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Accordingly, it is preferable that the melt index is a minimum of 0.1 g/10 minutes. It's preferable that the elastomer has an capability to be modified in order that a softened polyphenylene sulfide, which is prepared by mixing with the elastomer and kneading them with melting, has a flexural modulus of at most 30000 (ASTM D 790) and a tensile elongation at break of at least 5% (ASTM D 638). Representative examples of such an elastomer are, for example, an olefin copolymer containing an epoxy group (ethylene content material: 88% by weight, glycidyl methacrylate content material: 12% y weight), a hydrogenated styrenebutadience copolymer (TUFTEC M 1913 commercially available from Asahi Chemical Industry Co., Ltd.), an ethylene-propylene copolymer (TAFMER PO 680 commercially obtainable from MITSUI PETRO CHEMICAL INDUSTRIES, LTD.), and the like. The tetrafluoroethylene-perfluoroalkylvinyl ether copolymer is prescribed in ASTM D 3307, and has two sorts, i.e. Type I and sort II. The terminology "melt index" is intended to imply a price when the melt index is measured in accordance with Method A of ASTM D 1238 in this specification. As an example, a method comprising ading the organopolysiloxane having an ultra-high viscosity and the organopolysiloxane having a decrease viscosity individually to the thermoplastic resin whereas heating and kneading the thermoplastic resin and uniformly dispersing them, a way comprising adding the organopolysiloxane, which is previously ready by mixing the organopolysiloxane having an extremely-excessive viscosity and the organopolysiloxane having a lower viscosity in a prescribed proportion, to the melted thermoplastic resin and uniformly dispersing them, and the like will be exemplified.

Accordingly, when an inner coat is produced from the polytetrafluoroethylene, so-called a paste-extrusion methodology is employed. Accordingly, an organopolysiloxane having an ultra-high viscosity and an organopolysiloxane having a lower viscosity are used in the present invention so as to enhance extruding stability during producing a liner and to sufficiently release these organopolysiloxanes on the floor of the resin sufficiently. Because the above-mentioned organopolysiloxane having an extremely-excessive viscosity, a linear organopolysiloxane, a branched organopolysiloxane and the like can be exemplified. It is especially preferable that the content of the organopolysiloxane having an ultra-excessive viscosity is 50 to 80% by weight and the content material of the organopolysiloxane having a lower viscosity is 50 to 20% by weight. Within the above-talked about liner, a thermoplastic resin containing thirteen to 20% by weight of an dispersed in the resin, is used. Therefore, in some cases, as diclosed in Japanese Patent Unexamined Publication No. 231009/1985, a flexible tubular liner manufactured from a synthetic resin is formed on the inside floor of the conduit. The control cable of the present invention comprises a conduit having flexibility, the inside surface of which being set up with a liner and an interior cable having an internal coat, and the internal cable is inserted into the conduit in order that the internal cable freely slides within the conduit as mentioned above.

The thing of the current invention is to delete the above-mentioned disadvantages of conventional management cables and to supply a management cable which does not necessitate a lubricant to avoid a fancy coating operation and which can be used with clean sliding operation of the interior cable for an extended time frame. The present invention relates to a management cable, and more notably to a control cable glorious in load effectivity, and the inner cable of which being able to be easily operated for a long period of time. As an illustration, in case the shortage of lubricants is generated because of the lengthy period use of the management cable, there are some issues that the liner is totally worn down and the operationability of the control cable is excessively lowered, and the like. In the current invention, because the organopolysiloxane having an ultra-excessive viscosity and the organopolysiloxane having a lower viscosity are dispersively contained in the thermoplastic resin used within the above-talked about liner, it is of course that there is no such thing as a necessity to make use of a lubricant between the interspace of the conduit and the internal cable, and a wonderful function that the sliding operation of the conduit and the interior cable might be smoothly carried out for a long time period, is exhibited.

Because the polyphenylene sulfide is generally poor in elongation and suppleness as it is, it is preferable to use a polyphenylene sulfide containing 5 to 40% by weight of an elastomer. When the content of the organopolysiloxane having an ultra-excessive viscosity is much less that 45% by weight and the content material of the organopolysiloxane having a lower viscosity is extra that 55% by weight, an extruded product can't be produced because a slide between a screw and a resin occurs in an extruder and the feed of the resin cannot be carried out. Because the above-talked about organopolysiloxane having a lower viscosity, a linear organopolysiloxane and a branched organopolysiloxane are cited. The polymerization degrees of these varieties are totally different respectively. Hereinafter, the control cable of the present invention and the technical impact are defined in detail with evaluating some examples and comparative examples. However, in such a control cable, frictional resistance increases when the conduit is instantly contacted with the interior cable. However, there are several problems, within the control cable during which a lubricant is used, comparable to problem of operation for coating because dispersion of the load effectivity of products is attributable to the unevenness of a coating, rubbishes and dusts are easily adhered to the lubricant when making use of the lubricant to the control cable, and drip and the like are generated.