TW201319469A - Burner for H2 and burning method of burner for H2 - Google Patents

Abstract

The present invention provides a burner that uses H2 gas as a fuel with safety in ignition and that is capable of shortening a burning time of H2 gas in a catalyst. The burner for H2 of the present invention is burner (1) for H2 having two different passages A and B for gas flowing. The first flow passage B is formed to flow H2 gas and a first supporting gas, and the second flow passage A is formed to flow H2 gas and a second supporting gas. A flame which is positioned at the end of the second flow passage A is ignited by a flame formed at the end of the first flow passage B. The first flow passage B has a catalyst (4) which can be ignited depending on the supply of H2 gas and the first supporting gas.

Description

Burning method for burner for H 2 and burner for H 2

The present invention relates to a combustion method for a burner for H _{2 and} a burner for H ₂ .

In recent years, in order to prevent the increasing global warming, attention has been paid to renewable energy such as the sun, wind, geothermal, ocean, and hydropower. However, it is not only this, but also expects that H will not be emitted by combustion. ₂ Gas is effectively used as an ideal fuel.

The present application claims priority based on Japanese Patent Application No. 2011-178212, filed on Jan. 17, 2011, in Japan, which is incorporated herein.

However, the H ₂ gas system is difficult to apply a combustion technology such as a hydrocarbon gas, a reformed gas, or a natural gas, which has been used so far because of its wide range of combustion and fast burning speed. And limits its use as an industrial heating source.

And, H ₂ gas compared with other systems since the fuel combustion more easily, so in general the hydrogen combustion, countermeasures to backfire or NO _X production inhibitory responses has become an important issue.

On the other hand, since the H ₂ gas system can continue to burn at a lower temperature than other fuels, it is a stable and efficient burner when the catalyst is used to burn the H ₂ gas. It is well known.

Moreover, when the H ₂ gas system is compared with a hydrocarbon-based gas, most of the metal or metal oxide will become an effective combustion catalyst. Although it is a special case, an extremely low-temperature catalyst combustion method has been introduced as a liquid. Automatic ignition method of hydrogen.

In addition, in Japan in the 1970s, the Sunshine project of the Institute of Industrial Technology of the Ministry of Industry and Technology was started, and a number of studies have been completed for hydrogen absorbing alloy or hydrogen combustion technology. In particular, in the Osaka Industrial Laboratory, the characteristics of various metals or metal oxides have been investigated, and the equivalent ratio of H ₂ gas and air to the catalyst layer filled with the catalyst having high H ₂ activity has been investigated. It is possible to perform combustion at room temperature.

(previous technical literature)

Non-Patent Document 1: Hydrogen Energy Utilization Technology Otsuka Taiji, AGNE Technology Center

Non-Patent Document 2: The most advanced technology of hydrogen energy Hydrogen combustion technology p565 to p579 NTS

However, in the ignition of industrial furnaces, a direct ignition type pilot burner using an ignition transformer is generally employed.

Here, as far as the fuel of the pilot burner is used, a fuel having a combustion rate of, for example, a hydrocarbon gas or natural gas of about several tens of cm/sec is not problematic, but when H ₂ gas is used as a fuel, it is burned. The speed is as fast as 2.6m/sec, so there is a problem of security.

In particular, if there is a poor flushing or a failure in the combustion furnace, when it is re-ignited in a state of being filled with a mixed gas of fuel and air, there is a possibility of detonation, which is very dangerous. .

Further, the pilot burner is not only used as a continuous ignition for ignition, but even when it is used as a time-limited ignition, it is necessary to burn it for a certain period of time until it is ignited to the main burner.

Therefore, the inventors of the present invention have conducted a careful review on a burner using H2 gas as a fuel and burning it with a catalyst, but found that there is a problem in that when it is continuously burned by a catalyst for a certain period of time, The catalyst may be deteriorated by sintering, oxidation, or the like, or the high-temperature resistance of the carrier may reach a limit to deteriorate the catalyst.

Under such circumstances, although a burner and a burner combustion method capable of performing safe ignition while using H ₂ gas for fuel and shortening the combustion time of H ₂ gas under a catalyst are desired, the actual situation is However, it is a combustion method that does not provide an effective burner and burner.

