Combustion method and installation with optimized energy recuperation

Patent metadata

Field	Value
Publication number	US-10208952-B2
Application number	US-201415107538-A
Country	US
Kind code	B2
Filing date	Dec 19, 2014
Priority date	Dec 23, 2013
Publication date	Feb 19, 2019
Grant date	Feb 19, 2019

Abstract

Combustion method and installation in which an oxygen-rich oxidant is preheated by exchange of heat with a heat-transfer fluid, upstream of the combustion chamber, in which method and installation an auxiliary gas is heated by heat exchange with a first proportion of the hot flue gases discharged from the chamber, and in which method and installation the heat-transfer fluid comprises a mixture of at least a proportion of the heated auxiliary gas with a proportion of hot flue gases.

First claim

The invention claimed is:

1. A process for the combustion, in a combustion chamber, of a fuel with a preheated oxygen-rich oxidant with generation of heat and hot flue gases inside said combustion chamber, wherein the process comprises the steps of:
discharging the hot flue gases from the combustion chamber, wherein the resulting discharged flue gases contain residual heat;
recovering residual heat by heating an auxiliary gas by heat exchange with at least a part of the discharged hot flue gases in an auxiliary heat exchanger, with a hot auxiliary gas and tempered flue gases being obtained,
introducing at least a first part of the hot auxiliary gas into a main exchanger in which oxygen-rich oxidant is preheated by heat exchange with a first heat-exchange gas comprising said at least a first part of the hot auxiliary gas, with a preheated oxidant and a tempered heat-exchange gas being obtained; and
supplying the preheated oxygen-rich oxidant to the combustion chamber for the combustion of the fuel,
wherein a portion of the discharged hot flue gases is not introduced into the auxiliary exchanger and is instead mixed with said at least a first part of the hot auxiliary gas before it is introduced into the main exchanger in order to increase the thermal energy content of the first heat-exchange gas.

2. The process as claimed in claim 1 , wherein the first heat-exchange gas consists of a mixture of hot auxiliary gas and the portion of the discharged hot flue gases.

3. The process as claimed in claim 1 , wherein the auxiliary gas is a predominantly inert gas, preferably chosen from steam, CO 2 and the mixtures of these two gases.

4. The process as claimed in claim 1 , wherein the auxiliary gas is chosen from air or a mixture of air with a predominantly inert gas.

5. The process as claimed in claim 1 , wherein the content of discharged hot flue gases of the first heat-exchange gas is less than or equal to 30 vol %.

6. The process as claimed in claim 1 , wherein the ratio by volume of, on the one hand, discharged hot flue gases to, on the other hand, the first hot auxiliary gas in the first heat-exchange gas is less than or equal to 45 vol %.

7. The process as claimed in claim 1 , wherein the combustion chamber is a melting chamber, a refining chamber, a melting/refining chamber or a combustion chamber of a boiler.

8. The process as claimed in claim 7 , wherein the combustion chamber is a glass melting chamber, a glass refining chamber or a glass melting/refining chamber.

9. A process for the combustion, in a combustion chamber, of a fuel with a preheated oxygen-rich oxidant with generation of heat and hot flue gases inside said combustion chamber, the process comprising the steps of:
discharging the hot flue gases from the combustion chamber, said discharged flue gases containing residual heat;
recovering residual heat by heating an auxiliary gas by heat exchange with at least a part of the discharged hot flue gases in an auxiliary heat exchanger, with a hot auxiliary gas and tempered flue gases being obtained;
introducing at least a first part of the hot auxiliary gas into a main exchanger in which oxygen-rich oxidant is preheated by heat exchange with a first heat-exchange gas comprising said at least a first part of the hot auxiliary gas, with a preheated oxidant and a tempered heat-exchange gas being obtained; and
supplying the preheated oxygen-rich oxidant to the combustion chamber for the combustion of the fuel, wherein the process further includes:
a first mode of operation in which the first heat-exchange gas does not comprise discharged hot flue gases, and
a second mode of operation in which a portion of the discharged hot flue gases is not introduced into the auxiliary exchanger and is instead mixed with said at least a first part of the hot auxiliary gas before it is introduced into the main exchanger in order to increase the thermal energy content of the first heat-exchange gas.

10. The process as claimed in claim 9 , wherein, in the first mode of operation, the heat-exchange gas consists of hot auxiliary gas.

11. An installation comprising a combustion chamber, a first heat exchanger, referred to as auxiliary exchanger, and a second heat exchanger, referred to as main exchanger,
the combustion chamber being provided with injectors for the injection of a fuel and for the injection of an oxidant into the combustion chamber and with an outlet for flue gases;
the auxiliary exchanger comprising, on the one hand, an inlet for hot flue gases and an outlet for tempered flue gases and, on the other hand, an inlet for auxiliary gas to be heated and an outlet for hot auxiliary gas, the outlet for hot flue gases of the combustion chamber being fluidly connected to the inlet for hot flue gases of the auxiliary exchanger; and
the main exchanger comprising, on the one hand, an inlet for hot heat-exchange gas and an outlet for tempered heat-exchange gas and, on the other hand, an inlet for oxidant to be preheated and an outlet for preheated oxidant, the outlet for hot auxiliary gas of the auxiliary exchanger being fluidly connected to the inlet for hot heat-exchange gas of the main exchanger, the outlet for preheated oxidant being fluidly connected to at least one of the injectors of the combustion chamber,
wherein the installation also comprises a pipeline configured to fluidly connect the outlet for hot flue gases to the inlet for the hot heat-exchange gas of the main exchanger in parallel with the auxiliary exchanger, so as to enable the flow of a controlled part of the hot flue gases resulting from the outlet for flue gases toward the inlet for the hot heat-exchange gas of the main exchanger.

12. The installation as claimed in claim 11 , wherein the injectors for the injection of fuel and oxidant are incorporated in burners and/or injection lances.

13. The installation as claimed in claim 11 , wherein the combustion chamber is a melting chamber, a refining chamber, a melting/refining chamber or the combustion chamber of a boiler, preferably a glass melting chamber, a glass refining chamber or a glass melting/refining chamber.

Assignees

• Air Liquide

Inventors

• Jarry Luc
• Joumani Youssef
• Leroux Bertrand
• Tsiava Remi

Classifications

• Y02P40/57

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

• Y02E20/322

  Cross-Sectional Technologies · mapped topic

• F23K2900/01041

  Heating by using exhaust gas heat · CPC title

• C03B5/237

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

• F23L7/007 Primary

  Supplying oxygen or oxygen-enriched air · CPC title