CONDUCTIVE FILM FOR PACKAGING

Abstract: A conductive film comprises a transparent matrix of a thermoplastic resin having short conductive fibers in contact with one another dispersed therein such that the film has an opacity of not more than 30% and a surface resistivity of not more than 1 × 10⁸ Ω cm. The conductive film is produced by mixing a thermoplastic synthetic pulp slurry with the short conductive fibers, forming a raw paper sheet from the resultant mixture by means of paper-making apparatus and heating the raw paper sheet under pressure at a temperature higher than the melting point of the thermoplastic synthetic pulp. The film is useful for packaging electronic components.

Description: DESCRIPTION TITLE: CONDUCTIVE FILM FCR PACKAGING This invention relates to a conductive film suitable for packaging. More particularly, this invention relates to a conductive film having conductivity enough to protect packed contents from electrostatic faults, transparency enough to observe the packed contents therethrough and heat-sealability. In the course of packaging, shipping and storing electronic parts such as semiconductor, IC, LSI, print circuit and magnetic tape, these products should be protected from the adsorption of dust and other annoying troubles caused by electrostatic charge. In particular, resently prevailing C-MOS IC is very sensitive to the electrostatic charge and apt to incur dielectric breakdown. Accordingly, the prevention of electrification is indispensable for the C-MOS IC. In order to protect those products from such electrostatic faults, it is worth-while to pack them with a conductive film having a low surface resistivity. As to the conductivity, the conductive films as the packaging material are demanded to have the surface resistivity of from about 108-106D to to about 100-10-2#¯cm. The surface resistivity around 108-106#.cm is sufficient to prevent the adhesion of minute dust by the electrostatic charge, the surface resistivity around 106 100 #.cm is efficient to prevent the electrostatic faults and further the surface resistivity around 100-10-2#¯cm is efficient to shield electromagnetic waves. In addition, the packaging materials for print circuit, IC, records and the like are desirable to be transparent for enabling the inspection of the packed contents by observing them therethrough. Hitherto, there have been proposed some conductive films, for instance, a conductive paper prepared by mixing cellulose pulp slurry with conductive inorganic fine powders such as carbon black followed by processing the mixture into paper (Japanese Patent Laying Open No. 68194/81) and a conductive paper prepared by mixing paper-making pulp slurry with chopped carbon fibers followed by processing the mixture into paper (Japanese Patent Publication No. 32766/70). However, these conventionally known conductive papers are all not transparent but colored black or white since much amount of carbon black is incorporated therein or the matrix thereof consisting essentially of paper-making pulp is opaque. Furthermore, since they contain cellulose pulp as a main component, it is completely impossible to heat-seal. Besides, there is known another conductive paper formed from synthetic pulp and conductive additives, for instance, a conductive paper in which acrylic synthetic pulp forms the matrix thereof and carbon fibers are dispersed in the matrix (Japanese Patent Laying Open No. 18702/75). However, such conductive paper is also not transparent due to the opaquness of both the matrix and the incorporated conductive additives. Synthetic resin films deposited with vaporized metal such as nickel is likewise known as the conductive film, but it has drawbacks such as exfoliation of the metallic layer from the vacuum metallized film and high cost. The other proposed conductive film containing antistatic additives is rather tacky and so it is impossible to avoid the adhesion of dust. The object of the present invention is to delete the defects found in the conventional conductive films or papers. Another object of the present invention is to provide a conductive film having conductivity enough to protect the packed contents from the electrostatic faults. Further object of the present invention is to offer to such conductive film the transparency enabling the inspection of the packed contents by observing them therethrough and the heat-sealability. The other objects of the present invention will be apparent from the descriptions hereinafter. The conductive film according to this invention comprises a transparent filmy matrix of thermoplastic resin and short conductive fibers dispersed therein in an electrical contact state to each other and has an opacity of not more than 30 % and a surface resistivity of not more than 1 x 108Q cm. The conductive film is produced by mixing thermoplastic synthetic pulp slurry with short conductive fibers followed by subjecting the resultant mixture to a paper machine to form a raw paper or raw sheet, and then by heating under pressure the obtained raw sheet at a temperature of higher than the melting point of the thermoplastic synthetic pulp. The thermoplastic synthetic pulp is formed into the raw sheet by the paper machine and becomes the transparent thermoplastic resin matrix of the conductive film after receiving the specified heat-treatment under pressure. The short conductive fibers are dispersed in the pulp slurry in the mixing step and subsequently dispersed in the electrical contact state in the sheet and matrix by subjecting to the paper machine and the specified heattreatment under pressure According to the first aspect of the invention, the short conductive fiber is a carbon fiber. The carbon fiber hereinafter described in detail is contained in the conductive film by the amount of 0f5 to 20 % by volume, preferably 1 to 10 % by volume thereof, while the residue of 99.5 to 80 % by volume is the thermoplastic resin matrix. According to the second aspect of the invention, the short conductive fiber is a metal fiber or a metal-coated fiber selected from the group consisting of stainless steel fiber, aluminum fiber, brass fiber, carbon fiber coated with aluminum or nickel and glass fiber coated with aluminum or nickel. The metal fiber or the metal-coated fiber hereinafter described in detail is contained in the conductive film by the amount of 0.5 to 30 % by volume thereof, while the residue of 99.5 to 70 8 by volume is the thermoplastic resin matrix. A chemical pulp may be contained in the conductive film from the view points of the convenience in the production thereof and the production cost. In this case, less than 50 % by volume, preferably less than 30 % by volume of the thermoplastic synthetic pulp is displaced by the chemical pulp, and the incorporating amount of the conductive carbon fiber is preferably reduced to less than 6 % by volume while that of another conductive fiber, i.e., metal or metal-coated fiber is preferably reduced to less than 15 % by volume. In the present invention, it has been found that the whity and opaque raw sheet formed by mixing the synthetic pulp, the conductive fiber and, as occasion demands, the chemical pulp in the specified blending ratio mentioned above followed by subjecting to the paper machine is still remained to be opaque and has a higher surface resistivity after the calender finish usually employed in the manufacturing of paper under the normal conditions of temperature and pressure, but the same sheet is contrary changed to be transparent