Preparing an intercalation compound

Abstract: A conductive coating composition comprising a graphite intercalation compound, carbon black, a binder, and a solvent is provided. The graphite intercalation compound is prepared by a process comprising reacting a dried metal chloride, a salt capable of forming a molten salt together with the metal chloride, and a graphite in a molten state in a chlorine gas stream under atmospheric pressure or a process comprising reacting a dried metal chloride, a salt capable of forming a molten salt together with said metal chloride, a salt capable of forming a double salt in a gas phase together with the metal chloride, and a graphite in a molten state in a chlorine gas stream under atmospheric pressure.

Description: The present invention relates to a process for preparing a graphite intercalation compound. A conductive coating composition known in the art comprises a fine powder having electrically conductive materials therein, such as silver, copper, nickel, or graphite and carbon black, dispersed in various binders and solvents. When the metallic fine powder is used, an electrical conductivity of about 10⁻⁵ Ω.cm in terms of volume specific resistance is obtained. However, silver is not only very high in terms of price per unit weight of the composition but is also subject to large price fluctuations. The powder of the other metals undergoes chemical change, such as oxidation and other phenomenon occur, such as migration, wherein the fine metallic powder migrates between adjacent coating films. Although a coating composition containing carbon black dispersed therein brings about no problem accompanying the use of the fine metallic powder, the electrical conductivity is not very high and 10⁻² Ω.cm at the highest. It is known that a conductive coating composition prepared by graft polymerizing various monomers in a solvent and dispersing carbon black therein is mixed with a silver dispersion coating composition for the purpose of preventing the migration of silver in a coating composition containing silver dispersed therein. However, this expedient is disadvantageous in that the conductive coating composition is poor in the compatibility with the silver dispersion coating composition. On the other hand, as is known, a graphite intercalation compound (hereinafter abbreviated to "GIC") comprises graphite and various metals or compounds intercalated between crystalline layers of the graphite. Known metals which are intercalated into graphite include alkali metals such as Li, Na, and K and known compounds which are intercalated into graphite include metal halides such as SbF₅, CuCl₂, NiCl₂, and FeCl₂ and acid compounds such as HNO₃ and H₂SO₄. The above-described GIC has attracted attention as a substitute for metals because it has excellent electrical conductivity, and various processes for preparing GIC are known. For example, GIC wherein a metal chloride is intercalated is prepared by the following process (a) or (b). (a) A process in which a mixture of an anhydrous metal chloride with graphite or a mixture of a molten salt of a metal chloride with graphite is heated in vacuo, in an inert gas or in a chlorine gas atmosphere. In this process, a reaction is usually conducted by putting a mixture of the starting materials in a glass tube or putting graphite and metal chloride at different positions in a glass tube, melt-sealing or sealing the glass tube, and heating the glass tube at 400 to 500°C to react the starting materials. (b) A process in which a mixture of graphite with a metal chloride is heated in a chlorine gas stream. Chemical Abstracts, vol. 108, no. 8, February 1988, page 160, Abstract No. 58888K, is concerned with the manufacture of graphite-metal chloride intercalation compounds by reacting a fused metal chloride salt with graphite in an inert atmosphere. Since process (a) uses a melt-sealed or sealed glass tube or vessel, it is unsuitable for production of GIC on a commercial scale. Specifically, there is no vessel material suitable for heating a metal chloride at 400°C or above except for glass. Furthermore, although depending upon the kind of metal chlorides used, a considerable internal pressure builds up at such a high temperature due to the vapour pressure of a metal chloride itself and a chlorine gas generated by thermal dissociation of the chloride, so that it is very difficult to use a glass vessel having a large opening in a sealed state. Further, in process (a), the reaction rate is low and the reaction time is as long as at least a day, which also makes it difficult to prepare GIC on a commercial scale. In the case of process (b) as well, the reaction rate is low, and it takes several to ten days or longer to prepare GIC containing an intended amount of a metal, a compound, or the like