Process for the production of graphite powders of increased bulk density

Abstract

The invention relates to a method for increasing the Scott density of synthetic and/or natural graphite powders of any particle size distribution, preferably of highly-pure graphite, by subjecting the graphite powder to an autogenous surface treatment. The inventive powder is used, in particular, for producing dispersions, coatings with an increased graphite/binder ratio and increased electric and thermal conductivity, gas and liquid-tight coatings on metal substrates, thermoplastic or duroplastic graphite-polymer composites, or for producing metallic, non-ferrous sintering materials.

Description

[0001] This is a continuation of application Ser. No. 10/130,261, which was accepted as a filing under 35 U.S.C. 371 on Jul. 15, 2002 and which is a 371 filing of PCT Application No. PCT/CH00/00514, filed Sep. 22, 2000, which claims priority to Swiss Application 2165/99, filed Nov. 26, 1999. All of these applications are incorporated herein by reference in their entirety.

[0002] The present invention relates to a process for the production of graphite powders of increased bulk density. The present invention relates in particular to an autogenous surface treatment of any pulverulent graphitic materials, their bulk density and tamped density being markedly increased and other important material properties being advantageously modified as a result of the mutual physical-mechanical action of the individual powder particles.

[0003] Graphitic materials, especially those with a high graphite content, are known per se and are used in industry in a variety of ways. High-purity graphitic carbons have xylene densities (also called single-crystal densities or real densities) ranging from 1.80 to 2.27 g.cm.sup.-3 and a crystal structure which can be characterized by a c/2 value of 0.3354 to 0.3360 nm and an L.sub.c value of more than 40 nm (L.sub.c>40 nm). These materials are obtained from natural sources, enriched and purified or produced synthetically from amorphous carbon products in a high temperature process. Subsequent grinding processes produce pulverulent materials with different mean particle sizes in each case. A given particle size for a powder is normally always a mean value of a specific particle size distribution. The particle size distribution to be used for a particular purpose depends especially on the composition of the graphitic material and the associated properties, as well as on the intended use.

[0004] The particle shape is always platelet-like, the anisotropy of the particles being the more pronounced the higher the xylene density and L.sub.c values. The Scott density (also referred to as bulk density) of such materials, for example with particle sizes smaller than 100 micron (particle size <100 .mu.m, determined by laser diffraction analysis), is normally below 0.25 g.cm.sup.-3, the Scott density being the lower the smaller the particle size. Comminution of the particles by grinding generally results in a lowering of the Scott density. The Scott density can be somewhat increased by an optimized particle size distribution. Thus, for example, Scott densities up to max. 0.3 g.cm.sup.-3 are achieved by an optimized composition of fine and coarse fractions for such materials with particle sizes below 100 micron.

[0005] The tamped density, the compressibility and the absorption capacity for polymeric binder materials and liquids such as oils, and for organic solvents and aqueous systems, are equally important properties of graphite powders. These properties correlate with the composition of the graphite powders and especially with the particle size distribution. It has now been found that, surprisingly, the values of the Scott density for a particular graphite powder of any particle size distribution is considerably increased when the graphite powder is subjected to an autogenous surface treatment in which the particles impact with one another at an appropriate speed and for a sufficient length of time. The impacts and the associated mutual physical-mechanical action change the structure or surface of the graphite particle in such a way as to result in a considerable increase in the Scott density. The other properties mentioned above are also modified to a considerable extent.

[0006] Under the electron microscope, the crude, ground, platelet-like graphite particle has an irregular shape and sharp edges. The irregular particle contours are abraded and the edges rounded off by the treatment according to the invention. If the energy dose is appropriately optimized, the grinding effect which occurs with other mechanical treatments, leading to a noticeable lowering of the bulk density, is considerably reduced or minimized. Although the abrasion of the particles creates dust, which, together with a minimal grinding effect, leads to a slight reduction in particle size and Scott density (bulk density), this particle size effect is far outweighed by the surprisingly large total increase in Scott density, and the change in the other properties, caused by the treatment according to the invention. The present invention can be at least partly explained by the observed changes in the particle contours, but the invention is not bound to this explanation.

[0007] The present invention is defined in the Claims. In particular, the present invention relates to a process for increasing the Scott density of graphite powders of any particle size distribution, characterized in that the graphite powder is subjected to an autogenous surface treatment.

BRIEF DESCRIPTION OF THE DRAWING

[0008] FIG. 1A is a diagram of an apparatus for treating graphite particles.

[0009] FIG. 1B is an alternative view of the apparatus in FIG. 1A.

