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Publication numberUS2002891 A
Publication typeGrant
Publication dateMay 28, 1935
Filing dateJun 4, 1931
Priority dateJun 4, 1931
Publication numberUS 2002891 A, US 2002891A, US-A-2002891, US2002891 A, US2002891A
InventorsHarriet L Hall
Original AssigneeMetals Disintegrating Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Bronze, bronze powders, and method of making the same
US 2002891 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

y 8, 1935. E. J. HALL 2,002,891

BRONZE, BRONZE POWDERS, AND METHOD OF MAKING THE SAME Filed June 4, 1931 INVENTOR I BY W ATTORNEYS Patented May 28, 1935 UNITED STATES PATENT OFFICE BRONZE, BRONZE POWDERS, AND METHOD OF MAKING THE SAME Application June 4, 1931, Serial No. 542,189

Claims. (Cl. 134-76) ments of metal in the form of flakes or plates or scales. This flake form is desirable, in order that a small weight of metal may be made to cover the maximum surface and produce a metal-like coating when applied as a paint. The flake form of the particle is, however, only one important feature of a desirable bronze powder. Another is the requirement that when the powder is applied as a paint, the flakes shall lie parallel to the surface. How completely this result is attained depends upon the characteristics of the flake surface, and to some extent, upon the character of the medium or vehicle in which the powder is dispersed. Considering effective bronze powders now known to the trade, it is believed that the surfaces of the flakes are provided with a film which gives the so-called leafing. or mirroring property and causes some of the particles to float on the surface of the vehicle in the same manner as a greasy needle will float onthe surface of water.

In current practice the metal'in pieces of convenient size, to be converted to bronze powder, is placed in a stamp mill with a small fraction of a per cent of some lubricating material such as tallow, olive oil, etc., and pounded or stamped.

As the particles are suflicientlyreduced in size they are either continuously or periodically removed by screening or a current of gas. This may entail several repeated operations. Following the stamping and sizing operation the powder is placed in a drum which is provided with polishing brushes. These brushes are caused to travel over the inner surface of the drum, giving a polishing action and cause to be distributed over the surface of the particles stearic acid which is added with the powder or subsequently. After polishing fora number of hours varying with conditions, the powder is then stored and allowed to age. In this aging operation certain changes take place which enhance the leafing property.

I have discovered that stearic acid or its equivalent, when dissolved in a suitable liquid can be made to impart expeditiously the desired leafing property. And, further, that this property can be developed coincidentally with the grinding or flaking operation. It has further developed that several factors are important in the accomplishment of this result. For instance, if the combined operation of flaking and film development is to be carried out the grinding must be by impact and not attrition, and the metal must not be overworked. That is, there is an optimum force or blow at which the metal particle should be struck and as the force increases beyond that point results become progressively less satisfactory. The temperature at which the operation is carried on must be controlled, because here again an optimum condition exists. There must also be a relation between the amount of metal, the size of metal particle, the amount of stearic acid and aluminum stearate, the amount and kind of liquid, atmosphere and temperature. These aforementioned factors are not capable of calculation and therefore must be empirically arrived at.

I have found that the leafing property can be imparted to a clean flaked metal powder by treating it with the leafing agent in solution in a suitable liquid, in the presence of an oxygen available atmosphere, and that the action is accelerated by heating. As an example: A given weight of flaked metal is heated with agitation in the presence of air to C. with five times its weight of a 2% solution of stearic acid in benzene and the excess liquid then removed. The resulting product will leaf in benzene.

As the leafing and flaking operations can be more conveniently carried on simultaneously I prefer to so operate. While the comminution can be carried on in various grinding devices that operate by impact I prefer to utilize a ball mill.

In the drawing, Figs. 1 and 2 illustrate a ball mill such as may be used in the practice of my invention.

. Fig. 1 illustrates the proper operation of the mill, as hereinafter set forth, so that the balls act on the metal particles largely by impact; and

Fig. 2 shows What happens when the proper operating conditions do not obtain, and there is too much of attrition and rubbing action.

Per 1 pound of 100 mesh comminuted aluminum (see paragraphs A and B) it has been found that 1 pound of a petroleum fraction oil, such as "Varnolene (see paragraph C), 3% of stearic.

acid (see paragraphs D and E), 1% of aluminum stearate (see paragraph E) and 20 pounds of balls (see paragraphs F and J) give good results when ground for seven hours (see paragraph G) in a mill 16" diameter x 6" (see paragraph H) using A. Aluminum is used as an illustration because it is the bronze powder in greatest demand and most representative. The same principles, however, apply to other metals and alloys.