and the surface resistivity thereof is reduced to the extent of the raw sheet or less after subjecting to the calender treatment under the condition of the temperature higher than the melting point of the thermoplastic synthetic pulp Furthermore, the conductive film produced in such a manner has been found to remain the heat-sealability inherent to the thermoplastic resin. The thermoplastic synthetic pulp of the invention includes pulp consisting of thermoplastic resin, thermoplastic synthetic fiber and thermoplastic synthetic fibrous binder. As the thermoplastic resin, polyolefins, polyacrylonitriles, polyesters, polyamides, polyvinyl alcohols, etc. are usually employable. That is, the thermoplastic synthetic pulps which can be processed into the raw paper sheet by the paper machine and thereafter can be softened and melted into a transparent film by heating under pressure are all employable in the present invention. The melting point of the thermoplastic synthetic pulp is in the range of 100 to 260 C. From the viewpoint of carrying out the heat-seal without difficulty, the melting point is preferably lower than 2000C, and practically lower than 1700C. According to the invention, though the thermoplastic resin is usually employed after forming the pulp thereof, the resin may be employed in the form of fiber as well unless the effects of the invention are not spoiled. Therefore, the synthetic pulp is herein defined to include the pulp per se and the fiber. Among those synthetic pulps, polyolefin pulp or fiber is especially preferable. The polyolefin includes, for instance, polyethylene, polypropylene, copolymer of ethylene with propylene, copolymer of ethylene or propylene with a-olefin, copolymer of ethylene or propylene with other copolymerizable comonomer such as vinyl acetate and acrylic acid, mixture of these polymers and a polymer obtained by chemically modifying these polymers This polyolefin pulp or fiber is processed advantageously in combination with polyvinyl alcohol binder usually employed in the manufacturing of paper. The carbon fiber as the short conductive fiber according to the first aspect of the invention may be any one of those prepared from the starting material such as pitch, rayon, polyacrylonitrile and so on. The graphite fiber which is obtained by further heating the carbon fiber is also advantageously employed as the conductive fiber. Therefore, the carbon fiber described in the specification and claims is defined to include the graphite fiber. As the form of carbon fiber, short fiber (so-called chopped fiber) having a fiber length of 1 to 25 mm and a fiber diameter of 5 to 30 pm is preferable. The carbon fiber of shorter than 1 mm in length is li#kely removed by dropping off during the steps of forming the raw paper sheet to create a difference of the conductive fiber content between both surfaces of the conductive film, so that it is not desirable for ensuring a uniform surface resistivity. Though the carbon fiber of longer than 25 mm in length is advantageous for producing a conductive film having a low surface resistivity with low content of the fiber, such too long fiber results in a bulky sheet and in the formation of uneven dispersion or mass of the conductive fiber in the inside of conductive film. With respect to a fiber diameter, the commercially available carbon fiber having a diameter of 5 to 30 Vm may be employable. For obtaining high transparency and high surface resistivity, the fiber having a relatively large diameter is preferable, and on the other hand, for obtaining high transparency and low surface resistivity, the fiber having a relatively small diameter is preferable. The fiber diameter can be appropriately selected depending upon the final use of the conductive film. The amount of the carbon fiber contained in the conductive film is in the range of 0.5 to 20 % by volume of the conductive film. The less amount of the carbon fiber may cause an insufficient conductivity of the conductive film, while the more amount of the carbon fiber may lead to the damage of transparency of the conductive film. The short conductive fiber according to the second aspect of the present invention is a metal fiber or an inorganic fiber such as carbon fiber and glass fiber coated with a metal on its surface. In addition to these conductive fibers, a material that can be transformed into short fiber and has a small surface resistivity, for example, a vacuum metallized film cut fibrously and organic conductive fiber such as polyacetylene is also employable. The metal fiber includes steel fiber, stainless steel fiber, aluminum fiber, brass fiber, copper fiber and bronz fiber, but the stainless steel fiber, aluminum fiber and brass fiber which are resistant to oxidation are preferable The metal fiber is manufactured in various diameters generally by an extrusion process, skiving process and the like. In the present invention, the employable metal fiber has a diameter of 1 to 100 l'm, preferably 20 Wm or less, and a fiber length of 1 to 25 mm, preferably 3 to 15 mm. The metal fiber of more than 100 wm in diameter provides the conductive film of thickness exceeding 100 um, so that such too large diameter is undersirable. In addition, such metal fiber of too large diameter is apt to precipitate in the one side of the conductive film due to its weight, providing the conductive film unevenly dispersed with the conductive fiber. Further, although the metal fiber of relatively large diameter is advantageous for reducing the opaqueness of the conductive film, it is preferable to use the fiber having the diameter of 20 wm or less in order to disperse the fiber uniformly in the steps of forming the raw paper sheet. The metal fiber having a fiber length of less than 1 mm is not desirable because such too short fiber makes the formation of fiber network in the conductive film difficult. On the other hand, the use of the metal fiber having a fiber length of 25 mm or longer results in the easy formation of a vacant area of no conductive fiber or the formation of a huge mass of the conductive fiber in the conductive film, so that such too long fiber is undesirable. The metal for coating the inorganic fiber such as the carbon fiber or glass fiber is preferably an oxidation-resistant metal such as aluminum and nickel. The employable metal-coated fiber in the present invention has a diameter of 1 to 100 pm, preferably 20 vm or less and a fiber length of 1 to 25 mm, preferably 3 to 15 mm, as in the metal fiber described hereinbefore. The carbon fiber used as the core material of the metal-coated conductive fiber is the same as the carbon fiber hereinbefore described. As the form of the core carbon fiber, a short fiber (so-called chopped fiber) having a fiber length of 1 to 25 mm and a diameter of 5 to 30 pm is preferable. The core carbon fiber may be coated with aluminum or nickel in thickness of about 0.5 to 3 vm by electroplating or vacuum deposition. When the glass fiber is used as the core material, the chopped strand of glass having a length of 7 to 10 mm and a diameter of about 5 to 15 pm is preferably employable and may be coated with aluminum or nickel in thickness of about 3 to 5 Wm by means of vacuum deposition or dipping into a metal bath. The chopped strand of glass coated with metal is available commercially. The chemical pulp of the present invention includes, for instance, needle-lief tree bleached kraft pulp (NBFP) and needle-lief tree bleached sulfite pulp (NBSP). By displacing the synthetic pulp with