[0010] The process of autogenous surface treatment consists in allowing the individual powder particles to impact with one another at a measured speed so that, as a result of the associated mutual physical-mechanical action of the individual particles, their surface structure changes but the individual particle remains substantially unbroken, i.e. no substantial grinding effect occurs. This change in the particle contour or surface structure of the individual particle gives rise to the increase in Scott density according to the invention. The autogenous surface treatment is carried out, and the individual particles are allowed to act on one another, until the desired Scott density is achieved. The measured speed means that the speed or energy with which the individual particles are charged is adjusted so that the particles do not disintegrate on impact or collision, thereby practically avoiding a grinding effect. This adjustment is a question of process optimization and does not present a problem to those skilled in the art.

[0011] The Scott density achievable by means of the optimized grinding effect for a graphite powder of any particle size distribution can be increased in each case by at least about 10% to about 100%, preferably by about 20% to 80%, by the autogenous surface treatment according to the invention. Hitherto unattained Scott densities of 0.45 g/cm.sup.3 or more are thus achieved for graphitic materials.

[0012] The tamped density achievable by means of the optimized grinding effect for a graphite powder of any particle size distribution can also be increased by at least about 10% to 100%, preferably by about 20% to 80%, by the process according to the invention. Hitherto unattained tamped densities of at least 0.90 g/cm.sup.3 are thus achieved for graphite powders.

[0013] In the case of particle sizes of <100 .mu.m, the autogenous surface treatment according to the invention is preferably carried out by fluidizing or dispersing the graphite powder particles in an inert carrier gas and accelerating the particles with the aid of the carrier gas, as described below. The intensity of this treatment is determined by the carbon type and the mass of the particles, their speed and the amount of material used per treatment, i.e. the concentration of the fluidized particles dispersed in the gas. The intensity of the treatment increases with the softness of the graphitic carbon used, the mass of the particles, their speed and the amount used. For particle sizes of <300 .mu.m, the dispersion and acceleration of the particles are preferably effected by means of rotating mechanical tools, for example in the present process by means of a turbine or directly by means of a rotating disk.

[0014] However, the grinding effect which occurs also increases simultaneously with increasing intensity of the treatment. Thus, to achieve the maximum bulk density of a material, there is a maximum intensity which results from the optimized parameters of particle speed, particle mass and amount used. The formation of agglomerates due to the agglutination of smaller particles, which would also lead to a sustained increase in the Scott density, has not been observed. Treated particles larger than the untreated particles used did not appear in any of the experiments performed. Analyses of the treated materials by scanning electron microscopy also showed no such agglomeration.

[0015] The treatment according to the invention not only increases the Scott density but also improves the compressibility properties of the graphite powders and reduces their absorption capacity for polymeric binder materials and liquids such as oils, organic solvents and aqueous systems. The crystallinity of the graphitic carbon particles, on the other hand, remains unaffected by the mechanical surface treatment. The structural parameters and the xylene density also remain unchanged compared with the untreated particles.

[0016] The process according to the invention also increases the pressed density achievable by the optimized grinding effect for a graphite powder of any particle size distribution by at least about 0.5% to 10%, preferably by about 1% to 8%. If the powders treated according to the invention are used to produce mouldings by compression under a pressure of 2.5 to/cm.sup.2, markedly higher pressed densities can be achieved compared with the untreated materials.

[0017] Furthermore, the powders treated according to the invention exhibit a markedly reduced oil absorption capacity and binder uptake ranging from about 10% to 50% and especially from an average of about 20% to 45%, values in excess of 50% also being obtainable. This effect is achieved by the treatment according to the invention because the porosity (pore structure) of the particles is not affected by the treatment, as can be demonstrated by the fact that the nitrogen adsorption properties and xylene densities hardly change.

[0018] Said markedly reduced absorption properties also result in markedly lower viscosities of dispersions of the graphite powders treated according to the invention in liquid media, so dispersions with a correspondingly increased solids content can be prepared with the graphite powders treated according to the invention. The solids content of liquid carbon dispersions can be increased by more than 5% to over 30% by using graphite powders treated according to the invention.

[0019] Graphite powders suitable for the use according to the invention are especially those with a high graphite content in the particle, and particularly so-called high-purity graphites, preferably with xylene densities ranging from 1.80 to 2.27 g.cm.sup.-3 and a crystal structure characterized by a c/2 value of 0.3354 to 0.3360 nm and an L.sub.c value of more than 40 nm (L.sub.c>40 nr). The powders can be obtained from natural sources or prepared synthetically from amorphous carbon products and can have any mean particle size and particle size distribution. Preferred pulverulent graphitic materials are those with a mean particle size of up to 150 .mu.m, preferably of 1 .mu.m to 50 .mu.m, and especially high-purity pulverulent graphites. Such graphites are known per se.