In order to solve the above problems, the invention of claim 1 provides a burner for H ₂ having two different gas flow paths, characterized in that the first flow path is configured to be available for H ₂ gas and 1 supporting the flow of the flammable gas, the second flow path being configured to allow the H ₂ gas or the second flammable gas to flow, and the flame at the front end of the second flow path disposed at the front end of the first flow path to be movable In the position of the fire, a catalyst that can be ignited by supplying the H ₂ gas and the first supporting combustion gas is provided in the first flow path.

The invention of the invention of claim ₂ , wherein the catalyst contains at least one of Pt, Pd, PdO or PtO ₂ .

The invention of claim 3, wherein the burner for H ₂ according to claim 1 or 2, wherein the front end of the first flow path is provided with a flame detecting formation Detection agency.

Further, the invention of claim 4 provides a combustion method of a burner for H ₂ having a flow path of two different gases and having a catalyst in a first flow path, the combustion method having: H ₂ gas And the first supporting combustion gas flows through the first flow path, and the gas is ignited by the catalyst to form a flame at a front end of the first flow path; and the H ₂ gas or the second supporting combustion gas is used. a step of flowing through the second flow path of the H ₂ burner; a step of igniting the flame formed at the front end of the first flow path to the front end of the second flow path; and the H ₂ gas and the first support flammability The gas in the gas and the gas flowing through the second flow path are the same type of gas, and the flow stops in the first flow path.

The invention of claim 5, wherein the method of burning a burner for H ₂ according to claim 4, wherein the flame is formed at the front end of the first flow path, and the H ₂ gas or the first 2 Supporting the flow of the flammable gas to the second flow path.

Further, the invention of claim 6 is the method for burning a burner for H ₂ according to the fourth or fifth aspect of the invention, wherein the catalyst contains Pt, Pd, PdO or PtO ₂ Any kind or more.

In the burner for H _{2 of the} present invention, a catalyst that can be ignited by supplying H ₂ gas and supporting a combustion gas is provided in the first flow path. By allowing the combustion-supporting gas and the H ₂ gas to flow through the first flow path, the catalyst can be ignited without using a transformer or the like. As a result, since the transformer is not used for ignition, although H ₂ gas is used as the fuel, knocking or the like does not occur, and safety can be ensured.

Moreover, the front end of the second flow path is formed at a position where the front end of the first flow path can be ignited.

Therefore, the fire is formed by the catalyst provided in the first flow path, and at the same time or before or after, the H ₂ gas or the supporting combustion gas flows to the second flow path, and the fire is transferred to the second stage. At the front end of the flow path, the same type of gas as the gas flowing through the second flow path is stopped, and the flow to the first flow path is stopped, whereby deterioration of the catalyst can be prevented. That is, the fire is formed by the catalyst, and after the fire is transferred, the supply of the H ₂ gas supplied to the catalyst or the supply of the flammable gas is stopped, whereby the H ₂ under the catalyst can be stopped. The combustion of the gas prevents deterioration of the catalyst. Further, even if one of the H ₂ gas or the supporting combustion gas is stopped from flowing to the first flow path, since the same gas can be supplied from the second flow path, the second flow path can be provided at the front end of the second flow path. Continue to form a flame.

Moreover, the catalyst formed in the first flow path of the burner for H _{2 of the} present invention contains at least one of Pt, Pd, PdO or PtO ₂ . Thereby, the catalyst can be ignited efficiently.

Further, the burner for H _{2 of the} present invention is provided with a detecting mechanism capable of detecting the formation of a flame at the front end of the first flow path. Thereby, it is possible to accurately detect whether or not a fire is formed at the front end of the first flow path, and the supply of the stop gas to the first flow path can be performed accurately.

Moreover, the combustion method of the burner for H _{2 of the} present invention ignites by supplying H ₂ gas and supporting combustion gas to the catalyst formed in the first flow path. Therefore, since the transformer is not used during the fire, knocking or the like does not occur, and safety can be ensured.

Further, in the combustion method of the burner for H _{2 of the} present invention, the catalyst is ignited, and at the same time or before or after, the H ₂ gas or the supporting combustion gas is caused to flow to the second flow path and the fire is moved. The fire is the same type of gas as the gas flowing through the second flow path among the gas flowing through the first flow path, and the flow is stopped. As a result, the combustion of the H ₂ gas under the catalyst can be stopped, and the deterioration of the catalyst can be prevented. In addition, even if one of the H ₂ gas or the supporting combustion gas flowing through the first flow path is stopped, the same gas is flown to the second flow path, so that it can be at the front end of the second flow path. Continue to form a flame.

