Method for homogenizing the heat distribution as well as decreasing the amount of NO
View Patent ↗Method for homogenizing the heat distribution as well as decreasing the amount of NO x in combustion products when operating an industrial furnace with at least one conventional burner using air as an oxidant. An additional oxidant including at least 50% oxygen gas is caused to stream into the furnace through a lance. The total amount of oxygen supplied is balanced against the amount of fuel being supplied through the air burner. Firstly, the combination of at least 40% of the supplied oxygen is supplied through the additional oxidant, the lance is arranged at a distance from the air burner of at least 0.3 meters, and the additional oxidant streams into the furnace through the lance with at least sonic velocity, and secondly the additional oxidant is supplied only when the air burner is operated at a certain lowest power or at a higher power.
1. Method for homogenizing the heat distribution as well as decreasing the amount of NO x in the combustion products when operating an industrial furnace ( 1 ) with at least one conventional burner ( 2 a , 2 b , 2 c , 2 d ) using air as oxidant, where a lance ( 3 a , 3 b , 3 c , 3 d ) is introduced into the furnace ( 1 ), the method comprising streaming an additional oxidant comprising at least 50% oxygen gas into the furnace ( 1 ) through the lance ( 3 a , 3 b , 3 c , 3 d ), and the total amount of oxygen supplied, partly through the air, partly through the additional oxidant, is supplied in a predetermined ratio in relation to the amount of fuel being supplied through the air burner ( 2 a , 2 b , 2 c , 2 d ), wherein
at least 40% of the supplied oxygen is supplied through the additional oxidant,
the lance ( 3 a , 3 b , 3 c , 3 d ) is caused to be arranged at a distance from the air burner ( 2 a , 2 b , 2 c , 2 d ) of at least 0.3 meters,
the additional oxidant is caused to stream into the furnace ( 1 ) through the lance ( 3 a , 3 b , 3 c , 3 d ) with at least sonic velocity, and
the additional oxidant is supplied only when the air burner ( 2 a , 2 b , 2 c , 2 d ) is operated at or above a certain lowest power.
2. Method according to claim 1 , wherein the predetermined ratio between the total supplied oxidant and supplied fuel is caused to be such that a stoichiometric surplus of oxidant is present during the combustion, and the surplus of oxidant in relation to fuel is controlled so that Lambda is lower when the proportion of additionally supplied oxidant is higher.
3. Method according to claim 2 , the distance ( 4 ) between the burner ( 2 a , 2 b , 2 c , 2 d ) and the lance ( 3 a , 3 b , 3 c , 3 d ) is caused to be between 1.5 and 4 times the diameter of a circle that encloses all supply openings for air and at least 0.3 meters.
4. Method according to claim 1 , wherein only one lance ( 3 a , 3 b , 3 c , 3 d ) is used for each burner ( 2 a , 2 b , 2 c , 2 d ) in the industrial furnace ( 1 ).
5. Method according to claim 4 , wherein the distance ( 4 ) between the burner ( 2 a , 2 b , 2 c , 2 d ) and the lance ( 3 a , 3 b , 3 c , 3 d ) is caused to be between 1.5 and 4 times the diameter of a circle that encloses all supply openings for air and at least 0.3 meters.
6. Method according to claim 1 , wherein the distance ( 4 ) between the burner ( 2 a , 2 b , 2 c , 2 d ) and the lance ( 3 a , 3 b , 3 c , 3 d ) is caused to be between 0.5 meters and 1.2 meters.
7. Method according to claim 6 , wherein the distance ( 4 ) between the burner ( 2 a , 2 b , 2 c , 2 d ) and the lance ( 3 a , 3 b , 3 c , 3 d ) is caused to be between 0.7 and 0.9 meters.
8. Method according to claim 1 , wherein the distance ( 4 ) between the burner ( 2 a , 2 b , 2 c , 2 d ) and the lance ( 3 a , 3 b , 3 c , 3 d ) is caused to be between 1.5 and 4 times the diameter of a circle that encloses all supply openings for air and at least 0.3 meters.
9. Method according to claim 8 , wherein the distance ( 4 ) between the burner ( 2 a , 2 b , 2 c , 2 d ) and the lance ( 3 a , 3 b , 3 c , 3 d ) is caused to be between 2.5 and 4 times the diameter of the circle.
10. Method according to claim 8 , wherein several burners ( 2 a , 2 b , 2 c , 2 d ) are arranged with one respective lance ( 3 a , 3 b , 3 c , 3 d ) each, and the center-to-center distance ( 5 ) between two adjacent burners in a plane which is parallel to the furnace wall is caused to be at least about 2 times the diameter of the circle.
11. Method according to claim 1 , wherein the lance ( 3 a , 3 b , 3 c , 3 d ) is arranged in such a direction so that the stream of additional oxidant does not cross the flame of the burner ( 2 a , 2 b , 2 c , 2 d ).
12. Method according to claim 1 , wherein at least 50% of the supplied oxygen is supplied through the additional oxidant.
13. Method according to claim 12 , wherein between 50% and 80% of the supplied oxygen is supplied through the additional oxidant.
14. Method according to claim 1 , wherein the additional oxidant being supplied through the lance is an oxidant having at least 85 percent by weight of oxygen.
15. Method according to claim 1 , wherein the additional oxidant is supplied through a de laval nozzle in the lance ( 3 a , 3 b , 3 c , 3 d ).
16. Method according to claim 1 , wherein the additional oxidant is supplied at a velocity of at least 1.5 times the sonic velocity.
17. Method according to claim 16 , wherein the additional oxidant is supplied at a velocity of between 1.5 times the sonic velocity and 1.8 times the sonic velocity.
18. Method according to claim 1 , wherein several burners ( 2 a , 2 b , 2 c , 2 d ) are arranged with one respective lance ( 3 a , 3 b , 3 c , 3 d ) each, and the center-to-center distance ( 5 ) between two adjacent burners in a plane which is parallel to the furnace wall is caused to be at least about 2 meters.
19. Method according to claim 1 , wherein the certain lowest power is 20% or higher of full power.