CN219933972U - Gas distribution component for a burner - Google Patents

Abstract

A gas distribution member for a burner includes an oxidant inlet for introducing an oxidant stream into the burner; an oxidant inlet channel in fluid connection with the oxidant inlet; and a diffusion buffer chamber for providing a space for buffering and diffusing the oxidant after flowing out of the oxidant inlet channel and communicating the oxidant inlet channel with each oxidant delivery component, wherein a plurality of through holes are arranged on the wall of the oxidant inlet channel adjacent to the diffusion buffer chamber and the wall of the oxidant inlet channel adjacent to the diffusion buffer chamber. The gas distribution part is easy to process, does not need to be provided with a complex valve structure, and greatly reduces the manufacturing cost; meanwhile, the effects of convenience in use and maintenance, reduction in the requirement on the pressure value of an upstream air source, reduction in the influence of air source fluctuation on the combustion effect and the like are achieved.

Description

Gas distribution component for a burner

Technical Field

The present utility model relates to a gas distribution member for a burner. In particular, the present utility model relates to a gas distribution member for distributing a reactant fluid to a burner.

Background

In metallurgical or glass industry furnaces, oxy-fuel combustion has lower investment costs, higher combustion efficiency, lower NOx emissions and higher product quality than conventional air combustion.

In the prior art, common staged oxy-fuel burners have at least one fuel channel and at least one oxidant channel. By means of the oxygen classification, a part of the oxygen can be split and thus combustion can be retarded. The nozzle end of the burner produces a substantially flat fuel-rich flame and the staged nozzle introduces a portion of the oxidant from above or below the fuel-rich flame, thus producing a fuel-lean flame.

Chinese patent publication No. CN114667412a discloses a synchronous oxyfuel combustion-supporting system for a regenerative glass furnace, the first bipolar fuel burner of which has a main oxygen valve for distributing an oxygen flow between main oxygen and staged oxygen, and a staged mode valve for distributing a staged oxygen flow between an upper staged port and a lower staged port. The staged oxygen may be directionally controlled and proportioned via a staged mode valve through one or both upper or lower staged ports near the main prechamber. While such a staged mode valve may provide several benefits, there are problems with significant manufacturing difficulties and high manufacturing costs in practical applications. In particular, for some conditions where frequent adjustment of the staged flow is not required, such a complex adjustment valve need not be provided.

Based on the above discussion, there is a market need for a gas distribution member that is easier to process and more stable to overcome the above-described deficiencies.

Disclosure of Invention

The present utility model is intended to solve the above-mentioned technical problems of the prior art and to provide a gas distribution member which is easy to process, low in manufacturing cost and easy to adjust, and is mainly used for introducing an oxidizing agent into a multistage burner.

In order to achieve the above object, in a first aspect of the present utility model, there is provided a gas distribution member for a burner, the gas distribution member comprising:

an oxidant inlet for introducing an oxidant stream into the burner;

an oxidant inlet channel in fluid connection with the oxidant inlet;

and a diffusion buffer chamber providing a space for diffusion of the oxidant after flowing out of the oxidant inlet channel and communicating with each oxidant delivery member, wherein a plurality of through holes are arranged on the wall of the oxidant inlet channel adjacent to the diffusion buffer chamber.

Further, the ratio between the total area of the practically usable oxidant flow of the diffusion buffer chamber and the total volume of the diffusion buffer chamber is set to a buffer ratio coefficient ranging from 5 to 50% m ² /m ³ Preferably between 10% and 40% m ² /m ³ More preferably between 15% and 35% m ² /m ³ More preferably between 20% and 30% m ² /m ³ . Wherein the total area of the actual available oxidant flow refers to the effective oxidant flow passage area of the diffusion buffer chamber to each oxidant delivery means. The purpose of this factor is to control the flow rate of the oxidant, to achieve a buffering effect, to accommodate low intake pressure conditions.

Further, a baffle may be disposed between the junction of the diffusion buffer chamber and each oxidant delivery member, the baffle partially shielding the inlet of the oxidant delivery member. The baffles may define the flow of the oxidant to each oxidant delivery member, thereby adjusting the distribution ratio of the oxidant.

Further, the pore size distribution of the plurality of through holes is not uniform.

Further, the smaller the aperture of the plurality of through holes is configured as the central through hole, the larger the aperture of the peripheral through hole. Wherein the middle through hole refers to a through hole having a shorter distance from the oxidant inlet.

Further, the burner is provided with a fuel inlet, the oxidant inlet being non-communicating with the fuel inlet. That is, there is no structure in which fuel and oxidant are mixed.

