Combustion system comprising an annular shroud burner
AssigneeJupiter Oxygen Corporation
InventorsBrydger Van Otten, Steven Harold Krimsky, Kevin Davis, Andrew Paul Chiodo
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AssigneeJupiter Oxygen Corporation
InventorsBrydger Van Otten, Steven Harold Krimsky, Kevin Davis, Andrew Paul Chiodo
Estimating the term…
The present disclosure is directed to systems and methods for high flame temperature oxy-combustion that enables the capture of CO2 cost effectively. One part of the presently disclosed subject matter comprises an annular shroud burner which utilizes a supply of undiluted oxygen and minimal flue gas recycle to generate a high flame temperature to maximize efficiency. The annular shroud burner may deliver oxygen into a combustion zone where mixing of the oxygen and a stream of fuel occurs. Flue gas recycled from the exit of the combustion system serves the dual purpose of conveying the coal into the reaction zone, as well as providing local cooling and protection from high incident heat fluxes through the novel shroud cooling design. The annular shroud burner may be configured to produce an axial jet flame that controls the rate of mixing of oxygen and fuel, thereby extending the heat release. Oxygen and coal may be mixed in a ratio such that peak flame temperatures exceed 4,500° F. (2,482° C.) while the flow of recycled flue gas is regulated to control flame temperature and protect burner components and near-burner surfaces.
An oxy-combustion system, comprising:
A method for generating a flue gas stream for CO2 processing using a system comprising a furnace, an oxy-combustion burner, a mill configured to receive a fuel and to provide the fuel to the oxy-combustion burner, an air heater configured to receive a first flue gas from the furnace and to exhaust the first flue gas as a second flue gas, a heat exchanger configured to receive a cold feed water, the heat exchanger further configured to heat the cold feed water via the second flue gas to produce a hot feed water and to exhaust the second flue gas as a third flue gas, an electrostatic precipitator configured to receive the third flue gas and to exhaust the third flue gas as a fourth flue gas, and a direct contact cooler polishing scrubber configured to receive the fourth flue gas and to exhaust the fourth flue gas as a cooled flue gas, the cooled flue gas providing a first cooled flue gas recycle supply stream configured to supply the cooled flue gas to the air heater, the method comprising:
Dependencies are inferred from the claim text.