Steel Spring Company||Process of producing protected metal articles|
|US2407579 *||Jul 7, 1943||Sep 10, 1946||Du Pont||Electrodeposition of tin|
|US2673836 *||Nov 22, 1950||Mar 30, 1954||United States Steel Corp||Continuous electrolytic pickling and tin plating of steel strip|
|US2915444 *||Dec 9, 1955||Dec 1, 1959||Enthone||Process for cleaning and plating ferrous metals|
|US3260580 *||Nov 19, 1962||Jul 12, 1966||American Can Co||Tin plate having a tin-nickel-iron alloy layer and method of making the same|
|US3445351 *||Oct 21, 1964||May 20, 1969||Du Pont||Process for plating metals|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US4157694 *||Mar 16, 1978||Jun 12, 1979||Tokyo Kohan Co. Ltd.||Method of producing a tin-plated seamless container|
|US4236977 *||Aug 25, 1978||Dec 2, 1980||Italsider, S.P.A.||Method for preplating steel surfaces|
|US4601957 *||Aug 29, 1985||Jul 22, 1986||Toyo Kohan Co., Ltd.||Method for producing a thin tin and nickel plated steel sheet for welded can material|
|US5700366 *||Sep 3, 1996||Dec 23, 1997||Metal Technology, Inc.||Electrolytic process for cleaning and coating electrically conducting surfaces|
|US5958604 *||Sep 22, 1997||Sep 28, 1999||Metal Technology, Inc.||Electrolytic process for cleaning and coating electrically conducting surfaces and product thereof|
|US5981084 *||Sep 22, 1997||Nov 9, 1999||Metal Technology, Inc.||Electrolytic process for cleaning electrically conducting surfaces and product thereof|
|US7056806||Sep 17, 2003||Jun 6, 2006||Micron Technology, Inc.||Microfeature workpiece processing apparatus and methods for controlling deposition of materials on microfeature workpieces|
|US7235138||Aug 21, 2003||Jun 26, 2007||Micron Technology, Inc.||Microfeature workpiece processing apparatus and methods for batch deposition of materials on microfeature workpieces|
|US7258892||Dec 10, 2003||Aug 21, 2007||Micron Technology, Inc.||Methods and systems for controlling temperature during microfeature workpiece processing, e.g., CVD deposition|
|US7279398||Jan 6, 2006||Oct 9, 2007||Micron Technology, Inc.||Microfeature workpiece processing apparatus and methods for controlling deposition of materials on microfeature workpieces|
|US7282239||Sep 18, 2003||Oct 16, 2007||Micron Technology, Inc.||Systems and methods for depositing material onto microfeature workpieces in reaction chambers|
|US7323231||Oct 9, 2003||Jan 29, 2008||Micron Technology, Inc.||Apparatus and methods for plasma vapor deposition processes|
|US7335396||Apr 24, 2003||Feb 26, 2008||Micron Technology, Inc.||Methods for controlling mass flow rates and pressures in passageways coupled to reaction chambers and systems for depositing material onto microfeature workpieces in reaction chambers|
|US7344755||Aug 21, 2003||Mar 18, 2008||Micron Technology, Inc.||Methods and apparatus for processing microfeature workpieces; methods for conditioning ALD reaction chambers|
|US7387685||Sep 2, 2004||Jun 17, 2008||Micron Technology, Inc.||Apparatus and method for depositing materials onto microelectronic workpieces|
|US7422635||Aug 28, 2003||Sep 9, 2008||Micron Technology, Inc.||Methods and apparatus for processing microfeature workpieces, e.g., for depositing materials on microfeature workpieces|
|US7481887||Dec 29, 2004||Jan 27, 2009||Micron Technology, Inc.||Apparatus for controlling gas pulsing in processes for depositing materials onto micro-device workpieces|
|US7581511||Oct 10, 2003||Sep 1, 2009||Micron Technology, Inc.||Apparatus and methods for manufacturing microfeatures on workpieces using plasma vapor processes|
|US7584942||Mar 31, 2004||Sep 8, 2009||Micron Technology, Inc.||Ampoules for producing a reaction gas and systems for depositing materials onto microfeature workpieces in reaction chambers|