Further, the oxidant delivery means comprises a primary oxidant fuel delivery means, a secondary oxidant delivery means and a tertiary oxidant delivery means;

the secondary oxidant delivery member and the tertiary oxidant delivery member are disposed on the same side of the primary oxidant fuel delivery member, and the secondary oxidant delivery member is located between the tertiary oxidant delivery member and the primary oxidant fuel delivery member.

Further, the primary oxidizer fuel delivery component comprises:

at least one fuel supply passage through which fuel flows, one end of the at least one fuel supply passage being provided with a fuel nozzle; and

at least one primary oxidant supply passage through which a primary oxidant flows, the primary oxidant supply passage being configured to surround an outer wall of the fuel supply passage, and one end of the primary oxidant supply passage being provided with an annular nozzle surrounding the fuel nozzle;

the secondary oxidant delivery member includes at least one secondary oxidant supply channel through which a secondary oxidant flows, one end of the at least one secondary oxidant supply channel being provided with a secondary oxidant nozzle;

the tertiary oxidant delivery member includes at least one tertiary oxidant supply channel through which a tertiary oxidant flows, one end of the at least one tertiary oxidant supply channel being provided with a tertiary oxidant nozzle.

The gas distribution component provided by the utility model has the following advantages:

1. the gas distribution component is easy to process, does not need to be provided with a complex valve structure, and greatly reduces the processing and manufacturing cost.

2. The arrangement of the oxidant inlet channel and the diffusion buffer cavity enhances the sufficient diffusion of the oxidant before flowing into each oxidant delivery component, effectively reduces the flow rate of the oxidant, and obviously reduces the pressure loss of the oxidant in the link. The pressure loss of the oxidant in the process of the existing pure oxygen burner which is common at present is about 5KPa to 20KPa, and the pressure loss in the process of the utility model is lower than 1KPa. Thus, the pressure requirement on the upstream oxygen source can be greatly reduced, for example, for on-site oxygen production VSA equipment, the load of the booster pump can be reduced, or the booster pump is not required to be arranged.

3. The pore diameters of the plurality of through holes are unevenly distributed, and the flow rate is faster at the through holes (namely, at the middle through holes) with shorter distance from the oxidant inlet, so that the flow rates of the oxidants at different positions on the plane can be better equipped, and the stable oxidant flow rate is beneficial to the subsequent flame stabilization.

4. The gas distribution member has a large adjustment range of the distribution of the oxidizing agent, and the distribution of the oxidizing agent can be adjusted between the oxidizing agent supply passages of each stage to a large extent (for example, the adjustment range of the secondary oxidizing agent distribution ratio can be 1% to 80% of the total oxidizing agent, for example). The performance can be adapted to the change of different types of fuels (such as switching from natural gas to hydrogen, biomass gas, or mixed fuel of natural gas and hydrogen, etc.), and to the change of oxidant performance or variety (such as the change of oxygen temperature from normal temperature to preheating to about 500 ℃ or the change of oxygen purity of oxygen). When the above large condition change occurs, the desired combustion effect can still be obtained.

Drawings

The advantages and spirit of the present utility model will be further understood from the following detailed description of the utility model and the accompanying drawings.

Fig. 1 shows a schematic perspective view of a gas distribution member for a burner.

FIG. 2 shows a schematic view of an oxidant inlet and an oxidant inlet channel;

FIG. 3 shows a schematic view of the gas distribution member with inlets of the respective oxidant delivery members;

FIG. 4 shows a schematic of a diffusion buffer chamber;

fig. 5a and 5b show schematic views of baffles between the diffusion buffer chamber and the junction of each oxidant delivery member, wherein fig. 5b is a cross-sectional view of fig. 5a along the direction C-C.

Reference numerals illustrate: oxidant inlet channel 101, oxidant inlet 102, diffusion buffer chamber outer side wall 103, fuel inlet channel 104, fuel inlet 105, oxidant supply conduit 106, baffle 201, bolts 301, primary oxidant fuel delivery member 302, secondary oxidant delivery member 303, tertiary oxidant delivery member 304, diffusion buffer chamber 401, baffle 501.

Detailed Description

The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings. It will be apparent that the described embodiments are some, but not all, embodiments of the utility model. All other embodiments, which can be made by those skilled in the art based on the embodiments of the present utility model without making any inventive effort, shall fall within the scope of the present utility model.

In the description of the present utility model, it must be interpreted that the orientation and positional relationship indicated by terms such as "upper", "lower", "left", "right", "vertical", "horizontal", "inner" and "outer" are based on the orientation or positional relationship shown in the drawings, and are merely intended to facilitate the simplified description of the present utility model, without indicating or implying that the apparatus or elements being referred to must have a specific orientation or be constructed and operated in a specific orientation, and thus should not be construed as limiting the present utility model. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.

