Plastics extruder dimension and viscosity control system
View Patent ↗An extrusion control system that controls the cross section and viscosity during extrusion of even hard to control plastics like polyurethane. Cross section, A, is determined by measuring volumetric rate of deliver of melt through a gear pump V/t and the speed of the extrudate at a puller N/t. The cross-section area, A=(V/t)/(N/t), is controlled by controlling the puller speed. Pressure drop across the die, P, and the volume of melt delivered by the gear pump are measured and a term indicative of the viscosity of the melt is determined based on Vs=(KP)/V, Vs being the viscosity and K being a constant dependent on the size and shape of the die orifice. Viscosity variations are compensated by varying heat applied to the melt.
1. An extrusion system comprising:
(a) an extruder having a screw for moving plastic internally toward an end thereof,
(b) a screw motor connected in driving relation to the screw,
(c) a gear pump connected to the extruder to receive hot viscous plastic delivered thereto by the extruder,
(d) a gear pump motor connected in driving relation to the gear pump to move the hot viscous plastic therethrough,
(e) a die downstream of the gear pump for receiving hot viscous plastic moved through the gear pump to form an extrudate,
(f) a puller for pulling the extrudate away from the die,
(g) a puller motor connected in driving relation to the puller,
(h) a controller connected in controlling relation to the screw motor, the gear pump motor and the puller motor to control the speeds of the screw, the gear pump and the puller,
(i) a speed sensor operative to generate an electrical output indicative of the speed of the extrudate, the electrical output indicative of the speed of the extrudate being connected as an input to the controller,
(j) a gear pump speed encoder operatively connected to the gear pump to generate an electrical output indicative of the volume per unit of time of hot viscous plastic being forced through the die, the electrical output indicative of the volume per unit time being connected as an input to the controller,
(k) a screw speed encoder operatively connected to the screw to generate an electrical output indicative of the speed of the screw, the electrical output indicative of the speed of the screw being connected as an input to the controller,
(l) the extruder having at least one heater for imparting heat to the plastic being moved by the screw, the controller being connected in controlling relation to the at least one heater to control the amount of heat being imparted by the heater to the plastic being moved by the screw,
(m) a temperature sensor located to sense the temperature of the extruder where heat is being introduced to plastic being moved through the heater,
(n) a pressure sensor located upstream and proximate the die in the path of flow of the hot viscous plastic to the die and having an electrical output indicative of pressure there connected as an input to the controller,
(o) the controller being programmed to increase and decrease at least one of the gear pump speed and the speed of the puller motor, the puller and the extrudate in response to a change in the cross-sectional area of the extrudate derived from an indication of the speed of the gear pump delivered to the controller by the gear pump encoder and an indication of the speed of the extrudate delivered to the controller by the puller encoder, and
(p) the controller being programmed to increase and decrease the temperature of the viscous plastic in the extruder to maintain the viscosity of the viscous plastic in the extruder in response to a detected change in viscosity as indicated by a change in pressure in the hot viscous plastic by the pressure sensor upstream of and proximate the die.
2. The extrusion system according to claim 1 , wherein the controller is operative to calculate, from the puller encoder output indicative of speed N/t of the extrudate, and the gear pump encoder indicative of volume per unit time V/t of hot viscous plastic being pumped, the cross-sectional area of the extrudate A, per the formula
A
=
V
/
t
N
/
t
,
and the controller is operative to calculate, from the volume V of hot viscous plastic being pumped by the gear pump, and the pressure drop P across the die, a term proportional to the viscosity Vs of the hot viscous plastic at the die, per the formula
Vs
=
KP
V
,
where K is a constant.
3. The extrusion system according to claim 2 , wherein the controller is operative to increase or decrease the speed of the screw motor to increase or decrease heat delivered to the hot viscous plastic in the extruder upon detection of a changed viscosity.
4. The extrusion system according to claim 2 , wherein the controller is operative to increase or decrease heat delivered to the hot viscous plastic in the extruder by the at least one heater upon detection of a changed viscosity.
5. The extrusion system according to claim 2 , wherein the controller is operative to increase or decrease heat delivered to the hot viscous plastic in the extruder by controlling the movement of a coolant.
6. The extrusion system according to claim 5 , wherein the coolant is a liquid coolant introduced to coolant paths in heat transfer proximity to the hot viscous plastic in the extruder.
7. The extrusion system according to claim 5 , wherein the coolant is air, the system further comprising a fan under the control of the controller and operative to direct coolant air across the extruder.
8. The extrusion system according to claim 1 , wherein the speed sensor is an encoder coupled to a puller to provide an output indicative of the speed of the extrudate being pulled by the puller.
9. The extrusion system according to claim 1 , further comprising a gauge operative to measure a cross-sectional dimension of the extrudate.
10. The extrusion system according to claim 9 , wherein the extrudate is tubular, the gauge being operative to measure the outside diameter of the extrudate and the controller being operative to maintain the desired inside diameter of the extrudate based upon the measured outside diameter and calculated cross-sectional area.
11. An extrusion control system comprising:
(a) an extruder controller,
(b) means for measuring the speed of an extrudate,
(c) means for measuring the speed of a gear pump delivering hot viscous plastic to a die,
(d) means for controlling at least one of the speed of the extrudate and the speed of the gear pump to thereby control the cross-section of the extrudate,
(e) means for measuring the pressure in the hot viscous plastic proximate and upstream of the die as a measure of the pressure drop across the die, and
(f) means for controlling heat applied to the hot viscous plastic to control the viscosity of the plastic in the extruder as a function of a viscosity-indicative measure calculated from quantity of hot viscous plastic delivered to the die by the gear pump and pressure drop across the die.
12. The extrusion control system according to claim 11 , wherein the means for measuring the speed of the extrudate comprises an encoder coupled to a puller.
13. The extrusion control system according to claim 11 or 12 , wherein the means controlling the speed of the extrudate comprises a puller motor under control of the controller.
14. The extrusion control system according to claim 13 , wherein the means for measuring the speed of a gear pump comprises an encoder coupled to a gear pump motor.
15. The extrusion control system according to claim 13 , wherein the means for controlling heat applied to the hot viscous plastic comprises means for controlling the speed of an extruder screw moving the plastic in the extruder.
16. The extrusion control system according to claim 13 , wherein the means for controlling heat applied to the hot viscous plastic comprises means for controlling heaters proximate a path of movement of plastic in the extruder.
17. The extrusion control system according to claim 13 , wherein the means for controlling heat applied to the hot viscous plastic comprises the means for delivering a coolant to the extruder.
18. The extrusion control system according to claim 13 , wherein the controller comprises programming for (i) calculating the viscosity-indicative measure using the relationship
Vs
=
KP
V
,
where Vs is viscosity, P is the pressure drop across the die, V is the volume of hot viscous plastic delivered to the die by the gear pump, and K is a constant, and (ii) calculating cross section area,
A
=
V
/
t
N
/
t
,
where V/t is the volumetric rate of delivery of the hot viscous plastic by the gear pump, and N/t is the speed of the extrudate.
19. The extrusion control system according to claim 18 , further comprising means for measuring a cross-sectional dimension of the extrudate, the controller being operative to control an internal dimension of the extrudate based upon a calculated cross-sectional area of the extrudate and the measured cross-sectional dimension.
20. The extrusion control system according to claim 19 , wherein the extrudate is tubular, the measured cross-sectional dimension is outside diameter and the internal dimension is inside diameter.