Method of manufacturing a conductive resin composition

Abstract: A method of manufacturing a conductive resin composition. The method comprises kneading carbonaceous conductive material, together with a solvent, in a medium stirring mill, and mixing the resultant slurry-form kneaded mixture which contains the carbonaceous conductive material pulverized to an average particle size of up to 20 µm into a resin matrix. The invention achieves a highly uniform dispersion of the carbonaceous conductive material in resins. Furthermore, the conductive material is easily mixed into the resin matrix, and the final resin has an excellent conductivity.

Description: The present invention relates to a method of manufacturing a conductive resin composition. More particularly, the present invention relates to a method of manufacturing a novel conductive resin composition which is useful in a wide range of areas including paint, ink, rubber, and plastics, has a uniform dispersion of carbonaceous conductive material, permits the achievement of a high conductivity, and is easy to handle. Resin compositions having imparted conductivity have conventionally been used for applications such as paint, ink, rubber and various plastics. As such conductive resin compositions there are known materials prepared by blending a conductive filler such as metal powder or fibre, carbon black or carbon fibre with a resin. Among others, carbonaceous conductive materials such as carbon black and carbon fibre are most commonly utilized as components of conductive resin compositions. However, such a carbonaceous conductive material which is added to impart conductivity is difficult to disperse into a resin as compared with ordinary carbon black. It has therefore been impossible to inhibit agglomeration by secondary agglutination of such conductive materials and it has been difficult to meet the requirements for uniform dispersion, a high conductivity and a satsifactory formability. Uniform dispersion into a resin to a high degree is actually very difficult even with conductive carbons such as Ketchen black and acetylene black, which are known to provide a high conductivity in small amounts, and with carbon fibrils comprising microfibrils which are attracting attention as new carbonaceous materials (those disclosed, for example, in U.S. Patent No.4,663,230 and Japanese Patent Provisional Publication No. 60-500,943). For the purpose of dispersing these carbonaceous conductive materials, it has been the conventional practice to impart softness to a resin by, for example, heating and mixing or by the use of a plasticizer in a large quantity, and then directly adding a conductive material. These practices have however the drawback of possibly causing degradation and deterioration of the resin itself and involve problems in that the properties as a resin composition and even the areas of application thereof may be limited. In order to uniformly disperse a conductive material and obtain a high conductivity with the addition of the conductive material in a slight amount, it is necessary to achieve a higher contact probability of particles of the conductive material and a lower contact resistance between particles. A carbonaceous material as a conductive material is however poor in wettability with a solvent and a resin matrix. In addition, while larger particles having a larger specific surface area are preferable for imparting conductivity, particles having a larger specific surface area tend to easily agglutinate, form aggregates presenting an exterior view of chains of fringes (spawns), and this is a problem in that it is not easy to break these aggregates. It has thus been very difficult to achieve uniform dispersion of a carbonaceous conductive material and a satisfactory conductivity. The present invention was developed in view of the circumstances as described above, and has an object the provision of a method of manufacturing a novel resin composition, which solves the drawbacks in the conventional blending technique of a carbonaceous conductive material is a resin, and permits the achievement of a high conductivity and uniform dispersion of the conductive material. The present invention provides a method of manufacturing a conductive resin composition, which method comprises the steps of kneading an agglomeration of microcarbon fibrils having a diameter of 150Å and length of 20 µm, said microcarbon fibrils having been prepared by treatment in a colloid mill from fibrils of average diameter 65 µm and maximum diameter 100 µm, with a solvent in an annular continuous wet-type stirring mill so that said carbonaceous conductive material is pulverized to an average particle size of 1 to 2 µm, and mixing the resultant slurry kneaded mixture into a resin as matrix. In the conventional