intercalated between crystalline layers thereof. EP-A-0212940 teaches a production process of a graphite intercalant compound in which the intercalation is a metal chloride. The reaction is carried out in the presence of a second metal chloride of a relatively low boiling point. The addition of the second metal chloride permits the reaction to proceed in the absence of chlorine gas. A first object of the present invention is to provide an industrial process for preparing GIC as a component of a conductive coating composition. A second object of the present invention is to provide an industrial process for preparing highly heat-resistant GIC comprising a high melting point metal chloride intercalated between crystalline layers of graphite. According to the present invention there is provided a process for preparing a graphite intercalation compound, comprising reacting, in a chlorine gas stream, graphite with a) a dried metal chloride and a salt which forms a melt with said metal chloride, and b) optionally a further salt which forms a double salt in the gas phase with said metal chloride. Process (a) for preparing GIC comprises reacting a dried metal chloride, a salt capable of forming a molten salt together with the metal chloride and graphite in a chlorine gas stream in a molten state under atmospheric pressure. Examples of the metal chloride to be intercalated into graphite include CdCl₂, CuCl₂, CoCl₂, NiCl₂, and CrCl₃. Among them, CdCl₂, CuCl₂, CoCl₂, NiCl₂, and CrCl₃ are preferable. The above-described metal chlorides are used in combination with a salt for forming a molten salt of these metal chlorides. KCl, NaCl, CaCl₂, etc. are used as a salt for forming a molten salt, among which KCl and NaCl are preferable from the viewpoint of cost, easiness of recovery, and handleability. KCl and NaCl may be used alone or in the form of a mixture of them. In general, the combination of the metal chloride with the salt for forming a molten salt and proportions of the metal chloride and the salt can be selected from a molten salt phase diagram described in, e.g., Phase Diagrams for Ceramists; Phase Diagrams, A Literature Source Book, Parts A and B, and various related technical journals etc. The combination of the metal chloride with the salt for forming a molten salt and composition at the eutectic point picked up from the above literature for use in the present invention are shown in the following Table 1. The combination of the metal chloride with the salt for forming a molten salt used in the present invention is not limited to a particular one, and any combination may be used. In the present invention, the metal halide intercalated into graphite is used in an amount larger than the ratio at the eutectic point of the metal chloride to the salt for forming a molten salt together with the chloride. This is to surely intercalate the metal chloride into graphite. Although the amount of the excessive metal chloride is varied depending upon the combination of the metal chloride with the salt for forming a molten salt, the metal halide intercalated into graphite is generally used in an amount 5 to 10 times larger than the composition of the metal chloride at the eutectic point. The proportion of the metal chloride relative to graphite is also varied depending upon the kind of the metal chloride, and the metal chloride is used in an amount of 0.5 to 1.2 mol per mol of graphite. For examples, in the case of CuCl₂-KCl, the metal chloride is used in an amount of at least 0.82 mol (0.67 mol in the case of KCl) per mol of graphite. Although the upper limit is varied depending upon the temperature, CuCl₂ may be used in such an amount as will not bring about the coexistence of solid phase CuCl₂ in the molten reaction system. When the amount of CuCl₂ is less than 0.82 mol, it becomes difficult to prepare a low stage GIC. The graphite used in the present invention may be any of natural graphite and powdery, fibrous and sheet-like artificial graphite, and single crystal artificial graphite known as HOPG. The graphite is preferably purified natural graphite having a fixed carbon content of more than 99%. It is preferred from the viewpoint of preparation of an intercalation compound that the graphite have a large particle size. When graphite having a larger average particle diameter is used, a lower stage GIC is prepared. However, when the average particle diameter is too large, it becomes difficult to conduct screen process printing. For this reason, the graphite used has an average particle diameter of generally 20 to 70 µm, preferably 40 to 50 µm and a particle size distribution of 5 to 140 µm, preferably 20 to 100 µm. In the present invention, it is preferred that the above-described individual starting materials are sufficiently dried prior to the reaction. In