Low nox, high efficiency, high temperature, staged recirculating burner and radiant tube combustion system
US-2022275932-A1 · Sep 1, 2022 · US
US10684010B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10684010-B2 |
| Application number | US-201314910051-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 6, 2013 |
| Priority date | Aug 6, 2013 |
| Publication date | Jun 16, 2020 |
| Grant date | Jun 16, 2020 |
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Burner assembly and method for combustion of gaseous of liquid fuel The invention relates to a burner assembly ( 1 ) and a method for combustion of gaseous or liquid fuel to heat an industrial furnace ( 9 ) having a combustion chamber ( 2 ), at least one main combustion air inlet ( 3 ) for the supply of preheat-ed combustion air ( 4 ) into the combustion chamber ( 2 ), a burner ( 5 ) with at least one fuel feed ( 7 ) and at least one air feed ( 8 ) for supply of fuel and primary air into a the combustion chamber ( 2 ), wherein the burner ( 5 ) is positioned adjacent to a combustion zone of the combustion chamber ( 2 ) such that the combustion air ( 4 ) flowing into the combustion chamber ( 2 ) through the main combustion air inlet ( 3 ) is passing the burner ( 5 ) in the combustion zone and is then deflected such that the flow of preheated combustion air and the smaller flows of fuel and primary air are flowing mainly in parallel from the burner ( 5 ) to the furnace ( 9 ), and a control unit for controlling the supply of fuel and maybe primary air into the combustion chamber ( 2 ). The control unit is adapted to supply the fuel and/or the primary air from the fuel and/or air feed ( 7, 8 ) into the combustion chamber ( 2 ) with an exit velocity higher than 150 m/s.
Opening claim text (preview).
The invention claimed is: 1. Method for combustion of gaseous or liquid fuel to heat an industrial furnace ( 9 ) having process air with an amount of oxygen of 16 to 18 Vol-% comprising: providing a burner assembly ( 1 ) having a combustion chamber ( 2 ), at least one main combustion air inlet ( 3 ) for supplying preheated combustion air ( 4 ) with an amount of oxygen of ambient air into the combustion chamber ( 2 ), a burner ( 5 ) with at least one fuel feed ( 7 ) and at least one air feed ( 8 ) for the supply of fuel and primary air into a the combustion chamber ( 2 ), positioning the burner ( 5 ) adjacent to a combustion zone of the combustion chamber ( 2 ) such that the combustion air ( 4 ) flowing into the combustion chamber ( 2 ) through the main combustion air inlet ( 3 ) is passing the burner ( 5 ) in the combustion zone and is then deflected such that the flow of preheated combustion air and the smaller flows of fuel and primary air are flowing mainly in parallel from the burner ( 5 ) to the furnace ( 9 ); and controlling the supply of fuel from the fuel feed ( 7 ) into the combustion chamber to produce an exit velocity that is higher than 150 m/s and less than the sound velocity; and controlling the supply of primary air from the air feed ( 8 ) into the combustion chamber ( 2 ) such that the excess air ratio of primary air to fuel during the supply of fuel and primary air into the combustion chamber ( 2 ) is between 0.1 and 0.6, wherein controlling the supply of primary air from the air feed ( 8 ) into the combustion chamber ( 2 ) includes controlling the primary air from the air feed ( 8 ) such that the velocity of the primary air is higher than the velocity of the fuel feed by a factor of about 2.0. 2. Method according to claim 1 , wherein positioning the burner ( 5 ) adjacent to a combustion zone includes feeding combustion air ( 4 ) into the combustion chamber ( 2 ) through the main combustion air inlet ( 3 ) with a temperature of more than 750° C. 3. Method according to claim 1 , wherein controlling the supply of primary air from the air feed ( 8 ) includes, after ignition of the burner, initially controlling the supply of the primary air to produce an exit velocity lower than 150 m/s through the fuel feed ( 8 ) into the combustion chamber ( 2 ) until the combustion air ( 4 ) in the main combustion air inlet ( 3 ) and/or in the combustion chamber ( 3 ) has a temperature higher than a predefined temperature value, and, upon exceeding the predefined temperature value, subsequently controlling the primary air through the air feed ( 8 ) into the combustion chamber ( 2 ) to produce an exit velocity higher than 150 m/s and less than the second velocity. 4. Method according to claim 1 , wherein controlling the supply of primary air from the air feed ( 8 ) includes controlling the primary air from the air feed ( 8 ) into the combustion chamber ( 2 ) via a compressor. 5. Method according to claim 1 , wherein controlling the supply of fuel from the fuel feed ( 7 ) includes pressurizing the fuel in the fuel feed such that the exit velocity is attained. 6. Method according to claim 1 , wherein controlling the supply of fuel from the fuel feed ( 7 ) includes controlling the supply of fuel from the fuel feed ( 7 ) such that excess air ratio of primary air to fuel during supply of fuel and primary air into the combustion chamber ( 2 ) is between 0.2 to 0.5. 7. Method according to claim 1 , wherein controlling the supply of fuel from the fuel feed ( 7 ) includes, after ignition of the burner, initially controlling the supply of the fuel to produce an exit velocity lower than 150 m/s through the fuel feed ( 7 ) into the combustion chamber ( 2 ) until the combustion air ( 4 ) in the main combustion air inlet ( 3 ) and/or in the combustion chamber ( 3 ) has a temperature higher than a predefined temperature value, and, upon exceeding the predefined temperature value, subsequentialy controlling the supply of the fuel through the fuel feed ( 7 ) into the combustion chamber ( 2 ) to produce an exit velocity higher than 150 m/s and less than the sound velocity.
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