Distributing Fuel Flow in a Reaction Chamber
A substantially homogeneous air/fuel mixture is distributed into an oxidation reaction chamber at a plurality of discrete locations about an interior of the oxidation reaction chamber. The oxidation reaction chamber has an internal temperature sufficient to oxidize the fuel in the air/fuel mixture. The air/fuel mixture are retained in the oxidation reaction chamber as the fuel of the air/fuel mixture oxidizes. The heat released by the oxidation maintains a temperature substantially throughout the reaction chamber at a temperature sufficient to oxidize the fuel in the air/fuel mixture.
1 . A system for oxidizing fuel, the system comprising:
an oxidation reaction chamber;
an inlet to the oxidation reaction chamber arranged to receive a substantially homogeneous air/fuel mixture; and
a gas distributor system in the oxidation reaction chamber and coupled to the inlet, the gas distributor system adapted to distribute the air/fuel mixture at a plurality of discrete locations throughout the interior of the oxidation reaction chamber such that when the fuel of the distributed air/fuel mixture is oxidized in the reaction chamber, heat released by the oxidation maintains a temperature substantially throughout the reaction chamber sufficient to oxidize the fuel in the air/fuel mixture.
2 . The system of claim 1 , wherein the gas distributor system is adapted to distribute the air/fuel mixture at a plurality of discrete locations about the interior of the oxidation reaction chamber such that when the fuel of the distributed air/fuel mixture is oxidized in the reaction chamber, heat released by the oxidation maintains a temperature substantially throughout the reaction chamber sufficient to oxidize the fuel in the air/fuel mixture and below a temperature that causes formation of nitrogen oxides.
3 . The system of claim 1 , wherein the heat released by the oxidation maintains a temperature throughout at least 90% of the internal volume of the reaction chamber at a temperature sufficient to oxidize the fuel in the air/fuel mixture.
4 . The system of claim 1 , further comprising:
a second inlet to the oxidation reaction chamber arranged to receive the substantially homogeneous air/fuel mixture; and
the gas distributor system comprises:
a first gas distributor in the oxidization reaction chamber and coupled to the first mentioned inlet, the first gas distributor dispersing the air/fuel mixture at a first plurality of discrete locations about the interior of the oxidation reaction chamber; and
a second gas distributor in the oxidation reaction chamber and coupled to the second inlet for dispersing the air/fuel mixture at a second, different plurality of discrete locations about the interior of the oxidation reaction chamber.
5 . The system of claim 1 , wherein the air/fuel mixture cannot sustain a flame.
6 . The system of claim 5 , further comprising a supplemental gas distributor in the oxidation reaction chamber and arranged to receive a supplemental fuel at a higher concentration or energy per unit mass than the fuel of the air/fuel mixture.
7 . The system of claim 1 , wherein the gas distributor system further comprises a plurality of ports adapted to output the air/fuel mixture into the interior of the oxidization reaction chamber, the ports arranged substantially throughout the oxidation reaction chamber.
8 . The system of claim 1 , wherein the oxidation reaction chamber defines a primary direction of air/fuel mixture flow from the gas distributor system to an outlet of the oxidation reaction chamber; and
wherein the gas distributor system further comprises a plurality of ports residing at discrete, spaced-apart locations substantially along the primary direction of air/fuel mixture flow, the ports adapted to output the air/fuel mixture into the interior of the oxidation reaction chamber.
9 . The system of claim 1 , further comprising a heater in the oxidation reaction chamber adapted to produce heat in addition to the heat released by oxidation of the air/fuel mixture.
10 . The system of claim 1 , further comprising a fill material in the oxidation reaction chamber that absorbs heat from oxidation of the air/fuel mixture and imparts heat to the unoxidized air/fuel mixture.
11 . The system of claim 1 , further comprising a supplemental gas inlet into the reaction chamber arranged to receive a supply of supplemental cooling gas.
