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Publication numberUS2995780 A
Publication typeGrant
Publication dateAug 15, 1961
Filing dateDec 2, 1959
Priority dateDec 9, 1958
Publication numberUS 2995780 A, US 2995780A, US-A-2995780, US2995780 A, US2995780A
InventorsLlewelyn David M, West De Witt H
Original AssigneeInt Nickel Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Treatment of metal powder
US 2995780 A
Abstract  available in
Images(2)
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Claims  available in
Description  (OCR text may contain errors)

1961 DE WITT H. WEST ETAL 2,995,780

TREATMENT OF METAL POWDER 2 Sheets-Sheet 1 7 Filed Dec. 2, 1959 DEWITT H.WEST

DAVID M. LLEWELYN FIG.2

ATTORNEY INING 2 Sheets-Sheet 2 MESH ass.

FIG. 4

ON A IOO DEWITT H. WEST DAVID M. LLEWELYN INVENTOR.

Q ATTORNEY PER CENT PRODUCT REMA OE. m mmoiom OE. 4 5m DE WITT H. WEST HAL TREATMENT OF METAL POWDER 80 DUCT MESH B55.

FIG. 5

8O 9O UCT REMAINING IOO-MESH ass.

FIG. 3

40 PER CENT MILLED PRO REMAINING ON A I00 Aug. 15, 1961 Filed Dec. 2, 1959 mmDOI I MEI. 023 :2 wwmqIo LO HIQGB PER CENT PROD ON A United States Patent 2,995,780 TREATIVIENT OF BIETAL POWDER' De Witt H. West, Port Eynon, and David M. Llewelyn,

Cwmdwr, Clydach, England, assignors to The International Nickel Company, Inc., New York, N.Y., a corporation of Delaware Filed Dec. 2, 1959, Ser. No. 855,754 Claims priority, application Great Britain Dec. 9, 1958 2 Claims. (Cl. IS-48) The present invention relates to the mechanical treatment to agglomerate soft metal powders of very fine particle size and, more particularly, to a method for milling fine metal powder such as nickel powder so that the particles thereof will coalesce and grow in size.

It is well known that metal powders of very fine particle size are extremely difiicult to handle, use, and/or package. This is particularly true whenever metal powder is employed as an addition in an alloying process.

It is also well known that the fiowability of metal powders is an important factor wherever large-scale powder metallurgical manufacturing processes depend on rapid filling of the molds, as, for example, in the manufacture of porous bearings or machine parts. Since feeding is ordinarily accomplished by volumetric measure, rapid and uniform filling with the elimination of pockets in the die cavity or in the feeding device is of great importance. Thus, if the metal powder has superior fiow characteristics, it is suitable for high-speed compacting equipment. Conversely, if the powder has poor flow characteristics, an uneconomical feeding results. One of the methods used in the art to abate the poor flowability of powders is to add equipment such as vibrators to the feed mechanism. However, this entails additional expense and increases the cost of the article formed from the powders.

Although many attempts were made to overcome the foregoing difiiculties and other disadvantages, none, as far as we are aware, was entirely successful when carried into practice commercially on an industrial scale.

It has now been discovered that powders of fine particle size coalesce and agglomerate when subjected to mechanical stresses under controlled conditions, and that the fiowability of such treated powders is greatly enhanced.

It is an object of the present invention to provide an inexpensive, readily available method for increasing the particle size of fine powders and their flowability by the application of external mechanical forces.

Another object of the invention is to provide a process for coalescing carbonyl metal powders by external mechanical stresses without the use of binding and/or agglomerating agents to produce discrete, granular particles of larger size.

The invention also contemplates providing a powder of controlled minimum particle size.

Still another object is to provide a granular powder having superior fiowability properties.