particular, when the metal chloride has water of crystallization, insufficient dehydration makes it very difficult to intercalate the metal chloride into the graphite. Therefore, it is particularly preferred that, in addition to the drying of the graphite, the hydrous metal chloride be sufficiently dried. The reaction is conducted by homogeneously mixing a metal chloride, a salt for forming a molten salt of the metal chloride, and graphite, placing the mixture in a glass vessel, and passing a chlorine gas through the reaction system under atmospheric pressure while heating and melting the mixture. By this reason, there is prepared an intended graphite intercalation compound. It is not always necessary to pass the chlorine gas through the reaction mixture, and satisfactory results can be attained simply by flowing the chlorine gas above the reaction mixture. The chlorine gas may be used in such an amount as will supplement the chlorine gas formed by the decomposition of the metal chloride. The reaction is conducted under atmospheric pressure. There is no need of using an autoclave or melt-sealing or sealing the vessel. The reaction temperature is 380 to 450° C. When the reaction temperature is lower than 380° C, there is a possibility that a solid phase component might coexist in the liquid phase. On the other hand, when the reaction temperature exceeds 450° C, it is difficult to prepare a low stage GIC. It is not particularly necessary to conduct agitation during the reaction. However, when a reaction vessel having a large capacity is used, it is preferred that agitation be conducted in order to uniformly progress the reaction. According to process (A) for preparing GIC, a molten salt can be prepared from a metal chloride and a salt for forming a molten salt of the metal chloride. Therefore, in this process, not only the reaction temperature may be by 50 to 80° C lower than that of the case where a metal salt is reacted alone with the graphite,but also it is possible to conduct a homogeneous reaction in a liquid phase. Further, since the reaction is conducted under atmospheric pressure, the use of a glass vessel suffices for attaining the purpose, so that it possible to use a glass vessel having a large capacity. There is no need of using an autoclave. Further, since the reaction is conducted in a chlorine gas stream, it is possible for the reaction rate to be remarkably improved through the function of the chlorine gas similar to that of a catalyst with respect to the reaction for intercalating the metal salt into the graphite layer. Therefore, the present invention is suitable for the preparation of a graphite intercalation compound on a commercial scale. Process (B) for preparing GIC will now be described. As can be seen in the following Table 2, GIC containing a metal chloride intercalated thereinto has a tendency that its thermal stability (ceiling temperature of GIC in continuous use) is improved with the rise of the melting point of the intercalated metal chloride of GIC. For example, the stability of GIC of CuCl₂ (ceiling temperature of GIC in continuous use: 150° C) is superior to that of GIC of AlCl₃ or FECl₃ (ceiling temperature of GIC in continuous use: 150° C). GICs of CdCl₂, CoCl₂, NiCl₂ and CrCl₃ have higher ceiling temperature in continuous use than that of GIC of CuCl₂, i.e., is superior to GIC of CuCl₂ in the heat resistance. This fact shows that excellent electromagnetic and infrared shielding materials can be provided by using GIC of a metal chloride having a high melting point as a conductive coating, a plastic filler or the like. Accordingly, process (B) for preparing GIC provides a process for efficiently preparing GIC exhibiting excellent stability particularly at high temperatures and excellent electrical conductivity. metal chloride melting point (° C) ceiling temp. of GIC in continuous use (° C) AlCl₃ 190 < 150 FeCl₃ 303 < 150 CdCl₂ 568 275 CuCl₂ 598 150 CoCl₂ 735 275 NiCl₂ 993 325 CrCl₃ 1150 500 In the process (B) for preparing GIC, a dried metal chloride, a salt for forming a molten salt of the metal chloride, a salt for forming a double salt in a gas phase together with the metal chloride, and graphite are reacted with each other in a molten state in a chlorine gas stream under atmospheric pressure. The description about the metal chloride and the salt for forming a molten salt of the metal chloride given above in connection with process (A) is applicable to the case of process (B). An important feature of process (B) resides in the use of a salt for forming a double salt in a gas phase together with a metal chloride to be intercalated into graphite. Specific examples of the salt for forming a double salt in a gas phase include AlCl₃ and FeCl₃. The amount of addition of this salt is 1 to 3% by weight based on the total amount