technique, it is difficult to achieve uniform dispersion of a carbonaceous conductive material, and degradation in quality of resin or compositions thereof and restrictions in the scope of application are unavoidable. In the present invention, in contrast, in which the carbonaceous conductive material is pulverized in a medium stirring mill to an average particle size of 1 to 2 µm and mixed in a slurry state into a resin matrix, dispersion of the carbonaceous conductive material becomes uniform and a satisfactory conductivity can be achieved with addition in a slight amount. Because, according to the method of the present invention, the carbonaceous conductive material is finely pulverized to an average particle size of 1 to 2 µm, and it is possible to uniformly pulverize within a narrow range of particle size distribution into slurry, it is possible to determine the state of dissociation of aggregates and dispersion from changes in the particle size and conductivity during formation of the slurry, and there is readily available a state of dispersion meeting the purpose such as conductivity, coloring, prevention of aging caused by heat or ultraviolet ray, or reinforcement. As a result, wettability is improved remarkably, and uniform mixing with the resin matrix becomes easier by adjusting the particle size of the slurry. The above-mentioned functions and effects are achieved by producing a slurry-form pulverized kneaded mixture through kneading of the carbonaceous conductive material and a solvent in a medium stirring mill as mentioned above. For the carbonaceous conductive material, there is no limitation imposed on the kind; preferred materials include such known carbon blacks as Ketchen black,vulcan X72 and acetylene black which give a high conductivity with addition in slight amounts, and the carbon fibrils mentioned above having unique microstructure and properties. From among several types and constructions of medium stirring mill, an annular continuous wet-type stirring mill using such pulverizing medium particles as zirconium and steel is a typical one applicable for the present invention. This mill pulverizes a material by causing the material to be pulverized and a solvent to continuously flow, together with pulverizing medium, through the space between an inner cylinder and an outer cylinder of which the peripheral speed is controllable. The mill is capable of achieving even submicron pulverizing and has a feature of easy control of the particle size distribution. Various models, including known ones, of this type of stirring mill are now available. A solvent is used during kneading and pulverizing in the medium stirring mill, and since the produced slurry-form kneaded mixture is mixed into the resin matrix, it is desirable to select a solvent by taking account of miscibility with the resin, properties such as separability from the resin, operability and safety. Usually, any of various general-purpose solvents including such aromatic hydrocarbon solvents as toluene and xylene, organic solvents such as dioxane, THF and ether, aliphatic hydrocarbon solvents such as pentane and hexane, halogenated hydrocarbon solvents, and glycol-based solvents such as diethylene glycol may be appropriately employed. Pulverizing may be conducted under conditions including a solid concentration of, for example, about 2 to 10%, an amount of treatment of 30 to 800 g/minute, and room temperature. These figures are not of course limitative. It is needless to mention that selection must be made in response to the type and construction of the mill, the target particle size and the kind and size of the carbonaceous conductive material to be treated. Mixing of the produced slurry into the resin matrix may be accomplished by master batch method or into a composition for product. There is no particular limitation as to the kind of resin. Applicable thermo-plastic resins include, for example, acrylonitrile-butadiene-styrene resin ( ABS resin), acrylonitrile-ethylene/propylene-styrene resin (AES resin), methyl methacrylate-butadiene-styrene resin (MBS resin), acrylonitrile-butadiene-methyl methacrylate-styrene resin (ABMS resin), acrylonitrile-n-butylacrylate-styrene resin (AAS resin), rubber modified polystyrene (high-impact polystyrene), polyethylene resin, poly-propylene resin, polystyrene resin, polymethyl methacrylate resin,polyvinyl chloride resin, cellulose acetate resin, poly-amide resin, polyester resin, polyacrylonitrile resin, poly-carbonate resin, polyphenyleneoxide resin, polyketone resin, polysulfone resin, polyphenylenesulfide resin, fluorine resin, silicon resin, polyimide resin, polybenzimidazole resin, and polyamide elastomer, and applicable thermo-setting resins include, for example, phenol resin, urea resin, melamine resin, xylene