Continuous mixer

Abstract

A continuous mixer with twin parallel rotors, a feed end and a discharge end is disclosed which is characterized by mismatched rotors. The apexes, or points at which the rotor tips change direction, are substantially misaligned as between the individual rotors of the pair.

What is claimed is: .[.1. Apparatus comprising 
     
        different from the first distance or the second distance..]. .[.2. Apparatus as in claim 1 further comprising a means for driving the first rotor and the second rotor in contrarotation so that they move toward the discharge orifice as they sweep by each other with the screw flights of the feed portions of the first rotor and the second rotor rotating so as to advance material toward the discharge orifice..]. .[.3. Apparatus as in claim 2 further comprising a means for driving the first rotor at a faster rate of rotation than the second rotor, said faster rate of rotation being in the range of from about 1.05 to about 1.3 times the rate of rotation of the second rotor..]. .[.4. Apparatus as in claim 3 wherein the twist lengths of the first tips on the first and second mixing portions of the first rotor are about equal and are in the range of 0.7-2 times the length of the mixing section, wherein the twist lengths of the second tips on the first and second mixing portions of the first rotor are about equal and are in the range of 0.7-2 times the length of the mixing section, wherein the twist lengths of the first tips on the first and second mixing portions of the second rotor are about equal and are in the range of 0.7-2 times the length of the mixing section, and wherein the twist lengths of the second tips on the first and second mixing portions of the second rotor are about equal and are in the range of 0.7-2 times the length of the mixing section..]. .[.5. Apparatus as in claim 4 wherein the first apex is positioned at a distance in the range of about 0.3 to about 0.7 mixing section lengths from the discharge end of the mixing section, wherein the second apex is positioned in the range of from about 0.2 to about 0.6 mixing section lengths from the discharge end of the mixing section, wherein the third apex is positioned in the range of from about 0.45 to about 0.8 mixing section lengths from the discharge end of the mixing section, and wherein the fourth apex is positioned in the range of from 0.4 to about 0.8 mixing section lengths from the discharge end of the mixing section..]. .[.6. Apparatus as in claim 5 wherein the second apex is positioned in the range of 0.3 to 0.5 mixing section lengths from the discharge end and is the closest apex to the discharge end of the mixing section and wherein the third apex is positioned in the range of 0.5 to 0.8 mixing section lengths from the discharge end of the mixing section and is the furtherest apex from the discharge end of the mixing section..]. .[.7. Apparatus as in claim 6 wherein about 0.2 to about 0.6 mixing section lengths separates the second apex from the third apex..]. .[.8. Apparatus as in claim 7 wherein about 0.25 to about 0.5 mixing section lengths separates the second apex from the third apex..]. .[.9. Apparatus as in claim 8 wherein the upstream edge of the discharge orifice is positioned at a distance in the range of from about 0.1 to about 0.3 mixing section lengths from the discharge end of the mixing section..]. .[.10. Apparatus as in claim 9 wherein the means for driving the first rotor at a faster rate of rotation than the second rotor drives the first rotor at about 1.1 times the rate of the second rotor, wherein the twist length of the first rotor first tips is about 1.4 times the length of the mixing section, wherein the twist length of the first rotor second tips is about 1.4 times the length of the mixing section, wherein the twist length of the second rotor first tips is about 1.3 times the length of the mixing section, wherein the twist length of the second rotor second tips is about 1.5 times the length of the mixing section, wherein the first apex is positioned about 0.45 mixing section lengths from the discharge end of the mixing section, wherein the second apex is positioned about 0.4 mixing section lengths from the discharge end of the mixing section, wherein the third apex is positioned about 0.65 mixing section lengths from the discharge end of the mixing section and wherein the fourth apex is positioned about 0.6 mixing section lengths from the discharge end of the 
     