of the metal chloride to be intercalated and the salt for forming a molten salt of the metal chloride. When the amount of addition of the salt for forming a double salt in a gas phase is less than 1% by weight, it is impossible to sufficiently promote the reaction for intercalating the metal chloride into the graphite. On the other hand, when the amount exceeds 3% by weight, the formed double salt is discharged together with the chlorine gas outside the reaction system and cooled to solidify, which hinders the flowing of the chlorine gas. AlCl₃ and FeCl₃ may be used alone or in the form of a mixture of them. The addition of the salt for forming a double salt in a gas phase enables the reaction for intercalating the metal chloride into graphite to be remarkably promoted. The reason why the reaction is promoted by the addition of a salt for forming a double salt in a gas phase has not been yet elucidated. However, M. Schäfer: Z. anorg. allg. Chem., 403 , 116-126 (1974) and E. Stumpp: Materials Science & Eng. 31 , 53-59 (1977) each describe that, for example, AlCl₃ and a metal chloride form a stable salt in a gas phase as shown in the following formula and the double salt dissociates into the initial salts at a low temperature: wherein M is a metal atom. Therefore, it is believed that this double salt promotes the reaction for intercalating the metal chloride into graphite. In the present invention, it is preferred that the above-described individual starting materials are sufficiently dried prior to the reaction. In particular, when the dehydration of a metal chloride having water of crystallization and a salt for forming a double salt in a gas phase is insufficient, it becomes difficult to intercalate the metal chloride into the graphite. Therefore, it is particularly preferred that, in addition to the drying of the graphite, the hydrous metal chloride and the salt for forming a double salt in a gas phase be sufficiently dried to remove the water of crystallization and adherent water. In process (B), the reaction is conducted by homogeneously mixing a metal chloride, a salt for forming a molten salt of the metal chloride, a salt for forming a double salt in a gas phase together with the metal salt, and graphite, placing the mixing in a glass vessel, heating the mixture under atmospheric pressure to prepare a melt, and flowing a chlorine gas above the melt. By this reaction, there is prepared an intended graphite intercalation compound. The chlorine gas may be used in such an amount as will supplement the chlorine gas formed by the decomposition of the metal chloride. There is no need of using an autoclave or melt-sealing or sealing the glass vessel. The reaction is conducted at a temperature by 10 to 20° C higher than the eutectic point of the formed molten salt, i.e. usually at 380 to 450° C. As with the case of process (A), the metal chloride is kept at a proportion higher than that at the eutectic point. This is to surely intercalate an intended metal chloride into graphite. It is not particularly necessary to conduct agitation during the reaction. However, when a reaction vessel having a large capacity is used, it is preferred that agitation be conducted in order to uniformly progress the reaction. In the above-described process (B) as well, as described above, GIC can be easily prepared through a reaction in a chlorine gas stream in a molten state under atmospheric pressure, which makes it possible to prepare GIC in a gas vessel on a commercial scale. In particular, in process (B), the addition of a salt for forming a double salt together with a metal chloride enables the reaction for intercalating a metal chloride having a high melting point into graphite to be remarkably promoted. The present invention will now be described with reference to the following Examples. Example 1: A 1000-ml heat-resistant round-bottom flask and a four-necked lid which can be fitted onto the flask were provided. The lid was equipped with a glass agitator, chlorine gas inlet and outlet tubes, and a thermometer. The above vessel was charged with 4.1 mol of CuCl₂.2H₂O and 3.35 mol of KCl. The mixture was heated in vacuo to remove water of crystallization and adherent water. 