Hereinafter, a combustion method of a burner for H _{2 and} a burner for H ₂ according to an embodiment of the present invention will be described with reference to the drawings.

<H ₂ burner>

Fig. 1 is a cross-sectional view showing a burner 1 for H ₂ according to an embodiment of the present invention.

The burner 1 for H _{2 is} a tubular structure having flow rates A and B of two different gases therein, and as shown in Fig. 1, has a configuration in which an outer tube 2 is disposed and the outer tube 2 is disposed. The inner tube 3, the catalyst 4 formed on the front end 3a side of the inner tube 3, and the inner tube 5 disposed in the inner tube 3.

The outer tube 2 is a tubular hollow tube body, and an inner tube 3 is disposed inside, and an opening portion 2c is formed at a front end 2a of the outer tube 2. Also, under the opening 2c The side of the swimming side becomes the burning portion 6, and is configured to be able to form the flame F.

Further, on the side 2b (rear end) on the opposite side of the front end 2a of the outer tube 2, the combustion-supporting gas supply device 7 is connected through the pipe 8, and the outer tube 2 is formed to be capable of supplying combustion support to the combustion portion 6. Sex gas (second support flammable gas).

The inner tube 3 is a tubular hollow tube body, and is disposed in the outer tube 2 while being formed in the same axial direction as the outer tube 2, and a flame (not shown) can be formed at the front end 3a of the inner tube 3.

On the opposite end side 3b (rear end) side of the front end 3a of the inner tube 3, an H ₂ gas supply device 9 is connected through the pipe 10, and the inner tube 3 is formed to be capable of supplying the catalyst 4 and the combustion portion 6 H ₂ gas.

Further, the inside of the front end 3a side of the inner tube 3 is filled with a catalyst 4 (catalyst layer), and the front end 3a of the inner tube 3 is formed in a nozzle shape in which a plurality of ejection holes 3c are formed. Further, the arrangement position of the inner tube 3 may be any position as long as the flame formed at the front end 3a of the inner tube 3 can be ignited to the position of the front end 2a of the outer tube 2. For example, the position of the front end 3a of the inner tube 3 can be set to a position that is more concave than the position of the front end 2a of the outer tube 2, or a more prominent position. In this case, the region where the flame is formed by the front end 3a of the inner tube 3 is formed in the inner tube 3 as long as at least a portion overlaps with the formation region of the flame F formed by the front end 2a of the outer tube 2. The flame of the front end 3a can be fired to the front end 2a of the outer tube 2, so the position of the front end 3a of the inner tube 3 can be arbitrarily adjusted for the position of the front end 2a of the outer tube 2 to conform to such a positional relationship.

The catalyst 4 may be any one that can be ignited by supplying H ₂ gas and supporting a combustion gas, and may contain Pt (platinum), Pd (palladium), PdO (palladium oxide) or PtO ₂ ( When any of the types of platinum dioxide is used, it is possible to ignite efficiently.

In particular, when Pd or PdO is used as a catalyst, even if the flow rate of the supplied combustion-supporting gas is changed, it can be applied as an H ₂ dissociation catalyst, and even if the flow rate of the H ₂ gas is excessive In the state of the state, it still has sufficient ignition performance, so it is more desirable.

In addition, the catalyst 4 reaches a temperature of up to 500 to 800 degrees.

Further, inside the inner tube 3, the inner tube 5 is repeatedly disposed on the upstream side of the catalyst 4.

The inner tube 5 is a tubular hollow tube body, and is disposed in the inner tube 3 while forming the same axial direction as the inner tube or the outer tube 2.

On the side of the opposite end 5b (rear end) of the front end 5a of the inner tube 5, a combustion-supporting gas supply device 21 is connected through the pipe 22, and the inner tube 5 is formed to be capable of the catalyst 4 and the combustion portion 6. Supply of combustion-supporting gas (first support combustion gas). Further, the arrangement position of the inner tube 5 may be any position as long as the front end 5a of the inner tube 5 can spray the catalytic gas to the catalyst 4 at a position.

In the H ₂ burner 1 , a flow path A (second flow path) is formed in a space between the outer tube 2 and the inner tube 3 disposed in the outer tube 2 , and the inner tube 3 and the inner tube 3 are disposed in the inner tube 3 . A flow path C is formed in the space between the inner tubes 5, and a flow path D is formed in the inner tube 5. Further, on the front end 3a side of the inner tube 3, a flow path B (first flow path) in which the flow path C and the flow path D are merged is formed.

