Furnace

Patent metadata

Field	Value
Publication number	US-2017336070-A1
Application number	US-201515534556-A
Country	US
Kind code	A1
Filing date	Dec 17, 2015
Priority date	Dec 17, 2014
Publication date	Nov 23, 2017
Grant date	—

Abstract

A furnace, and a method of firing it, wherein part of the fuel supplied to the furnace is produced from waste plastics by a depolymerisation process, waste heat from the furnace being used to promote the depolymerisation process. The furnace is equipped with regenerators for waste heat recovery and is fired alternately in first and second opposed directions, with the direction of firing periodically reversing between the first direction and the second direction. The supply of fuel to the furnace is temporarily interrupted while the direction of firing is reversing, means being provided to accommodate the fuel produced during the temporary interruption. The furnace may be used for producing glass.

First claim

1 .- 15 . (canceled)

16 . A method of firing a furnace by burning fuel, comprising:
providing a supply of fuel to the furnace, wherein part of the fuel supplied to the furnace and burnt in the furnace is produced from waste plastics by a depolymerisation process, waste heat from the furnace being used to promote the depolymerisation process, wherein the furnace is equipped with regenerators for waste heat recovery, firing the furnace alternately in first and second opposed directions, with the direction of firing periodically reversing between the first direction and the second direction, temporarily interrupting the supply of fuel to the furnace while the direction of firing is reversing, means being provided to accommodate the fuel produced during the temporary interruption.

17 . The method as claimed in claim 16 , wherein substantially all the heat needed to promote the depolymerisation process is supplied from the furnace.

18 . The method as claimed in claim 16 , wherein the fuel produced from waste plastics contains at least 70% hydrocarbons.

19 . The method as claimed in claim 16 , wherein the fuel produced from waste plastics contains at least 80% hydrocarbons.

20 . The method as claimed in claim 16 , wherein the fuel produced from waste plastics contains at least 90% hydrocarbons.

21 . The method as claimed in claim 16 , wherein the fuel produced from waste plastics has a lower heating value (LHV) from 10 to 100 MJ/Nm3.

22 . The method as claimed in claim 16 , wherein the fuel produced from waste plastics has a lower heating value (LHV) from 20 to 80 MJ/Nm3.

23 . The method as claimed in claim 16 , wherein the fuel produced from waste plastics has a lower heating value (LHV) from 25 to 70 MJ/Nm3.

24 . The method as claimed in claim 16 , wherein the fuel produced from waste plastics has a lower heating value (LHV) from 30 to 50 MJ/Nm3.

25 . The method as claimed in claim 16 , wherein the fuel is produced from waste plastics by depolymerisation at 350° C. to 650° C.

26 . The method as claimed in claim 16 , wherein the fuel is produced from waste plastics by depolymerisation at 400° C. to 450° C.

27 . The method as claimed in claim 16 , wherein the fuel produced by the depolymerisation process is stored before being supplied to the furnace.

28 . The method as claimed in claim 16 , wherein the fuel produced by the depolymerisation process is supplied directly to the furnace, i.e. without storing the fuel.

29 . The method as claimed in claim 16 , wherein burning fuel in the furnace produces exhaust gases containing waste heat which is used to promote the depolymerisation process, and the depolymerisation process takes place in a reactor, which comprises means of exchanging waste heat between the exhaust gases of the furnace and the waste plastics.

30 . The method as claimed in claim 29 , wherein the exhaust gases are supplied directly to the reactor.

31 . The method as claimed in claim 29 , wherein waste heat is supplied to the reactor via a secondary circuit, the exhaust gases being supplied to a heat exchanger in the secondary circuit, the heat exchanger abstracting heat from the exhaust gases and supplying the heat to the reactor via the secondary circuit.

32 . The method as claimed in claim 16 , wherein the waste plastics are compressed prior to the depolymerisation process.

33 . The method as claimed in claim 16 , wherein the depolymerisation process is carried out under an inert atmosphere.

34 . A furnace which is fired by burning fuel and a plant for producing fuel from waste plastics by a depolymerisation process, wherein the plant supplies fuel to the furnace, and waste heat from the furnace is used to promote the depolymerisation process, the furnace being equipped with regenerators for waste heat recovery, wherein the furnace is fired alternately in first and second opposed directions, with the direction of firing periodically reversing between the first direction and the second directions, means being provided to accommodate the fuel produced during the reversing of the direction of firing.

35 . The furnace as claimed in claim 34 , comprising a cracking reactor and a means of supplying waste heat from the furnace to the cracking reactor.

36 . The furnace as claimed in claim 35 , comprising a means of supplying fuel produced in the cracking reactor from the cracking reactor to the furnace.

Assignees

• Pilkington Group Ltd

Inventors

• Inskip Julian

Classifications

• Y02P20/143

  the feedstock being recycled material, e.g. plastics · CPC title

• F27D7/02 Primary

  Supplying steam, vapour, gases or liquids · CPC title

• C03B5/235

  Heating the glass (C03B5/02, C03B5/18, C03B5/225 take precedence) · CPC title

• C03B5/237

  Regenerators or recuperators specially adapted for glass-melting furnaces · CPC title

• Y02P40/57

  Improving the yield, e-g- reduction of reject rates · CPC title