|US7588804||Aug 19, 2004||Sep 15, 2009||Micron Technology, Inc.||Reactors with isolated gas connectors and methods for depositing materials onto micro-device workpieces|
|US7647886||Oct 15, 2003||Jan 19, 2010||Micron Technology, Inc.||Systems for depositing material onto workpieces in reaction chambers and methods for removing byproducts from reaction chambers|
|US7699932||Jun 2, 2004||Apr 20, 2010||Micron Technology, Inc.||Reactors, systems and methods for depositing thin films onto microfeature workpieces|
|US7771537||May 4, 2006||Aug 10, 2010||Micron Technology, Inc.||Methods and systems for controlling temperature during microfeature workpiece processing, E.G. CVD deposition|
|US7906393||Jan 28, 2004||Mar 15, 2011||Micron Technology, Inc.||Methods for forming small-scale capacitor structures|
|US8133554||May 6, 2004||Mar 13, 2012||Micron Technology, Inc.||Methods for depositing material onto microfeature workpieces in reaction chambers and systems for depositing materials onto microfeature workpieces|
|US8384192||Mar 14, 2011||Feb 26, 2013||Micron Technology, Inc.||Methods for forming small-scale capacitor structures|
|US8518184||Jul 20, 2010||Aug 27, 2013||Micron Technology, Inc.||Methods and systems for controlling temperature during microfeature workpiece processing, E.G., CVD deposition|
|US9023436||Mar 13, 2012||May 5, 2015||Micron Technology, Inc.||Methods for depositing material onto microfeature workpieces in reaction chambers and systems for depositing materials onto microfeature workpieces|
|US20050045100 *||Oct 5, 2004||Mar 3, 2005||Derderian Garo J.||Reactors, systems with reaction chambers, and methods for depositing materials onto micro-device workpieces|
|US20050059261 *||Sep 17, 2003||Mar 17, 2005||Cem Basceri||Microfeature workpiece processing apparatus and methods for controlling deposition of materials on microfeature workpieces|
|US20050120954 *||Dec 29, 2004||Jun 9, 2005||Carpenter Craig M.||Apparatus for controlling gas pulsing in processes for depositing materials onto micro-device workpieces|
|US20050217575 *||Mar 31, 2004||Oct 6, 2005||Dan Gealy||Ampoules for producing a reaction gas and systems for depositing materials onto microfeature workpieces in reaction chambers|
|US20060193983 *||Apr 27, 2006||Aug 31, 2006||Micron Technology, Inc.||Apparatus and methods for plasma vapor deposition processes|
|US20070102994 *||Dec 21, 2006||May 10, 2007||Wright James P||Wheel Trim Hub Cover|
|US20080029028 *||Oct 15, 2007||Feb 7, 2008||Micron Technology, Inc.||Systems and methods for depositing material onto microfeature workpieces in reaction chambers|
|US20100282164 *||Nov 11, 2010||Micron Technology, Inc.||Methods and systems for controlling temperature during microfeature workpiece processing, e.g., cvd deposition|
|US20110163416 *||Jul 7, 2011||Micron Technology, Inc.||Methods for forming small-scale capacitor structures|
|WO1997025454A2 *||Dec 20, 1996||Jul 17, 1997||Weirton Steel Corporation||Electrolytic plating of steel substrate|
|WO1997025454A3 *||Dec 20, 1996||Sep 4, 1997||Weirton Steel Corp||Electrolytic plating of steel substrate|
|WO1997035051A1 *||Aug 30, 1996||Sep 25, 1997||Metal Technology, Inc.||An electrolytic process for cleaning and coating electrically conducting surfaces|
|U.S. Classification||205/87, 205/226, 205/210, 205/211, 205/217, 205/154|
|International Classification||C25D5/10, C25D5/44, C25D5/34, C25F1/00, C25D5/48, C25F1/06, C25D5/36, C25D3/30, C23G1/08, C25D5/12, C25D5/50|
|Cooperative Classification||C23G1/08, C25D5/44, C25D5/505, C25D5/36|
|European Classification||C23G1/08, C25D5/44, C25D5/36, C25D5/50B|