In other words, the flow path A is configured to support the flow of the flammable gas, the flow path B is for supplying the H ₂ gas and the flammable gas, and the flow path C is for the H ₂ gas to flow, and the flow path D is for supporting the combustion. Sexual gas flow.

Further, as shown in Fig. 2 (a) and Fig. 2 (b), the burner 1 for H ₂ may be provided inside the outer tube 2 and at a space on the downstream side of the front end 3a of the inner tube 3 for use. A flame detecting mechanism 23 is detected. Thereby, it is possible to correctly detect whether a flame has been formed in the inner tube 3 as early as possible. Examples of the detecting mechanism 23 include a flame rod, a thermometer, a UV sensor, and the like.

The burner 1 for H _{2 of the} present embodiment has the above configuration.

Further, in the above-described embodiment, the supporting combustion gas supply device 7 is connected to the outer tube 2, the H ₂ gas supply device 9 is connected to the inner tube 3, and the supporting combustion gas supply device 21 is connected to the inner tube 5, However, it is not necessarily limited to such an aspect. For example, the H ₂ gas supply device can also be connected to the outer tube 2. Further, the supporting combustion gas supply device may be connected to the inner tube 3, and the H ₂ gas supply device may be connected to the inner tube 5.

<H ₂ burner combustion method>

Next, the combustion method of the burner for H _{2 of the} burner 1 for H ₂ described above will be described.

First, the combustion-supporting gas supply device 21 is used to flow the supporting combustion gas to the flow path D of the inner tube 5, and the H ₂ gas supply device 9 is used to flow the H ₂ gas to the inner tube 3 and the inner tube 5. The flow path between the spaces C.

Further, the combustion-supporting gas supplied from the combustion-enhancing gas supply device 21 may be, for example, air or oxygen.

Thereby, the flow path B formed on the front end 3a side of the inner tube 3 can supply the H ₂ gas and the supporting combustion gas by converging the gas flowing through the flow path C and the gas flowing through the flow path D. The flow and the catalyst 4 provided on the front end 3a side of the inner tube 3 can be supplied with H ₂ gas and a combustion-supporting gas. As a result, the H ₂ gas system starts to burn (ignition) by the catalyst 4, and a flame (not shown) is formed at the front end 3a of the inner tube 3 which is the front end of the flow path B.

Depending on the ignition principle of the H ₂ gas of the catalyst 4, although the details thereof are mostly unknown, it can be qualitatively considered as follows depending on the investigation of the H ₂ penetration phenomenon depending on the Pd film.

First, the H ₂ molecule is adsorbed on the catalyst 4, and the H ₂ molecule is dissociated into the H atom on the catalyst 4. Then, the dissociated H atoms generate heat of reaction by reacting with oxygen. As a result, it is considered that the reaction heat is regarded as the ignition energy to move the H ₂ to the combustion state.

In addition, the flow rate of the gas flowing to the flow path C and the flow path D is also a temperature of 530 ° C which exceeds the natural ignition temperature of H ₂ as long as the temperature of the H ₂ and the supporting combustion gas passing through the catalyst 4 exceeds the natural ignition temperature of H ₂ . It can be any flow rate and can be determined as appropriate.

After the flame is formed at the front end of the flow path B, the flammable gas supply device 7 is used to flow the support flammable gas to the flow path A formed between the outer tube 2 and the inner tube 3 at the same time or before and after. . Thereby, the flame formed at the front end of the flow path B is transferred to the front end 2a of the outer tube 2 belonging to the front end of the flow path A, and the flame F is formed at the front end of the flow path A.

In addition, the flammable gas to be supplied by the flammable gas supply device 7 may be, for example, air or oxygen, and is not necessarily required to be the same as the flammable gas supplied to the flammable gas supply device 21. body.

After the flame F is formed at the front end of the flow path A, the support of the flammable gas supply device 21 is stopped, and the supporting combustion gas is caused to flow to the flow path C or even the flow path B, and the end side of the flow path B is stopped. The H ₂ gas under the catalyst 4 is on fire.

In addition, when the combustion time of the H ₂ gas in the catalyst is long, the deterioration of the catalyst is abrupt. Therefore, it is preferable to stop the supply of the combustion gas after the formation of the flame at the front end of the flow path B. Or, after the flame F is formed at the front end of the flow path A, it is performed substantially simultaneously without interruption.