Other objects and advantages will become apparent from the following descriptoin taken in conjunction with the accompanying drawings in which:

FIGURE 1 is a plan view of a high-speed ball mill;

FIGURE 2 is a front view of only 2 containers of the ball mill of FIGURE 1;

FIGURE 3 is a graphical representation showing the effect of milling time upon particle size;

FIGURE 4 depicts a graph of ball size plotted against particle size; and

FIGURE 5 illustrates the effect of the total weight of .the charge on the particle size of the product.

Broadly stated, this invention contemplates and relates to the treatment of relatively soft metal powder exemplified by nickel powder produced by the decomposition of nickel carbonyl and commonly known as carbonyl nickel powder, carbonyl iron powder of low carbon content, copper powder, and aluminum powder. Thepowders to which the invention relates are those of very fine particle size, i.e., less than about 8 microns. According to this invention, relatively soft powder is subjected to sufficient translational and rotational forces while being simultaneously peripherally restrained to cause movement of the powders in a direction toward the peripheral restraint. That is, the powders are charged into a confining means or other receptacle containing grinding balls, and said charge, comprising balls and powder, is subjected to a first acceleration of at least about 1 gravity induced by rotation of the confining means about its axis while substantially simultaneously subjecting the charge to a second acceleration. This induced second acceleration is at least 2 times greater than the acceleration induced by rotation of the mill about its own axis and the second acceleration, which is advantageously about 2 to about 12 times greater than the first induced acceleration, is applied in a direction that is substantially perpendicular to the axis of the confining means. Ball milling is well known as a method of reducing the particle size of the milled product. If a soft metal powder is milled under high-energy, high-speed conditions, as shown hereinbefore, such that the powders are subjected to the combination of sum cient translational and rotational forces, the result of the milling according to the invention is most surprisingly exactly the opposite, namely, that the particle size grows. In consequence thereof, coarse powder, i.e., over 500 microns, can be produced from finer powder, i.e., powder having a particle size of from about 2. microns to about 8 microns. In addition, the coarse particles formed thereby have substantially improved fiowability' and a greater apparent density.

FIGURES l and 2 depict a suitable high-speed ball mill 11 that is provided with a main central drive shaft 12 and an outer casing 13. A cage 14 adapted to carry a plurality of cylindrical containers or pots 15 in spaced relationship is suitably mounted to drive shaft 12. Each pot is provided with a lid 16 which is secured to the pot by securing arm 17 and screw cap 18. In order to hold the pots in place, an arm 19 is attached to screw cap 18 by fastening nut 20. The pots have vertical drive shafts 21 which along with main central drive shaft 12, are connected to a geared mechanism (not shown) that is designed to set up a planetary motion as shown in FIGURE 1. For example, while drive shaft 12 is turning the cage 14 and pots 15 counter-clockwise, shafts 21 are spinning the pots clockwise or directly opposite to the direction of rotation of main central drive. By this assembly, the cylindrical containers or pots 15 are moved as a whole through a circular path around a vertical axis (main drive shaft 12) at high speed while they are simultaneously rotated about their own axis .(shafts 21) in the opposite direction, also at high speed. This type of movement causes a turbulent agitation of the balls and soft metal powder which results in multiple contact of the balls with the powder and the transmission of high energy by means of translational and rotational forces to the powder. As a consequence of this action, the particles charged into the mill actually grow in size and yet remain substantially discrete. In other words, the whole mass of the feed powder does not coalesce as a unit. The particles so formed are substantially granular and have a high particle density approaching that of the metal concerned. Furthermore, these agglomerated powders have good flo'wability as defined by the angle of repose.

In the same connection, we also find that powders of different average particlesize can be made by varying the milling conditions. Thus, particle size of the feed, the weight of the charge including the balls and powder, the ball-to-powder ratio, the composition of the balls, the residence time of the charge in the mill, the speed of rotation of the mill, the energy input to the mill, alone or in any combination, with materially aflEect the particle size of the end product.

Thus, the particle size of the powder used afiects the final size after milling, the coarser the initial powder, the greater being the average particle size of the product. Oftentimes, the particle size of the feed will be dictated by the kind of powder used. For example, carbonyl nickel power may average from 2 microns to 8 microns according to the conditions of decomposition.

