Rotating nozzle structure and method

Patent metadata

Field	Value
Publication number	US-11911949-B2
Application number	US-202117386129-A
Country	US
Kind code	B2
Filing date	Jul 27, 2021
Priority date	Jul 27, 2021
Publication date	Feb 27, 2024
Grant date	Feb 27, 2024

Abstract

Aspects of the disclosure are directed to methods and apparatus involving the extrusion of polymers or other materials. As may be implemented in accordance with various embodiments, a polymer is delivered into an inlet of a nozzle structure having the inlet and an outlet. The polymer is viscously heated and melted by rotating the nozzle structure about an axis extending through the inlet and the outlet, therein facilitating extrusion of the melted polymer through the nozzle structure outlet. A polymer supply may deliver the polymer into the nozzle structure inlet, and a coupler may facilitation rotation of the nozzle structure. A driver may further operate to control rotation of the nozzle structure relative to the coupler, for instance by generating a rotational output that causes rotation of the nozzle structure.

First claim

What is claimed is:

1. An apparatus comprising:
a nozzle structure having an inlet and an outlet, the inlet being configured to receive a polymer into the nozzle structure;
a polymer supply configured to deliver the polymer in a solid state into the nozzle structure inlet;
a coupler to facilitate rotation of the nozzle structure about an axis extending through the outlet; and
a driver configured and arranged with the nozzle structure and the coupler to viscously heat and melt the polymer within the nozzle structure, from the solid state into a melted state, by rotating the nozzle structure about the axis, therein facilitating extrusion of the melted polymer through the outlet along the axis.

2. The apparatus of claim 1 , wherein
the nozzle structure includes a lead-in portion and an end portion including a graduated nozzle, the lead-in portion being configured to receive the polymer in a solid state and to viscously heat and melt the polymer while the lead-in portion is rotated with the graduated nozzle; and
the driver is configured and arranged with the nozzle structure and the coupler to viscously heat and melt the polymer, by rotating the nozzle structure about the axis to cause friction between an inner wall of the nozzle structure and a portion of the polymer in contact therewith.

3. The apparatus of claim 1 , wherein:
the coupler couples the nozzle structure to a frame and is configured to facilitate rotation of the nozzle structure relative to frame; and
the driver includes a motor coupled to the nozzle structure and configured to apply a rotational force to the nozzle structure that causes the nozzle structure to rotate about the axis.

4. The apparatus of claim 1 , wherein the nozzle structure is fixed to a frame and the coupler is configured to facilitate rotation of the nozzle structure by rotating the frame and nozzle structure together.

5. The apparatus of claim 4 , wherein the driver includes a motor coupled to the frame and configured to apply a rotational force to the frame that causes the frame and nozzle structure to rotate together about the axis.

6. The apparatus of claim 1 , further including a heater configured to heat the nozzle structure and therein facilitate melting of the polymer.

7. The apparatus of claim 1 , wherein the driver includes a motor having an output coupled to drive rotation of the nozzle structure via a rotational output force.

8. The apparatus of claim 1 , wherein the driver is configured and arranged with the nozzle structure to control heating of the polymer by controlling a speed at which the nozzle structure rotates, including increasing the speed to increase heating of the polymer, and including decreasing speed to decrease heating of the polymer.

9. The apparatus of claim 8 , further including a feedback circuit configured to sense temperature of the polymer being passed through the nozzle structure, and to generate a feedback output that variably controls the speed at which the nozzle structure rotates based on the sensed temperature.

10. The apparatus of claim 8 , further including a feedback circuit configured to sense backpressure upon the polymer being introduced into the nozzle structure inlet, the backpressure being indicative of characteristics of the melted polymer, and to generate a feedback output that variably controls the speed at which the nozzle structure rotates based on the sensed backpressure.

11. The apparatus of claim 1 , wherein the driver is configured and arranged with the nozzle structure and the coupler to viscously heat and melt the polymer by introducing shear stress in the polymer via the rotation of the nozzle structure and therein viscously heating the polymer as the polymer passes through the nozzle structure.

12. An apparatus comprising:
a nozzle structure having a cylindrical lead-in portion having an inlet, an end portion including a graduated nozzle and having an outlet, and an inner wall defining an opening extending to the inlet and outlet;
a coupler to facilitate rotation of the nozzle structure about an axis extending through the outlet and to melt polymer received in a solid state at the inlet and to present the melted polymer to the graduated nozzle, including rotating the cylindrical lead-in portion and the graduated nozzle together; and
a driver configured and arranged with the nozzle structure and the coupler to rotate the nozzle structure about the axis.

13. The apparatus of claim 12 , wherein the driver is configured and arranged with the nozzle structure and the coupler to introduce shear stress within a polymer being extruded through the nozzle structure by rotating the nozzle structure about the axis and therein viscously heating and melting the polymer as the polymer passes through the lead-in portion of the nozzle structure.

14. The apparatus of claim 12 , wherein the driver is configured and arranged to rotate the nozzle based on feedback indicative of characteristics related to the nozzle and including at least one of: temperature, pressure and a combination thereof.

15. A method comprising:
delivering a polymer in a solid state into an inlet of a cylindrical lead-in portion of a nozzle structure that also has a graduated nozzle having an outlet; and
viscously heating and melting the polymer in the cylindrical lead-in portion by rotating the nozzle structure about an axis extending through the inlet and the outlet, therein facilitating extrusion of the melted polymer through the outlet.

16. The method of claim 15 , wherein:
the nozzle structure is coupled to a coupler configured to facilitate rotation of the nozzle structure about an axis extending through the outlet; and
rotating the nozzle structure includes using a driver do drive rotation of the nozzle structure about the axis and relative to the coupler.

17. The method of claim 15 , wherein viscously heating and melting the polymer includes causing shear stress in the polymer via engagement of an inner wall of the nozzle structure with the polymer and corresponding rotation of the nozzle structure.

18. The method of claim 15 , wherein viscously heating and melting the polymer includes dynamically controlling a speed at which the nozzle structure rotates, including increasing the speed to increase heating of the polymer, and decreasing speed to decrease heating of the polymer.

19. The method of claim 15 , further including sensing temperature of the polymer being passed through the nozzle structure, and generating a feedback output that variably controls rotational speed at which the nozzle structure rotates based on the sensed temperature.

20. The method of claim 15 , further including sensing backpressure upon the polymer being introduced into the nozzle structure inlet, the backpressure being indicative of characteristics of the melted polymer, and generating a feedback output that variably controls rotational speed at which the nozzle structure rotates based on the sensed backpressure.

Assignees

• Wisconsin Alumni Res Found

Inventors

• Redmann Alec
• Osswald Tim
• Román Allen Jonathan

Classifications

• B29C48/33 Primary

  with parts rotatable relative to each other · CPC title

• B29C35/0255 Primary

  using friction · CPC title

• B29C35/0288

  Controlling heating or curing of polymers during moulding, e.g. by measuring temperatures or properties of the polymer and regulating the process (controlling or regulating chemical, physical or physico- chemical processes in general B01J19/0006) · CPC title

• B29C48/865

  Heating · CPC title

• B29C48/92

  Measuring, controlling or regulating · CPC title