[0020] The process according to the invention is preferably carried out in such a way that the graphite powder particles to be treated are dispersed and fluidized in a gas. This can be done using any method of fluidization technology known per se in which the particles impact with one another in the fluidized state and thereby change their surface contours and surface structures, as is the case e.g. in a fluidized bed. However, to carry out the process according to the invention, the fluidized particles are preferably provided with higher speeds so that the particles fluidized in this way are accelerated with higher energies. Preferably, the fluidized particles are continuously concentrated and diluted again in the gaseous environment. The resulting collisions between the particles set in rotation, and the friction between them, result in surface abrasion of the particles, the energy transferred to the particles being adjusted so that the collisions and friction cause substantially no disintegration of the particles.

[0021] The process according to the invention can be put into optimum effect e.g. in the device shown in FIGS. 1A and 1B. This device consists specifically of a circular disk 100 with radial impact pins 101 flush-mounted on the rim, said disk being sheathed by a cylindrical treatment chamber 110 closed to the outside (turbine with associated turbine effect). The dimensions of the cylindrical treatment chamber 110 are adjusted so that it encloses the disk 100 and can allow some space between its inner wall and the rotating disk 100. The disk 100 is connected to a motor 160, located outside the treatment chamber 110, by means of a shaft 150 through the wall of the treatment chamber and can be set in rotation by this motor 160. The cylindrical treatment chamber is provided with a radial aperture 111 (hole). An additional aperture 112 (hole) is provided in the cylinder jacket of the treatment chamber 110, perpendicular to the disk and disk axis. Apertures 111 and 112 are connected by a tube 120 located outside the treatment chamber. Thus tube 120 running outside the treatment chamber 110 and attached to the wall of the treatment chamber 110, connects the periphery of the treatment chamber 110 to its centre. The gas (fluid) containing the fluidized particles, accelerated centrifugally by the rotating disk 100, circulates through this external treatment tube 120, exiting through the tube at the periphery of the treatment chamber 110 as a result of the centrifugal force and flowing back through the other end of this tube into the centre of the treatment chamber 110, where it is accelerated again. The particles of material are accelerated by the impact pins 101 of the rotating disk 100 and driven away in a peripheral direction by the centrifugal forces produced by the high-speed rotor. The particles dispersed and accelerated into the gas in this way circulate in the machine along the inside of the cylinder jacket. The particles reaching the inlet of the circulation tube, input 130 enter the tube and return to the treatment chamber in the region of the centre of the machine. This results in a continuous concentration and dilution of the particles in the surrounding gaseous medium. A fraction of the treated particles is continuously fed into input 130 or withdrawn from an attached tube, output 140, but the process can also be carried out as a batch process. The graphite powders treated according to the invention can advantageously be used as pigments in aqueous or solvent-based dispersions, thereby achieving higher solids contents than with untreated powders. The viscosity of liquid dispersions of materials treated according to the invention is markedly lower for the same solids content. Also, when dispersions according to the invention are applied to substrates and dried, coatings with markedly lower porosity values are obtained because the content of liquid phase is markedly lower. The higher solids content also means that smaller binder/carbon ratios are needed to stabilize a dried carbon coating on a substrate. The low polymeric binder contents result in a marked increase in the electrical and thermal conductivities of such carbon layers.

[0022] Dispersions containing mixtures of synthetic and/or natural graphitic carbons treated according to the invention and a polymeric binder in an aqueous or solvent-based medium can be applied to metal foils and dried to give stable coatings (for thicknesses of 10 to 5000 .mu.m) with an increased graphite/binder ratio and hence also increased electrical and thermal conductivities. The porosities of the dried films are normally below 50% and are thus appreciably lower than those of films formed of conventional graphites. Such dispersions can therefore advantageously also be used for gas-tight and liquid-tight coatings on metal substrates, which can be used as electrically conducting anticorrosive films on metal foils and plates.

[0023] The dried coatings formed by the graphites treated according to the invention can be compressed by a calender without the graphite film delaminating from the metal foil. This delamination from the metal foil is frequently observed with untreated graphites. The calendering of graphite films produced from graphite powders treated according to the invention affords coatings with porosities below 30% without altering the texture or particle structure of the graphite powders used. Such film coatings on metal foils, characterized by porosities below 30% and stabilized with lower binder/carbon ratios, can be used in lithium ion batteries as negative electrodes with charge densities above 550 Ah/l. The current-carrying capacity of such electrodes is markedly higher than that of electrodes made of conventional graphite powders. Such negative electrodes can thus be used very advantageously for lithium ion cells with a high power density.