the chemical pulp, it is possible to enhance the machinability of paper machine for producing the conductive film of the invention and to save the production cost. However, a small mixing ratio of the chemical pulp is preferable for obtaining a favorable transparency and heatsealability of conductive film. Though the use of no chemical pulp results in the best transparency and heat-sealability, the small amount of the chemical pulp may be preferably incorporated into the conductive film from the practical viewpoint. Thus, the incorporating amount of the chemical pulp is at most equal to that of the synthetic pulp by volume and is preferably smaller than that of the synthetic pulp. For obtaining the conductive film of low basis weight, a long fiber pulp such as manila hemp pulp may be employable. In addition, various other kinds of chemical pulp, for example, sode pulp, semichemical pulp and unbreached cellulose pulp are not obstructive in this invention. The conductive film according to the present invention is produced mainly by applying the paper-manufacturing technology. The matrix consisting of the thermoplastic synthetic resin is formed from the above-mentioned thermoplastic synthetic pulp. The conductive film may be produced by the following manner. First, the thermoplastic synthetic pulp is mixed with the short conductive fiber. In mixing, the thermoplastic synthetic fiber is in advance dispersed in water, preferably warm water to prepare the slury thereof, and separately the conductive fiber is likewise dispersed in water. After that, both dispersions are mixed with each other. The mixing ratio of the synthetic pulp to the conductive fiber has an important influence on the characteristic of the conductive film such as the surface resistivity and the transparency. With too little conductive fiber, the mutual contact of the conductive fiber to form the network thereof in the conductive film becomes insufficient, and so the conductive film having a small surface resistivity cannot be obtained. With too much conductive fiber, the conductive film becomes too opaque. The optimum mixing ratio of the conductive fiber varies with the kind of conductive fiber and the size thereof. In case that the conductive fiber is the carbon fiber, 80 to 99.5 % by volume of the synthetic pulp and 20 to 0.5 % by volume of the carbon fiber are mixed with each other in the foregoing mixing step. For obtaining the conductive film with the surface resistivity of less than 1 x 108Q cm, at least 0.5 % by volume of the carbon fiber is indispensable, while more than 20 % by volume of the carbon fiber causes the fear of damaging the transparency of the conductive film and raises the opacity thereof more than 30 %. In particular, it is preferable to mix 7 % or less by volume of the carbon fiber having the diameter of 5 to 10 Wm, 12 % or less by volume of the same fiber having the diameter of 10 to 15 pm and 20 % or less by volume of the same fiber having the diameter of 15 to 30 vm. On the other hand, in case that the conductive fiber is the metal fiber or metal-coated fiber, 70 to 99.5 % by volume of the synthetic pulp and 30 to 0.5 * by volume of the metal or metal-coated fiber are mixed with each other in the foregoing mixing step. For obtaining the conductive film with the surface resistivity of less than 1 x 10 cm, particularly less than 1 x 106#.cm, at least 0.5 % by volume, preferably more than 3 % by volume of the metal or metal-coated fiber is indispensable. For obtaining the conductive film with the opacity of less than 30 %, the amount of the metal or metal-coated fiber should be less than 30 % by volume, preferably less than 10 % by volume while depending on the diameter thereof. In particular, it is preferable to mix 7 % or less by volume of the metal or metalcoated fiber having the diameter of S to 10 um, 12 % or less by volume of the same fiber having the diameter of 10 to 15 Vm, 20 % or less by volume of the same fiber having the diameter of 15 to 20 Vm and 30 8 or less by volume of the same fiber having the diameter of more than 20 pm. When the chemical pulp is incorporated into the conductive film, the chemical pulp after beating may be preferably mixed with the synthetic pulp and the conductive fiber in the foregoing mixing step. The mixture should be sufficiently stirred and homogenized before sending to the paper machine. For forming the raw paper sheet from the abovementioned mixture, the paper machine provided with wire cloth, press and dryer, which is conventionally used in the manufacturing of paper, is advantageously employed. The dried raw paper sheet after subjecting to the paper machine is then heated and pressed to be made transparent. The heat-treatment under pressure can be carried out by a calender which makes paper glossy and the surface of paper smooth in the conventional paper-manufacturing process or by a hot press. The pressure condition is appropriately selected in a linear pressure ranging from 40 to 200 kg/cm for the calender-treatment or in a pressure ranging 2 from 30 to 200 kg/cm for the hot press-treatment. Further, the heat-treatment under pressure according to the invention can also be carried out with a calender for plastic processing provided that the saxne conditions of temperature and pressure are applied. The temperature condition in the heat-treatment under pressure is different from that in the usual calendertreatment and it is indispensable to heat the raw paper sheet above the melting point of the thermoplastic synthetic pulp. For instance, the heating temperature for the thermoplastic resin of polyolefin is about 130-200 ec This heat-treatment under pressure is necessary for making the thermoplastic resin matrix formed from the thermoplastic synthetic pulp transparent and also for reducing the surface resistivity of the resultant conductive film. The conductive film of the present invention should preferably have a thickness of 100 Vm or less from the respect of transparency, flexibility and the like. The conductive film produced in the above-mentioned manner evenly disperses the short conductive fibers in the transparent filmy matrix of thermoplastic resin while remaining transparent areas therein. The dispersion of the short conductive fiber in the matrix is in the electrical contact state, by which each conductive fiber is brought into contact with another conductive fiber. Accordingly, the conductive film becomes electrically conductive by many contacts of the conductive fibers and the small surface resistivity of less than 1 x 108Q cm, particularly less than 1 x 105Q cm is obtainable. Furthermore, the light transmits the transparent areas of the conductive film wherein no conductive fiber is presented, and so the opacity of less than 30 % is obtainable. The present invention will be further explained hereinafter with referring to the drawings. Fig. 7 illustrates the relation between the temperature at which the raw paper sheet was heat-treated by a super calender and the surface resistivity of the conductive film produced by the heat-treatment. For forming the sheet, Swp#UL400 (polyethylen-e resin, m.p.: 122¯C, specific gravity: 0.9, average fiber length: 0.9 mm, brightness: above 94 %', as the thermoplastic synthetic pulp, wood pulp (NBKP, the specific gravity thereof is determined to be 0.9 since a normal NBKP paper after the super calender treatment under high 3 pressure has a density of around 0.9 g/cm ) as the chemical pulp and carbon fiber (Kureha Carbon Fiber Chop