GRADUAL OXIDATION WITH HEAT CONTROL
Described herein are embodiments of systems and methods for oxidizing gases. In some embodiments, a reaction chamber is configured to receive a fuel gas and maintain the gas at a temperature within the reaction chamber that is above an autoignition temperature of the gas. The reaction chamber may also be configured to maintain a reaction temperature within the reaction chamber below a flameout temperature. In some embodiments, heat and product gases from the oxidation process can be used, for example, to drive a turbine, reciprocating engine, and injected back into the reaction chamber.
1 . A method for oxidizing fuel, comprising:
determining, in a reaction chamber, with an inlet and an outlet, that is configured to maintain an oxidation process of an oxidizable fuel, at least one of (i) an actual reaction temperature of the fuel in the reaction chamber, and (ii) an inlet temperature of the reaction chamber;
determining, with a sensor, when at least one of (a) the actual reaction temperature approaches or exceeds a flameout temperature of the fuel, and (b) the inlet temperature approaches or drops below an autoignition threshold of the fuel; and
determining at least one of (i) a reduction of the actual reaction temperature within the reaction chamber to remain below the flameout temperature, and (ii) an increase in the inlet temperature to maintain the inlet temperature above the autoignition threshold.
2 . The method of claim 1 , wherein the reduction of the actual reaction temperature comprises removal of heat from the reaction chamber.
3 . The method of claim 2 , wherein removal of heat from the reaction chamber comprises introducing a fluid into the reaction chamber.
4 . The method of claim 3 , wherein removal of heat further comprises evacuating the fluid from the reaction chamber.
5 . The method of claim 4 , wherein the reaction chamber is configured to evacuate the fluid in the form of steam.
6 . The method of claim 1 , wherein the increase in the inlet temperature comprises directing the fuel through a heat exchanger.
7 . The method of claim 6 , wherein the heat exchanger is positioned within the reaction chamber.
8 . The method of claim 1 , wherein the flameout temperature is about 2300° F.
9 . The method of claim 1 , wherein the oxidizable fuel comprises at least one of hydrogen, methane, ethane, ethylene, natural gas, propane, propylene, propadiene, n-butane, iso-butane, butylene-1, butadiene, iso-pentane, n-pentane, acetylene, hexane, and carbon monoxide.
10 . A method for oxidizing fuel, comprising:
determining, in a reaction chamber, with an inlet and an outlet, that is configured to maintain an oxidation process of an oxidizable fuel, at least one of (i) an actual reaction temperature of the fuel in the reaction chamber, and (ii) an inlet temperature of the gas at the inlet;
determining when at least one of (a) the actual reaction temperature approaches or exceeds a flameout temperature of the fuel and (b) a reaction chamber inlet temperature approaches or drops below an autoignition threshold of the fuel; and
outputting instructions to at least one of (i) reduce the actual temperature or reduce increase of the actual temperature within the reaction chamber to be maintained below the flameout temperature, and (ii) increase the inlet temperature to be above the autoignition threshold of the fuel.
11 . The method of claim 10 , wherein the outputting comprises instructions to remove heat from the reaction chamber.
12 . The method of claim 11 , further comprising removing heat from the reaction chamber by introducing a fluid into the reaction chamber.
13 . The method of claim 12 , wherein removing heat further comprises evacuating the fluid from the reaction chamber.
14 . The method of claim 13 , wherein the fluid is evacuated from the reaction chamber in the form of steam.
15 . The method of claim 10 , wherein the outputting comprises increasing the inlet temperature by directing the fuel through a heat exchanger.
16 . The method of claim 15 , wherein the heat exchanger is positioned within the reaction chamber.
17 . The method of claim 10 , wherein the flameout temperature is about 2300° F.
18 . The method of claim 10 , wherein the oxidizable fuel comprises at least one of hydrogen, methane, ethane, ethylene, natural gas, propane, propylene, propadiene, n-butane, iso-butane, butylene-1, butadiene, iso-pentane, n-pentane, acetylene, hexane, and carbon monoxide.