Further, when the detecting means 23 is provided in the outer tube 2, since the detecting means 23 can correctly detect whether or not a flame has been formed at the front end of the flow path B, the support can be accurately performed. The cessation of the supply of the flammable gas to the flow path B.

Further, in the above-described embodiment, the case where the supporting combustion gas flows into the flow path A and the flow path D and the H ₂ gas flows to the flow path C has been described, but the present invention is not necessarily limited to this aspect. .

It is also possible to cause the H ₂ gas to flow to the flow path A. In addition, when both the H ₂ gas and the supporting combustion gas are allowed to flow to the flow path B, the selection of the gas flowing to the flow path C and the flow path D may be appropriately determined.

In such a case, if the flame F is formed at the front end of the flow path A, the supply of the flow path B is stopped for the gas of the same type as the gas flowing to the flow path A among the H ₂ gas and the supporting combustion gas. Just fine. Here, when the supply of the same type of gas is stopped, the supply of the gas to be supplied to the flow path A is air, and when the combustion-supporting gas supplied to the flow path B is oxygen, the supply is stopped. The supply of the combustion gas (in this case, oxygen) to the flow path B is supplied.

In the burner ₂ for H _{2 of the} present embodiment, the catalyst 4 that can be ignited by supplying H ₂ gas and supporting combustion gas is provided in the flow path B. Thereby, the combustion gas and the H ₂ gas can be supplied to the flow path B, and the catalyst 4 can be used to ignite without using a transformer or the like. As a result, since the transformer is not used for ignition, although H ₂ gas is used as the fuel, knocking or the like does not occur, and safety can be ensured.

Further, the front end of the flow path A is formed at a position where the front end of the flow path B can be ignited. Therefore, the flame is formed by the catalyst 4 placed on the flow path B, and at the same time or before and after the supply of the combustion-supporting gas to the flow path A, the fire is transferred to the front end of the flow path A, and then the combustion resistance is stopped. The supply of the gas convection path B prevents deterioration of the catalyst. In other words, after the fire is formed by the catalyst and the fire is transferred, the supply of the combustion-supporting gas supplied to the catalyst is stopped, and both the H ₂ gas and the combustion-supporting gas are shortened. The time of the medium and the deterioration of the catalyst can be prevented by stopping the combustion under the catalyst. In addition, even if the supply of the flammable gas to the flow path B is stopped, the flammable gas which is the same gas as the flammable gas can be supplied from the flow path A, so that the flame can be continuously formed at the front end of the flow path A.

Further, in the combustion method of the burner 1 for H _{2 of the} present embodiment, the H ₂ gas and the combustion-supporting gas are supplied to the catalyst 4 formed in the flow path B to be ignited. Therefore, since the transformer is not used at the time of ignition, knocking or the like does not occur, and safety can be ensured.

Further, the catalyst 4 is ignited and a fire is formed at the front end of the flow path B, and at the same time or before and after the flow path A flows to support the combustion gas, and the fire is transferred to the front end of the flow path A, and Stop supporting the flow of the flammable gas to the flow path B. As a result, since the supply of the combustion gas is stopped, the combustion of the H ₂ gas under the catalyst can be shortened, and the deterioration of the catalyst can be prevented. Further, even if the supply of the combustion-supporting gas to the flow path B is stopped, the combustion-supporting gas is allowed to flow to the flow path A, so that the flame can be continuously formed.

The burner 1 for H ₂ described above has a configuration in which the inner tube 3 is disposed inside the outer tube 2. However, as long as two different flow paths can be formed, the flame formed at the front end of the first flow path can be ignited. Up to the front end of the second flow path, the structure of the burner may be any configuration, and may also be composed of two separate tubes.

In the example in which the two tubular bodies are formed, for example, as shown in FIG. 3, the inner tube 3 disposed inside the outer tube 2 may be disposed beside the outer tube 2.

Further, in the above-described embodiment, the case where the inner tube 5 is repeatedly provided inside the inner tube 3 has been described. However, it is also possible to supply the H ₂ gas and the combustion in the inner tube 3 without providing the inner tube 5. The composition of both sides of the gas.