C-203, graphatized, fiber length: 3 mm, diameter: 12.5 vm, specific resistance: 5.5 x 10-3#.cm) , hereinafter referred to as CF, were employed. Three kinds of the raw paper sheet with basis weight of 50 g/m2 were formed by making the mixing ratio of CF constant and by changing the mixing ratio of both SWP and NBKP. The beating degree of NBKP was 300 ml CSF (determined by means of Canadian standard freeness tester). SWP and CF were dispersed into water separately and then both were homogeneously mixed with NBKP. The linear pressure of the super calender was adjusted to 60 Kg/cm constantly and the speed thereof was adjusted to 4.5 m/min constantly. The surface temperature of the super calender rolls was changed as shown in Fig. t. Then, the surface resistivity of the heat-treated sheet, i.e., the conductive film was determined. In Fig. 1, the dot marked with O represents the conductive film with the mixing ratio of SWP/NBXP/CF=70/30/5 in weight ratio (68/29/3 % by volume), the dot marked with. represents that of SWP/NBKP/CF=50/50/5 in weight ratio (48.5/48.5/ 3% by volume) and the dot marked with A represents that of SWP/NBKP/CF=80/20/5 in weight ratio (78/19/3 % by volume). As apparent from Fig. 1, there is almost no difference in the surface resistivity between the original sheets not subjected to the heat-treatment by the super calender, while the surface resistivity once increases after subjecting to the heat-treatment by the super calender at a temperature of 60 C which is in the range of the normal temperature condition in the manufacturing of paper. When the temperature is further raised and approaching to the melting point of the synthetic pulp SWP, the surface resistivity of the conductive film is found to be approaching to that of the untreated original sheet, and moreover when SWP melts completely, the surface resistivity of the conductive film is found to be lower than that of the untreated original sheet. Furthermore, it is also apparent from Fig. 1 that the above-mentioned tendency of the surface resistivity is remarkable when the mixing ratio of SWP is large. Incidentally, surface resistivity described in the specification and claims is represented by the following formula: EMI16.1 wherein p is the surface resistivity (Q cm), L is the distance (cm) between the electrodes, R is the determined resistance lQ), T is the thickness (cm) of the specimen and W is the length of electrode (cm). The determination of the surface resistivity in the present invention is based on ASTM D-257. The resistance (R) and the thickness (T) of the untreated original sheet and the conductive film with the mixing ratio of SWP/NBKP/CF=70/30/5 after subjected to the heat-treatment at 1300C were determined and listed in the following Table 1. The influence of the heat-treatment on the surface resistivity (p) was inspected from the measurement of R and T. Table 1 Resistance Thickness Surface resistivity (n) (,) (fl#cm) Untreated sheet 2727 133.5 10.4 x 100 Conductive film 2136 77.0 4.7 x 100 Ratio of conductive film/ 78.3 % 57.7 % 45.2 % untreated sheet From Table 1, it can be understood that the reduction of the surface resistivity does not depend only on the reduction of the thickness since the determined resistance is likewise reduced. Fig. 2 illustrates the relation between the opacity of the same specimen as in Fig. 1 and the temperature at which the heat-treatment under pressure was carried out. As apparent from Fig. 2, under the constant linear pressure of 60 ICg/cm, the opacity of the conductive film is not changed remarkably in the temperature range upto the softening point of SWP (103 C), while the opacity is rapidly reduced at the temperature above the softening point. Furthermore, it is apparent from Fig. 2 that the conductive film becomes more transparent when the mixing ratio of SWP is larger. Incidentally, the determination of the opacity described in the specification and claims is based on TAPPX Standard T425 OS-75 and carried out by means of photovolt photoelectric reflection meter. The results of Fig. 1 and Fig. 2 shows that the heating at the temperature higher than the melting point of the thermoplastic synthetic pulp is indispensable to obtain the desired surface resistivity and opacity. Fig. 3 illustrates the relation between the opacity of the conductive film and the mixing ratio of the conductive carbon fiber incorporated therein. In Fig. 3, the dot marked witho represents the conductive film produced from the thermoplastic synthetic pulp (SWP) and the carbon fiber while changing the mixing ratio of the carbon fiber, and the dot marked with ¯ represents the conductive film produced from the synthetic pulp (SWP), the chemical pulp (NBKP) and the carbon fiber while making the relative ratio of SWP/NBKP constant (70/30 in weight ratio) and changing the mixing ratio of the carbon fiber. As apparent from Fig. 3, the conductive film containing no chemical pulp has the opacity of less than 30 % under the incorporating amount of the carbon fiber less than 20 % by volume, while the conductive film containing the chemical pulp has the opacity of less than 30 8 even if the carbon fiber is incorporated by the amount of about 10 % by volume. Fig. 4 illustrates the relation between the surface resistivity of the conductive film and the mixing ratio of the carbon fiber incorporated therein. In Fig. 4, the dot marked with o represents the conductive film having the basis weight of 50 gim2 and the mixing ratio of SWP/NSKP = 70/30 in weight ratio, the dot marked witho represents that having the basis weight of 30 g/m2 and the mixing ratio of SWP/NBFP = 70/30 in weight ratio, the dot marked with A respresents that having the basis weight of 50 g/m2 and the mixing ratio of SWP/NBKP = 80/20 in.weight ratio and the dot marked with A represents that having the basis weight of 30 g/m2 and the mixing ratio of SWP/NBKP = 80/20 in weight ratio. The carbon fiber was incorporated into each conductive film by the amount indicated with the scale of abscissa in Fig. 4. Fig. 4 shows that for obtaining the surface resistivity of, for instance, 1 x 10Q cm, 4 parts by weight of the carbon fiber may be incorporated into the conductive film of 30 g/m2 basis weight, while 2 parts by weight of the carbon fiber may be 2 incorporated into the conductive film of 50 g/m basis weight. Furthermore, Fig. 4 shows that the conductive film having a larger basis weight may contain a smaller amount of the carbon fiber to obtain the same value of surface resistivity. When taking into consideration the result of Fig. 1 that the high mixing ratio of the synthetic pulp makes the surface resistivity low and the results of Fig. 4 that the surface resistivity varies largely by the small change in the mixing ratio of the carbon fiber if the mixing ratio is in the range of less than 5 parts by weight, while the variation of the surface resistivity is small if the mixing ratio of the carbon fiber is in the range of more than 5 parts by weight, the optimum content of each component in the conductive film can easily be determined to obtain the desired surface resistivity. Fig. 5 illustrates the distribution of fiber length of the carbon fiber in the conductive film and the variation of this distribution of fiber length between before and after the heat-treatment under pressure according to the present invention. The abscissa of Fig. 5 represents the fiber length of the carbon fiber and the ordinate of Fig. 5 represents the frequency. In Fig. 5, curve 1 represents the distribution of