5 mol (60 g) of natural graphite (ash content: 0.3%; average particle size: 45 µm; particle size distribution: 20 to 100 µm) was added thereto and the vacuum dehydration was further continued, followed by heating of the mixture. Since the metal salt melted at 400° C, the agitator was rotated, and a chlorine gas was passed through the flask. The chlorine gas was discharged after neutralization with an aqueous NaOH or Ca(OH)₂ solution. The heating of the mixture at 420° C was continued for 4 hr, and the mixture was then allowed to stand for cooling. Then, water was added thereto to elute unreacted CuCl₂ and KCl, thereby separating GIC. The GIC was filtered and dried in vacuo to obtain a product. Water of the recovered aqueous solution of unreacted metal chloride was evaporated in vacuo to recover the metal chloride. The recovered metal chloride can be reused. The yield of GIC was 89 g and it was found from a calculation based on the chemical formula C 6n CuCl₂ (wherein n is the number of stage) that the GIC thus prepared is that of stage 2. This was confirmed also from an X-ray diffraction pattern. The electrical conductivity was measured by kneading GIC with carbon black, a binder, and a solvent to prepare a paste, applying the paste to a polyester film, and measuring the resistance of the coating film. As a result, it was found that the resistance of the coating film was 2.8 x 10⁻³ Ω.cm. By contrast, the resistance of a paste prepared by using graphite instead of GIC was 1.5 x 10⁻² Ω.cm. Example 2: A reaction (reaction time: 4 hr) for preparation of GIC was conducted in the same manner as that of Example 1, except that 4 mol of CoCl₂ was used instead of CuCl₂.2H₂O and 5 mol (60 g) of graphite and 5.7 mol of NaCl were used. Thus, there was prepared 82 g of CoCl₂GIC. It was found from an X-ray diffraction pattern that the GIC thus prepared is that of stages 2 and 3. Example 3: A reaction for preparation of GIC was conducted in the same manner as that of Example 1, except that the following two kinds of graphite were used instead of the graphite used in Example 1: average particle diameter: 300 µm and 10 µm, particle size distribution: 1000 to 100 µm and 1 to 40 µm, ash content: 0.3% in both kinds. The yields of GIC were 84 g and 78 g, respectively. It was found from an X-ray diffraction pattern that these GIC were that of stages 2 to 3 and that of stage 6, respectively. A paste was prepared in the same manner as that of Example 1 for measurement of the resistance. As a result, it was found that the resistance of the pastes were 4.3 x 10⁻³ Ω.cm and 5.6 x 10⁻³ Ω.cm, respectively. Comparative Example 1: The reaction of Example 1 was conducted without supplying a chlorine gas to prepare 63 g of a product. It was found from an X-ray diffraction pattern of the product that the reaction for a period of 4 hr brought about no intercalation of the metal chloride into the graphite. Comparative Example 2: A reaction for preparation of GIC was conducted in the same manner as that of Example 1, except that the starting materials, i.e., CuCl₂.2H₂O and KCl, were simultaneously dried before the reaction was conducted. A reaction product was taken out 4 hr after the initiation of the reaction. It was found that there occurred no intercalation of CuCl₂ into the graphite. Comparative Example 3: A reaction for preparation of GIC was conducted in the same manner as that of Example 1, except that CuCl₂.2H₂O and KCl were used in amounts of 2.7 mol and 2.2 mol per mol of graphite, respectively, i.e., the amounts of the metal chlorides were reduced to 2/3. The yield of GIC 4 hr after the initiation of the reaction was 73.5 g, and the GIC thus prepared was that of stage 6. A conductive coating was prepared from the GIC, and the resistance was measured. As a result, it was found that the resistance of the coating is 9.2 x 10⁻³ Ω.cm. Example 4: A 1000-ml heat-resistant round-bottom flask and a four-necked lid which can be fitted onto the flask were provided. The lid was equipped with a glass agitator, chlorine gas inlet and outlet tubes, and a thermometer. The above vessel was charged with 4 mol of CrCl₃, 2.35 mol of NaCl, and 15 g of AlCl₃ (2% by weight based on the total amount of CrCl₃ and NaCl). The mixture was heated in vacuo to remove adherent water. Thereafter, 5 mol (60 g) of natural graphite (ash content: 0.3%; average particle size: 45 µm; particle size distribution: 20 to 100 µm) was added thereto, and the vacuum dehydration was further continued, followed by heating of the mixture. Since the salts melted at 450° C, the agitator was rotated, and a chlorine gas was passed through the flask. After the mixture was heated at 460° C for 4 hr, it was allowed to stand for cooling. Then water was added thereto to elute unreacted CrCl₃, NaCl, etc., thereby separating GIC. The GIC was then filtered and dried in vacuo to obtain a product. The yield of GIC was 87.5 g and the analysis of an X-ray diffraction pattern has revealed that the GIC thus prepared is a mixture of that of stage 2 and that of stage 3. The amount of AlCl₃ contained in GIC was very small. Example 5: A reaction for preparation of GIC was conducted in the same manner as that of Example 4, except that instead of CrCl₃ used in Example 4, 4 mol of NiCl₂, 10 mol of KCl, 18 g of AlCl₃ (1.4% by weight based on the total amount of NiCl₂ and KCl), and 5 mol (60 g) of graphite were used and the mixture was