[0024] The high packing density of the synthetic or natural graphites treated according to the invention, combined with the relatively low polymeric binder absorption capacity, is advantageous in the production of graphite/polymer composites which can be compressed to gas-tight graphite plates of high electrical conductivity. Such plates are advantageously used as bipolar plates in polymer electrolyte fuel cell technology.

[0025] Mixtures of polymers with synthetic or natural graphites or graphitic carbons treated according to the invention form thermoplastic or thermosetting composites with a higher proportion of carbon filler and a lower processing viscosity: Thermoplastic polymer/graphite composite materials with graphites treated according to the invention have higher (and hence improved) values in respect of their isotropic, mechanical, thermal and electrical properties and behave more isotropically than composites with untreated graphitic carbons.

[0026] Metallic non-ferrous sintered materials which have been produced with synthetic or natural graphitic carbons treated according to the invention, or contain such carbons, have improved isotropic, mechanical and tribological properties.

[0027] The Examples which follow describe the invention.

[0028] Examples 1 to 6 show the material properties of various graphites before and after the autogenous surface treatment according to the invention. The experiments were performed in the device described in the above section. The rotating disk used had a periphery of 0.75 m and a speed of rotation of 4800 rpm.

[0029] Examples 1-6 were carried out under the experimental conditions given in Table 1. TABLE-US-00001 TABLE 1 Type of Speed of Example graphite Amount used Treatment time rotating disk 1 TIMREX .RTM. 150 g 5 min 4800 rpm KS-graphite 2 TIMREX .RTM. 150 g 5 min 4200 rpm SLX-graphite 3 TIMREX .RTM. 150 g 5 min 4800 rpm SLM-graphite 4 TIMREX .RTM. 200 g 5 min 4800 rpm SFG-graphite 5 TIMREX .RTM. 200 g 7 min 4800 rpm NP-graphite 6 TIMREX .RTM. 200 g 5 min 4800 rpm KS 5-75 TT TIMREX .RTM. KS-graphite = TIMREX .RTM. KS 5-25 from TIMCAL AG TIMREX .RTM. SLX-graphite = TIMREX .RTM. SLX 50 from TIMCAL AG TIMREX .RTM. SLM-graphite = TIMREX .RTM. SLM 44 from TIMCAL AG TIMREX .RTM. SFG-graphite = TIMREX .RTM. SFG 44 from TIMCAL AG TIMREX .RTM. NP-graphite = TIMREX .RTM. NP 44 from TIMCAL AG

[0030] Examples 1 to 6 show a marked increase in Scott density (bulk density) and tamped density for the powders treated according to the invention. The treated powders exhibited no agglomerates whatsoever. The resulting change in particle size distribution is indicative of a small grinding effect. The slight lowering of d values, however, is caused especially by the dust produced by the abrasion of the particles. The pore structure of the treated particles is not affected by the surface treatment. It is assumed that the dust produced by the treatment and the slight decrease in particle size distribution are the main reason for the slight lowering of the L.sub.c values and the xylene densities. The elastic recovery of the compressed treated materials drops sharply. The pressed density of mouldings produced from the treated materials under a pressure of 2.5 to/cm.sup.2 increases sharply. Although the BET values are increased somewhat, the oil absorption and binder absorption of the particles treated according to the invention decrease markedly. Dispersions of treated carbon particles in liquid media exhibit markedly lower viscosities than dispersions of untreated carbon particles. The solids content of liquid carbon dispersions can be increased by more than 5% by using carbon particles according to the invention. The electrical resistance of the carbons treated according to the invention increases. The changes in surface contours of the individual particles which result from the treatment of powders according to the invention can be clearly seen from scanning electron micrographs.

Experimental Section

[0031] The particle size distribution of the materials was determined by laser diffraction analysis using a MALVERN Mastersizer. The structural parameters were obtained from X-ray diffraction experiments based on the CuK.sub..alpha.1 line. The crystallographic cell constant in the c direction (c/2) was determined from the relative position of the (002) or (004) diffraction reflex. The maximum height of the single-crystal domains in a particle in the crystallographic c direction, L.sub.c, and the resulting number of ideally stacked graphite planes were obtained from the (002) or (004) diffraction reflex according to the model of Scherrer and Jones (P. Scherrer, Gottinger Nachrichten 2 (1918) p. 98; F. W. Jones, Proc. Roy. Soc. (London) 166 A (1938) p. 16). The xylene density was determined according to DIN 51 901. Determination of the Scott density was based on ASTM B 329. The tamped density was determined according to AKK-19. The specific surface areas were determined by the method of Brunauer, Emmett and Teller using a Micromeritics ASAP 2010. To determine the elastic recovery, the material was placed under a pressure of 0.5 to/cm.sup.2. The recovery was obtained from the height of the moulding with and without applied pressure and is given in percent. The electrical resistance was measured according to DIN 51 911 using a moulding produced under a pressure of 2.5 to/cm.sup.2. The pressed density of this moulding is also given. The oil absorption was measured on the basis of DIN ISO 787 with initial weights of 0.5 g of material and 1.5 g of oil. The mixture was centrifuged in a Sigma 6-10 centrifuge for 90 min at a speed of 1500 rpm.

