TWI876968B - Regenerative hydrogen combustion equipment - Google Patents
Regenerative hydrogen combustion equipment Download PDFInfo
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- TWI876968B TWI876968B TW113115129A TW113115129A TWI876968B TW I876968 B TWI876968 B TW I876968B TW 113115129 A TW113115129 A TW 113115129A TW 113115129 A TW113115129 A TW 113115129A TW I876968 B TWI876968 B TW I876968B
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/02—Premix gas burners, i.e. in which gaseous fuel is mixed with combustion air upstream of the combustion zone
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details
- F23D14/66—Preheating the combustion air or gas
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C9/00—Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details
- F23D14/48—Nozzles
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details
- F23D14/62—Mixing devices; Mixing tubes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/002—Gaseous fuel
- F23K5/007—Details
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L5/00—Blast-producing apparatus before the fire
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L9/00—Passages or apertures for delivering secondary air for completing combustion of fuel
- F23L9/02—Passages or apertures for delivering secondary air for completing combustion of fuel by discharging the air above the fire
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C2900/00—Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
- F23C2900/9901—Combustion process using hydrogen, hydrogen peroxide water or brown gas as fuel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Air Supply (AREA)
- Pre-Mixing And Non-Premixing Gas Burner (AREA)
Abstract
Description
本發明係關於一種蓄熱式氫燃燒設備,其係在蓄熱式燃燒設備中使用氫於燃料中者,該蓄熱式燃燒設備係進行:燃燒動作,係從燃料噴出噴嘴噴出燃料於爐內,並且使通過收容有蓄熱體之蓄熱部而加熱的空氣從供/排氣口噴出於爐內,而使燃料與空氣混合且使之在爐內燃燒;及蓄熱動作,係將燃料在爐內被燃燒後的燃燒排氣從供/排氣口引導至蓄熱部而使燃燒排氣的熱蓄熱於收容於蓄熱部的蓄熱體。 The present invention relates to a heat storage type hydrogen combustion device, which uses hydrogen in fuel. The heat storage type combustion device performs: a combustion action, in which fuel is ejected from a fuel ejection nozzle into a furnace, and air heated by passing through a heat storage part containing a heat storage body is ejected from a supply/exhaust port into the furnace, so that the fuel and air are mixed and burned in the furnace; and a heat storage action, in which combustion exhaust gas after the fuel is burned in the furnace is guided from the supply/exhaust port to the heat storage part, so that the heat of the combustion exhaust gas is stored in the heat storage body contained in the heat storage part.
以往,在將鋼材等各種被處理物進行加熱處理的工業爐等中,已知有一種蓄熱式燃燒設備,該蓄熱式燃燒設備為了有效地利用在爐內使燃料燃燒後之燃燒排氣的熱,係進行:燃燒動作,係從燃料噴出噴嘴噴出燃料於爐內,並且使通過收容有蓄熱體之蓄熱部而加熱的空氣從供/排氣口噴出於爐內,而使燃料與空氣混合且使之在爐內燃燒;及蓄熱動作,係將燃料在爐內被燃燒後的燃燒排氣從供/排氣口引導至蓄熱部而使燃燒排氣的熱蓄熱於收容於蓄熱部的蓄熱體。 In the past, in industrial furnaces that heat various processed materials such as steel, a heat storage type combustion device is known. In order to effectively utilize the heat of the combustion exhaust gas after the fuel is burned in the furnace, the heat storage type combustion device performs: a combustion action, in which the fuel is sprayed into the furnace from the fuel spray nozzle, and the air heated by passing through the heat storage part containing the heat storage body is sprayed into the furnace from the supply/exhaust port, so that the fuel and the air are mixed and burned in the furnace; and a heat storage action, in which the combustion exhaust gas after the fuel is burned in the furnace is guided from the supply/exhaust port to the heat storage part, so that the heat of the combustion exhaust gas is stored in the heat storage body contained in the heat storage part.
