Boiler producing steam from flue gases under optimized conditions
This invention relates to a boiler ( 1 ) drying, igniting and combusting refuse and producing steam ( 2, 2 a ) by heat exchange with flue gases ( 3 ), said boiler defining a main flow direction ( 5 ) of gases, said boiler ( 1 ) comprising a separator element ( 4 ) and an end superheater ( 8 ), the separator element ( 4 ) being adapted for separating said flue gases ( 3 ) into streams of a less-corrosive gas flow ( 6 ) and a corrosive gas flow ( 7 ), said separator element ( 4 ) being located substantially in and along said main flow direction ( 5 ), said end superheater ( 8 ) being located in proximity to said separator element ( 4 ) and in the flow ( 6 ) of said less-corrosive gas. Said separator element ( 4 ) comprises a plate ( 4 a ) or a wall ( 4 b ), which in a number of said separator elements ( 4 ) forms a channel as another separator element. This provides for an increased lifetime of said superheater and makes the boiler provide a high and efficient electrical power output.
1. A boiler for drying, igniting and combusting refuse and producing steam by heat exchange with flue gases, the flue gases being the results of incineration of the refuse and the flue gases including both a less-corrosive gas flow and a corrosive gas flow, the boiler defining a main flow direction of the flue gases, the boiler comprising a separator element and an end superheater, the separator element being positioned in the path of both the less-corrosive gas flow and the corrosive gas flow to separate the flue gases into streams of less-corrosive gas flow and corrosive gas flow, the separator element extending in a direction substantially along the main flow direction of the flue gases, the separator element comprising a pipe having one or more nozzles adapted to blow cool recirculated cleaned flue gases following the main flow direction in between the less-corrosive gas flow and the corrosive gas flow, wherein these gas flows continue in two separate streams in the main flow direction, and wherein the end superheater is located in proximity to the separator element and in the path of the less-corrosive gas flow.
2. The boiler according to claim 1 , wherein a plurality of the separator elements forms a channel.
3. The boiler according to claim 1 , wherein the pipe is located substantially perpendicular to the main flow direction.
4. The boiler according to claim 1 , wherein the separator element is adapted to be movable in a direction substantially perpendicular to the main flow direction.
5. The boiler according to claim 1 , wherein the separator element is adapted to be suspendable on or from the walls of the boiler.
6. The boiler according to claim 1 , wherein the less-corrosive gas and corrosive gas are cooled by means of an evaporation wall in the radiation zone and one or more superheaters, which produce steam at between 300 and 450 degrees Celsius.
7. The boiler according to claim 6 , wherein the steam is heated in the end superheater.
8. The boiler according to claim 6 , wherein the end superheater heats the steam to become steam of an increased temperature, resulting in a temperature increase of between 25 and 200 degrees Celsius as compared to the temperature of the steam.
9. The boiler according to claim 1 , wherein the less-corrosive gas is essentially free from Cl, K, Na, Zn and Pb.
10. The boiler according to claim 1 , wherein the corrosive gas comprises one or more of Cl, K, Na, Zn and Pb.
11. The boiler according to claim 1 further comprising a blow unit adapted to, by blowing secondary air, effectively mix the less-corrosive gas with the corrosive gas, whereby the mix can be effectively burnt out before it reaches the top zone of the boiler.
12. The boiler according to claim 1 , wherein steam leaving the end superheater at around 450 degrees Celsius is utilized to produce electricity, when the steam is fed into a steam turbine driving a generator.
13. A boiler for drying, igniting and combusting refuse and producing steam by heat exchange with flue gases, the flue gases being the results of incineration of the refuse and the flue gases including both a less-corrosive gas flow and a corrosive gas flow, the boiler defining a main flow direction of the flue gases, the boiler comprising a separator element and an end superheater, the separator element being positioned in the path of both the less-corrosive gas flow and the corrosive gas flow to separate the flue gases into streams of less-corrosive gas flow and corrosive gas flow, the separator element extending in a direction substantially along the main flow direction of the flue gases, the end superheater is located in proximity to the separator element and in the path of the less-corrosive gas flow, and comprising a blow unit adapted to, by blowing secondary air, effectively mix the less-corrosive gas with the corrosive gas, whereby the mix can be effectively burnt out before it reaches the top zone of the boiler.