EXAMPLE 1

[0032] TABLE-US-00002 TIMREX .RTM. KS synthetic graphite TIMREX .RTM. KS synthetic graphite Untreated After treatment Particle size Particle size d.sub.10 = 7.0 micron d.sub.10 = 5.9 micron d.sub.50 = 15.2 micron d.sub.50 = 13.5 micron d.sub.90 = 30.2 micron d.sub.90 = 27.4 micron L.sub.c(002)/L.sub.c(004) L.sub.c(002)/L.sub.c(004) 120 nm/68 nm 101 nm/64 nm c/2 (002)/c/2 (004) c/2 (002)/c/2 (004) 0.3355 nm/0.3355 nm 0.3355 nm/0.3355 nm Xylene density Xylene density 2.254 g cm.sup.-3 2.248 g cm.sup.-3 Scott density Scott density 0.23 g cm.sup.-3 0.30 g cm.sup.-3 Tamped density Tamped density 0.539 g cm.sup.-3 0.674 g cm.sup.-3 BET specific surface area BET specific surface area 8.6 m.sup.2 g.sup.-1 9.3 m.sup.2 g.sup.-1 Elastic recovery Elastic recovery 17% 12.3% Electrical resistance Electrical resistance 1.911 m.OMEGA. cm 2.085 m.OMEGA. cm Oil absorption Oil absorption 113.5% .+-. 1.3% 64.3% .+-. 0.2% Pressed density (2.5 to/cm.sup.2) Pressed density (2.5 to/cm.sup.2) 1.863 g cm.sup.-3 1.957 g cm.sup.-3

EXAMPLE 2

[0033] TABLE-US-00003 TIMREX .RTM. SLX synthetic graphite TIMREX .RTM. SLX synthetic Untreated graphite After treatment Particle size Particle size d.sub.10 = 11.6 micron d.sub.10 = 7.4 micron d.sub.50 = 27.3 micron d.sub.50 = 20.4 micron d.sub.90 = 52.5 micron d.sub.90 = 40.8 micron L.sub.c(002)/L.sub.c(004) L.sub.c(002)/L.sub.c(004) >500 nm/232 nm 368 nm/158 nm c/2 (002)/c/2 (004) c/2 (002)/c/2 (004) 0.3354 nm/0.3354 nm 0.3354 nm/0.3354 nm Xylene density Xylene density 2.261 g cm.sup.-3 2.258 g cm.sup.-3 Scott density Scott density 0.30 g cm.sup.-3 0.38 g cm.sup.-3 Tamped density Tamped density 0.641 g cm.sup.-3 0.778 g cm.sup.-3 BET specific surface area BET specific surface area 4.0 m.sup.2 g.sup.-1 5.9 m.sup.2 g.sup.-1 Elastic recovery Elastic recovery 7.7% 4.6% Electrical resistance Electrical resistance 0.986 m.OMEGA. cm 1.166 m.OMEGA. cm Oil absorption Oil absorption 94.7% .+-. 11.9% 73.3% .+-. 1.9% Pressed density (2.5 to/cm.sup.2) Pressed density (2.5 to/cm.sup.2) 2.036 g cm.sup.-3 2.051 g cm.sup.-3

EXAMPLE 3

[0034] TABLE-US-00004 TIMREX .RTM. SLM synthetic TIMREX .RTM. SLM synthetic graphite Untreated graphite After treatment Particle size Particle size d.sub.10 = 7.3 micron d.sub.10 = 4.3 micron d.sub.50 = 23.2 micron d.sub.50 = 13.9 micron d.sub.90 = 49.4 micron d.sub.90 = 35.0 micron L.sub.c(002)/L.sub.c(004) L.sub.c(002)/L.sub.c(004) 241 nm/139 nm 196 nm/116 nm c/2 (002)/c/2 (004) c/2 (002)/c/2 (004) 0.3354 nm/0.3354 nm 0.3354 nm/0.3354 nm Xylene density Xylene density 2.254 g cm.sup.-3 2.252 g cm.sup.-3 Scott density Scott density 0.19 g cm.sup.-3 0.34 g cm.sup.-3 Tamped density Tamped density 0.408 g cm.sup.-3 0.738 g cm.sup.-3 BET specific surface area BET specific surface area 4.9 m.sup.2 g.sup.-1 7.7 m.sup.2 g.sup.-1 Elastic recovery Elastic recovery 14.0% 8.6% Electrical resistance Electrical resistance 1.278 m.OMEGA. cm 1.741 m.OMEGA. cm Oil absorption Oil absorption 109.5% .+-. 2.7% 75.0% .+-. 5.3% Pressed density (2.5 to/cm.sup.2) Pressed density (2.5 to/cm.sup.2) 1.930 g cm.sup.-3 2.036 g cm.sup.-3