In the description of the present utility model, it must be interpreted that the terms "mounted," "connected together," and "connected" are to be construed broadly, e.g., may mean connected in a fixed manner, but may also mean removably connected or integrally connected, unless explicitly stated and defined otherwise; may represent a mechanical connection; may refer to being directly connected together, but may also refer to being indirectly connected together via an intervening medium; and may represent internal communication between two elements. The specific meaning of the above terms in the present utility model can be understood by those skilled in the art according to specific circumstances.

Each aspect or embodiment defined herein may be combined with any other aspect or embodiment unless clearly indicated otherwise. In particular, any preferred or advantageous feature indicated may be combined with any other preferred or advantageous feature indicated.

As used herein, the expression "surrounding" or "encircling" substantially means forming a ring shape, generally meaning that the inner ring is enclosed within the outer ring such that there is a gap between the inner and outer layers. This gap may be an annular gap or a non-annular gap. As used herein, this may mean that the primary oxidant supply channel surrounds a portion (e.g., more than half) of the circumference of the fuel supply channel, or that the primary oxidant supply channel surrounds the entire circumference of the fuel supply channel. The latter case may be interpreted to mean that the primary oxidant supply channels are arranged so as to completely encircle the circumference of the fuel supply channels in the circumferential direction. The design of the fuel nozzle and the annular nozzle may be understood in a similar manner.

As used herein, the expression "staged" means that the fuel and oxidant are mixed at different times and locations such that low nitrogen oxide emissions and control of the gas atmosphere near the surface of the molten material can be achieved. By staged it is meant that the oxidant can be supplied at different rates or flow rates via another nozzle spaced from the fuel nozzle. For example, when the classification of the secondary oxidant and the tertiary oxidant is 95%, this means that the remaining 5% of the oxidant is supplied to the primary oxidant fuel delivery means together with the fuel.

As used herein, the expression "fuel" means a gaseous, liquid or solid fuel that can be used interchangeably or in combination. The gaseous fuel may be natural gas (mainly methane), propane, hydrogen or any other hydrocarbon compound and/or sulfur-containing compound. The solid or liquid fuel may be predominantly any compound in the form of carbon and/or hydrocarbon and/or sulfur. The solid fuel may be selected from petroleum coke, coal fines, biomass particles, or other fossil fuels, which typically require a carrier gas (e.g., air or carbon dioxide) to form the transport wind transport. The liquid fuel may be selected from liquid hydrocarbons or coal tar. The manner of introduction of the gaseous, liquid or solid fuel can be determined by one skilled in the art as desired. The present utility model is not intended to impose any limitations in this respect. Some of the data presented herein uses natural gas as a fuel, but the results are considered applicable to other fuels, such as hydrogen and other gaseous fuels.

As used herein, the expression "oxidizing agent" may be constituted by an oxidizing agent such as air or oxygen-enriched air. The oxidizing agent is preferably composed of an oxidizing agent having a molar oxygen concentration of at least 50%, preferably at least 80%, more preferably at least 90%, and most preferably at least 95%. These oxidants include oxygen enriched air comprising at least 50% oxygen by volume, such as 99.5% pure oxygen produced by cryogenic air separation plants, or non-pure oxygen produced by vacuum pressure swing adsorption processes (88% by volume or greater), or oxygen produced by any other source.

Here, the use of oxy-fuel may purge nitrogen from the melting operation and reduce NOx and particulate emissions to below standard. The use of oxy-fuel burners may achieve different flame momentums, melt coverage and flame radiation characteristics. In the furnace, the main sources of nitrogen are air leakage, low purity oxygen supplied from a vacuum pressure swing adsorption apparatus or pressure swing adsorption apparatus, nitrogen in fuel (e.g., natural gas), or nitrogen contained in molten raw materials charged in a heating furnace.

As used herein, the fuel supply channel, the primary oxidant supply channel, the secondary oxidant supply channel, and the tertiary oxidant supply channel may be generally annular channels, and may have regions of inlet and outlet. Each of the generally annular channels is preferably annular when viewed in cross-section from a plane perpendicular to the axial flow direction, but this shape may also be non-annular.

The chinese patent application of utility model CN202080084376.9 discloses a burner for burning fuel and its burning method, the disclosure of which and its whole content are incorporated into the present utility model.