fiber length of the carbon fiber in the conductive film having the mixing ratio of SWP/NBKP/CF = 70/30/5 in weight ratio, curve 2 represents that in the untreated raw sheet having the same mixing ratio and curve 3 represents that in a paper produced from only NBKP and CF without the synthetic pulp SWP, the mixing ratio of which is NBKP/CF = 100/5 in weight ratio. Comparing curve 1 with curve 2, it can be found that the distribution of fiber length of the carbon fiber scarcely varies between before and after the heat-treatment under pressure by the super calender according to the invention. The distribution of curve 3 shows that the almost all carbon fibers are broken into fine particles in the paper produced without the synthetic pulp. The tendency to break the carbon fiber into fine particles as shown in curve 3 was confirmed to be reduced in proportion to the increase in the mixing ratio of the thermoplastic synthetic pulp. According to the present invention, the carbon fiber is dispersed in the thermoplastic resin matrix of the conductive film without broken into fine particles as shown in Fig. 5. Therefore, the conductive carbon fiber can exist in the matrix while forming a lot of contacts therebetween like network structure even if the mixing ratio thereof is relatively low. In other words, the carbon fiber is dispersed in the matrix in the electrical contact state to make the finally obtainable film electrically conductive. This is the reason why the conductive film of the invention can have a low surface resistivity even if the content of carbon fiber is relatively low. Fig. 6 illustrates the relation between the surface resistivity of the conductive film and the mixing ratio of the stainless steel fiber incorporated therein. Fig. 7 illustrates the relation between the opacity of the conductive film and the mixing ratio of the same stainless steel fiber. The conductive film of Fig. 6 and Fig. 7 has the basis weight of about 50 g/cm2 and was produced from SW UL410 (product of Mitsui Petroleum Chemical Co., Ltd., polyethylene resin, m.p.: 1230C, specific gravity: 0.9, average fiber length: 0.9 mm, brightness: above 94 %) as the thermoplastic synthetic resin and the stainless steel fiber (product of Nippon Metallurgy Co., Ltd., average fiber length: 3 mm, diameter of fiber: 8 zm, specific gravity: 7.8) as the conductive fiber while changing the mixing ratio thereof. SW g UL410 and the stainless steel fiber were dispersed in water separately and then mixed with each other. The raw paper sheet formed from these materials was dried at 80 to l00eC and then heat-treated at l300C under the linear pressure of 60 Kg/cm by the super calender, thereby producing the conductive film with various mixing ratio. Fig. 6 shows that the conductive film incorporated with more than 0.5 % by volume of stainless steel fiber has a sufficiently low surface resistivity less than 1 x 102 fl.cm and that the surface resistivity is rapidly reduced when the stainless steel fiber is incorporated by the amount of less than about 2 to 3 % by volume. Accordingly, the conductive film having the desired low surface resistivity can be produced by appropriately adJusting the mixing ratio of the stainless steel fiber in the range of more than 0.5 % by volume. Fig. 7 shows that though the opacity of the coductive film is increased in proportion to the increase in the mixing ratio of the stainless steel fiber, the conductive film with the opacity of less than 30 % may be produced by incorporating the stainless steel fiber by the amount of 12 % by volume or less. When the stainless steel fiber is incorporated by the amount of 8 % by volume or less, the opacity becomes 20 % or less, and furthermore when it is incorporated by the amount of 5 % by volume or less, the opacity becomes 15 % or less and the conductive film with superior transparency is obtainable. The optimum mixing ratio of the stainless steel fiber is in the range of 3 to 5 % by volume from the view points of both the surface resistivity and the transparency. Fig. 8 illustrates the relation between the surface resistivity of the couductive film and the mixing ratio of the nickel-coated carbon fiber incorporated therein. Fig. 9 ialus- trates the relation between the opacity of the same conductive film and the mixing ratio of the same conductive fiber as Fig. 8. The conductive film of Fig. 8 and Fig. 9 was produced in the same manner as in Fig 6 and Fig. 7 except for employing as the conductive fiber the carbon fiber (product of Kureha Chemical Industry, Ltd., carbon fiber prepared from pitch, average fiber length: 6 mm, diameter of fiber: 12.5 pm) of which surface was coated with nickel by chemical plating. The nickel coat has a thickness of about 1 vm. The conductive film thus produced is dotted in Fig. 8 and Fig. 9 with the mark 0. On the other hand, another conductive fiber was also produced in the same manner as in Fig. 6 and Fig. 7 except for employing the above-mentioned nickel-coated carbon fiber and displacing 20 % by volume of the thermoplastic synthetic pulp, SWP, with the chemical pulp, NBKP. This conductive film is dotted in Fig. 8 and Fig. 9 with the mark . Fig. 8 shows that the conductive film having the surface resistivity of less than 1 x 103 n¯cm, which is far below the value of l x 106 Q*cm, is obtainable and that the conductive film having the smaller surface resistivity is obtainable in proportion to the increase in the mixing ratio of the nickel-coated carbon fiber. The surface resistivity of both conductive films is found to be rapidly reduced to the value of 1 x 101 n¯cm or less if the nickel-coated carbon fiber is incorporated by the amount of more than 1 to 1.5 % by volume. Fig. 9 shows that with respect to the opacity the conductive film containing no NBKP indicates the nearly similar tendency to the conductive film of Fig. 7, which is incorporated with the stainless steel fiber. The conductive film containing NBKP is shown in Fig. 9 to have a relatively high opacity and likely to raise its opacity in proportion to the increase in the mixing ratio of the conductive nickel-coated carbon fiber. However, the NBKP-containing film with the opacity of less than 30 % may be obtainable by incorporating the nickel-coated carbon fiber by the amount of less than 4 % by volume. Fig. 10 illustrates the relation between the surface resistivity of the conductive film and the mixing ratio of the aluminum-coated glass fiber incorporated therein. Fig. 11 illustrates the relation between the opacity of the same conductive film and the mixing ratio of the same conductive fiber. The conductive film of Fig. 10 and Fig. 11 was produced in the same manner as in Fig. 6 and Fig. 7 except for employing as the conductive fiber the commercially available aluminum-coated glass fiber (product of Diamond Shamrock Corp., average fiber length: 4 mm, diameter: 20 um, specific gravity: 2.6) As apparent from Fig. 10, the conductive film thus produced has a sufficiently low surface conductivity of less than 1 x 10 n¯cm. With respect to the opacity of this conductive film, the increasing rate of opacity to the increase in the mixing ratio of the aluminum-coated glass fiber was found to be relatively small since the employed conductive fiber had relatively large diameter of 20 vm. The conductive film with the transparency of less than 30 % may be obtainable by adjusting the incorporating amount of the aluminum-coated glass fiber to 30 % by volume or less, and the film with the opacity of less than 20 % may