B. A IOO-mesh is specified because it has been found convenient to disintegrate the metal to this degree of fineness before starting the flaking and leafing development operation.

0. A petroleum fraction such as Varnolene is selected as the grinding liquid because it is a common constituent of varnish, further, its boiling range is such that there is no excessive loss by evaporation or great fire hazard, yet the liquid can readily be removed by evaporation when a dry product is desired. Liquids such asturpentine, benzol, or naphtha may be substituted for the Varnolene, as the liquid in which the leaf or mirror-producing film is developed. It

does not necessarily follow, however, that the particles will leaf in this liquid. For instance, if the aluminum is ground in Varnolene it will leaf in that liquid, and also in the paint vehicle. If aluminum is ground in naphtha it will not leaf in the naphtha but will leaf in the paint vehicle. The quantity used is adjusted to give the desired emulsion. (See paragraph E).

D. There is distinct evidence of chemical reaction between the metal and the stearic acid, in

which oxygen plays a part. As grinding proceeds the amount of stearic acid in solution decreases and a compound, probably aluminum stearate appears. If the grinding is carried on in a tightly closed mill there will be a drop in pressure, provided the temperature rise is not suflicient to give a compensating vapor pressure. Further, if an oxygen-free gas, such as hydrogen, is used a drop in pressure does not occur and the leafing or mirroring action does not develop. The fllmproducing agent must have an aflinity for the metal being treated and develop a film which has a certain deportment with the vehicle of application, the exact nature of which is not definitely known. Addition of the agent may be made at of the operation or toward the end. While stearic acid is given as the film-producing agent,,such substances as palmitic acid may be employed. Particularly where the leafing film is to be produced on the metal during the flaking operation, an excess of stearic acid in the sludge as herein set forth seems to give a very good result. This may be for the reason that stearate dislodged from the flakes as by attrition during the milling operation does not re-attach itself, but the leafing film is repaired or restored by reaction of some of the excess stearic acid with the denuded flake. 3% of stearic acid seems to provide a sufllcient excess or reserve, though manifestly the proportion may be varied.

E. In the operation of a ball mill such as illustrated there are different zones of action (see J) and it isnecessary to have the metal acted upon so far as possible in the impact zone. To prevent the metal from filtering through the interstitial of the ball mass and appearing largely in the attrition zone, it is necessary to produce an emulsion or froth carrying the metal particles which has sufficient body and tenacity to coat the balls and travel with them through the impact zone, yet permit suflicient mobility of the particles that they may present their flattened sides to adjacent balls and mill sides on contact. Stearic acid and aluminum stearate are indicated for this purpose, though any number of substances may be employed, such as palm oil, oleic acid, olive oil, palmitic acid, etc. The froth producing agent may also have the function of imparting the leafing film to the metal during grinding, e. g., stearic or palmltic acid; or it may subserve only the froth producing function, e. g., palm oil, etc. In the latter case an additional agent will be employed to impart the leafing film, and the froth producing agent will be selected and/or controlled as to amount so as to hinder as little as possible the development of the leafing film.

F. A ratio of 20 to 1 of balls to aluminum has proven satisfactory for the efiicient grinding with the production of a brilliant flake and good leafing quality.

G. The grinding time required is influenced by practically all the other factors mentioned and fineness of product desired.

H. The length and diameter of mill determine its capacity and output and the selection of size is a matter of economics.

1. For the given set-up balls were used, but it is to be understood that the force required is dependent upon the physical properties of the metal and the size of the pieces being ground, and that this will influence either or both the ball size and the mill diameter. It is to be further understood that the specific gravity of the metal being treated has a bearing on the ratio of metal to other factors. If it is desired to treat scrap foil or sheet directly they are first cut, into pieces approximately 4; to /2 inch square and for foil 2/1000 to 4/1000 of an inch thick grinding can be carried on to advantage in two stages-first, balls in a 16" mill and finished as above; second, for sheet 2 to 3" balls can be used to advantage'for the initial stage.

