Abstract: A co-extruded sheet contains a polycarbonate resin, and includes a core layer formed from a foam resin, a skin layer formed from a non-foaming resin and laminated to one major surface of the core layer, and a second skin layer laminated to another major surface of the core layer. A melt volume-flow rate of the polycarbonate resin contained in the core layer (MVRc) and a melt volume-flow rate of the polycarbonate resin contained in one of the skin layers (MVRs) satisfy the following expression, (1): 1.5 ? MVRs / MVRc ? 8. .

Abstract: A co-extruded sheet reduces swelling and/or cracking of the surface occurring during thermal shaping such as vacuum forming and provides improved mechanical strength. A co-extruded sheet contains a polycarbonate resin, and includes a core layer formed from a foam resin and skin layers formed from a non-foaming resin. The skin layer is laminated to one major surface of the core layer, while the skin layer is laminated to the other major surface of the core layer. The core layer has an expansion ratio of 1.6 to 3. The co-extruded sheet has a thickness of 1 to 5 mm and satisfies expression (1): 0.10? (t1+t2)/T?0.5. In expression (1), t1 indicates the thickness of the skin layer, t2 indicates the thickness of the second skin layer, and T indicates the thickness of the co-extruded sheet.

Abstract: A co-extruded sheet reduces swelling and/or cracking of the surface occurring during thermal shaping such as vacuum forming and provides improved mechanical strength. A co-extruded sheet contains a polycarbonate resin, and includes a core layer formed from a foam resin and skin layers formed from a non-foaming resin. The skin layer is laminated to one major surface of the core layer, while the skin layer is laminated to the other major surface of the core layer. The co-extruded sheet has a density of 0.4 to 0.9 g/cm3. The co-extruded sheet has a thickness of 1 to 5 mm and satisfies expression (1): 0.10?(t1+t2)/T?0.5. In expression (1), t1 indicates the thickness of the skin layer, t2 indicates the thickness of the second skin layer, and T indicates the thickness of the co-extruded sheet.

Abstract: A resin sheet is provided that provide both light-weight properties and mechanical strength using a thermoplastic resin with high deflection temperature under load. The resin sheet is formed from a thermoplastic resin, including: a core layer being a foam resin layer; and skin layers located outward of the core layer as determined along the thickness direction, the core and skin layers forming a continuity. The core layer includes a region A1 and regions A2 each located between the region A1 and the associated skin layer. The regions A2 has a lower average porosity than the region A1, said average porosity being lower than 50%. The thermoplastic resin has a deflection temperature under load not lower than 90° C. The resin sheet has a thickness of 1 to 40 mm. Each skin layer has a thickness of 5 to 50% of the thickness of the resin sheet.

Abstract: A method of decomposing an organic compound includes decomposing an organic compound by alkyl carbonate at 250° C. or more. The organic compound includes a cross-linked polymer. The cross-linked polymer includes a polymer cross-linked by organic peroxide cross-linking, radiation cross-linking, or silane cross-linking The alkyl carbonate includes dimethyl carbonate or diethyl carbonate.

Abstract: There is provided an insulated wire, including: a copper conductor containing copper and having an oxide layer on its surface, with a thickness of 5 nm or more and 300 nm or less; and an insulation coating formed on a surface of the oxide layer and made of a resin composition including engineering plastic having a melting point or a softening point of 220° C. or more.

Abstract: An insulated wire includes a conductor and an insulation covering formed thereon. The insulation covering includes a first insulation covering layer formed directly on the conductor and a second insulation covering layer formed on a periphery of the first insulation covering layer. The first insulation covering layer includes a resin composition including a resin (A) including polyphenylene sulfide and a resin (B) including polyamide mixed at a mass ratio in a range of “30/70?B/A?90/10”. The second insulation covering layer includes a resin composition mainly including a resin (C) including polyphenylene sulfide or polyetheretherketone.

Abstract: A method of treating a polymer includes oxidatively treating the polymer including a carbon-carbon bond framework in a gas atmosphere at a pressure of not less than 5.0 MPa and at a temperature of higher than 140° C. and lower than 200° C. by using oxygen included in the gas atmosphere.

Abstract: A method of treating a polymer compound has the steps of: mixing and agitating the polymer compound and a chemical agent in an extruder while controlling the inside of the extruder to be kept at a high temperature and a high pressure to have a reaction mixture containing a polymer treated product; supplying the reaction mixture continuously into a high-pressure container disposed following the extruder and retaining the reaction mixture at the high temperature and high pressure for a predetermined time; then supplying the reaction mixture continuously to a chemical agent separator to separate the polymer treated product; and supplying the separated polymer treated product continuously to a molding means to form it into a molded material.

Abstract: A method of treating a polymer includes oxidatively treating the polymer including a carbon-carbon bond framework in a gas atmosphere at a pressure of not less than 5.0 MPa and at a temperature of higher than 140° C. and lower than 200° C. by using oxygen included in the gas atmosphere.