Here, when the inner tube where the inner tube 5 is disposed inside the 3, without mixing in advance since the H ₂ gas and combustion support gas, and the catalyst 4 for supply of H ₂ gas and combustion support gas, so that when the ignition The possibility of a backfire is low. On the other hand, when the inner tube 5 is not provided and only the H ₂ gas and the combustion-supporting gas are supplied to the inner tube 3, since these gases are mixed in advance, it is preferably taken to be appropriate. Measures to prevent backfire.

Next, the advantages of the burner for H _{2 of the} present embodiment will be further described by taking a heating treatment method of a heating target gas and a flare stack as an example.

<heat treatment method of target gas>

As shown in Fig. 4, the heat treatment device 24 for heating the target gas of the burner for H _{2 of the} present embodiment is roughly composed of a main burner 25 and H ₂ provided at the front end of the main burner 25. It is composed of the burner 1.

The main burner 25 is composed of a pipe 27 that supplies a target gas to a combustion portion 26 that is a space of a front end portion of the main burner 25, and a main burner body 28 that surrounds the pipe. 27 is formed in a peripheral manner, and is provided with a discharge port 28a that supplies fuel to the combustion portion 26. Further, a pipe 29 for introducing fuel into the main burner body 28 is connected to the main burner body 28.

In the case where the heat treatment device 24 is used to heat-treat the heating target gas, first, the H ₂ burner 1 as a pilot burner is ignited. Then, separately from the supply of heating gas to the main burner 25 of the pipe 27, 28 for supplying fuel from the main burner body, and H ₂ using a flame of a burner to ignite the main burner 25. Thus, the combustion portion 26 at the front end of the main burner 25 forms a flame (not shown), and heats the processing target gas.

In general, when H ₂ gas is used as the fuel of the main burner, in order to prevent knocking caused by the mixture of H ₂ gas and supporting combustion gas in the furnace, the pilot burner is previously provided as described above. After the ignition, the main burner is introduced with fuel.

Here, conventionally, since H ₂ gas cannot be used as a fuel for a pilot burner, an apparatus for introducing a fuel such as a hydrocarbon-based gas different from the fuel of the main burner and a device for detecting leakage thereof are required in the pilot burner. . Therefore, there is a problem that the cost required for the ignition operation of the main burner is increased.

On the other hand, if the H ₂ burner 1 of the present embodiment is used, even if H ₂ gas is used as the fuel, the fuel can be safely ignited, so that the supply device of the fuel other than H ₂ is not required and the leak is detected. The device can suppress the cost of ignition of the main burner 25.

<torch chimney>

Next, the advantages of the flare stack of the burner 1 for H _{2 of the} present embodiment will be described.

As shown in Fig. 5, the flare stack 41 is composed of a discharge tower 43 connected to a storage device 42 for burning a desired gas, and a burner 1 for H ₂ provided at the front end of the discharge tower 43.

In the case where the gas is burned using the flare stack 41, first, the burner 1 for H ₂ is ignited. Then, as long as the desired gas burned from the storage device 42 is sent to the discharge tower 43, and at the front end of the discharge tower 43, the flame of the burner 1 for H _{2 is} used, and the desired gas is ignited and burned.

Here, in the case of a conventional flare chimney, since it is a burner installed at the front end of the discharge tower, it is necessary to use an ordinary pilot burner. Ignite with an electrical energy source such as a spark plug.

Therefore, it is necessary to supply electrical equipment, and even if a flare chimney is used as a security device, it is necessary to prepare a standby power source called a battery or an emergency generator that is provided at the time of power failure.

However, when the burner 1 for H _{2 of the} present embodiment is used, since the H ₂ gas and the combustion-supporting gas can be ignited by the catalyst 4, it is possible to ignite. Therefore, it is not necessary to supply an electric device and a backup power source. Therefore, it is possible to suppress the supply of electrical equipment and the preparation of the power supply and the maintenance of such expenses.

Further, when the gas to be burned stored in the storage device 42 is H ₂ gas, since the H ₂ gas is only required to be a fuel for the burner for H ₂ , the fuel of the burner and the fuel are not required. The equipment used to supply the fuel can suppress the cost.

Further, a flame using H ₂ gas as a fuel is more likely to be blown out than when a hydrocarbon-based gas is used as a fuel as in a conventional burner, so that when the burner 1 for H _{2 is} used, even When the wind speed in the discharge tower 43 is increased, the function of not blowing out is also exerted.

