The present invention relates to a burner to be used in general to produce combustion devices having one or more combustion stages. The burner according to the invention can also be used as total burner to generate heat or as partial burner, for example in reforming processes, for generating combustible gases or hydrogen rich gases, or to power fuel cells.
The present invention also relates to a multi-stage combustion device comprising a burner according to the invention.
As it is known, different types of burners exist and their structure is usually linked to the particular application for which they are destined. Burners can be used to produce complete combustion of a mixture formed by combustion air or fuel or, alternatively, they can be used as a combustion stage within multi-stage combustion devices. Normally, burners can be gaseous fuel (such as methane) or liquid fuel burners according to requirements.
A first type of burner, including for example those normally used in boilers for domestic or industrial use, has the primary objective of heating, through the combustion flame, the fumes that strike coils or heat exchangers inside which a carrier fluid to be heated circulates. More precisely, in these applications, the burners are positioned in combustion chambers inside which the heat exchangers containing the carrier fluid are also positioned. This fluid is therefore heated partly through radiation by the combustion flame and partly through convection by the fumes produced by combustion which lick the outer surface of the heat exchangers.
An example of burners of this type is described in the patent application EP1335163. More precisely, according to this solution, the burner comprises a device called LSV (large scale vortex) used as flame stabilizer. The burner has a structure formed of three concentric pipes. Combustion air is introduced into the innermost pipe and the outermost pipe, while the fuel is introduced into the central pipe in a ratio suitable to create a very lean mixture. The flame develops at the outlet of the central pipe at a widening of the section. The combustion products and excess air subsequently flow into a combustion chamber, on the wall of which there are disposed according to various geometries, and level with the outlet thereof, combustion nozzles for injection of further fuel, having orifices with a particular inclination.
Although being relatively efficient from a functional viewpoint, burners of this type have technical limits deriving above all from the significant dimensions that distinguish their structure. Consequently, they are somewhat unsuitable for those applications in which generation and transmission of high thermal power in small or limited spaces is required, as may be the case, for example, in methane reforming plants or the like.
In these operating conditions “radiant” burners have proved more efficient. More precisely, radiant burners are use in those circumstances where there must be no physical contact between combustion fumes and the material to be heated, thereby producing heat exchange entirely by radiation. From a constructional viewpoint, these burners usually comprise a linear or curved chamber, in which the fumes deriving from combustion circulate. More precisely, these burners are used in those circumstances where there must be no physical contact between combustion fumes and the material to be heated, thereby producing heat exchange entirely by radiation. The fumes deriving from combustion are evacuated directly from the burner and often their enthalpic content is exploited to pre-heat the air in order to increase the performance of the plant. In many solutions of this type the combustion reagents (this expression being intended as indicating the oxidizer and the fuel) are mixed before being introduced into the combustion chamber according to a swirling motion.
The burners of this second type are accompanied by some drawbacks, a first of which is identified in the difficulty in controlling the flow rates. In other words, the composition of the mixture that reaches the combustion area varies continuously. This translates into poor flame stability due to the variable conditions of the mixture. Added to this drawback is the possibility of flash backs, especially in those cases in which the burner does not work in optimal operating conditions. This aspect is particularly critical in terms of safety. Another limit of conventional radiant burners lies in the fact that the radiant walls of the burner are not licked continuously and efficiently by the flame due to its poor stability. This naturally limits the efficiency of the burner as the thermal energy that can be transmitted by the burner through radiation is limited.
On the basis of these considerations, the need emerges for new technical solutions that allow the drawbacks currently accompanying conventional radiant burners to be overcome. Therefore, the main aim of the present invention is to provide a burner that allows the aforesaid limits and drawbacks to be overcome.
Within this aim, a main object is to provide a burner that is functionally versatile, or that can be used for different applications. Another object is to provide a burner of radiant type that allows the transmission of high thermal power deriving from stable and constant combustion. A further object of the present invention is to provide a burner which is compact, reliable and easy to manufacture at competitive costs.
The present invention relates to a burner comprising a main body provided with a substantially cylindrically shaped cavity which extends along an axial direction and which is open at least on a first side. The burner also comprises first feed means to introduce a flow of a first reagent into the operating cavity in an intake position of the first reagent. These first feed means are configured so as to define a tangential intake of the first reagent into the operating cavity. The burner also comprises second feed means to introduce a flow of a second reagent into said operating cavity in an intake position of said second reagent. Said second feed means are configured so as to introduce the second reagent according to a direction parallel to the axial direction.