resin, diacyl phthalate resin, epoxy resin, aniline resin, furan resin, and polyurethane resin. The carbonaceous conductive material in the slurry-form kneaded mass may be mixed in an appropriate ratio into the resin selected from those listed above. From the consideration of kneading efficiency, conductivity and dispersibility, it is desirable to blend the carbonaceous conductive material in an amount of 0.5 to 4 parts by weight per 100 parts by weight of the resin composition. In addition to the carbonaceous conductive material of the present invention, known additives such as fillers, softeners, processing aids, slip additives, aging preventive agents, ultraviolet absorbers, or foaming agents such as carbon fibrils, carbon black, silica, diatomaceous earth, pulverized lime, talc, clay, mica, calcium silicate, magnesium silicate, glass powder, calcium carbonate, barium sulfate, zinc carbonate, titanium oxide, alumina, glass fibre, other carbon fibres, and organic fibres may be mixed as required into the resin composition. The method of the present invention will now be described in detail by means of examples. Examples An annular continuous wet-type stirring mill (Kobol mill manufactured by Shinko-Bantech Co., Ltd.) was used as the medium stirring mill. The construction and operating specifications for the mill were set as follows: Medium (diameter) : zirconium (0.5 to 1.5 mm dia.) Pulverizing gap : 6.5 mm Medium filling rate : 70% Rotor peripheral speed : 13 m/second Supply pressure : 0.2 to 0.5 kg/cm Under these conditions, an agglomeraation of micro-carbon fibrils having a diameter of 150 Å and a length of 20 µm, which had previously been treated into fibrils having an average diameter of 65 µm and a maximum diameter of 100 µm in a colloid mill, was mixed with toluene so as to give a concentration of 4%, and stirred at a throughput of 500 g/minute. Three cycles of this operation were carried out. A slurry-form kneaded mass containing pulverized carbonaceous conductive material having a maximum particle size of 3 µm and an average particle size of 1.6 µm was obtained. This slurry-form kneaded mixture was mixed into an acrylic resin so as to achieve a content of carbonaceous conductive material of 3 wt.%. This resulted in a satisfactory disperson of the conductive material, with a specific resistance of the resin of 1.2 kΩ.cm and an excellent conductivity. In the application to a paint, almost no painting irregularities were observed. With a concentration of 6%, pulverizing to a maximum particle size of 2 to 3 µm and to an average particle size of 1.4 µm was possible with two passes, and an excellent conductivity as above was obtained. In all cases, uniform dispersion of spherical particles was confirmed through observation by means of an optical microscope (200 magnifications). Ketchen black having an average particle size of 120 µm was treated in the same manner as in the case described above. Blending of 3 wt.% (maximum particle size: 8 µm/average particle size : 5 µm) into a resin gave an excellent conductivity as represented by a specific resistance of 3 kΩ.cm. According to the present invention, as described above in detail, it is possible to produce a highly uniform dispersion of a carbonaceous conductive material in a resin, with easy uniform mixing into a resin matrix, and to achieve an excellent contuctivity.

Claims: A method of manufacturing a conductive resin composition, which method comprises the steps of kneading an agglomeration of microcarbon fibrils having a diameter of 150Å and length of 20 µm, said microcarbon fibrils having been prepared by treatment in a colloid mill from fibrils of average diameter 65 µm and maximum diameter 100 µm, with a solvent in an annular continuous wet-type stirring mill so that said carbonaceous conductive material is pulverized to an average particle size of 1 to 2 µm, and mixing the resultant slurry kneaded mixture into a resin as matrix. A method as claimed in claim 1 wherein said solvent is toluene. A method as claimed in claim 1 or claim 2 wherein said resin is a thermoplastic resin or a thermosetting resin. A method as claimed in any one of the preceding claims wherein said resin is an acrylic resin. A method as claimed in any one of the preceding claims wherein the carbonaceous conductive material is mixed into said resin matrix in an amount of 0.5 to 4 parts by weight per 100 parts by weight of the resin composition. A method as claimed in any one of the preceding claims wherein the carbonaceous conductive material is present in said solvent in a concentration of 2 to 10%.

Inventors: NISHIWAKI ATSUSHI, NISHIWAKI, ATSUSHI
Applicants: NISHIWAKI ATSUSHI, NISHIWAKI, ATSUSHI
Application year: 1993
Main classification: H01B1
IPC codes: C08K3, C08J3, C08L101, H01B1, C08K9, C09C1, C09D5