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A method and high-pressure mixing device for co-injection of polymeric reactive components, in particular for polyurethane and epoxy mixtures. The polymeric components are supplied in a common pressure chamber where they flow at a same pressure and in an unmixed state into a forwardly converging for

A method and high-pressure mixing device for co-injection of polymeric reactive components, in particular for polyurethane and epoxy mixtures. The polymeric components are supplied in a common pressure chamber where they flow at a same pressure and in an unmixed state into a forwardly converging fore portion of the pressure chamber, and through a settable co-injection orifice to be co-injected, in the unmixed state, into a mixing chamber transversely oriented to the pressure chamber. The settable co-injection orifice consists in an elongated restriction that longitudinally extends on a side wall of the mixing chamber orthogonally oriented to an intersecting the forwardly converging fore portion of the pressure chamber; a first cleaning member and a second cleaning member are sequentially reciprocable in the pressure chamber to eject the remaining unmixed polymeric components, respectively in the mixing chamber to eject the remaining mixture, and stop elements are provided to set an open section of the elongated restriction, by adjustably stopping the fore end of the cleaning member for the mixing chamber, in respect to the same elongated restriction of the co-injection orifice.

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1. A method for mixing a first and at least a second polymeric reactive component by a self-cleaning high-pressure mixing device comprising the steps of: configuring the mixing device with a pressure chamber having a forwardly converging fore portion in fluid communication with a mixing chamber thro