12 . The system of claim 1 wherein, in addition to air and fuel, the substantially homogeneous air/fuel mixture comprises other gases.
13 . The system of claim 1 wherein the air/fuel mixture comprises fuel from multiple fuel sources.
14 . A method of oxidizing fuel, the method comprising:
distributing a substantially homogeneous air/fuel mixture into an oxidation reaction chamber at a plurality of discrete locations about an interior of the oxidation reaction chamber, the oxidation reaction chamber having an internal temperature sufficient to oxidize the fuel in the air/fuel mixture; and
retaining the air/fuel mixture in the oxidation reaction chamber as the fuel of the air/fuel mixture oxidizes and the heat released by the oxidation maintains a temperature substantially throughout the reaction chamber at a temperature sufficient to oxidize the fuel in the air/fuel mixture.
15 . The method of claim 14 , wherein the heat released by the oxidation maintains a temperature substantially throughout the reaction chamber at a temperature sufficient to oxidize the fuel in the air/fuel mixture and below a temperature that causes formation of nitrogen oxides.
16 . The method of claim 14 , wherein retaining the air/fuel mixture in the oxidation reaction chamber as the fuel of the air/fuel mixture oxidizes comprises retaining the air/fuel mixture at a pressure above atmospheric.
17 . The method of claim 14 , controlling the temperature substantially throughout the reaction chamber by at least one of changing a rate of flow of the air/fuel mixture distributed into the oxidation reaction chamber, changing a ratio of the fuel and air in the air/fuel mixture, operating a heater in the oxidation reaction chamber, or providing supplemental gases into the oxidation reaction chamber.
18 . The method of claim 14 , wherein the heat released by the oxidation maintains a temperature throughout 90% of the interior volume of the reaction chamber at a temperature sufficient to oxidize the fuel in the air/fuel mixture.
19 . The method of claim 14 , wherein the air/fuel mixture cannot sustain a flame.
20 . The method of claim 19 , further comprising supplying a supplemental fuel at a higher concentration or energy per unit mass than the fuel of the air/fuel mixture.
21 . The method of claim 14 , wherein the oxidation reaction chamber defines a primary direction of air/fuel mixture flow from a gas distributor system to an outlet of the oxidation reaction chamber; and
wherein distributing a substantially homogeneous air/fuel mixture into an oxidation reaction chamber at a plurality of discrete locations about the interior of the oxidation reaction chamber comprises distributing the substantially homogeneous air/fuel mixture into the oxidization chamber at a plurality of discrete locations substantially along the primary direction of air/fuel mixture flow.
22 . The method of claim 14 , further comprising cooling the oxidized fuel prior to providing it to a turbine.
23 . The method of claim 14 , further comprising oxidizing any volatile organic compounds and carbon monoxide in the air/fuel mixture while the air/fuel mixture in the oxidation reaction chamber oxidizes.
24 . A gas turbine system, comprising:
an oxidation reaction chamber;
a gas distributor system in the oxidation reaction chamber arranged to receive a substantially homogeneous air/fuel mixture and having a plurality of ports adapted to output the air/fuel mixture into an interior of the oxidization reaction chamber, the ports arranged substantially throughout the oxidation reaction chamber;
a turbine generator comprising a turbine inlet in communication with an outlet of the oxidation reaction chamber, the turbine generator adapted to convert energy from the oxidized fuel into electricity.
25 . The gas turbine system of claim 24 , further comprising a compressor arranged to receive an air/fuel mixture and output a compressed air/fuel mixture to the oxidation reaction chamber.
26 . The gas turbine system of claim 24 , further comprising a port between the oxidization reaction chamber and the turbine generator for supplying a cooling fluid.
27 . The gas turbine system of claim 24 , wherein the oxidation reaction chamber defines a primary direction of air/fuel mixture flow from the gas distributor system to an outlet of the oxidation reaction chamber; and
wherein the plurality of ports reside at discrete locations substantially along the primary direction of air/fuel mixture flow.