In carrying the invention into practice, it is advantageous to control the variable factors of the process oping powder used in the examples consisted of discrete.

spherical particles of less than about 8 microns average size. The mill was operated 'so that it was moving at 190 revolutions per minute through a circular path of 6 inches radius and turning about its own axis at 100 revolutions per minute. To contact the powder the mill was charged with balls, steel balls of /2 inch diameter being used. Advantageously, the milling is carried out dry, no advantage being obtained if a liquid, e.g., an alcohol, is added, and if water is added the particle size of the final product is descreased. For example, 6 pounds of fine nickel powder previously moistened with 9% water were milled with steel balls and the ball-to-powder ratio was 3 to 1. After 2 hours of milling in the mill operated under the aforementioned conditions, the average particle diameter was reduced to less than one-half its original size.

The result of varying these conditions is' shown by the hereinafter listed tables. Table I shows the effect of varying the milling time when milling with a 10:1 ball-to-powder ratio and 11 pound charge (balls plus powder) as when such a mill is used for grinding the container is usually run about half full of the charge of balls and material.

Table 1 Percent of End Product Romain- Milling Time (Hours) ing on a lmMesh B.S.S.

A 100-mesh British Standard Sieve has openings of 147 microns or 0.0058 inch.

Table II Percent of End Product Romain- Ball-to-powder Ratio ing on 100-Mesh B.S.S.

From these tables FIGS. 3 and 4 are respectively plotted and both curves indicate that as either the ballto-powder ratio and/or the time increases, their slopes become asymptotic. This demonstrates that there is an optimum milling time, and if this time is exceeded the average output of larger particle size begins to decrease per unit time. Furthermore, the higher the ball-topowder ratio, the greater is the final average particle size obtainable, but again the output of powder of this size in unit time decreases. The probable cause of this is work-hardening, which reduces the tendency of the particles to coalesce as the powder stores part of the energy expended on it after being worked. Therefore, by reducing the ball-to-powder ratio, the amount of workhardening can also be reduced. Thus, if the aim be the maximum output of the coarsest powder per unit time, there is therefore also an optimum ball-to-powder ratio,

as is shown by the curve of FIGURE 4, wherein ball-topowder ratios are plotted against percent product remaining on a 100-mesh British standard sieve.

As was shown by the foregoing experiments, when the milling is carried on under optimum economic conditions, only a'proportion of the powder produced is of the average size required. This can, of course, be separated by sieving and it is found that the remaining under-. sized fraction can be caused to grow in size by being recharged. It is also discovered that the yield when recharged powder is milled can be substantially increased if the powder is annealed between successive millings. For example, nickel powder may be annealed under hydrogen for one hour 'at 800" -C.

To further illustrate the effects of another variable factor in order to obtain the desired particle size in the end product, additional tests were run in the same mill under the same conditions as in the previous experiments holding the duration of operation of the mill constant at 3 hours and using a ball-to-powder ratio of 10:1 and varying the weight of the charge'with the results as shown in Table III.

Table III British Standard Sieve Weight of Run N 0. Charge,

lbs. +30 30 60 1 1 British Standard Sieve scale wherein 100-mesh is equal to 147 microns Using the data of Table III, Figure 5 is drawng wherein the abscissa is the percentage of powder remaining on a 100-mesh British Standard Sieve and the ordinate is the weight of the charge. The curve isparabolic showing that there is an optimum weight of charge. Therefore, the best yields of coarse particles are obtained when the total charge occupies about half the container.

As a result of these tests with the aforementioned mill operating at high speed, the optimum economic conditions for particles larger than 500 microns-(+30 mesh B.S.S. scale) from a starting material of less than 8.0 microns average particle size are 3 hours milling with 11 pounds charge (ball+powder) and a 3:1 ballzpowder ratio using /2 inch steel balls. Furthermore it is apparent that these conditions provide suflicient energy coacting translational and rotational forces to agglomerate the particles.

