Method for combusting a fuel, and combustion device

Patent metadata

Field	Value
Publication number	US-10539322-B2
Application number	US-201715481743-A
Country	US
Kind code	B2
Filing date	Apr 7, 2017
Priority date	Apr 8, 2016
Publication date	Jan 21, 2020
Grant date	Jan 21, 2020

Abstract

A method for determining fatigue lifetime consumption of an engine component, by defining a reference thermal load cycle, the reference thermal load cycle being characterized by a reference load cycle amplitude and a reference load cycle time, and determining a reference load cycle lifetime consumption. The method includes measuring a temperature of the engine component, determining a thermal load cycle based upon the temperature measurement, determining a load cycle amplitude, determining a load cycle time, relating the load cycle time to the reference load cycle time, thereby determining a load cycle time factor, relating the load cycle amplitude to the reference load cycle amplitude, thereby determining a load cycle amplitude factor, combining the load cycle time factor and the load cycle amplitude factor into a combined load cycle factor for determining a load cycle lifetime consumption.

First claim

The invention claimed is:

1. A method for combusting a fuel, the method comprising:
providing a first oxidizer mass flow;
providing a second oxidizer mass flow;
discharging a fuel mass flow into the first oxidizer mass flow thereby providing a fuel/oxidizer mass flow;
apportioning the fuel mass flow such as to achieve an overstoichiometric ratio of the fuel mass flow related to the first oxidizer mass flow;
initiating a combustion of the fuel mass flow with the first oxidizer mass flow, thereby generating a flow of combustion products, wherein the flow of combustion products includes residual combustible components;
providing the flow of combustion products to at least one first duct of a heat exchange appliance;
providing the second oxidizer mass flow to at least one second duct of the heat exchange appliance, whereby the flow of combustion products is provided in a heat exchange relationship with the second oxidizer mass flow through the heat exchange appliance
exchanging heat between the flow of combustion products and the second oxidizer mass flow, thereby heating the second oxidizer mass flow and cooling the flow of combustion products;
discharging the flow of combustion products from the at least one first duct of the heat exchange appliance at a downstream end of the heat exchange appliance;
discharging the second oxidizer mass flow from the second duct of the heat exchange appliance at a downstream end of the heat exchange appliance;
combusting the residual combustible components provided in the flow of combustion products in a presence of the second oxidizer mass flow;
discharging the flow of combustion products and the second oxidizer mass flow such as to avoid intermixing of the flow of combustion products and the second oxidizer mass flow, thus providing an interface between the second oxidizer mass flow and the flow of combustion products downstream of the heat exchange appliance; and
combusting the residual combustible components provided in the flow of combustion products at the interface between the second oxidizer mass flow and the flow of combustion products.

2. The method according to claim 1 , comprising:
apportioning the fuel mass flow and the first and second oxidizer mass flows such that an overstoichiometric fuel/air ratio is achieved when relating the fuel mass flow to the first oxidizer mass flow, and an understoichiometric fuel/air ratio is achieved when relating the fuel mass flow to the combined first and second oxidizer mass flows.

3. A method for combusting a fuel, the method comprising:
providing a first oxidizer mass flow;
providing a second oxidizer mass flow;
discharging a fuel mass flow into the first oxidizer mass flow thereby providing a fuel/oxidizer mass flow;
apportioning the fuel mass flow such as to achieve an overstoichiometric ratio of the fuel mass flow related to the first oxidizer mass flow;
initiating a combustion of the fuel mass flow with the first oxidizer mass flow, thereby generating a flow of combustion products, wherein the flow of combustion products includes residual combustible components;
providing the flow of combustion products to at least one first duct of a heat exchange appliance;
providing the second oxidizer mass flow to at least one second duct of the heat exchange appliance, whereby the flow of combustion products is provided in a heat exchange relationship with the second oxidizer mass flow through the heat exchange appliance;
exchanging heat between the flow of combustion products and the second oxidizer mass flow, thereby heating the second oxidizer mass flow and cooling the flow of combustion products;
discharging the flow of combustion products from the at least one first duct of the heat exchange appliance at a downstream end of the heat exchange appliance;
discharging the second oxidizer mass flow from the second duct of the heat exchange appliance at a downstream end of the heat exchange appliance;
combusting the residual combustible components provided in the flow of combustion products in a presence of the second oxidizer mass flow; and
wherein the second oxidizer mass flow exceeds the first oxidizer mass flow.