J. The speed of a ball mill determines whether grinding is done by attrition (Fig. 2), or by impact largely (Fig. 1). When the mill is revolved the balls are carried up the side with a tendency to slippage. Thisslippage is retarded by the insertion of internal ribs. When a certain height is reached, see Fig. 1, dependent on the charge, and below certain speeds, the balls in the upper layers roll'down while the layers of balls adjacent to mill wall are being carried up with the balls revolving on unoriented axes. The points in contact have a rubbing motion and therefore an abrading action which, in the lower layers, is intensified by the weight of superincumbent balls. This is not a satisfactory flaking action but results in the production of an excessive amount of slimes, as well as being destructive of the leafing film. The effect is less pronounced with a decrease in the size of balls and an increase in the number of points of contact. By carrying the proper charge of balls in the mill, about twofifths full, and revolving at the proper speed the balls by a combination of centrifugal force and gravity, are carried up to a point where they are thrown clear of the mill shell and ascending balls and fall in a free path striking the opposite side of the mill and balls that have preceded them, with the production of desired flakes. From the point of impact, in the direction'of rotation,.there is a zone of attrition but the major reduction in particle size is by impact. For the most efiicient grinding metal particles must lie between the impacting surfaces, and this is accomplished by the aforementioned froth or emulsion. It is also patent that the size of the ball and diameter of p the mill determine the force of impact. Too heavy a blow is destructive of the flake and. the film surface and these two factors, with the resistance of the metalparticles, determine the ratio of mill diameter to ball size.

ethanolamine stearate is desirable.

K. To properly charge a 16" diameter x 6" mill, 2 lbs. of aluminum and lbs. of balls are required for the desired height. Reducing the amount of metal increases the fineness of product, while conversely increasing the metal increases the coarseness of product, other things being the same.

L. 50 C. is adopted as a satisfactory temperature for operation. As the temperature rises above 50 C. there is a progressive tendency to loss of leafingf and when at 100 C. it is seriously reduced. V

The material as taken from the mill, with the removal of a part of the liquid, is a finished paste product without further treatment and can be stored indefinitely without losing its mirroring property. It is an established fact that ready mixed bronze powder paints lose their brilliancy on standing and therefore it is customary to market the powder and vehicle separately and mix on the job. This has several inconveniences due to the extremely light character of the powder. Therefore, I prefer to market my product in paste form and for that purpose an emulsifying agent such as aluminum stearate or tri- In grinding with stearic acid in solution there is apparently aluminum stearate formed and this formation increases with temperature and by proper control a satisfactory paste can be produced. However, I prefer to add aluminum stearate to the charge as it increases grinding efiiciency as well.

A typical product in paste form contains 58% aluminum; 1% stearic acid; 1% aluminum stearate, which as stated helps the grinding action and also helps in the production and maintenance of the homogeneous paste form; and 40% of a petroleum fraction, such as Varnolene. The flakes of the product possess the leafing quality,

.manifestable in ordinary paint liquids, and include no ingredients which will impair the leafing quality.

If a dry product is desired, the liquid can be evaporated under carefully controlled temperature and atmospheric conditions and the leafing property will be maintained. It is safe to heat the paste to 50 C. in an oxygen containing atmosphere; if the temperature goes much above there is a tendency to loss of leafing property, and, if heated until thoroughly dried, at 100 C.,

. the leafing property is more or less completely destroyed in the presence of oxygen.

In a non-oxidizing atmosphere such as city gas it is permissible to dry the paste at 200 C. and above without destroying the leafing property. It is possible to use a vacuum in drying, but this lowers the permissible temperature as compared to drying in a gas atmosphere.

Because of the composition of the liquid, there will be no undesirable residue on evaporation. Thus if the product in its paste form should he accidentally subjected to evaporation there would be no dried paint film skin such as would make aluminum, copper, zinc and tin, with no reason to doubt a similar behavior with their alloys.

Where particular materials are mentioned in the claims, it is to be understood that equivalentmaterials may be substituted, except where the language of a claim clearly excludes equivalents.

And where in,a claim it is stated that a certain procedure, involving certain materials, temperatures, etc., is followed, substantially as set forth, reference is implied to typical examples given in the specification, not as limitative of the claim, but as illustrating the technique which constitutes the real invention-empirically determined control and regulation of various factors, each in view of the other.

Varnolene, referred to herein, as a petroleum fraction oil with a boiling point from in the neighborhood of 307 F. to around 405 F. (See U. S. patent to this applicant, No. 1,569,484.)

