F23L7/005

Method and apparatus for the treatment of waste material
12434280 · 2025-10-07 · ·

A method and an apparatus for treating comminuted waste material the method comprising: a) providing a heating chamber (28) and one or more combustion heating means (40a-f) for heating the contents of the heating chamber (28), the heating chamber (28) having an inlet (21) and an outlet (22), b) feeding comminuted waste material through the inlet (21) and into the heating chamber (28); c) heating the comminuted waste material in the heating chamber (28), using the combustion heating means (40a-f), to generate a combustible gas; and d) supplying at least a portion of the generated combustible gas to the one or more combustion heating means (40a-f) for heating the heating chamber (28).

Injecting fuel-steam mixture into turbine engine combustor
12449126 · 2025-10-21 · ·

An assembly is provided for a turbine engine. This assembly includes a combustor, a fuel injector nozzle and a fuel system. The combustor includes a combustion chamber. The fuel injector nozzle is configured to inject a fuel-steam mixture into the combustion chamber for combustion. The fuel system includes a fuel source, a steam source and a manifold. The manifold is configured to mix fuel received from the fuel source with steam received from the steam source to provide the fuel-steam mixture. The fuel system is configured to deliver the fuel-steam mixture to the fuel injector nozzle.

Combustor having a main chamber and one or more trapped vortex cavities

A combustor having a main chamber and a trapped vortex cavity. The main chamber includes an outer liner and an inner liner. The trapped vortex cavity extends from at least one of the outer liner or the inner liner. A plurality of mixing assemblies operably injects a fuel-air mixture into the trapped vortex cavity to produce combustion gases. The trapped vortex cavity injects the combustion gases into the main chamber. A steam system is in fluid communication with the main chamber. The steam system operably injecting steam into the main chamber such that the steam flows downstream of the trapped vortex cavity.

Conduit preheating control

A conduit is preheated with steam having steam drain valve(s) therein open to allow draining and control valve(s) therein closed to prevent steam downstream flow. A gas may backfill the conduit from a downstream gas source to further preheat, and gas drain valve(s) may be provided to drain the gas. A predicted exit temperature of the steam or gas for a respective drain valve is calculated using a linear regression model based on initial temperature and pressure of the steam or gas and a Joule-Thompson cooling effect for the steam or gas at the respective drain valve. The preheating is stopped for the respective section of conduit when one or a combination of the predicted exit temperatures is greater than or equal to a respective required exit temperature of the steam or gas at a respective drain valve. The system sequentially ensures adequate preheating of sections of the conduit.

Vent gas recovery with flare control during a flare event

Flare control with vent gas recovery is disclosed. Vent gas is recovered for end use (e.g., process gas, fuel gas, etc.) while a flare is in a standby state. Upon detection of a flare event that causes vent gas to flow to the flare, the flare is changed from the standby state to an active state. The flare is controlled for efficient combustion of vent gas that flows to the flare during the flare event. Upon detection of a subsidence of the flare event, the flare is changed from the active state to the standby state. The flare can remain in standby until another flare event is detected. The flare event is detected when one or more of the disclosed flare activation conditions are detected, and subsidence of the flare event is detected when the flare deactivation conditions are detected.

Systems and methods for oxy-combustion

A method of oxy-combustion includes providing an electrolyzer feedstock to at least an electrolyzer cell; separating the electrolyzer feedstock into a hydrogen feedstock and an oxygen feedstock using the at least one electrolyzer cell; combusting a first feedstock derived from the hydrogen feedstock and a second feedstock derived from the oxygen feedstock in a furnace; controlling one or more of a second feedstock composition or a pressure in the furnace; and recycling an exhaust steam from the furnace, wherein at least one portion of exhaust steam from the furnace is recycled in at least one of a steam feedstock and the electrolyzer feedstock.

Combustion method for controlling and monitoring exhaust gas emissions in boilers

A combustion method for controlling and monitoring exhaust gas emissions in boilers is provided. The combustion method comprises the following steps: providing a liquid fuel in a boiler, burning the liquid fuel under atmospheric pressure; measuring a first combustion temperature in the boiler, and monitoring an initial concentration of a first exhaust gas in the boiler; adding a combustion improver to the boiler in batches and monitoring an emission concentration of the first exhaust gas in the boiler, wherein the emission concentration is less than the initial concentration; and repeating the above steps, and monitoring the boiler until a second combustion gas is generated, stop adding the combustion improver, and measuring the temperature in the boiler as a second combustion temperature, and reducing the amount of the combustion improver to avoid the generation of the second exhaust gas.

Fluidized bed reactor system and a method of operating a fluidized bed reactor system
12601475 · 2026-04-14 · ·

A reactor system and control method. The method includes feeding solid fuel and oxygen containing gas to a first fluidized bed reactor to form a fluidized bed of particles and combusting a first portion of the fuel in the bed with the oxygen containing gas to generate hot bed particles and a first stream of hot flue gas, conveying the first stream to the flue gas channel, transferring hot bed particles including a second portion of the solid fuel at a predetermined hot particles transfer rate from the first reactor to a second fluidized bed reactor, feeding fluidizing gas to the second reactor to form a second fluidized bed, and transferring bed particles from the second reactor to the first. The method includes first and second operation modes. In the first, the fluidizing gas is oxygen containing gas and, in the second, the gas includes steam, CO.sub.2, or inert gas.