EXAMPLE 4

[0035] TABLE-US-00005 TIMREX .RTM. SFG synthetic TIMREX .RTM. SFG synthetic graphite Untreated graphite After treatment Particle size Particle size d.sub.10 = 7.5 micron d.sub.10 = 4.4 micron d.sub.50 = 24.1 micron d.sub.50 = 15.0 micron d.sub.90 = 49.2 micron d.sub.90 = 35.5 micron L.sub.c(002)/L.sub.c(004) L.sub.c(002)/L.sub.c(004) 320 nm/138 nm 283 nm/199 nm c/2 (002)/c/2 (004) c/2 (002)/c/2 (004) 0.3354 nm/0.3354 nm 0.3354 nm/0.3354 nm Xylene density Xylene density 2.262 g cm.sup.-3 2.258 g cm.sup.-3 Scott density Scott density 0.20 g cm.sup.-3 0.36 g cm.sup.-3 Tamped density Tamped density 0.420 g cm.sup.-3 0.766 g cm.sup.-3 BET specific surface area BET specific surface area 5.9 m.sup.2 g.sup.-1 7.4 m.sup.2 g.sup.-1 Elastic recovery Elastic recovery 9.2% 5.6% Electrical resistance Electrical resistance 0.925 m.OMEGA. cm 0.986 m.OMEGA. cm Oil absorption Oil absorption 110.2% .+-. 6.4% 81.8% .+-. 6.9% Pressed density (2.5 to/cm.sup.2) Pressed density (2.5 to/cm.sup.2) 2.005 g cm.sup.-3 2.036 g cm.sup.-3

EXAMPLE 5

[0036] TABLE-US-00006 TIMREX .RTM. NP TIMREX .RTM. NP purified natural graphite purified natural graphite Untreated After treatment Particle size Particle size d.sub.10 = 6.6 micron d.sub.10 = 3.7 micron d.sub.50 = 23.0 micron d.sub.50 = 13.8 micron d.sub.90 = 49.5 micron d.sub.90 = 36.9 micron L.sub.c(002)/L.sub.c(004) L.sub.c(002)/L.sub.c(004) 364 nm/166 nm 255 nm/103 nm c/2 (002)/c/2 (004) c/2 (002)/c/2 (004) 0.3354 nm/0.3354 nm 0.3354 nm/0.3354 nm Xylene density Xylene density 2.263 g cm.sup.-3 2.258 g cm.sup.-3 Scott density Scott density 0.24 g cm.sup.-3 0.42 g cm.sup.-3 Tamped density Tamped density 0.495 g cm.sup.-3 0.862 g cm.sup.-3 BET specific surface area BET specific surface area 5.0 m.sup.2 g.sup.-1 7.9 m.sup.2 g.sup.-1 Elastic recovery Elastic recovery 4.9% 3.8% Electrical resistance Electrical resistance 0.910 m.OMEGA. cm 1.359 m.OMEGA. cm Oil absorption Oil absorption 107.2% .+-. 3.6% 58.9% .+-. 0.6% Pressed density (2.5 to/cm.sup.2) Pressed density (2.5 to/cm.sup.2) 2.066 g cm.sup.-3 2.064 g cm.sup.-3