As a result, in the case where the gas of the same flow rate is to be treated by the flare stack 41, when the burner 1 for H _{2 is} used, the inner diameter of the tower of the discharge tower 43 can be further reduced as compared with the case of using a conventional burner, and The flare stack 41 itself can be miniaturized.

The present invention has been described above with reference to the embodiments, and the invention is not limited thereto, and various modifications can be made without departing from the spirit and scope of the invention.

Hereinafter, the present invention will be described in more detail by way of examples, but The invention is not limited to the embodiments described below.

(Example 1)

In the first embodiment, the same H ₂ burner as the above-described H ₂ burner 1 is used, and the outer tube 2 is supplied with H ₂ gas at a flow rate of 10 L/min, and the inner tube 5 is supplied with 1.5 L/min. The flow of H ₂ gas, and the time required to change the flow rate of the air supplied to the inner tube 3 until the ignition occurs. The catalyst used was Pd, and the ambient and initial gas temperatures were set to 20 °C. In addition, the confirmation of the ignition is performed using a thermometer provided on the front end side of the outer tube 2.

As shown in Fig. 6, when the H ₂ concentration on the catalyst is from about 20% by volume to about 30% by volume, the time required for the ignition becomes short.

This confirmed that the measurement result of the minimum ignition energy generated by the spark in each H ₂ concentration (refer to Fig. 7) was very consistent, and the combustion of H ₂ was performed on the catalyst.

(Example 2)

In the second embodiment, when the burner for H ₂ similar to the burner 1 for H ₂ described in the embodiment is used, and each of Pd, Pt, PdO or PtO ₂ is used as a catalyst, ignition is carried out. Comparison of performance. Specifically, by supplying the H ₂ gas having a flow rate of 10 L/min to the outer tube 2, the inner tube 5 is supplied with H ₂ gas at a flow rate of ₂ L/min, and the flow rate of the air supplied into the inner tube 3 is changed. Performance comparison was performed while measuring the maximum temperature reached 30 seconds after the ignition operation. Further, as shown in Fig. 8, the measurement of the highest temperature is performed using the temperature sensor 44 provided on the outer wall of the front end 3a of the inner tube 3. The results are shown in Figure 9.

As shown in Fig. 9, it can be seen that even in which type of catalyst, there is an air volume indicating the H ₂ gas passing through the catalyst and the temperature at which the combustion-promoting gas exceeds the natural ignition point of H ₂ at a temperature of 530 ° C. Range, and has the properties required for ignition of H ₂ gas.

Further, in the case of using Pd or PdO as a catalyst, according to the above 530 ℃ temperature over a wide range of air flow through the catalyst reaches the H ₂ gas and combustion support gas, as can be learned from ₂ Solution H Catalyst is very useful.

Further, in the case where Pd or PdO is used as the catalyst, even when the flow rate of the air passing through the catalyst is less than the theoretical air ratio with respect to the amount of H ₂ gas, a high temperature rise can be confirmed. This is because, under the condition that the theoretical air ratio is not exceeded, the unburned H ₂ gas heated by the catalyst is naturally ignited at the tip end of the nozzle discharge hole, and a flame is generated. Therefore, in the case of using such a catalyst, sufficient ignition performance is obtained even in an air ratio in which the fuel is excessive.

Further, in Example 2, it was confirmed that although the temperature was raised up to 750 ° C, no backfire was confirmed under any of the conditions, and the H ₂ gas and the supporting combustion gas were not mixed beforehand. According to the structure, even if the temperature of H ₂ rises, no backfire occurs, and ignition can be performed.

(industrial availability)

According to the present invention, since the combustion-supporting gas and the H ₂ gas are caused to flow to the first flow path of the burner for H ₂ without using a transformer, the H ₂ gas is used as the fuel, but the explosion does not occur. Shock, etc., to ensure safety. Thus, the present invention is applicable to a burner for H ₂ and a combustion method therefor.