be obtainable by adjusting the incorporating amout of the same conductive fiber to 10 % by volume or less. In the present invention, to enhance the transparency of the conductive film, a thermoplastic resin such as hot melt wax, terpenpolymer, alkyl acrylate polymer and vinyl copolymer, a thermosetting resin of low molecular weight such as phenol resin, urea formaldehyde resin, melamine formaldehyde resin, alkyd resin and phthalic polyester, a photopolymerizable monomer or oligomer such as acrylic acid ester and methacrylic acid ester and other known additives, those additives having a refractive index equal to or lower than that of cellulose and a melting point nearly equal to that of the thermoplastic synthetic pulp, may be incorporated into the mixture for forming the raw paper sheet or may be coated on the raw paper sheet followed by drying to permeate into the raw sheet. Cellulose fiber other than the chemical pulp, for instance, mechanical pulp and semisynthetic fiber such as rayon may also be included and dispersed in the conductive film in the range of maintaining the effects of the present invention. In addition, binders, surfactans, reinforcing agents of paper strength, antifoaming agents, etc. may be added to the mixture for forming the raw paper sheet. Dampening the raw sheet with steam before the heat-treatment by the super calender and raising the linear pressure in the range that the conductive fiber is hardly broken thereby are included in the scope of this invention, which advantageously enhance the transparency of the conductive film. Besides, a hot air heater, an infrared heater and the like are employable in the step of heat-treatment under pressure. It is preferable to carry out the step of forming the raw paper sheet at a temperature below the softening point of thermoplastic synthetic pulp. The conductive film according to the present invention has the transparency equal to or higher than that of glassine paper as well as the antistatic and heat-sealing properties. According to the invention, an optional surface resistevity may be offered to the conductive film by adjusting the mixing ratio of the conductive fiber. The conductive film having the surface resistivity of 1 x 10 to 1 x 10 %.cm is suitable for a package preventing the dust adhesion and other electrostatic faults, and the film having that of 1 x 10 to 1 x 10 2 Q cm is suitable for use in the field requiring the shielding effect of electromagnetic waves. The conductive film may be laminated with other transparent film or other partially opaque film, or may be embossed while forming partially opaque areas therein. Though the process of producing the conductive film according to the invention was explained hereinbefore based on the paper manufacturing process, the dry type process for manufacturing nonwoven fabric may be applied to produce the conductive film while obeying the spirit of the present invention. The present invention will be more specifically described with the aid of the following specific, but nonlimiting examples. EXAMPLE 1 A given quantity of thermoplastic synthetic pulp, SW#UL400 (product of Mitsui Petroleum Chemical Co., Ltd. polyethylene resin, m.p.: 1220C, specific gravity: 0.9), was put into warm water of 500C so that the concentration thereof became 3 % by weight, and then agitated for 20 min to disperse. Needle-lief tree breached kraft pulp (NBKP) was beated by means of a beater until the beating degree thereof became 300 ml CSF. Carbon fiber (product of Kureha Chemical Industry, Ltd., Carbon Fiber C-203, graphatized grade, average fiber length: 3.0 mm, diameter: 12.5 um, specific gravity: 1.6) was dispersed into water so that the concentration thereof became 1 % by weight, and then added with a small amount of antifoaming agent, Trimin > DF130 (product of Miyoshi Yushi Co., Ltd.). These three materials were put into a mixing vessel so that the mixing ratio of SWP/NBKP/CF=70/30/5 parts by weight was obtained, and then agitated for 10 min. Thereafter, a dispersing agent, PEO¯#PF (product of Seitetsu Kagaku Co., Ltd.), was added thereto by the amount of 0.06 parts by weight to the resultant mixture. The resultant mixture was processed into a raw paper sheet by means of a paper machine. In the above-mentioned manner, two raw paper sheet 2 was produced; one had the basis weight of about 50 g/m and the other had the basis weight of about 30 g/m2. The drying of each sheet was carried out at 80 to 1000C. The dried sheet was heat-treated at 1300C under the linear pressure of 60 Kg/cm by a super calender to produce a conductive film of this invention. The properties of both the raw paper sheet and the conductive film are indicated in the following Table 2. Table 2 EMI29.1 <tb> <SEP> Raw <SEP> paper, <SEP> Film <SEP> of <SEP> Raw <SEP> paper, <SEP> Film <SEP> of <tb> <SEP> basis <SEP> weight <SEP> around <SEP> basis <SEP> weight <SEP> around <tb> <SEP> 30 <SEP> g/m2 <SEP> 50 <SEP> g/m2 <tb> <SEP> Raw <SEP> paper <SEP> Conductive <SEP> Raw <SEP> paper <SEP> Conductive <tb> <SEP> sheet <SEP> film <SEP> Sheet <SEP> film <tb> Basis <SEP> weight <SEP> 32.8 <SEP> 30.4 <SEP> 48.8 <SEP> 48.6 <tb> <SEP> (g/m2) <SEP> <tb> Thickness <SEP> (pm) <SEP> <SEP> 85.3 <SEP> 42.2 <SEP> 114.4 <SEP> 65.0 <tb> <SEP> <tb> Density <SEP> (g/cm3) <SEP> 0.39 <SEP> 0.72 <SEP> 0.43 <SEP> 0.75 <tb> Opacity <SEP> (%) <SEP> 90.3 <SEP> 13, <SEP> <SEP> 7 <SEP> 96.1 <SEP> 24.0 <tb> Brightness <SEP> (%)¯ <SEP> <SEP> 78.1 <SEP> - <SEP> <SEP> 76.9 <SEP> <SEP> - <SEP> <tb> Air <SEP> permeability <SEP> 6 <SEP> 8,800 <SEP> 11 <SEP> 89,000 <tb> <SEP> (sec/lOOml) <tb> Tensile <SEP> strength <SEP> 0.97 <SEP> 1.55 <SEP> 1.82 <SEP> 3.65 <tb> <SEP> (longitudinal) <tb> <SEP> (kg) <SEP> <tb> Heat-seal <SEP> strength <SEP> - <SEP> <SEP> 370 <SEP> - <SEP> 460 <tb> <SEP> (longitudinal) <tb> <SEP> (g/10mm3 <SEP> <tb> Surface <SEP> > 108 <SEP> 7.4 <SEP> x <SEP> 101 <SEP> > 108 <SEP> 3.2 <SEP> x <SEP> 100 <tb> resistivity <tb> <SEP> (fl.cm) <SEP> <tb> Water-vapor <SEP> 6,057 <SEP> 164 <SEP> 5,945 <SEP> 53 <tb> permeability <tb> <SEP> (g/m2/24hr) <tb> The heat-seal strength in Table 2 was determined based on TAPPI Standard T51?-69 under the following conditions. Heat-Seal: applied pressure 2 kg/cm2 sealing time 1 sec temperature l500C seal width 10 mm Tensile test: peeling speed 50 mm/min chuck interval 10 cm specimen width 2.5 cm universal tensile tester (t'Tensilon" manufactured by Toyo-Baldwin Co., Ltd.) Each raw paper sheet had high hrightness and high opacity, as shown in Table 2, and had an appearance of wood free paper since the black carbon fiber incorporated therein was inconspicuous due to its small mixing ratio. The opacity of the conductive film was nearly the same as that of glassine paper or less, and the packed contents lapped with the conductive film could be observed therethrough. The low air permeability of the conductive film, i.e., the long time required for a given quantity of air to permeate therethrough, and the low water-vapor permeability of the conductive film were due to the fusion of thermoplastic synthetic pulp. When one liter of water was put into a package produced by heat-sealing the conductive film and left as it was for a long time, there could be observed no percolation of water. The tensile strength of the conductive film was improved and higher than the raw paper sheet by 1.6 to 2 times. The heat-seal strength of the conductive film was likewise sufficient. EXAMPLE 2 A conductive film was produced by preparing a mixture of synthetic resin pulp (SWP)/chemical pulp (NBKP)/ carbon fiber (70/30/2 parts by weight, 69/30/1 % by volume) followed by subjecting to the paper machine to form a raw paper sheet with basis weight of about 50 g/m21 and then by heat-treating under pressure by means of the super calender in the same manner as in Example 1. The thus produced conductive film had the opacity of 20.5 % and the surface resistivity of 1 x fl.cm. The film was suitable for a package preventing the dust adhesion. EXAMPLE 3 In this example, there was obtained a conductive film by making the mixing ratio of synthetic pulp low and making that of chemical pulp high. The conductive film was produced by preparing a mixture of SWP/NBKP/CF (50/50/3 parts by weight, 49/49/2 % by volume) followed by subjecting to the paper machine to form 2 the raw paper sheet with basis weight of about 30 g/m , and then by heat-treating under pressure by means of the super calender in the same manner as in Example 1. The thus produced conductive film had basis weight 2 3 of 31.2 g/m2, , density of 0.68 g/cm , opacity of 28.5 %, air permeability of 4000 sec/lOOmi, tensile strength (longitudinal) of 2.71 kg, water-vapor permeability of 333 g/m2/24hr, heat-seal strength (longitudinal) of 230 g/l0mm, surface resistivity of 4 2 x 10 n¯cm. Comparing the conductive film obtained in this example with the conductive film of Example 1 which had the 2. basis weight of 30 gum2, it was found that the transparency, air permeability and heat-seal strength were all lowered, but the water-vapor permeability and tensile strength were increased. Taking into the consideration the smaller density, the fear of breaking the carbon fiber and the surface resistivity of the conductive film in this example, the mixing ratio of the synthetic pulp in this example was considered to be nearly corresponding to the minimum amount to be added. However, the conductive film produced in this example was satisfactory for use in a conductive container. EXAMPLE 4 A thermoplastic synthetic pulp, Es-chop (product of Chisso Corp., composite fiber.of polyethylene and polypropylene, m.p.: 165 - 1700C, fiber length: 5 mm, 3 denier, specific gravity: 0.9), was blended with polyvinyl alcohol fibrous binder (specific gravity: 1.3) in the blending ratio of 90/10 (by weight). Then, 5 parts by weight of carbon fiber was added to 100 parts by weight of the blend. The resultant mixture was subjected to the paper machine in the same manner as in Example 1 to form the raw paper sheet with basis weight of about 50 g/m2. The thus formed sheet was subsequently heat-treated at 1800C under the linear pressure of 60 kg/cm by means of the super calender together with an infrared heater. The properties of the obtained conductive film are indicated in the following Table 3. Table 3 Raw paper Conductive sheet film Basis Weight (g/m2) 47.5 55.7 Thickness (ism) 193 85 Density (g/cm3) 0.25 0.66 Air permeability (sec/lOOml) 5 4000 Tensile strength (kg/15mm) 2.12 2.15 Opacity (8) 51.9 11.9 Surface resistivity (Q-cm) < 108 1.28 x Comparing with Example 1, the conductive film of this example was found to be more flexible and bulky and to have more excellent processibility for making a package and sufficient transparency. The conductive film was satisfactory for use in the field requiring the shielding effect of electromagnetic waves. EXAMPLE 5 A conductive film was produced by mixing thermoplastic synthetic pulp (SWP)/chemical pulp (NBKP)/carbon fiber (70/30/10 parts by weight, 66/29/5 parts by volume) followed by subjecting to the paper machine to form the raw paper sheet with basis weight of about 50 g/m2, and then by heat-treating under pressure by means of the super calender. The thus produced conductive film had basis weight of 49.1 g/m2, , opacity of 29.1 %, air permeability of 43100 sec/100 ml, water-vapor permeability of 94 g/m2 /24 hr and surface resistivity of 5.7 x 10-1#.cm. The opacity of the conductive film was relatively high and very near to the limit of transparency. The conductive film of this example was suitable for a package requiring the shielding effect of electromagnetic wave. EXAMPLE 6 In this example, there were produced two conductive films in the same manner as in Example 1 except for employing a mixture of SWP/CF (95/5 parts by weight, 97/3 parts by volume) or a mixture of SWP/polyvinyl alcohol fibrous binder (PVA)/CF (85.5/9.5/5 parts by weight, 90/7/3 parts by volume). The properties of each conductive film thus produced are indicated in the following Table 4. Table 4 Mixing ratio Raw paper sheet Conductive film (parts by SWP/CF SWP/PVA/CF SWP/CF SWP/PVAjCF weight) (95/5) (85.5/9.5/5) (95/5) (85.5/9.5/5) (parts by volume) (97/3) (90/7/3) (97/3) (90/7/3) Basis weight 2 49.2 49.4 50.8 48.7 (g/mê) Thickness (pm) 139 141 57 54 3 Density (g/cm ) 0.35 0.35 0.89 0.90 Air permeability (sec/l0Oml) 2 3 Tensile strength0.15 0.61 1.14 1.24 (kg/15mm) Opacity (%) 96.1 95.9 3.9 4.4 Surface > 1 o8 > 1 8 2.24x100 5.10x100 resistivity(#.cm) Comparing with Example 1, the conductive film of this example had a lower tensile strength, but had a better machinability for the paper machine. The transparency thereof was highest. The conductive film of this example was suitable for use in the field requiring the shielding effect of electromagnetic waves. EXAMPLE 7 A given quantify of thermoplastic synthetic pulp, sw R UL 410 (product of Mitsui Petroleum Chemical Co., Ltd. polyethylene resin, m.p.: 1230C), was put into warm water of 500C so that the concentration thereof became 3 % by weight,. and then agitated to disperse. Stainless steel fiber (SSF) (product of Nippon Metallurgy Co., Ltd., average fiber length: 3 mm, diameter: 8 #xn) was dispersed into water of normal temperature so that the concentration thereof became 1 % by weight, and then added with a small amount of antifoaming agent, Trimi DF130 (product of Miyoshi Yushi Co., Ltd.). These two materials were put i#nto a mixing vessel so that the mixing ratio of SWP/SSF = 60/40 parts by weight (swP/SSF = 93/7 parts by volume) was obtained, and then agitated for 10 min. Thereafter, a dispersing agent, PE#-PF (product of Seitetsu Kagaku Co., Ltd.), was added thereto by the amount of 0.06 parts by weight to the resultant mixture. The resultant mixture was subjected to a paper machine to form a raw paper sheet with basis weight of about 50 g/mê. The drying of the sheet was carried out at 80 to 1000C. The dried sheet was subsequently heat-treated at 1300C under the linear pressure of 60 Xg/cm by a super calender to produce a conductive film of this invention. The properties of the thus produced conductive film are listed in the following Table 5. Table 5 Conductive film Basis weight (g/m2) 50.7 Thickness (#m) 43 Density (g/cm3) 1.18 Opacity (%) 15.1 Air permeability (sec/100ml) o, Tensile strength (Kg) 1.27 Heat-Seal strength (g/10mm3 844 Surface resistivity (Q cm) 1.81 x Water-vapor permeability (g/m2/24 hr) 19.8 The opacity of the conductive film was nearly the same as that of glassine paper or less, and the packed contents lapped with the conductive film could be observed therethrough. The low air permeability and low water-vapor permeability of the conduvtive film were due to the fusion of synthetic resin When one liter of water was put into a package produced by heatsealing the conductive film and left as it was for a long time, there could be observed no percolation of water. The heat-seal strength of the conductive film was likewise sufficient. EXAMPLE 8 In this example, four conductive films were