EXAMPLE 6

[0037] TABLE-US-00007 TIMREX .RTM. KS TIMREX .RTM. KS purified natural graphite purified natural graphite Untreated After treatment Particle size Particle size d.sub.10 = 8.3 micron d.sub.10 = 3.1 micron d.sub.50 = 38.4 micron d.sub.50 = 38.4 micron d.sub.90 = 68.4 micron d.sub.90 = 68.4 micron L.sub.c(002)/L.sub.c(004) L.sub.c(002)/L.sub.c(004) 142 nm/62 nm 105 nm/52 nm c/2 (002)/c/2 (004) c/2 (002)/c/2 (004) 0.3355 nm/0.3355 nm 0.3356 nm/0.3356 nm Xylene density Xylene density 2.227 g cm.sup.-3 2.225 g cm.sup.-3 Scott density Scott density 0.44 g cm.sup.-3 0.46 g cm.sup.-3 Tamped density Tamped density 0.84 g cm.sup.-3 0.902 g cm.sup.-3 BET specific surface area BET specific surface area 4.1 m.sup.2 g.sup.-1 8.0 m.sup.2 g.sup.-1 Elastic recovery Elastic recovery 25% 14.68% Electrical resistance Electrical resistance 2.109 m.OMEGA. cm 2.311 m.OMEGA. cm Oil absorption Oil absorption 97.2% .+-. 1.6% 54.7% .+-. 0.8% Pressed density (2.5 to/cm.sup.2) Pressed density (2.5 to/cm.sup.2) 1.912 g cm.sup.-3 1.972 g cm.sup.-3

Claims

1-15. (canceled)

16. A process for increasing the pressed density of a starting graphite powder of any particle size distribution, the starting graphite powder chosen from synthetic graphitic carbon and natural graphitic carbon wherein the starting graphite powder has a high graphite content in the particle, comprising subjecting the starting graphite powder to an autogenous surface treatment in which individual graphite powder particles are allowed to impact with one another at a measured speed so that their surface structure changes while substantially retaining graphite particle shape without a substantial grinding effect occurring and wherein said autogenous surface treatment is carried out until the pressed density of the starting material has increased by at least about 0.5% to 10%

17. The process according to claim 16 wherein the graphite powder is high-purity graphite.

18. The process according to claim 16 wherein the graphite powder has a xylene density ranging from 1.80 to 2.27 g/cm.sup.3, a crystal structure characterized by a c/2 value of 0.3354 to 0.3360, and an L.sub.c value of more than 40nm (L.sub.c>40nm).

19. The process according to claim 16 wherein the graphite powder has a particle size of up to 150 .mu.m.

20. The process according to claim 19 wherein the graphite powder has a particle size of 1 pm to 50 .mu.m.

21. The process according to claim 16 wherein the autogenous surface treatment is carried out until the pressed density of the starting graphite powder has increased by about 1% to 8%.

22. The process according to claim 16 wherein the autogenous surface treatment is carried out by fluidizing or dispersing graphite powder particles with sizes of <100 .mu.m in an inert carrier gas with the aid of a carrier gas.

23. The process according to claim 16 wherein the autogenous surface treatment is carried out by dispersing graphite powder particles with sizes of <300 .mu.m by means of a rotating mechanical tool.

24. The process according to claim 23 wherein the rotating mechanical tool is a turbine.

25. A process for decreasing the absorption capacity of a starting graphite powder of any particle size distribution, the starting graphite powder chosen from synthetic graphitic carbon and natural graphitic carbon wherein the starting graphite powder has a high graphite content in the particle, comprising subjecting the starting graphite powder to an autogenous surface treatment in which individual graphite powder particles are allowed to impact with one another at a measured speed so that their surface structure changes while substantially retaining graphite particle shape without a substantial grinding effect occurring and wherein said autogenous surface treatment is carried out until the absorption capacity of the starting material has decreased by at least about 10% to 50%.

26. The process according to claim 25 wherein the graphite powder is high-purity graphite.

27. The process according to claim 25 wherein the graphite powder has a xylene density ranging from 1.80 to 2.27 g/cm.sup.3, a crystal structure characterized by a c/2 value of 0.3354 to 0.3360, and an L.sub.c value of more than 40 nm (L.sub.c>40 nm).

28. The process according to claim 25 wherein the graphite powder has an average particle size of up to about 150 .mu.m.

29. The process according to claim 28 wherein the graphite powder has an average particle size of about 1 .mu.m to 50 .mu.m.

30. The process according to claim 25 wherein the autogenous surface treatment is carried out until the absorption capacity of the starting graphite powder has increased by about 20% to 45%.

31. The process according to claim 25 wherein the autogenous surface treatment is carried out by fluidizing or dispersing graphite powder particles with sizes of <100 .mu.m in an inert carrier gas with the aid of a carrier gas.

32. The process according to claim 25 wherein the autogenous surface treatment is carried out by dispersing graphite powder particles with sizes of <300 .mu.m by means of a rotating mechanical tool.

33. The process according to claim 32 wherein the rotating mechanical tool is a turbine.

34. An apparatus for treating graphite particles comprising a cylindrical chamber comprising a base and a curved face, the cylindrical chamber further comprising a first aperture for graphite particles exiting the cylindrical chamber; a second aperture for graphite particles entering the cylindrical chamber; an internal disk for accelerating the graphite particles, having a diameter less than the inner diameter of the cylindrical chamber wherein the disk further comprises one or more impact pins and a rim; a motor for rotating the internal disk; a shaft for connecting the motor and the internal disk; and a tube for circulating graphite particles from the first aperture to the second aperture, further comprising an external input for adding graphite particles to the tube and an external output for removing graphite particles from the tube.