The agglomerated, discrete powders of this invention exhibit improved flow characteristics, as defined by the angle of repose. For example, the powders of Run 2, Table III, were tapped through a 30-mesh screen onto the end of a vertical cylinder having an 0.7 inch diameter. The base angle of the cone formed by such tapping was measured and found to be only 29 from the horizontal. However, when carbonyl nickel powder was identically tested, it had an angle of repose of about 66 from the horizontal. Thus, the powders of this invention have much the superior flowability. Furthermore, compacts produced therefrom are characterized by having good green strength.

However, if %-Vz inch steatite balls are used instead of steel balls in the mill described above, the optimum conditions are different, being in fact milling for 7 hours with 6 pounds of charge and a ball-to-powder ratio of 3:1.

The powders of the present invention are particularly adapted to be employed in general use in powder metal; lurgy, alloying and in the manufacture of welding electrodes.

Although the present invention has been described in conjunction with preferred embodiments, it is to be understood that modifications and variations may be resorted to without departing from the spirit and scope of the invention, as those skilledrjin the art will readily understand. Such modifications and variations are considered to be within the purview and scope of the invention and appended claims.

We claim:

1. A process for substantially increasing the size of soft metal particles selected from the group consisting of nickel, iron, aluminum and copper powders having a particle size in the range of about 2 to about 8 microns comprising providing a charge of grinding balls and substantially dry, soft metal powders and subjecting said substantially dry charge within a confining means to an acceleration of at least about one gravity induced by rotation of said confining means about its axis while substantially simultaneously subjecting said. charge to an acceleration of at least about two times greater than said rotationally-induced acceleration, said acceleration being induced externally with respect to said confining means, and being applied in a direction substantially perpendicular to the axis of said confining means.

2. The process as claimed in claim 1 wherein the soft metal particles are substantially dry nickel powders.

References Cited in the file of this patent UNITED STATES PATENTS 2,031,149 Eirich et a1. Feb. 18, 19 36 2,293,439 Lloyd Aug. 18, 1942 2,357,941 Eirich et al Sept. 12, 1944 2,696,019 Allan et al. Dec. 7, 1954 FOREIGN PATENTS 879,439 Germany June 11, 1953 915,072 Germany July 15, 1954 1,058,475 Germany June 4, 1959

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2031149 *Sep 21, 1931Feb 18, 1936Eirich LudwigEdge runner-like mixing and kneading machine
US2293439 *Jun 7, 1941Aug 18, 1942Dwight & Lloyd Sintering CompaApparatus for making noudles or pellets
US2357941 *Feb 3, 1940Sep 12, 1944Eirich GustavMethod of granulating pulverulent and plastic materials
US2696019 *Jul 14, 1952Dec 7, 1954C U R A Patents LtdMeans for the production of agglomerates from fine material such as fine coal
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3132020 *Jan 18, 1962May 5, 1964Kalk Chemische Fabrik GmbhProduction of granulated fertilizers
US3445555 *Mar 13, 1967May 20, 1969Int Nickel CoProcess for agglomerating fine metal powders
US3865572 *Jan 29, 1973Feb 11, 1975Int Nickel CoMechanical alloying and interdispersion cold bonding agents therefor
US3877930 *Jan 29, 1973Apr 15, 1975Int Nickel CoOrganic interdispersion cold bonding control agents for use in mechanical alloying
US3910188 *Apr 4, 1974Oct 7, 1975Us ArmyOne watt/one amp no-fire match type initiator
US4443249 *Mar 4, 1982Apr 17, 1984Huntington Alloys Inc.Production of mechanically alloyed powder
EP0209179A1 *Jul 2, 1986Jan 21, 1987Metallgesellschaft AgProcess for manufacturing a mechanically alloyed composite powder
Classifications
U.S. Classification419/61, 23/313.00R
International ClassificationB22F9/04, B22F9/02
Cooperative ClassificationB22F9/04
European ClassificationB22F9/04