heated at 515° C [eutectic point 507° C; NiCl₂ 28 mol%, KCl 72 mol%] for 4 hr. Thus, there was prepared 74.5 g of NiCl₂ GIC. It was found from an X-ray diffraction pattern that the GIC thus prepared was a mixture of that of stage 2 and that of stage 3. Example 6: A reaction for preparation of GIC was conducted in the same manner as that of Example 4, except that instead of CrCl₃ used in Example 4, 4 mol of CdCl₂, 2.8 mol of NaCl, 18 g of FeCl₃ (2% by weight based on the total amount of CdCl₂ and NaCl), and 5 mol (60 g) of graphite were used and the reaction was conducted at 420° C [eutectic point 397° C; CdCl₂ 58 mol%, KCl 42 mol%; D.L. Dreadmore., J.Am. Ceram. Soc., 43 , 593(1960)] for 4 hr. Thus, there was prepared 132 g of GIC of CdCl₂. It was found from an X-ray diffraction pattern that the GIC thus prepared was a mixture of that of stage 1 and that of stage 2. Comparative Example 4: A reaction for preparing GIC was conducted in the same manner as that of Example 4, except that AlCl₃ was not added. Thus, there was prepared 76.5 g of GIC of CrCl₃. It was found from an X-ray diffraction pattern that the GIC thus prepared was a mixture of that of stage 5 and that of stage 6. Comparative Example 5: A reaction for preparing GIC was conducted in the same manner as that of Example 5, except that AlCl₃ was not added. Thus, there was prepared 78.6 g of GIC of NiCl₂. It was found that the GIC thus prepared was a mixture of those of stages 6 and above. Comparative Example 6: A reaction for preparing GIC was conducted in the same manner as that of Example 6, except that FeCl₃ was not added. Thus, there was prepared 83 g of GIC of CdCl₂. It was found that the GIC thus prepared was a mixture of those of stages 4 to 60. Example 7: 13 g of a binder composed of a modified ether type polyester (Stafix P-LC; a product of Fuji Photo Film Co., Ltd.) was dissolved in 60 g of a solvent composed of EGDA while heating and agitating. 16.2 g (corresponding to 10 g of graphite) of GIC containing CuCl₂ intercalated thereinto (stage 3) which had been prepared in the same manner as that of Example 1, and 4.3 g of carbon black (Ketjen Black EC; a product of Nippon EC Co., Ltd.) were added thereto. The mixture was kneaded with an ink roll while sufficiently agitating to prepare a composition. The viscosity of the composition was 280 P. The amount of carbon (GIC in terms of graphite + CB) was 110 parts by weight based on 100 parts by weight of the binder resin. The ratio of graphite to CB was 7 : 3. Further, the volatile content was 64%. This composition was applied to a polyethylene terephthalate film (thickness: 125 µm) by screen printing to have a size of 60 mm x 60 mm. The resultant coating film was dried at 120° C for 15 min to cure the coating film, allowed to cool, and then subjected to the measurement of resistance with four probes for a surface ohmmeter. The volume specific resistance was 3.44 x 10⁻³ Ω.cm. Other physical properties of the coating film were as follows. The pencil hardness of the coating film was HB. The volume specific resistance as determined after bending at 180° and that after bending at 360° were 3.81 x 10⁻³ Ω.cm and 4.06 x 10⁻³ Ω.cm, respectively. Six fine lines each having a size of 2 mm x 60 mm were printed and subjected to the measurement of resistance. The variation in the resistance values was 7.7 to 16.7%. The composition was mixed with an equal amount of a silver paste ink (5007; a product of E.I. duPont de Nemours & Co.). The mixture was neither separated into two phases nor became turbid. The heat resistance, moisture resistance, and heat cycle of the composition were measured. The results are shown in the following Table. The conditions for the measurement were as follows: resistance: expressed in terms of volume specific resistance heat resistance: heated at 100° C moisture resistance: 50° C, 90%RH heat cycle: -30° C x 90° C, 12 hr for each cycle resistance before test (Ω.cm) resistance after 192 hr (Ω.cm) rate of change (%) resistance after 264 hr (Ω.cm) rate of change (%) heat resistance 2.44x10⁻³ 2.44x10⁻³ ± 0 2.37x10⁻³ -2.8 moisture resistance 6.36x10⁻³ 6.02x10⁻³ -5.3 6.53x10⁻³ +2.6 heat cycle 3.44x10⁻³ 3.32x10⁻³ -3.3 3.62x10⁻³ +5.3 Note: The heat resistance and moisture resistance tests were conducted by allowing the sample to stand under test conditions for one day and then at room temperature for one day. The test on the adhesion to a substrate film was conducted according to the cross cut cellophane adhesive tape method (JIS D 0202). With respect to each composition prepared in this Example and the Examples which will be described later, the adhesion was 100/100. Example 8: A coating composition was prepared from GIC containing CoCl₂ intercalated thereinto (stages 3 to 4) which had been prepared in the same manner as that of Example 