Abstract: A method of treating a polymer compound has the steps of: mixing and agitating the polymer compound and a chemical agent in an extruder while controlling the inside of the extruder to be kept at a high temperature and a high pressure to have a reaction mixture containing a polymer treated product; supplying the reaction mixture continuously into a high-pressure container disposed following the extruder and retaining the reaction mixture at the high temperature and high pressure for a predetermined time; then supplying the reaction mixture continuously to a chemical agent separator to separate the polymer treated product; and supplying the separated polymer treated product continuously to a molding means to form it into a molded material.

Abstract: A method of treating a polymer compound has the steps of: mixing and agitating the polymer compound and a chemical agent in an extruder while controlling the inside of the extruder to be kept at a high temperature and a high pressure to have a reaction mixture containing a polymer treated product; supplying the reaction mixture continuously into a high-pressure container disposed following the extruder and retaining the reaction mixture at the high temperature and high pressure for a predetermined time; then supplying the reaction mixture continuously to a chemical agent separator to separate the polymer treated product; and supplying the separated polymer treated product continuously to a molding means to form it into a molded material.

Abstract: A method of decomposing an organic compound includes decomposing an organic compound by alkyl carbonate at 250° C. or more. The organic compound includes a cross-linked polymer. The cross-linked polymer includes a polymer cross-linked by organic peroxide cross-linking, radiation cross-linking, or silane cross-linking The alkyl carbonate includes dimethyl carbonate or diethyl carbonate.

Abstract: The object of the present invention resides in providing a method and instrument of polymer processing treatment, wherein a sudden pressure change due to expansion by gasification of a reactant when it is exhausted from a reacting extruder is given in a little amount to a molding machine for a treated substance, and a change in the amount of the material supplied to the molding machine and a variation in molding are little, and hence continuous and uniform molding is possible. That is, the method of the present invention resides in a method of polymer processing treatment, which includes the steps of: reacting a polymer with a reactant under mixing and stirring at a high temperature and a high pressure in the inside of a reacting extruder to produce the treated substance; introducing said treated substance and a remaining reactant into a reactant-separation tank to separate the treated substance and the reactant; and molding the separated treated substance.

Abstract: A polymer treating method has the steps of: reacting a polymer compound with a reaction agent in a reaction vessel to generate a polymer treatment product; discharging the polymer treatment product containing the reaction agent from the reaction vessel; depressurizing the polymer treatment product; introducing the polymer treatment product into a degassing extruder; separating the reaction agent from the polymer treatment product through a vent box that is connected to upstream of the degassing extruder and that has a volume of equal to or more than that of the reaction vessel; and extruding the polymer treatment product from the degassing extruder.

Abstract: A cross-linked polymer is recycled by decomposing a C—C bond by an oxidative decomposition reaction using a nitrogen oxide in a supercritical carbon dioxide. A reaction temperature, a pressure and a reaction time are controlled such that a nitrogen oxide is sorbed at a branch point of a C—C bond of the cross-linked polymer. As a result, the branch point of the C—C bond is preferentially oxidized to cleave the C—C bond.

Abstract: A polymer treating method has the steps of: reacting a polymer compound with a reaction agent in a reaction vessel to generate a polymer treatment product; discharging the polymer treatment product containing the reaction agent from the reaction vessel; depressurizing the polymer treatment product; introducing the polymer treatment product into a degassing extruder; separating the reaction agent from the polymer treatment product through a vent box that is connected to upstream of the degassing extruder and that has a volume of equal to or more than that of the reaction vessel; and extruding the polymer treatment product from the degassing extruder.

Abstract: A polymer treating method has the steps of: reacting a polymer compound with a reaction agent in a reaction vessel to generate a polymer treatment product; discharging the polymer treatment product containing the reaction agent from the reaction vessel; depressurizing the polymer treatment product; introducing the polymer treatment product into a degassing extruder; separating the reaction agent from the polymer treatment product through a vent box that is connected to upstream of the degassing extruder and that has a volume of equal to or more than that of the reaction vessel; and extruding the polymer treatment product from the degassing extruder.

Abstract: A PWM signal generator comprises a pulse width indication signal generator outputting a pulse width indication signal, and a pulse width adjustment portion receiving the pulse width indication signal. The pulse width adjustment portion outputs an adjusted pulse width data which corresponds to the pulse width indication signal when the pulse width indicated by the pulse width indication signal is equal to or wider than a predetermined width. The pulse width adjustment portion accumulates the pulse width indicated by the pulse width indication signal when the pulse width indicated by the pulse width indication signal is narrower than the predetermined width. The pulse width adjustment portion outputs the adjusted pulse width data which corresponds to a sum data of the pulse width accumulated in the pulse width adjustment portion when the sum of the pulse width becomes equal to or wider than the predetermined width.

Abstract: A polymer treating method has the steps of: reacting a polymer compound with a reaction agent in a reaction vessel to generate a polymer treatment product; discharging the polymer treatment product containing the reaction agent from the reaction vessel; depressurizing the polymer treatment product; introducing the polymer treatment product into a degassing extruder; separating the reaction agent from the polymer treatment product through a vent box that is connected to upstream of the degassing extruder and that has a volume of equal to or more than that of the reaction vessel; and extruding the polymer treatment product from the degassing extruder.