A device for processing scrap rubber has a reactor with a screw conveyor disposed inside a heating chamber, a thermal decomposition unit, burners, a condenser, a cyclone filter, and devices for discharging solid residue and removing a gas-vapor mixture. The reactor has two sections connected in parallel. The thermal decomposition unit has screw conveyors in each section, the conveyors have axial heating pipes with a coil. Along the length of the conveyors plates are arranged at the corners of an equilateral triangle in contact with and perpendicular to the side surface of the heating tube. A cylinder furnace with an evaporator and a burner is connected to the ends of the pipes. An outlet of the condenser is connected to a liquid fraction separator, inlets of the coils are connected to an outlet of the evaporator, and an inlet of the evaporator is connected to an outlet from the separator.

The present invention relates to a process for extracting polymers, preferably polyolefins, from polymer-containing waste material comprising the steps of: providing polymer-containing waste material comprising polyolefin material; contacting the polymer-containing waste material with a non-polar solvent (8) comprising at least one hydrocarbon, optionally halogenated hydrocarbon, having from 4 to 10 carbon atoms, to form a composition (C); heating the composition (C) at a dissolution temperature (T) in the range of 135 to 200? C. and a pressure (P) in the range of 0.1 to 5 MPa for a period of from 5 min to 5 h (M), to obtain a solution comprising the solvent (S) and the polyolefin material dissolved in the solvent (S), and an undissolved material (U); separating the undissolved material (U) from the solution; separating the polyolefin material from the solution, and optionally separating the solvent (S) from the solution.

The present invention relates to a process for extracting polymers, preferably polyolefins, from polymer-containing waste material comprising the steps of: providing polymer-containing waste material comprising polyolefin material; contacting the polymer-containing waste material with a non-polar solvent (8) comprising at least one hydrocarbon, optionally halogenated hydrocarbon, having from 4 to 10 carbon atoms, to form a composition (C); heating the composition (C) at a dissolution temperature (T) in the range of 135 to 200? C. and a pressure (P) in the range of 0.1 to 5 MPa for a period of from 5 min to 5 h (M), to obtain a solution comprising the solvent (S) and the polyolefin material dissolved in the solvent (S), and an undissolved material (U); separating the undissolved material (U) from the solution; separating the polyolefin material from the solution, and optionally separating the solvent (S) from the solution.

A continuous method for depolymerizing polycaprolactam waste into caprolactam is described. In the method, a melt of the polycaprolactam waste and an inert gas are fed to a reactor in a continuous manner. Water and an aromatic hydrocarbon are also fed to the reactor and the polycaprolactam waste is contacted with superheated steam of the water/hydrocarbon mixture at a temperature of between 260? C. and 300? C. and at a gauge pressure from 1 barg to 70 barg. Turbulent mixing conditions are created in the reactor, and a caprolactam-containing vapor stream is created in the reactor which exits the reactor at an outlet. The caprolactam is separated from the exited caprolactam-containing vapor stream by partial condensation, and collected. A reactor system for carrying out the method is also described.

A continuous method for depolymerizing polycaprolactam waste into caprolactam is described. In the method, a melt of the polycaprolactam waste and an inert gas are fed to a reactor in a continuous manner. Water and an aromatic hydrocarbon are also fed to the reactor and the polycaprolactam waste is contacted with superheated steam of the water/hydrocarbon mixture at a temperature of between 260? C. and 300? C. and at a gauge pressure from 1 barg to 70 barg. Turbulent mixing conditions are created in the reactor, and a caprolactam-containing vapor stream is created in the reactor which exits the reactor at an outlet. The caprolactam is separated from the exited caprolactam-containing vapor stream by partial condensation, and collected. A reactor system for carrying out the method is also described.

The present invention relates to a method for purification of a polymer material from plastic waste, wherein said polymer material comprises at least one target polymer, at least one non-target polymer and at least one impurity, wherein the method comprises the steps of providing said plastic waste in solid form; dissolving said polymer material; optionally, a first liquid-solid separation step; optionally, adding at least one additive; precipitating the at least one impurity and the at least one non-target polymer from the solution; optionally, adding at least one additive; separating the precipitate; optionally, adding at least one additive and separating the at least one additive and adsorbed remaining impurities; removing the residual solvent and, optionally degassing the purified target polymer material. The present invention further relates to a recyclate obtainable by said method.

The present invention relates to a method for purification of a polymer material from plastic waste, wherein said polymer material comprises at least one target polymer, at least one non-target polymer and at least one impurity, wherein the method comprises the steps of providing said plastic waste in solid form; dissolving said polymer material; optionally, a first liquid-solid separation step; optionally, adding at least one additive; precipitating the at least one impurity and the at least one non-target polymer from the solution; optionally, adding at least one additive; separating the precipitate; optionally, adding at least one additive and separating the at least one additive and adsorbed remaining impurities; removing the residual solvent and, optionally degassing the purified target polymer material. The present invention further relates to a recyclate obtainable by said method.

A process of: providing a polyfunctional compound selected from polyisocyanate, polyacrylate, and polyepoxy; and reacting the polyfunctional compound with a hydroxyl- or amine-terminated silyl-containing compound. The polyfunctional compound and the sylil-containing compound are at least difunctional. A thermoset made by this process.

A process of: providing a polyfunctional compound selected from polyisocyanate, polyacrylate, and polyepoxy; and reacting the polyfunctional compound with a hydroxyl- or amine-terminated silyl-containing compound. The polyfunctional compound and the sylil-containing compound are at least difunctional. A thermoset made by this process.

A release solvent composition for releasing a thermosetting resin coating film coated on a thermoplastic resin molded article, and the release solvent composition containing 1,1,2,2,3,3,4-heptafluorocyclopentane and aromatic alcohols and having no flash point.