I claim: I

1. The method which comprises imparting the quality of leafing or mirroring to flake metal powder by subjecting such powder to the action of a leafing agent dissolved in a volatile paint thinner, the amount of liquid being suflicient to form a sludge with the metal, and thereafter removing excess liquid to leave the residue in the form of a substantially homogeneous stable paste.

2. The method which comprises imparting the quality of leafing or mirroring to flake metal powder by subjecting such powder to the action of a leafing agent dissolved in a volatile paint thinner with oxygen available, the amount of liquid being sufficient to form a sludge with the metal, and thereafter removing excess liquid to leave the residue in the form of a substantially homogeneous stable paste.

3. As a new article of manufacture, a stable and homogeneous paste adapted for ready admixture with a paint vehicle, such as varnish, including flake bronze powder having on its surface a leafing film, the remainder of the paste comprising a paint thinner which is innocuous to the leafing film.

4. The method of producing bronze powder from metal particles, which comprises charging a ball mill with balls and with a quantity of the metal particles and a quantity of liquid containing in solution a leafing agent of the kind and for the purpose set forth. which imparts a leafing film to the metal and forms a creamy sludge with the metal in the operation of the mill, rotating the mill with oxygen available at such speed as to cause cataracting of the balls and to throw them clear of the mill shell and ascending balls, continuing the rotation until the metal has been brought to the desired fineness and flake form, maintaining in the mill a temperature favorable to the creation and maintenance of the leafing film, removing the sludge from the mill, and reducing the proportion of liquid to metal to such an extent as to produce a substantially homogeneous bronze powder paste.

5. A method which comprises imparting the quality of leafing or mirroring to flake aluminum powder by subjecting such powder to the action of a leafing agent dissolved in a volatile paint thinner, and in the presence of an oxygen containing atmosphere, forming a leafing film comprising aluminum stearate upon such particles and removing the liquid and preventing loss of the leafing film.

quality of leafing or mirroring to flake metal taining atmosphere and removing the liquid in a non-oxidizing atmosphere at a temperature not substantially higher than about 200 0., whereby lossof the leafing film is prevented.

8. The method of producing bronze powder from aluminum particles, which comprises charging a ball mill with balls and with a quantity of the metal particles and a quantity of liquid containing in solution a leafing agent of the kind and for the purpose set forth, which imparts a leafing film to the metal and forms a creamy sludge with the metal in the operation of the mill, rotating the mill with oxygen available at such speed as to cause cataracting of the balls and to throw them clear of the mill shell and ascending balls, continuing the rotation until the metal has been brought to the desired fineness and flake form, maintaining in the mill a temperature favorable to the creation and maintenance of the leafing film, removing the sludge from the mill, and separating liquid constituents therefrom; the solution comprising a liquid having the'properties of- Varnolene" in which is dissolved stearic acid, the Varnolene being in the proportion of one pound per one pound of aluminum, and the stearic acid being in the proportion of 3% of the weight of aluminum.

9. As a new article of manufacture,'a mixture of about 58% of flaked aluminum particles, about 1% stearic acid, about 1% aluminum stearate, and about 40% Varnolene, the flaked aluminum having a leafing film, and the mixture being in 2, substantially homogeneous and persistent paste orm.

10. As a new article of manufacture, a wet pigment for admixture with a paint vehicle for the purpose of forming a paint, comprising flaked metal bronze powder, the powder flakes having on their surface a leafing film as evidenced by the ability of the flakes to leaf in a paint vehicle, such as varnish, and being dispersed in a liquid carrier innocuous to the leafing film and which forms with the flakes a stable paste in which the flakes retain their color and leafing quality during storage, as evidenced by the fact that the paste can be heated at temperatures up to about 50 C. without substantial impairment in those respects.

EVERETT J. HALL.