Fig. 1 shows a schematic perspective view of a gas distribution member for a burner. Oxidant enters the oxidant inlet channel 101 via the oxidant inlet 102. As shown in fig. 1 and 4, through holes 305 are provided in the wall of the oxidant inlet channel 101 adjacent to the diffusion buffer chamber, and the oxidant is dispersed to the diffusion buffer chamber 401 through these through holes 305. The outer side wall 103 of the diffusion buffer chamber 401 is removably connected to the diffusion buffer chamber. For example, the connection may be made by bolts 301. The detachable connection enables operators to quickly clean parts of the burner, so that the problem that the blockage such as accumulated ash and the like can be cleaned only by disassembling the whole burner part in the prior art is solved.

The oxidizer flowing out of the diffusion buffer chamber is directed to each oxidizer delivery component. In some exemplary descriptions, the through holes may be uniformly distributed. In some exemplary descriptions, these through holes may exhibit a distribution of small pore sizes for the intermediate through holes and large pore sizes for the peripheral through holes. The distribution can enable the effective area through which the oxidant flows to be larger, so that the oxidant flowing out of the diffusion buffer cavity flows uniformly on the unit area of the whole oxidant flow section, the distribution of the oxidant on each oxidant delivery component is ensured to be uniform, and the flame is ensured to be stable.

Although a separate buffer tank is also established in the burner of the prior art, the buffer tank is often far away from the burner positioned downstream of the buffer tank, and the buffer smoothing effect of the buffer tank is weakened. And because a plurality of combustors need to be connected behind the buffer tank, the buffer effect of each buffer tank is different under the influence of the positions of the combustors and the pipeline layout. The diffusion buffer chamber can ensure the buffer effect on the oxidant flow.

Illustratively, as shown in FIG. 2, a plurality of baffle plates 201 are disposed within the oxidant inlet passage 101. The baffle 201 is oriented in a direction substantially parallel to the central axis of the oxidant inlet. These baffles may serve to direct and guide the oxidant within the oxidant inlet channels.

As shown in fig. 3, the oxidant delivery means includes a primary oxidant fuel delivery means 302, a secondary oxidant delivery means 303, and a tertiary oxidant delivery means 304. The secondary oxidant delivery member and the tertiary oxidant delivery member are disposed on the same side of the primary oxidant fuel delivery member, and the secondary oxidant delivery member is located between the tertiary oxidant delivery member and the primary oxidant fuel delivery member. Accordingly, the oxidant inlet corresponds to a total inlet, delivering the oxidant to the primary oxidant fuel delivery member 302, the secondary oxidant delivery member 303, and the tertiary oxidant delivery member 304, respectively.

Fuel is delivered to the fuel inlet passage 104 via the fuel inlet 105, which in turn delivers a flow of fuel to the fuel supply passage. The primary oxidant supply channel for the primary oxidant stream may surround the outer wall of the fuel supply channel and be coaxial with the fuel supply channel.

The fuel supply passage may be a fuel conduit formed of a suitable material (e.g., refractory metal or ceramic). The beginning of the fuel conduit is removably connected to the entire gas distribution member, but may also be integrally formed therewith. The outlet end of the fuel conduit is connected to the fuel nozzle. The oxidant supply channels may be oxidant supply conduits formed of a particular material (e.g., refractory metal or ceramic), but may also be shaped conforming cavities or channels formed in the burner block. Illustratively, the secondary oxidant delivery member 303 includes 3 oxidant supply conduits 106.

The total oxidant can be separated into three streams: a primary oxidant stream, a secondary oxidant stream, and a tertiary oxidant stream. The primary oxidant stream surrounds the fuel nozzle and has a volumetric flow rate that is only a small percentage of the total oxidant, preferably less than 20% or less than 10% or less than 5% or about 2% -5%. The remaining oxidant is used as the secondary oxidant stream and the tertiary oxidant stream. This will correspond to a preferred fractionation ratio of at least 10% or at least 20% or at least 40% or at least 50% or at least 60% or even at least 70%, respectively. This means that a sufficient amount of oxidant flows through the secondary oxidant supply channel or the tertiary oxidant supply channel, or is distributed between the two supply channels, for classification. This not only reduces NOx production but also significantly improves the ability to control the atmosphere of the gas adjacent the molten surface of the heated material. In order to be able to control the atmosphere close to the molten surface so as to selectively perform oxidation or reduction according to the treatment conditions, it is desirable that the operation of the burner can be switched conveniently. To this end, the oxidant flow in the primary oxidant supply channel, the secondary oxidant supply channel and the tertiary oxidant supply channel may be independently controlled by means of an oxidant staging control mechanism.