4. The method according to claim 3 , comprising:
controlling the first oxidizer mass flow in order to control a ratio of the fuel mass flow to the first oxidizer mass flow.

5. The method according to claim 3 , comprising:
adding a second fuel mass flow to the second oxidizer mass flow, thereby providing a second fuel/oxidizer flow, wherein the second fuel mass flow is added upstream a downstream end of the heat exchange appliance or upstream the heat exchange appliance.

6. The method according to claim 5 , comprising:
apportioning the second fuel mass flow such as to achieve an understoichiometric fuel/oxidizer ratio for both the fuel/oxidizer ratio of the second fuel/oxidizer flow as well as for a combined fuel/oxidizer mass flow ratio of a combined fuel mass flow which includes the fuel mass flow added to the first oxidizer mass flow and the second fuel mass flow, related to a combined oxidizer mass flow including the first oxidizer mass flow and the second oxidizer mass flow.

7. The method according to claim 5 , comprising:
performing an addition of the second fuel mass flow such as to provide a lean premixed second fuel/oxidizer flow at the downstream end of the heat exchange appliance.

8. The method of claim 3 , wherein the second oxidizer mass flow is 4 to 20 times the first oxidizer mass flow.

9. The method of claim 3 , wherein the second oxidizer mass flow is at least 10 times the first oxidizer mass flow.

10. The method of claim 3 , wherein an equivalence ratio of the fuel mass flow to the first oxidizer mass flow is between 1.5 and 3.

11. The method of claim 3 , comprising:
discharging the flow of combustion products and the second oxidizer mass flow such as to avoid intermixing of the flow of combustion products and the second oxidizer mass flow, thus providing an interface between the second oxidizer mass flow and the flow of combustion products downstream the heat exchange appliance; and
combusting the residual combustible components provided in the flow of combustion products at the interface between the second oxidizer mass flow and the flow of combustion products.

12. The method of claim 3 , comprising:
apportioning the fuel mass flow and the first and second oxidizer mass flows such that an overstoichiometric fuel/air ratio is achieved when relating the fuel mass flow to the first oxidizer mass flow, and an understoichiometric fuel/air ratio is achieved when relating the fuel mass flow to the combined first and second oxidizer mass flows.

13. A combustion device for combusting a fuel, the combustion device comprising:
means for providing a first fluid flow;
fuel discharge means for discharging a fuel flow into the first fluid flow;
a first combustion zone adapted and configured to stabilize a flame and being disposed downstream the fuel discharge means and being in fluid communication with the means for providing the first fluid flow at an upstream end of the first combustion zone;
a heat exchange appliance, said heat exchange compliance having at least one first duct and at least one second duct and the heat exchange appliance being configured to enable an exchange of heat between a fluid provided in the at least one first duct that comprises combustion products having residual combustible components and a fluid provided in the at least one second duct, the at least one first duct of the heat exchange appliance, at an upstream end thereof being in fluid communication with the first combustion zone at a down

Assignees

• Ansaldo Energia Switzerland AG

Inventors

• Bolaños-Chaverri Felipe
• Wind Torsten
• Biagioli Fernando
• Syed Khawar

Classifications

• F23D14/02 Primary

  Premix gas burners, i.e. in which gaseous fuel is mixed with combustion air upstream of the combustion zone · CPC title

• F23D14/46

  Details · CPC title

• F23R3/18

  Flame stabilising means, e.g. flame holders for after-burners of jet-propulsion plants · CPC title

• F23C7/00 Primary

  Combustion apparatus characterised by arrangements for air supply (inlets for fluidisation air F23C10/20; baffles or shields with air supply passages F23M9/04) · CPC title

• F23R2900/03341

  Sequential combustion chambers or burners · CPC title