35. The apparatus of claim 34 wherein the first aperture is located on the curved face of the cylindrical chamber.

36. The apparatus of claim 34 wherein the second aperture located on the base of the cylindrical chamber.

37. The apparatus of claim 36 wherein the second aperture is located at about the center of the base of the cylindrical chamber.

38. The apparatus of claim 34 wherein the impact pins are mounted flush with the rim of the internal disk and extend towards the center of the internal disk.

39. The apparatus of claim 38 wherein the length of the impact pins are less than the radius of the internal disk.

40. The apparatus of claim 39 wherein the impact pins are located on a single face of the internal disk.

41. The apparatus of claim 40 wherein the impact pins are located on the face of the internal disk nearest to the second aperture.

42. The apparatus of claim 41 wherein the internal disk has a periphery of about 0.75m.

43. The apparatus of claim 34 wherein the motor rotates the internal disk at about 4800 rpm.

44. The apparatus of claim 34 wherein the graphite particles are added to the tube through the external input and removed from the circulation tube through the external output continuously.

45. A graphite powder subjected to the process of claim 16 or 25, having at least one property chosen from increased bulk density, decreased absorption capacity, and increased pressed density.

46. A graphite material with an average particle size of about 14 micron having a Scott density of about 0.30 g.cm.sup.-3; a tamped density of about 0.674 g.cm.sup.-3; a dibutyl phthalate (DBP) oil absorption of about 64 g DBP/100 g graphite; and a pressed density of about 1.957 g.cm.sup.-3.

47. A graphite material with an average particle size of about 20 micron having a Scott density of about 0.38 g.cm.sup.-3; a tamped density of about 0.778 g.cm.sup.-3; a dibutyl phthalate (DBP) oil absorption of about 73 g DBP/100 g graphite; and a pressed density of about 2.051 g.cm.sup.-3.

48. A graphite material with an average particle size of about 14 micron having a Scott density of about 0.34 g.cm.sup.-3; a tamped density of about 0.738 g.cm.sup.-3; a dibutyl phthalate (DBP) oil absorption of about 75.0 g DBP/100 g graphite; and a pressed density of about 2.036 g.cm.sup.-3.

49. A graphite material with an average particle size of about 15 micron having a Scott density of about 0.36 g.cm.sup.-3; a tamped density of about 0.766 g.cm.sup.-3; a dibutyl phthalate (DBP) oil absorption of about 81.8 g DBP/100 g graphite; and a pressed density of about 2.036 g.cm.sup.-3.

50. A graphite material with an average particle size of about 14 micron having a Scott density of about 0.42 g.cm.sup.-3; a tamped density of about 0.862 g.cm.sup.-3; a dibutyl phthalate (DBP) oil absorption of about 58.9 g DBP/100 g graphite; and a pressed density of about 2.064 g.cm.sup.-3.

51. A graphite material with an average particle size of about 38 micron having a Scott density of about 0.46 g cm.sup.-3; a tamped density of about 0.902 g.cm.sup.-3; a dibutyl phthalate (DBP) oil absorption of about 54.7 g DBP/100 g graphite; and a pressed density of about 1.972 g.cm.sup.-3.

52. A graphite material having a Scott density of about 0.45 g/cm.sup.3 or greater.

53. A graphite material having a tamped density of about 0.90 g/cm.sup.3 or greater.

54. A liquid dispersion comprising a detectable amount of at least one graphite material of any one of claims 46 to 53 and a liquid.

55. The liquid dispersion of claim 54, having an increased solids content.

56. The liquid dispersion of claim 55, wherein the solids content is increased by about 5% to about 30%.

57. A coating on a metallic substrate, the coating comprising a detectable amount of at least one graphite material of claim 45 and a polymeric binder.

58. A negative electrode of a lithium ion battery comprising the coating of claim 57.

59. A lithium ion battery comprising the negative electrode of claim 58.

60. A composite comprising a thermoplastic or thermosetting polymer and a detectable amount of at least one graphite material of claim 45.

61. The composite of claim 60, compressed to provide a graphite plate of high electrical conductivity.

62. An electrolyte fuel cell, comprising the graphite plate of claim 61 as a bipolar plate.

63. A metallic sintered material comprising a detectable amount of at least one graphite material of claim 45 wherein the metallic sintered material is substantially free of iron.