Alternate polymer extrusion method with reduced drool
View Patent ↗An alternate polymer extrusion method and system reduces “drool” effects that detract from precise control over the content of two or more materials in an extrudate along its length. In the system, two or more extruders direct melt to two or more gear pumps. Control of the speed of the gear pumps controls the amount of each material emergent from the pumps, proceeding to a convergence in the paths from the pumps and thence to a die. Melt in each path between each pump and the convergence tends to expand and drool into the convergence as its associated pump is slowed and stopped. To prevent this, in the die, a constriction in each path just upstream of the convergence greatly reduces drool past that point by requiring a much greater pressure to force the melt past the constriction. The increased pressure required increases compression and expansion of the melt between the pump and the construction as a pump starts or increases in speed, on one hand, and stop or decreases in speed, on the other hand. Compensatory pump speed changes are made to counter this effect.
1. A method of alternate polymer extrusion comprising:
(a) providing a first extruder including a first gear pump,
(b) providing a second extruder including a second gear pump;
(c) supplying a melt of a first material to the first gear pump;
(d) supplying a melt of a second material to the second gear pump;
(e) directing the melt of the first material along a first melt path from the first gear pump;
(f) directing the melt of the second material along a second melt path from the second gear pump;
(g) providing a convergence of the first and second melt paths;
(h) directing the melt of at least one of the first and second materials from the convergence of the first and second paths to an outlet of a die;
(i) extruding the melt of the at least one material by forcing through the die;
(j) varying the speed of the first and second gear pumps to vary the rate of flow of the melts of the first and second materials to the convergence; and
(k) providing constrictions constricting each of the first and second melt paths proximate the convergence sufficiently to at least substantially reduce drool of melt out of the first and second melt paths to the convergence upon substantial slowing or stopping of one of the gear pumps.
2. The method of alternate polymer extrusion according to claim 1 , further comprising:
(l) repeatedly varying the speed of each of the gear pumps to repeatedly vary the content of the first and second materials in an extrudate emerging from the die.
3. The method of alternate polymer extrusion according to claim 2 , further comprising:
(m) initially imparting a compensatory increase in the speed of each gear pump in addition to each speed increase of that pump for increased delivery of the melt of one of the first and second materials therethrough, the compensatory increase in speed compensating for initial compression of that melt between the gear pump and one of the constrictions as that pump starts or increases in speed.
4. The method of alternate polymer extrusion according to either of claims 2 or 3 , further comprising initially imparting a compensatory decrease in the speed of each gear pump in addition to each speed decrease of that pump for decreased delivery of the melt of one of the first and second materials therethrough, the compensatory decrease in speed compensating for the initial expansion of melt between the gear pump and one of the constrictions as that pump slows or stops.
5. The method of alternate polymer extrusion according to claim 2 , further comprising determining a dimension of an extrudate emerging from the die, and controlling a dimension-affecting parameter of the alternate polymer extrusion method to control said dimension.
6. The method of alternate polymer extrusion according to claim 5 , wherein the dimension-affecting parameter is the speed of at least one of the gear pumps.
7. The method of alternate polymer extrusion according to claim 6 , further comprising determining the lag time between a pump speed alteration and a resultant dimension variation, and wherein controlling the dimension-affecting parameter includes timing corrective pump speed of the at least one pump to control the dimension at a location along the extrudate that is subsequently extruded.
8. The method of alternate polymer extrusion according to claim 5 , wherein controlling a dimension-affecting parameter comprises controlling a pressure differential between the interior and the exterior of a hollow extruder.
9. The method of alternate polymer extrusion according to claim 5 , wherein controlling a dimension-affecting parameter comprises controlling the speed of a puller.