1‧‧‧H ₂ burner

2‧‧‧External management

2a‧‧‧ front end of the outer tube

2b‧‧‧One end of the opposite side of the front end of the outer tube

2c‧‧‧ openings

3‧‧‧Inside

3a‧‧‧ front end of the inner tube

3b‧‧‧One end of the opposite side of the front end of the inner tube

3c‧‧‧Spray hole

4‧‧‧ Catalyst

5‧‧‧Inner management

5a‧‧‧ front end of the inner tube

5b‧‧‧One end of the opposite side of the front end of the inner tube

6‧‧‧ burning part

7, 21‧‧‧ Supporting flammable gas supply

8, 10, 22, 27, 29‧‧‧ piping

9‧‧‧H ₂ gas supply device

23‧‧‧Detecting agencies

24‧‧‧heat treatment unit

25‧‧‧Main burner

26‧‧‧ burning part

28‧‧‧Main burner body

28a‧‧‧Spray outlet

41‧‧‧Torch Chimney

42‧‧‧Storage equipment

43‧‧‧ release tower

44‧‧‧temperature sensor

A‧‧‧flow path (second flow path)

B‧‧‧Flow path (first flow path)

C, D‧‧‧ flow path

F‧‧‧flame

Fig. 1 is a cross-sectional view showing an example of a burner for H _{2 of the} present embodiment.

Fig. 2(a) is a cross-sectional view showing an example of the burner for H _{2 of the} present embodiment, and Fig. 2(b) is a side view seen from the front end side of the burner for H ₂ .

Fig. 3 is a perspective view showing a part of another example of the burner for H _{2 of} the embodiment.

Fig. 4 is a schematic view showing a heat treatment apparatus using the burner for H _{2 of the} present embodiment.

Fig. 5 is a schematic view showing a flare stack using the burner for H _{2 of the} present embodiment.

Fig. 6 is a graph showing the relationship between the H ₂ concentration on the catalyst of one embodiment of the present invention and the time until the ignition is confirmed.

Figure 7 is a graph showing the minimum igniting energy depending on the concentration of the hydrogen-air mixture.

Figure 8 is a cross-sectional view showing a portion of a burner for H ₂ employed in an embodiment of the present invention.

Figure 9 is a graph showing the relationship between the air flow rate and the highest reached temperature of an embodiment of the present invention.

1‧‧‧H ₂ burner

2‧‧‧External management

2a‧‧‧ front end of the outer tube

2b‧‧‧One end of the opposite side of the front end of the outer tube

2c‧‧‧ openings

3‧‧‧Inside

3a‧‧‧ front end of the inner tube

3b‧‧‧One end of the opposite side of the front end of the inner tube

3c‧‧‧Spray hole

4‧‧‧ Catalyst

5‧‧‧Inner management

5a‧‧‧ front end of the inner tube

5b‧‧‧One end of the opposite side of the front end of the inner tube

6‧‧‧ burning part

7, 21‧‧‧ Supporting flammable gas supply

8, 10, 22‧‧‧ piping

9‧‧‧H ₂ gas supply device

A‧‧‧flow path (second flow path)

B‧‧‧Flow path (first flow path)

C, D‧‧‧ flow path

F‧‧‧flame

Claims (6)

A burner for H ₂ is a flow path having two different gases, wherein the first flow path is configured to allow H ₂ gas and the first supporting combustion gas to flow, and the second flow path is configured to be available The H ₂ gas or the second supporting combustion gas flows, and the front end of the second flow path is disposed at a position at which the flame formed at the front end of the first flow path can be ignited, and the first flow path is provided A catalyst that is ignited by the supply of H ₂ gas and the first flammable gas. The burner for H ₂ according to claim 1, wherein the catalyst contains at least one of Pt, Pd, PdO or PtO ₂ . The burner for H ₂ according to claim 1 or 2, wherein a detecting mechanism capable of detecting formation of a flame is provided at a front end of the first flow path. A method for burning a burner for H ₂ , wherein the burner for H ₂ has two different gas flow paths, and a catalyst is provided in the first flow path, and the combustion method of the burner for H ₂ has: The H ₂ gas and the first supporting combustion gas flow in the first flow path, and the gas is ignited by the catalyst to form a flame at the front end of the first flow path; and the H ₂ gas or the second support combustion gas flowing in the H ₂ step second flow passage burner only; formed step in the flame front in the first flow path of the shift fire to the front end of the second flow passage of; and for H ₂ gas and the second (1) A step of supporting a gas of the same type as the gas flowing through the second flow path in the combustion gas to stop flowing in the first flow path. The combustion method of the burner for H ₂ according to the fourth aspect of the invention, wherein the second flow is formed by flowing a H ₂ gas or a second supporting combustion gas after the flame is formed at the front end of the first flow path. road. The method for burning a burner for H ₂ according to the invention of claim 4, wherein the catalyst contains at least one of Pt, Pd, PdO or PtO ₂ .