1 in such a manner that the ratio of GIC to CB (Ketjzen Black EC) was 7 : 3, the PHR of carbon (in terms of graphite) relative to the binder (Stafix) was 110, and the amount of the solvent (EDGA) was such that the volatile content was 64%. The resistance of the coating film was 3.86 x 10⁻³ Ω.cm in terms of the volume specific resistance. The resistance after bending at 180° and that after bending at 360° were 4.32 x 10⁻³ Ω.cm and 4.61 x 10⁻³ Ω.cm, respectively. The variation in the resistance values as determined by making use of fine lines was 5.8 to 11.4%. Comparative Example 7: A composition was prepared and tested in the same manner as that of Example 7, except that 10 g of graphite SP-5 was used instead of 16.2 g of GIC. The volume specific resistance was 1.2 x 10⁻² Ω.cm, the pencil hardness of the coating film was H, and the resistance after bending at 180° and that after bending at 360° were 1.31 x 10⁻² Ω.cm and 1.42 x 10⁻² Ω.cm, respectively. The variation in the resistance values as determined by making use of fine lines was 6.4 to 13.5%. Comparative Example 8: Two kinds of carbon black, i.e., SP-20 manufactured by Nippon Graphite Industries, Ltd. having an average particle size of 45 µm and a particle size distribution of 1 to 25 µm and MBC-50 manufactured by the same company having an average particle size of 300 µm and a particle size distribution of 150 to 420 µm, were each reacted with CuCl₂ to prepare GICs. The GICs thus prepared were both those of stage 3. Compositions were prepared from these GICs in the same manner as that of Example 1. These compositions each had a carbon PHR of 110, a graphite to CB ratio of 7/3, and a volatile content of 66%. The volume specific resistance of each coating film was measured and found to be 1.3 x 10⁻² Ω.cm and 2.2 x 10⁻² Ω.cm, respectively. The resistance after bending at 180° and that after bending at 360° were 1.42 x 10⁻² Ω.cm and 1.47 x 10⁻² Ω.cm, respectively, for one sample and 2.5 x 10⁻² Ω.cm and 2.61 x 10⁻² Ω.cm, respectively, for the other sample. The variation in the resistance values determined by making use of six fine lines each having a size of 2 mm x 60 mm was 4.91 to 44.1% due to the influence of the particle size of the graphite. Comparative Example 8: A composition was prepared in the same manner as that of Example 1, except that GIC was used in an amount of 23.2 g (corresponding to 14.3 g of graphite) instead of 16.2 g and no Ketjen Black EC was used. The resistance of a coating film prepared from the composition was measured. The PHR value and the volatile content were 110 and 60%, respectively. The volume specific resistance was 2.6 x 10⁻² Ω.cm and the resistance after bending at 180° and that after bending at 360° were 2.81 x 10⁻² Ω.cm and 3.59 x 10⁻² Ω.cm, respectively. The variation in the resistance values was 18.7%.

Claims: A process for preparing a graphite intercalation compound, comprising reacting, in a chlorine gas stream, graphite with a) a dried metal chloride and a salt which forms a melt with said metal chloride, and b) optionally a further salt which forms a double salt in the gas phase with said metal chloride. A process according to claim 1, wherein said metal chloride is used in an amount larger than the proportion of said metal chloride at the eutectic point of a melt comprising said metal chloride and said salt capable of forming a melt. A process according to claim 1 or claim 2, wherein the amount of said metal chloride per mol of graphite ranges from at least 0.5 mol to such an amount as will not bring about the coexistence of a solid phase metal chloride in the molten reaction system. A process according to any preceding claim, wherein said graphite has an average particle diameter of 20µm to 70µm. A process according to any preceding claim, wherein said reaction is conducted at a temperature of 380°C to 450°C. A process according to any preceding claim, wherein said metal chloride is selected from the group consisting of CuCl₂, CdCl₂, CoCl₂, NiCl₂, and CrCl₃. A process according to any preceding claim, wherein said salt which forms a melt with said metal chloride is selected from KCl and Nacl. A process according to any preceding claim, wherein said further salt is employed and is selected from AlCl₃ and FeCl₃. A process according to any preceding claim, wherein said further salt which forms a double salt in the gas phase with said metal chloride is added in an amount of 1% to 3% by weight based on the total weight of said metal chloride and said salt which forms a melt with said metal chloride. A process according to any preceding claim which is carried out under atmospheric pressure.

Inventors: NISHINO HIROSHI, NISHINO, HIROSHI
Applicants: CABOTEX CO LTD, CABOTEX CO. LTD.
Application year: 1988
Main classification: C09D5
IPC codes: C01B31, C09D5