(US5464503-A)      Unreacted hydrocarbons and metal components from a tyre liquefying process reactor (4) are discharged onto a screw auger and heated to convert the hydrocarbons to liq. and gas. Most of the gas and liq. are drawn off. Residual gas is cooled, pref. by coils, and converted to condensate in a vertical conduit (45) from which it is drawn off. The metal components are discharged from the vertical conduit.    Pref. the components are heated to 900-1500 deg.F by a pyrolysis reactor (38) located about the auger.    USE -   Treating tyre pyrolysis residues, e.g. oil coated metal.    (JP9507506-W)      A discharge system (45) for tyre liquefying processes reacting tyres and oil using a reactor (14) comprises: (a) receiving components include hydrocarbon and metal components; (b) moving means (20) connected to receiving means moves unreacted components through heated area; (c) pyrolysis means (38) heats an area of the system to a temperature sufficient to convert unreacted hydrocarbon components to liquid and gas; (d) means to draw off liquid, and most gas, from pyrolysis; (e) converter converts remaining gas to a condensate; and (f) discharge means (45), connected to pyrolysis means, discharges metal components and draws off condensate.    USE -   The method discharges unreacted components from a reaction process where unreacted components are moved through a pyrolysis reactor (38).    ADVANTAGE -   Unreacted components are heated to a temperature sufficient to convert the unreacted hydrocarbons to a liquid and gas. They are then drawn off and the remaining gas is converted to a condensate and discharges the metal. Condensate is removed for further use.    (US5705035-A)      A discharge system (45) for tyre liquefying processes reacting tyres and oil using a reactor (14) comprises: (a) receiving components include hydrocarbon and metal components; (b) moving means (20) connected to receiving means moves unreacted components through heated area; (c) pyrolysis means (38) heats an area of the system to a temperature sufficient to convert unreacted hydrocarbon components to liquid and gas; (d) means to draw off liquid, and most gas, from pyrolysis; (e) converter converts remaining gas to a condensate; and (f) discharge means (45), connected to pyrolysis means, discharges metal components and draws off condensate.    USE -   The method discharges unreacted components from a reaction process where unreacted components are moved through a pyrolysis reactor (38).    ADVANTAGE -   Unreacted components are heated to a temperature sufficient to convert the unreacted hydrocarbons to a liquid and gas. They are then drawn off and the remaining gas is converted to a condensate and discharges the metal. Condensate is removed for further use.    (CN1141646-A)      A discharge system (45) for tyre liquefying processes reacting tyres and oil using a reactor (14) comprises: (a) receiving components include hydrocarbon and metal components; (b) moving means (20) connected to receiving means moves unreacted components through heated area; (c) pyrolysis means (38) heats an area of the system to a temperature sufficient to convert unreacted hydrocarbon components to liquid and gas; (d) means to draw off liquid, and most gas, from pyrolysis; (e) converter converts remaining gas to a condensate; and (f) discharge means (45), connected to pyrolysis means, discharges metal components and draws off condensate.    USE -   The method discharges unreacted components from a reaction process where unreacted components are moved through a pyrolysis reactor (38).    ADVANTAGE -   Unreacted components are heated to a temperature sufficient to convert the unreacted hydrocarbons to a liquid and gas. They are then drawn off and the remaining gas is converted to a condensate and discharges the metal. Condensate is removed for further use.