     
        mixing section..]. 11. A process for melting a particulate material, said particulate material .[.being characterized as a thermoplastic resin.]. .Iadd.comprising a polyolefin .Iaddend.having a flux point of between about 100° C. and 400° C.; said process comprising the steps of (a) introducing the particulate material into at least one screw feeder, and   (b) forcing the particulate material by the action of the at least one screw feeder into a mixing chamber having the following characteristics (i) the mixing chamber is formed by a first generally cylindrical chamber and a second generally cylindrical chamber which are interconnecting and parallel to each other in a housing;   (ii) the at least one screw feeder is positioned at a first end of the mixing chamber;   (iii) a discharge orifice is positioned near the second end of the mixing chamber;   (iv) a first rotor is positioned in the first generally cylindrical chamber, said first rotor being characterized by a first tip beginning at the first end of the mixing chamber and following a helical path spiraling in a first rotational direction at a pitch greater than about half of a mixing chamber length and a second tip beginning at the end of the first tip and following a helical path spiraling in a second rotational direction at a pitch greater than about half of a mixing chamber length, said first tip meeting with said second tip at an apex which is positioned at a distance from the first end of the mixing chamber of between about 30% and about 70% of the distance to the second end of the mixing chamber;   (v) a second rotor is positioned in the second generally cylindrical chamber, said second rotor being characterized by a first tip beginning at the first end of the mixing chamber and following a helical path spiraling in the second rotational direction at a pitch greater than about half of a mixing chamber length and a second tip beginning at the end of the first tip and following a halical path spiraling in the first rotational direction at a pitch greater than about half of a mixing chamber length, said first tip meeting with said second tip at an apex which is positioned at a distance from the first end of the mixing chamber of between about 30% and about 70% of the distance to the second end of the mixing chamber, the difference in the positioning of the apex of the first rotor and the apex of the second rotor being at least 20% of the distance between the first end of the mixing chamber and the second end of the mixing chamber; and     (c) counterrotating the first rotor and the second rotor to melt the particulate material, said first rotor and said second rotor being rotated in the direction away from the first rotor apex and the second rotor apex so that the first rotor second tip and the second rotor second tip are rotating in the direction of the discharge orifice as they sweep by each   
     
     
        other. 12. A process as in claim 11 further comprising introducing additives into the mixing chamber for mixing with the particulate 
     
     
        material. 13. A process as in claim 12 wherein the particulate material comprises polyethylene and the additives comprise carbon black and from about 0.5 to about 25 pounds of carbon black are introduced into the 
     
     
        mixing chamber per every 100 pounds of polyethylene. 14. A process as in claim 13 wherein a ribbon of polyethylene melt containing carbon black is forced through the discharge orifice from the mixing chamber by the forcing of additional particulate material into the mixing chamber by the 
     
     
        at least one screw feeder. 15. A process as in claim 14 wherein from about 0.05 to about 0.20 kilowatt hours of energy are supplied to the motor means for each kilogram of material forced from the discharge orifice. 
     
     
            A process as in claim 15 wherein the mixing chamber is further characterized in that the first rotor first tip and the first rotor second tip each have a twist length in the range of from about 0.7 to about 2 mixing chamber lengths and the first rotor apex is positioned from the first end of the mixing chamber at a distance in the range of from about 55 to about 70% of the distance to the second end of the mixing chamber; the second rotor first tip and the second rotor second tip each have a twist length in the range of from about 0.7 to about 2 mixing chamber lengths and the second rotor apex is positioned at a distance in the range of from about 30 to about 45 percent of the distance to the second end of 
     
     
        the mixing chamber. 17. A process as in claim 16 wherein each of the first rotor and the second rotor have a generally elliptical cross section in the mixing chamber, said first rotor being further characterized by a third tip generally opposed from the first tip and a fourth tip generally opposed from the second tip, said third tip and said fourth tip coming together to form a first rotor second apex pointing in the same rotational direction as the first rotor apex and spaced from the first end of the mixing chamber between the first rotor apex and the second rotor apex; said second rotor being further characterized by a third tip generally opposed from the first tip and a fourth tip generally opposed from the second tip, said third tip and said fourth tip coming together to form a second rotor second apex pointing in the same rotational direction as the second rotor apex and spaced from the first end of the mixing chamber 
     
     
        between the first rotor apex and the second rotor apex. 18. A process as in claim 17 further comprising rotating the first rotor at a rate in the range of 1.05 to about 1.3 times the rotational rate of the second rotor.