According to the invention, the operating cavity comprises a first portion between the intake position of the first reagent and the intake position of the second reagent. This first portion defines a stabilization chamber of the first reagent. The operating cavity also comprises a second portion that configures a combustion chamber downstream of the intake position of the second reagent or downstream of the stabilization chamber with respect to the direction in which the flow of second reagent extends. According to a preferred embodiment of the invention, the burner comprises combustion ignition means which are operatively positioned inside the operating cavity to ignite combustion between the two reagents.
For the purposes of the present invention, the expression reagents is intended as indicating the oxidizer and the fuel that generate combustion. Therefore, in a first possible application of the burner, the flow of first reagent can be a flow of oxidizer, while the flow of second reagent will be a flow of fuel. In a second application the nature of the reagents can be inverted with respect to the previous case and more precisely the first flow of reagent will correspond to a flow of fuel, while the second flow of reagent can be a flow of oxidizer.
It has been found that the presence of a stabilization chamber for flow of the first reagent allows flame conditions that are extremely stable and constant in time to be achieved. In fact, the distance between the intake positions for the two reagents allows precise adjustment of the flow rates, or a constant combustion stoichiometric ratio.
From an operational viewpoint, the reagent that acts as oxidizer for combustion can be air or alternatively a mixture of gases. Analogously, the reagent that acts as fuel can be formed by a flow of combustible gas or, alternatively can be a liquid fuel.
According to a further aspect of the present invention, the first portion of the operating cavity, which defines the stabilization chamber for the first reagent, has the same dimension of diameter as the second portion which defines the combustion chamber. It has been found that this solution allows optimization of the heating conditions of the walls delimiting the combustion chamber, or optimization of the radiation effect that can be obtained through these walls.
According to a further aspect of the present invention, the burner comprises a lance for introducing the flow of second reagent. This lance comprises a portion outside the main body of the burner and a portion inside this main body which extends parallel to the axial direction in which the operating cavity extends. The position of the lance in substance defines the length of the first portion of the operating cavity, or the extension of the stabilization chamber. This extension can be adjusted if necessary, through appropriate means for adjustment of the axial position, as a function of the type of reagents used and as a function of the mass flows thereof in order to optimize combustion.
According to another aspect of the present invention, the combustion ignition means are advantageously positioned inside the lance for intake of the second reagent. This solution is particularly advantageous as the ignition means in fact remain confined in an inert position from a fluid dynamic viewpoint, or in a position that does not obstruct on the one hand stabilization of the flow of the first reagent and on the other propagation of the flame.
The present invention also relates to a combustion device that is characterized in that it comprises a burner according to the present invention. According to a possible embodiment, the combustion device according to the invention comprises a first combustion stage defined by a burner according to the present invention and a second combustion stage defined by a further combustion chamber into which the combustion products produced by the burner flow. Preferably, the combustion device comprises further feed means to introduce a flow of oxidizer into said further combustion chamber.
Further features and advantages of the present invention shall be apparent from the description of particular embodiments of the present invention illustrated by way of non-limiting example in the accompanying drawings, wherein:
With reference to the aforesaid figures, the burner 1 according to the invention comprises a main body comprising a substantially cylindrically shaped operating cavity 11 which extends according to an axial direction X. The operating cavity 11 is open at least on a first side so as to be in communication with the environment outside the main body. More precisely, in the case illustrated the operating cavity 11 is delimited on a second side thereof, opposite the first, by a housing wall 12.
The burner 1 according to the invention comprises first combustion feed means to introduce a flow of a first reagent into the operating cavity 11 in an intake position of said first reagent (indicated with the reference P1 and hereafter also with the expression “first position P1”). More precisely, the first feed means are structured so as to configure a tangential intake of the flow of first reagent in the operating cavity 11. In other words, they configure a flow for the first reagent which enters the cavity 11 according to a direction tangent to the cross section of this cavity.
The burner 1 also comprises second feed means configured to introduce a flow of second reagent C into the operating cavity 11 in an intake position of said second reagent (indicated with the reference P2 and hereafter also with the expression “second position P2”). More precisely, these second feed means configure an axial flow of fuel inside the operating cavity 11.