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2431565 *May 19, 1943Nov 25, 1947Aluminum Co Of AmericaMethod and apparatus for working particles for production of metal powders or pastes
US2461352 *Nov 6, 1946Feb 8, 1949California Research CorpWater-in-oil emulsion paints containing a leafing pigment
US2478387 *Jun 10, 1944Aug 9, 1949Eastman Kodak CoPhosphorescent materials
US2587266 *Aug 10, 1948Feb 26, 1952Aluminum Co Of AmericaWater emulsifiable metallic paste pigments
US2587267 *Nov 19, 1948Feb 26, 1952Aluminum Co Of AmericaWater-emulsifiable metallic paste pigments
US2587268 *Nov 29, 1949Feb 26, 1952Aluminum Co Of AmericaWater-emulsifiable metallic paste pigments
US2642230 *Jul 25, 1949Jun 16, 1953Johnson & Company London Ltd AProcess for distributing wax in cemented carbide powders
US2701772 *Jul 10, 1952Feb 8, 1955Reynolds Metals CoRust inhibitive aluminum pigment composition
US2735787 *Apr 14, 1953Feb 21, 1956 Process for pulverizing solid materials
US2791382 *Oct 30, 1953May 7, 1957Myers John FProcess of simultaneously wet grinding and classifying a sulfide ore
US2882589 *May 10, 1954Apr 21, 1959American Cyanamid CoLubricant in powder metallurgy
US3022130 *Dec 13, 1957Feb 20, 1962Francesco CasigliaContinuous recording of graphs and instruments therefor
US3286604 *Aug 16, 1962Nov 22, 1966Prismo Safety CorpMarking materials
US3527415 *May 15, 1967Sep 8, 1970Intern Bronze Powders LtdFlake metallic pigment milling
US3709439 *Dec 2, 1970Jan 9, 1973Int Nickel CoProduction of reflective metal flake pigments
US3776473 *Mar 27, 1972Dec 4, 1973Int Nickel CoHighly reflective aluminum flake
US3901688 *Nov 19, 1973Aug 26, 1975Int Nickel CoHighly reflective aluminum flake
US4056230 *Nov 19, 1975Nov 1, 1977Alcan Research And Development LimitedMethod of crushing particles of material in a ball mill
US4065060 *Oct 6, 1976Dec 27, 1977Aluminum Company Of AmericaMetal flake production
US4172720 *Jul 6, 1978Oct 30, 1979United States Bronze Powders, Inc.Attrition, sparkle
US4482374 *Jun 7, 1982Nov 13, 1984Mpd Technology CorporationOrganometallic alcohol as lubricant, wet ball milling
US4484951 *Sep 6, 1983Nov 27, 1984Toyo Aluminum Kabushiki KaishaAluminum flake pigment composition for paint
US4486225 *Jun 7, 1982Dec 4, 1984Mpd Technology CorporationProduction of highly reflective metal flake
US4629512 *Mar 7, 1985Dec 16, 1986Tom KondisLeafing aluminum pigments of improved quality
US6561713Apr 11, 2002May 13, 2003Dri Mark Products, Inc.Metallic ink composition for wick type writing instruments
US6673134 *Dec 31, 2001Jan 6, 2004Mitsui Mining & Smelting Company, Ltd.Introducing a copper slurry having fine granular copper particles having an average particle size of 3 to 5 mu m dispresed in water into a medium type agitation mill and flattening the fine copper powder
US8163079May 28, 2009Apr 24, 2012Eckart GmbhPlatelet-shaped, copper-containing, metallic effect pigments, process for preparing them and use thereof
DE755850C *May 17, 1936Oct 29, 1951Metals Disintegrating CoVerfahren zur Herstellung von Metallpigmentpasten durch Behandlung von Metallpulvernin einer Kugelmuehle
DE3002175A1 *Jan 22, 1980Jul 31, 1980Toyo Aluminium KkMetallische flockenpigmentzubereitung und verfahren zu ihrer herstellung
EP0021439A1 *Jun 27, 1980Jan 7, 1981E.I. Du Pont De Nemours And CompanyFlake silver powders with chemisorbed monolayer of dispersant and process for preparing the same
EP0097017A2 *Jun 7, 1983Dec 28, 1983MPD Technology CorporationProduction of metal flake
EP2128203A1May 28, 2008Dec 2, 2009Eckart GmbHDie-form metal effect pigments containing copper, method for their manufacture and use
WO1980000127A1 *Jul 6, 1979Feb 7, 1980Us Bronze Powders IncFlaked metal powders and method of making the same
Classifications
U.S. Classification106/404, 241/21, 29/DIG.310, 241/3, 241/15, 106/DIG.300, 241/16
International ClassificationC09C1/62, B22F9/04
Cooperative ClassificationC09C1/62, Y10S29/031, Y10S106/03, B22F9/04, C01P2004/20
European ClassificationC09C1/62, B22F9/04