1. A method for mixing a first and at least a second polymeric reactive component by a self-cleaning high-pressure mixing device comprising the steps of: configuring the mixing device with a pressure chamber having a forwardly converging fore portion in fluid communication with a mixing chamber through a settable co-injection orifice consisting of an elongated restriction;a first cleaning member for the pressure chamber and a second cleaning member for the mixing chamber; each of first and second cleaning members having a fore end and being reciprocable between an advanced and a retracted position;feeding the first and at least the second polymeric reactive components into the pressure chamber maintaining the polymeric reactive component inside the pressure chamber at a same high pressure and in an unmixed state;flowing the polymeric reactive components at said high pressure and in the unmixed state, from the pressure chamber to said forwardly converging fore portion to increase the flowing velocity of the unmixed first and second polymeric reactive components;setting an open section of the elongated restriction of the co-injection orifice by adjusting the position of the fore end of the second cleaning member in respect to the same co-injection orifice, to adjust the high pressure of the unmixed polymeric reactive components in the pressure chamber;co-injecting the unmixed polymeric reactive components into the mixing chamber, causing a pressure drop and a mixing of the polymeric reactive components into a resulting reactive mixture, while the reactive components are flowing through the elongated restriction of the set open section of the co-injection orifice and into the mixing chamber of the mixing device; andejecting the remaining unmixed polymeric reactive components from the pressure chamber and from the forwardly converging fore portion, as well as ejecting the remaining reactive mixture from the mixing chamber, by sequentially moving the first and the second cleaning members in their advanced position in the pressure chamber, respectively in the mixing chamber of the mixing device. 2. The method according to claim 1, wherein a pressure drop equal to or greater than 40 bar is provided between the pressure chamber and the mixing chamber by changing the open section of the co-injection orifice to generate turbulent conditions in the flow of the unmixed polymeric reactive components awhile they are injected into the mixing chamber through the co-injection orifice. 3. The method according to claim 2, wherein the open section of the co-injection orifice is changed by adjusting the position of the fore end of the second cleaning member in the retracted position of the second cleaning member. 4. A self-cleaning high-pressure mixing device suitable for mixing polymeric reactive components in a resulting reactive mixture, comprising: a cylindrical pressure chamber having a first diameter D1 and a forwardly converging fore portion;a cylindrical mixing chamber having a second diameter D2 comparatively smaller than the first diameter of the pressure chamber;the forwardly converging fore portion of the pressure chamber being in fluid communication with the mixing chamber through a settable co-injection orifice;first and second cleaning members each having a fore end, the first and second cleaning members being reciprocable in the pressure chamber respectively in the mixing chamber between a retracted and an advanced condition; andhydraulic actuators to sequentially reciprocate the first and second cleaning members;the settable co-injection orifice consisting of an elongated restriction longitudinally extending on a side wall of the mixing chamber the elongated restriction being transversely oriented to and intersecting the forwardly converging fore portion of the pressure chamber;the mixing device comprising an adjustable stop element for the second cleaning member, the stop element being, configured to provide an open section of the elongated restriction to adjust a high pressure of the unmixed polymeric reactive components in the pressure chamber, by setting the fore end position of the second cleaning member in the retracted condition, in respect to the elongated restriction of co-injection orifice. 5. The high-pressure mixing apparatus according to claim 4, wherein the first diameter D1 of the pressure chamber and the second diameter D2 of the mixing chamber have a ratio D1/D2 comprised between 1.4 and 15. 6. The high-pressure mixing device according to claim 4, wherein the forwardly converging fore portion of the pressure chamber and a forwardly converging end portion of the first cleaning member of the pressure chamber have a convergence angle comprised between 40° and 180°. 7. The high-pressure mixing device according to claim 6, wherein the forwardly converging fore portion of the pressure chamber and the fore end of the first cleaning member intended to come into contact with one another, are configured with a forwardly slanted flat surface with respect to the co-injection orifice, by an angle comprised between 30° and 90°. 8. The high-pressure mixing device according to claim 6, wherein the forwardly converging fore portion of the pressure chamber and the fore end of the first cleaning member intended to come into contact with one another, are configured with mating conical surfaces. 9. The high-pressure mixing device according to claim 6, wherein the forwardly converging fore portion of the pressure chamber and the fore end portion of the first cleaning member intended to come into contact with one another, are configured with two opposite mating flat surfaces, forwardly converging towards the co-injection orifice, by an angle comprised between 40° and 180°. 10. The high-pressure mixing device according to claim 4, wherein the forwardly converging fore portion of the pressure chamber and the fore end portion of the first cleaning member are configured with matching semi spherical surfaces. 11. The high-pressure mixing device according to claim 4, wherein the second cleaning member of the mixing chamber is movable between an advanced closure position, a retracted opening, and a throttling position for the co-injection nozzle; and comprises a manually or automatically adjustable stop element for stopping the second cleaning member of the mixing chamber, in the retracted position for setting the open section of the co-injection orifice. 12. The high-pressure mixing device according to claim 4, wherein the pressure chamber, the mixing chamber and a delivering conduit are oriented according to three different vector directions. 13. The high-pressure mixing device according to claim 4 wherein the diameter of the second cleaning member and of the mixing chamber is at least one half the diameter of the pressure chamber. 14. The high-pressure mixing device according to claim 4, wherein the longitudinal axis of the mixing chamber forms, with the longitudinal axis of the pressure chamber, an angle comprised between 15° and 165°. 15. The high-pressure mixing device according to claim 4, comprising a delivery conduit for the resulting mixture, axially aligned to the mixing chamber, and to a self-cleaning spray nozzle. 16. The high-pressure mixing device according to claim 15, wherein the second cleaning member for the mixing chamber is movable between the retracted position for setting the open section of the co-injection orifice, and the advanced closure position in which the second cleaning member extends into the axially aligned mixing chamber, the delivery conduit and the spray nozzle. 17. The high-pressure mixing device according to claim 16, wherein the second cleaning member for the mixing chamber, the delivery conduit and the spray nozzle, is configured with a fore end conforming to an internal surface of an exit hole of the spray nozzle. 18. The high pressure mixing device according to claim 4, in which the mixing chamber axially extends in a cylindrical delivery conduit provided with a spray nozzle having an injection hole for ejecting the resulting polymeric reactive mixture, wherein the second cleaning member of the mixing chamber, in the advanced condition of the same second cleaning member, extends in the delivery conduit and through the an ejection hole of the spray nozzle, the fore end of the second cleaning member conforming to an internal surface of the ejection hole.