IP Library Granted Patent US 9,039,948
Granted Patent B2
US 9,039,948 · App. 13/794,506 · Granted May 26, 2015

Method and device for producing and treating pellets

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Quick Facts
Patent No.
US 9,039,948
App. No.
13/794,506
Granted
May 26, 2015
Kind
B2
Abstract

The invention relates to a method and a device for producing and treating plastic pellets. According to said method, a melt of the plastic material is granulated to give pellets, the pellets are cooled in a cooling fluid, the pellets are separated from the cooling fluid and the pellets are crystallized. The device according to the invention is characterized by comprising a control unit which monitors the crystallization step and controls the method in such a manner that, in case of a disturbance of crystallization, the pellets are supplied to an intermediate storage alter separation of the pellets from the cooling fluid and, as soon as the disturbance is removed, the pellets temporarily stored in the intermediate storage are supplied to crystallization and are crystallized.

Claims (23)

1. A method for producing and treating pellets made of a plastic material, comprising:

granulating a melt of the plastic material to form pellets;

cooling the pellets in a cooling fluid;

separating the pellets from the cooling fluid; and

crystallizing the pellets in a crystallization device;

wherein a control unit monitors at least the crystallizing of the pellets and controls the method in such a manner that, in case of a disturbance in crystallization of the pellets, the pellets are supplied, via a diverting device situated between a separating device for separating the pellets from the cooling fluid and said crystallization device for crystallizing the pellets and connected with an intermediate storage, to said intermediate storage after separation of the pellets from the cooling fluid, and temporarily stored in the intermediate storage and, once the disturbance has been removed, the pellets temporarily stored in the intermediate storage are supplied to said crystallization device and are crystallized.

2. The method according to claim 1 , wherein the plastic material is a thermoplastic condensation polymer.

3. The method according to claim 1 , wherein the control unit decreases a temperature of the cooling fluid from a temperature T 1 to a temperature T 2 <T 1 in the case of a disturbance in crystallization of the pellets, the temperature T 1 being an original temperature of the cooling fluid in the case of no disturbance in crystallization of the pellets, wherein the temperature of the cooling fluid is decreased in such a manner that the pellets present in the cooling fluid are cooled such that the temperature of the pellets supplied to the intermediate storage following the separation step lies within a range in which the pellets do not stick together.

4. The method according to claim 1 , wherein the control unit decreases an average temperature of the pellets from a temperature T 3 to a temperature T 4 <T 3 in the case of a disturbance in crystallization of the pellets, the temperature T 3 corresponding to an average temperature of the pellets prior to crystallization in the case of no disturbance in crystallization of the pellets, and the temperature T 4 corresponding to an average temperature of the pellets prior to the intermediate storage, and T 4 lying within a range in which the pellets do no stick together in the intermediate storage.

5. The method according to claim 1 , wherein, if a disturbance in crystallization of the pellets occurs, the control unit decreases an average temperature of the pellets from a temperature T 3 to a temperature T 4 <T 3 after separation of the pellets from the cooling fluid, the temperature T 3 lying within a range in which the pellets stick together in the intermediate storage and the temperature T 4 lying within a range in which the pellets do not stick together in the intermediate storage.

6. The method according to claim 4 , wherein the temperature T 4 lies below a glass transition temperature of the plastic material.

7. The method according to claim 4 , wherein the temperature T 3 lies above the glass transition temperature of the plastic material.

8. The method according to claim 1 , wherein, if the disturbance in crystallization of the pellets is removed, the control unit increases an average temperature of the pellets from a temperature T 4 to a temperature T 5 >T 4 , the temperature T 5 corresponding to an average temperature of the pellets prior to crystallization in the case of no disturbance in crystallization of the pellets, essentially corresponding to the temperature T 3 .

9. The method according to claim 1 , wherein a pellet temperature is decreased and/or increased by increasing or decreasing a temperature of at least a portion of the cooling fluid.

10. The method according to claim 1 , wherein a pellet temperature is decreased and/or increased by increasing or decreasing a contact time with at least a portion of the cooling fluid.

11. The method according to claim 1 , wherein, once the disturbance has been removed, the pellets temporarily stored in the intermediate storage are supplied to crystallization in such a manner that the pellets temporarily stored are mixed with additional pellets and then supplied to the crystallization device according to a fault-free process, the additional pellets being in a quantity of up to 20% of a total mass flow of pellets supplied to the crystallization device.

12. The method according to claim 1 , wherein, once the disturbance has been removed, all pellets temporarily stored in the intermediate storage are first supplied to the crystallization device, and additional pellets are subsequently supplied to the crystallization device according to a fault-free process.

13. The method of claim 2 , wherein the plastic material comprises polyamide, polyester, polycarbonate, polyactide, polyhydroxyalkanoate, or copolymers or compounds thereof.

14. The method of claim 2 , wherein the plastic material comprises polyethylene terephthalate or copolymers thereof.

15. The method of claim 6 , wherein the temperature T 4 is below 80° C.

16. The method of claim 6 , wherein the temperature T 4 is below 60° C.

17. The method of claim 7 , wherein the temperature T 3 is above 80° C.

18. The method of claim 7 , wherein the temperature T 3 is above 100° C.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 6, 2016
From: RIETER AUTOMATIK GMBH
To: POLYMETRIX AG
Reel/Frame 040533/0951 →
CHANGE OF NAME Recorded May 11, 2016
From: BÜHLER THERMAL PROCESSES AG
To: POLYMETRIX AG
Reel/Frame 038824/0711 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 24, 2014
From: GLOCKNER, FRANK; EUSEBIO, FERNANDO; CULBERT, BRENT ALLEN; MORGANTI, FRANZISKA
To: RIETER AUTOMATIK GMBH; BUHLER AG
Reel/Frame 032509/0102 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 25, 2014
From: BUHLER AG
To: BUHLER THERMAL PROCESSES AG
Reel/Frame 032295/0579 →