It should be noted that it is not ideal that the primary oxidant stream is zero; this will create a void or vacuum in the primary oxidant supply channel, thus drawing in hot corrosive furnace gases, which will destroy the burner very quickly and cause flame instability. Furthermore, if the primary oxidant stream is too small, flame stability will also decrease; moreover, the mixed state of the gaseous fuel and the oxidizer will be deteriorated, making it difficult to obtain a practical flame. In some cases, the secondary oxidant stream or the tertiary oxidant stream may be near zero; in this case, the burner is substantially close to or equivalent to a dual stage burner, and the corresponding combustion effects and characteristics can be predicted and adjusted according to the knowledge of those skilled in the art.

Although the technical proposal of the utility model omits complex designs such as valves for easy manufacture and operation, a simple adjusting mechanism is arranged for adjusting the flow rate flowing into each oxidant delivery component. As shown in fig. 5a and 5b, a cross-sectional view along the C-C direction shows that a baffle 501 may be provided between the junction of the diffusion buffer chamber and each oxidant delivery member. These baffles may block the inlet of the oxidant delivery members as needed, thereby defining the oxidant flow rate delivered to each oxidant delivery member.

Although there are a number of more accurate methods in the prior art for adjusting the staged proportion of the oxidant stream, such as the provision of oxygen staging valves and the like. However, the valve is more expensive to manufacture and occupies a larger space for the oxidant inlet passage, and is not suitable for use in a scenario where a faster and more convenient hierarchical control is required.

While the present utility model has been presented in detail by the foregoing preferred embodiments, it should be understood that the foregoing description should not be deemed to limit the utility model. Various modifications and alterations to this utility model will become apparent to those skilled in the art upon reading the foregoing. Accordingly, the scope of the utility model should be limited only by the attached claims.

Claims (10)

1. A gas distribution member for a burner, the gas distribution member comprising:

an oxidant inlet for introducing an oxidant stream into the burner;

an oxidant inlet channel in fluid connection with the oxidant inlet;

and a diffusion buffer chamber providing a space for diffusion of the oxidant after flowing out of the oxidant inlet channel and communicating with each oxidant delivery member, wherein a plurality of through holes are arranged on the wall of the oxidant inlet channel adjacent to the diffusion buffer chamber.

2. The gas distribution member according to claim 1, wherein a ratio between a total area of the diffusion buffer chamber for the actual available oxidant flow and a total volume of the diffusion buffer chamber is set to a buffer ratio coefficient in a range of 10 to 40% m ² /m ³ 。

3. The gas distribution member according to claim 2, wherein the buffer ratio coefficient is in the range of 15% to 35% m ² /m ³ 。

4. The gas distribution member according to claim 2, wherein the buffer ratio coefficient ranges from 20% to 30% m ² /m ³ 。

5. The gas distribution member of claim 1, wherein a baffle is disposed between the diffusion buffer chamber and the junction of each oxidant delivery member, the baffle partially shielding the inlet of the oxidant delivery member.

6. The gas distribution member according to claim 1, wherein the plurality of through holes have a non-uniform pore size distribution.

7. The gas distribution member of claim 1, wherein the plurality of through holes are configured such that the smaller the aperture of the central through hole, the larger the aperture of the peripheral through hole.

8. The gas distribution member according to claim 1, wherein the burner is provided with a fuel inlet, the oxidant inlet being non-communicating with the fuel inlet.

9. The gas distribution member of claim 1, wherein the oxidant delivery member comprises a primary oxidant fuel delivery member, a secondary oxidant delivery member, and a tertiary oxidant delivery member;

the secondary oxidant delivery member and the tertiary oxidant delivery member are disposed on the same side of the primary oxidant fuel delivery member, and the secondary oxidant delivery member is located between the tertiary oxidant delivery member and the primary oxidant fuel delivery member.

10. The gas distribution member of claim 9, wherein the primary oxidant fuel delivery member comprises:

at least one fuel supply passage through which fuel flows, one end of the at least one fuel supply passage being provided with a fuel nozzle; and

at least one primary oxidant supply passage through which a primary oxidant flows, the primary oxidant supply passage being configured to surround an outer wall of the fuel supply passage, and one end of the primary oxidant supply passage being provided with an annular nozzle surrounding the fuel nozzle;

the secondary oxidant delivery member includes at least one secondary oxidant supply channel through which a secondary oxidant flows, one end of the at least one secondary oxidant supply channel being provided with a secondary oxidant nozzle;

the tertiary oxidant delivery member includes at least one tertiary oxidant supply channel through which a tertiary oxidant flows, one end of the at least one tertiary oxidant supply channel being provided with a tertiary oxidant nozzle.