produced in the same manner as in Example 7 while changing the mixing ratio of each SWP or SSF as shown in the following Table 6; The properties of each conductive film are listed in Table 6. Table 6 Mixing ratio SWP 95 92.5 90 80 (parts by weight) SSF 5 7.5 10 20 SSF (% by volume) 0.6 0.9 1.3 2.8 2 Basis weight (g/m ) 51.5 50.8 53.4 53.5 Thickness (um) 56 56 54 47 Density (g/cm3) 0.92 0.91 0.99 1.14 Opacity (%) 3.3 3.6 4.5 6.1 Air permeability (sec/lOOmi) Tensile strength (Kg/15mm) 1.40 1.64 1.36 1.26 Surface resistivity (Q*cm) 2.1x101 4.2x100 2.4x100 7.7x10-1 Each conductive film was found to have excellent transparency.. EXAMPLE 9 In this example, three conductive films were produced in the same manner as in Example 7 except for employing as the conductive fiber the carbon fiber (product of Kureha Chemical Industry, Ltd., carbon fiber prepared from pitch, average fiber length: 6 mm, diameter: 12.5 #m) of which surface was coated with nickel in thickness of about 1 um by chemical plating (NI-CF conductive fiber). The properties of the thus produced conductive film are listed in the following Table 7. Table 7 Mixing ratio SWP 97 95 90 (parts by weight) Ni-CF 3 5 10 Ni-CF (% by volume) 0.8 1.4 2.9 Basis weight (g/cmê) 51.3 49.4 49.6 Thickness (pm) 58 62 60 Density (g/cm3) 0.88 0.79 0.83 Opacity (%) 4.9 6.9 13.8 Air permeability (sec/lOOmi) = ¯ 69000 Tensile strength (Xg/lSmmf 1.32 1.28 1.17 Surface resistivity (Q-cm) 5.4 x 102 2.8 x 101 1.8 x 100 EXAMPLE 10 A conductive film was produced in the same manner as in Example 9 while 20 % by volume of synthetic pulp SWP was displaced with chemical pulp. The employed chemical pulp was a needle-lief tree breached kraft pulp (NBKP) which had been beaten by means of a beater until the beating degree thereof became 300 ml CFS (Canadian Standard Freeness tester), and added to a slurry in which both SWP and Ni-CF were dispersed. The properties of the obtained conductive film are shown in the following Table 8. Table 8 Mixing ratio SWP 77.6 76 72 (parts by NBKP 19.4 19 18 weight) Ni-CF 3 5 10 Ni-CF (% by volume) 0.8 1.4 2.9 2 Basis weight (g/cm ) 50.9 51.1 50.6 Thickness ( > m} 58 56 55 Density (g/cm3) 0.88 0.92 0.92 Opacity (%) 12.3 13.5 19.7 Air permeability (sec/lOOmi) Tensile strength (Kg/l5mm) ' 2.30 2.27 2.11 Surface resistivity (g.cm) 1.9 x 102 8.5 x 10a 2.2 x 100 Comparing with the conductive film containing no NBKP in Example 9, the conductive film of this example had a relatively large opacity but it was enough to observe the packed contents therethrough when used as a package. EXAMPLE 11 A conductive film was produced in the same manner as in Example 7 except for employing as the conductive fiber a commercially available aluminum-coated glass fiber (A1-GF conductive fiber) (Product of Diamond Shamrock Corp., average fiber length: 4 mm, diameter of core glass: 13 Vm, aluminum coat: about 3.5 wm, total diameter: 20 #m). The properties of the thus produced conductive film are shown in the following Table 9. Table 9 Mixing ratio SWP 95 90 80 (parts by A1-GF 5 10 20 weight) SAI-GF (% by volume) 1.8 3.7 8.0 2 Basis weight (g/cm ) 50.7 52.7 52.3 Thickness (um) 55 54 54 Density (g/cm3) 0.92 0.97 0.97 Opacity t%) 5.0 6.9 11.3 )Air permeability (sec./100ml) ¯ 50000 10000 Tensile strength (Xg/lSmm) 1.06 1.00 0.77 Surface resistivity (n-cm) 1.7 x 100 1.1 x 100 2.2 x 10-1 The conductive film dispersed the silver colored aluminum coated glass fiber in the transparent resin matrix and had a wholly silver white colored and transparent appearance. EXAMPLE 12 Example 7 was repeated except for employing as the thermoplastic synthetic pulp ES-Chop# thermoplastic (product of Chisso Corp., composite fiber of polyethylene and polypropylene, m.p.: 165 - 170CC, fiber length: 5mm, 3 denier) and polyvinyl alcohol fibrous binder (PVA). The mixing ratio of ES#Chop¯/PVA/SSF was 72j8/20 parts by weight (90/7/3 % by volume). The properties of the obtained conductive film are listed in the following Table 10. Table 10 Basis weight (g/m2) 49.8 Thickness ( m) 45 Density (g/cm3) 1.11 Opacity (%) 14.5 Air permeability (sec/lOOml) 5000 Tensile strength (Rg/15mm) 2.11 Surface resistivity (Q-cm) 6.25 x 10 2 Comparing with Example 7, the conductive film of this example had a slightly low opacity and a surface resistivity of same degree.

Claims: CLAIMS 1. A conductive film comprising a transparent matrix of a thermoplastic resin having short conductive fibers in contact with one another dispersed therein such that the film has an opacity of 30S or less and a surface resistivity of 1 x 108#.cm or less. 2 A conductive film according claim 1 wherein the short conductive fibers are carbon fibers. 3. A conductive film according to claim 2 wherein the carbon fibers have a length of from 1 to 25 mm and a diameter of from 5 to 30 )Im, 4. A conductive film according to claim 2 or 3 wherein the carbon fiber is present in an amount of 0.5 to 20% by volume. 5. A conductive film according to claim 1 wherein the short conductive fibers are metal or metal-coated fibers selected from stainless steel fibers, aluminum fibers, brass fibers, carbon fibers coated with aluminum or nickel, and glass fibers coated with aluminum or nickel. 6. A conductive film according to claim 5 wherein the metal or metal-coated fibers have a length of from 1 to 25 mm a diameter of from 1 to 100 pm. 7. A conductive film according to claim 6 wherein the metal or metal-coated fibers have a length of from 3 3 to 15 mm and a diameter of 20 pm or less. 8. A conductive film according to any one of claims 5 to 7 wherein the metal or metal-coated fiber is present in an amount of 0.5 to 30% by volume. 9. A conductive film according to any one of the preceding claims wherein upto less than 50S of the volume of the thermoplastic resin is replaced by chemical pulp. 10. A conductive film according to claim 9 wherein up to less than 30% of the volume of the thermoplastic resin is replaced by chemical pulp. 11. A conductive film according to claim 9 or 10 wherein the carbon fibers are present in an amount of less than 6% by volume. 12. A conductive film according to claim 9 or 10 wherein the metal or metal-coated fibers are present in an amount of less than 15% by volume. 13. A conductive film according to any one of the preceding claims which has a surface resistivity of 1 x 106#.cm or less. 14. A conductive film according to any one of the preceding claims wherein cellulose fibers are further dispersed in the transparent matrix. 15. A conductive film according to any one of the preceding claims which has a thickness of not more than 100 pm. 16. A process of the preparation of a conductive film as claimed in any one of the preceding claims, which process comprises mixing a thermoplastic synthetic pulp slurry with the short conductive fibers forming a raw paper sheet from the resultant mixture by means of paper-making apparatus and heating the raw paper sheet under pressure at a temperature higher than the melting point of the thermoplastic synthetic pulp. 17. A process according to claim 16 wherein up to less than 50% of the volume of the thermoplastic synthetic pulp is replaced by chemical pulp. 18. A process according to claim 17 wherein up to less than 30% of the volume of the thermoplastic synthetic pulp is replaced by chemical pulp.

Inventors: EGAWA, HARUNOBU, KATOU, ITSUPEI, KOUNO, TOMIHISA, KOUYAMA, TOSHITAKA
Applicants: KUREHA KAGAKU KOGYO KABUSHIKI KAISHA, MISHIMA PAPER CO. LTD
Application year: 1983
Main classification: D21H5
IPC codes: C08K7, H01B1, C08J5