According to the invention, the operating cavity 11 comprises a first portion 11A, between the intake position P1 of said first reagent AC and the intake position P2 of said second reagent. This first portion 11A forms a stabilization chamber of the first reagent introduced through the first feed means. The operating cavity 11 also comprises a second portion 11B, in communication with the first portion 11A, which defines a combustion chamber downstream of the intake position P2 of the second reagent with respect to the axial direction of flow of this second reagent. For the purposes of the description, the expression “stabilization chamber 11A” will be used to indicate the first portion 11A, and the expression “combustion chamber 11B” will be used to indicate the second portion 11B.
With reference, for example, to the sectional view of
Again with reference to
Again with reference to the sectional view of
The feed duct 20 is in communication on the opposite side with the operating cavity 11 through an opening 8 whose position in substance defines the intake position P1 of the flow of combustion air AC (first reagent) into the cavity or into the stabilization chamber 11 defined thereby. As illustrated, the position of the opening 8 is substantially adjacent to the housing wall 12 so as to oblige the entire flow of combustion air to move in the direction of the combustion chamber 11B. In the case illustrated in
With reference to
As clearly illustrated, the first portion 30A of the lance element 30 is substantially coaxial with the operating cavity 11 and terminates with an emission end 33 through which the fuel C exits. The axial extension of this first portion 30A in practice defines the axial extension of the stabilization chamber as it stabilizes the distance between the intake position P1 of the first reagent (combustion air in the case illustrated) and the intake position P2 of the second reagent (fuel in the case illustrated). It has been found that excellent results in terms of combustion stability are obtained, given the same reagents used, when the ratio between the distance LT of the intake positions (or the distance between the position P1 and the position P2) and the internal diameter D of the stabilization chamber 11A (or of the first portion 11A) is comprised within an interval of values between 1 and 10. It has also been found that optimal results in terms of combustion stability are achieved when the ratio between the length LT of the first portion 11A and the length L of the second portion 11B is comprised within an interval of values between 0.1 and 2. Moreover, it has been found that particularly favorable combustion conditions are achieved when the ratio between internal diameter D of the stabilization chamber and diameter D1 of the first portion 30A of the lance element 30 is contained within an interval of values between 2 and 10.
In the case illustrated in the figures, the combustion ignition means comprise a spark igniter 40 arranged inside the lance element 30. More precisely, the spark igniter 40 comprises a central body 40A, made of insulating material, arranged coaxially inside the lance element 30 and connected by a first part to an electrical source (not shown) through an electrical connection plug 39. The opposite part of the central body 40A comprises an ignition end 40B, also called tip, which emerges with respect to the fuel delivery end 33 of the lance element. This emerging position of the tip allows the spark to strike in a region in which flammable mixture is undoubtedly present.
As illustrated in
With reference to
With reference to
The first wall 51 of the housing liner 50 comprises a discharge opening 55 to discharge products deriving from the second combustion. In particular, in the solution illustrated the discharge opening 55 is coaxial with the housing liner 50 or with the tubular element 10 of the burner 1. The combustion device 5 can advantageously comprise a conveying element 58 to convey the products of the second combustion. In the case illustrated, the conveying element 58 comprises a discharge outlet 59 connectable, through a flange element 59B, to an evacuation duct, not shown in the figures. According to requirements, these products can be conveyed to a further combustion stage of the combustion device 5 or inside another device. Alternatively, the combustion products could be released directly into the atmosphere if their temperature is sufficiently low.
The technical solutions adopted for the burner allow the aims and objects set to be fully achieved. In particular, the burner according to the invention has high functional versatility, which makes it suitable for use in different applications. In particular, it can be used for partial or total combustion or, alternatively, as heating element of heat carrying fluids or solid masses. The structure of the burner according to the invention allows it to be used to produce particularly compact and efficient multistage combustion devices with extremely limited manufacturing costs.
The burner and the combustion device thus conceived are susceptible to numerous modifications and variants, all falling within the scope of the inventive concept; moreover all details can be replaced by other technically equivalent details.
In practice, the materials used and the contingent dimensions and forms can be any, according to requirements and to the state of the art.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IT09/00599 | 12/30/2009 | WO | 00 | 6/29/2012 |