Rotary batch decoater

Patent metadata

Field	Value
Publication number	US-10788206-B2
Application number	US-201515758116-A
Country	US
Kind code	B2
Filing date	Sep 18, 2015
Priority date	Sep 18, 2015
Publication date	Sep 29, 2020
Grant date	Sep 29, 2020

Abstract

Systems and methods for efficiently performing rotary batch decoating can use time-offset batch reactors. A first batch reactor can operate out of phase with a second batch reactor, so that the burning of pyrolysis gases from the first reactor can be used to provide fuel to the incinerator used to heat the material in the second reactor. After the first reactor is dumped and filled with new material, the pyrolysis gases from the second reactor can be used to provide fuel to the incinerator, which heats the material in the first reactor.

First claim

What is claimed is:

1. A system, comprising:
an incinerator for generating heated gas;
a first decoating reactor having a first supply port and a first exhaust port, wherein the first supply port is coupled to the incinerator for receiving heated gas from the incinerator and the first exhaust port is coupled to the incinerator for providing first pyrolysis gas to the incinerator;
a second decoating reactor having a second supply port and a second exhaust port, wherein the second supply port is coupled to the incinerator for receiving heated gas from the incinerator and the second exhaust port is coupled to the incinerator for providing second pyrolysis gas to the incinerator;
a first sensor positioned to sense the presence of the first pyrolysis gas;
a second sensor positioned to sense the presence of the second pyrolysis gas; and
a controller configured to receive input from the first sensor and the second sensor and to control one or more flow control devices for:
directing the heated gas from the incinerator to the first decoating reactor in response to sensing by the second sensor; and
directing the heated gas from the incinerator to the second decoating reactor in response to sensing by the first sensor.

2. The system of claim 1 , wherein the incinerator is arranged to receive the first pyrolysis gas from the first exhaust port and receive second pyrolysis gas from the second exhaust port for combusting the first pyrolysis gas and second pyrolysis gas, respectively.

3. The system of claim 1 , wherein the first exhaust port, the incinerator, and the second supply port form a first pathway configured to provide the heated gas to the second decoating reactor when the first pyrolysis gas generated in the first decoating reactor is provided to the incinerator.

4. The system of claim 3 , wherein the second exhaust port, the incinerator, and the first supply port form a second pathway configured to provide the heated gas to the first decoating reactor when the second pyrolysis gas generated in the second decoating reactor is provided to the incinerator.

5. The system of claim 1 , further comprising one or more flow control devices coupled between the incinerator and at least one of the first supply port and the second supply port for directing the heated gas to one or both of the first decoating reactor and the second decoating reactor.

6. The system of claim 5 , further comprising a controller configured to control the one or more flow control devices for time-offsetting a first decoating process in the first decoating reactor from a second decoating process in the second decoating reactor.

7. The system of claim 1 , further comprising:
a source of purchased fuel coupled to the incinerator through a flow control device to provide the purchased fuel to the incinerator, wherein the flow control device is actuatable to cease providing purchased fuel to the incinerator when first pyrolysis gas or second pyrolysis gas is provided to the incinerator.

8. The system of claim 1 , further comprising an additional flow control device coupling a fuel source to the incinerator, wherein the controller is further coupled to the additional flow control device to close the additional flow control device in response to sensing the presence of the first pyrolysis gas.

9. A method using the system of claim 1 , comprising:
loading first material into the first decoating reactor;
loading second material into the second decoating reactor;
heating the first material in the first decoating reactor until first pyrolysis gases are released;
circulating the first pyrolysis gases into the incinerator;
combusting the first pyrolysis gases to generate heated gas; and
heating the second material in the second decoating reactor using the heated gas until second pyrolysis gases are released.

10. The method of claim 9 , wherein heating the first material in the first decoating reactor includes:
providing purchased fuel to the incinerator; and
combusting the purchased fuel in the incinerator.

11. The method of claim 10 , further comprising:
sensing the first pyrolysis gases; and
ceasing to provide the purchased fuel to the incinerator in response to sensing the first pyrolysis gases.

12. The method of claim 10 , wherein heating the second material is performed without combusting the purchased fuel.

13. The method of claim 9 , further comprising:
dumping the first material from the first decoating reactor;
loading third material into the first decoating reactor;
circulating the second pyrolysis gases into the incinerator;
combusting the second pyrolysis gases to generate additional heated gas; and
heating the third material in the first decoating reactor using the additional heated gas, wherein heating the third material in the first decoating reactor includes heating the third material until third pyrolysis gases are released.

14. A method using the system of claim 1 , comprising:
providing the first decoating reactor and the second decoating reactor coupled to the incinerator; and
performing decoating iterations using the first decoating reactor and the second decoating reactor, wherein the decoating iterations performed using the first decoating reactor are performed out of phase with respect to the decoating iterations performed using the second decoating reactor, and wherein performing each of the decoating iterations includes:
generating pyrolysis gases; and
providing the pyrolysis gases to the incinerator.

15. The method of claim 14 , wherein performing at least one of the decoating iterations further includes heating a material by combusting the pyrolysis gases in the incinerator.

16. The method of claim 14 , wherein performing a first one of the decoating iterations further includes:
providing purchased fuel to the incinerator; and
heating a material by combusting the purchased fuel in the incinerator.

17. The method of claim 16 , wherein performing a first one of the decoating iterations further includes:
sensing the pyrolysis gases; and
ceasing to provide the purchased fuel to the incinerator in response to sensing the pyrolysis gases.

18. The method of claim 16 , further comprising combusting the pyrolysis gases in the incinerator to generate heated gas during the first one of the decoating iterations, and wherein performing a second one of the decoating iterations includes heating additional material using the heated gas.

Assignees

• Novelis Inc

Inventors

• Rauch Edwin L

Classifications

• C22B1/005 Primary

  Preliminary treatment of scrap (C22B1/02 - C22B1/26 take precedence) · CPC title

• F23G7/065

  using gaseous or liquid fuel · CPC title

• C22B21/0007

  Preliminary treatment of ores or scrap or any other metal source (Bayer processes C01F) · CPC title

• F23G5/0273

  using indirect heating · CPC title

• C22B7/001

  Dry processes · CPC title