再者,作為此種蓄熱式燃燒設備來說,已知有一種如專利文獻1所揭示者,其係在燃料噴射噴嘴的兩側設置供/排氣口,交替地進行使在收容有蓄熱體之蓄熱部中被加熱過的空氣從一方的供/排氣口噴射於爐內,而使從燃料噴射噴嘴噴射於爐內的燃料燃燒的燃燒動作,另一方面,進行使燃料在爐內被燃燒後的燃燒排氣通過另一方的供/排氣口而將之引導至蓄熱部且使燃燒排氣的熱蓄熱於收容於蓄熱部之蓄熱體的蓄熱動作。
Furthermore, as such a heat storage combustion device, there is known a device disclosed in
此外,已知有一種如專利文獻2所揭示者,其係成對地設置具有燃料噴射噴嘴和供/排氣口的蓄熱式燃燒器,該燃料噴射噴嘴係使燃料噴出於爐內;該供/排氣口係進行使在收容有蓄熱體的蓄熱部中被加熱後的空氣噴射於爐內的動作、及將燃料在爐內被燃燒後的燃燒排氣引導至蓄熱部且使燃燒排氣的熱蓄熱於收容於蓄熱部之蓄熱體的動作;在一方的蓄熱式燃燒器中,係進行使燃料從燃料噴出噴嘴噴出於爐內,並且使通過收容有蓄熱體之蓄熱部而加熱的空氣從供/排氣口噴出於爐內,且使燃料與空氣混合且使之在爐內燃燒的燃燒動作,另一方面,在另一方的蓄熱式燃燒器中,係進行使燃料從燃料噴出噴嘴噴出於爐內之動作停止,且將燃料在爐內被燃燒後的燃燒排氣引導至蓄熱部且使燃燒排氣的熱蓄熱於收容於蓄熱部之蓄熱體的蓄熱動作,在成對的蓄熱式燃燒器中交替地切換而進行燃燒動作和蓄熱動作。 In addition, as disclosed in Patent Document 2, a regenerative burner having a fuel injection nozzle and an air supply/exhaust port is known, wherein the fuel injection nozzle causes the fuel to be ejected into the furnace; the air supply/exhaust port causes the air heated in the heat storage section containing the heat storage body to be ejected into the furnace, and causes the combustion exhaust gas after the fuel is burned in the furnace to be guided to the heat storage section and causes the heat of the combustion exhaust gas to be stored in the heat storage body contained in the heat storage section; in one regenerative burner, the fuel is ejected from the fuel injection nozzle into the heat storage section; and the heat storage section is used to eject the fuel from the fuel injection nozzle into the heat storage section. In the furnace, the air heated by the heat storage part containing the heat storage body is ejected from the air supply/exhaust port into the furnace, and the fuel is mixed with the air and burned in the furnace. On the other hand, in the other regenerative burner, the action of ejecting the fuel from the fuel ejection nozzle into the furnace is stopped, and the combustion exhaust gas after the fuel is burned in the furnace is guided to the heat storage part and the heat of the combustion exhaust gas is stored in the heat storage body contained in the heat storage part. The combustion action and the heat storage action are alternately switched in the paired regenerative burners.
在此,在習知之蓄熱式燃燒設備中之如前所述的各蓄熱式燃燒器中,一般使用了碳氫化合物氣體等化石燃料作為燃料。 Here, in the known regenerative combustion equipment, in the regenerative burners as described above, fossil fuels such as hydrocarbon gas are generally used as fuel.
在此,如前述專利文獻1所示,當構成為可交替地切換使碳氫化合物氣體等化石燃料從燃料噴射噴嘴噴出,並且使在收容有蓄熱體的
蓄熱部中被加熱後的空氣從一方的供/排氣口噴射於爐內,且使從燃料噴射噴嘴噴射於爐內的燃料燃燒的燃燒動作,及將燃料在爐內被燃燒後的燃燒排氣通過另一方的供/排氣口引導至蓄熱部且使燃燒排氣的熱蓄熱於收容於蓄熱部之蓄熱體的蓄熱動作時,會有在該切換時空氣暫時地不足,從燃料噴射噴嘴噴出於爐內的化石燃料未完全地燃燒而發生煤煙,而使被處理物遭受到污損的問題。
Here, as shown in the
此外,如前述專利文獻2所示,當構成為在一方的蓄熱式燃燒器中,進行使化石燃料從燃料噴出噴嘴噴出於爐內,並且使通過收容有蓄熱體之蓄熱部而加熱的空氣從供/排氣口噴出於爐內,且使化石燃料與空氣混合且使之在爐內燃燒的燃燒動作,另一方面,在另一方的蓄熱式燃燒器中,進行使燃料從燃料噴出噴嘴噴出於爐內之動作停止,且將化石燃料在爐內被燃燒後的燃燒排氣引導至蓄熱部且使燃燒排氣的熱蓄熱於收容於蓄熱部之蓄熱體的蓄熱動作,在成對的蓄熱式燃燒器中交替地切換而進行燃燒動作和蓄熱動作時,亦會有空氣暫時地不足,而於切換燃燒動作和蓄熱動作時,從燃料噴射噴嘴噴出於爐內的化石燃料未完全地燃燒而發生煤煙,而使被處理物遭受到污損的問題。 In addition, as shown in the aforementioned patent document 2, when the structure is such that in one regenerative burner, the fossil fuel is ejected from the fuel ejection nozzle into the furnace, and the air heated by passing through the heat storage part containing the heat storage body is ejected from the supply/exhaust port into the furnace, and the fossil fuel and the air are mixed and burned in the furnace, on the other hand, in the other regenerative burner, the action of ejecting the fuel from the fuel ejection nozzle into the furnace is stopped, and The combustion exhaust gas after the fossil fuel is burned in the furnace is guided to the heat storage part and the heat of the combustion exhaust gas is stored in the heat storage body contained in the heat storage part. When the combustion action and the heat storage action are alternately switched in the paired heat storage burners, there will be a temporary shortage of air. When switching the combustion action and the heat storage action, the fossil fuel ejected from the fuel injection nozzle into the furnace is not completely burned and soot is generated, causing the treated material to be contaminated.
再者,在如前述專利文獻2所示者中係揭示了如下的內容:如圖1所示,當交替地在一方的蓄熱式燃燒器1A中,進行使碳氫化合物氣體等化石燃料G從燃料噴出噴嘴2a噴出於爐R內,並且使通過收容有蓄熱體3a之蓄熱部4a而加熱的空氣Air從供/排氣口5a噴出於爐R內,且使化石燃料G與空氣Air混合且使之在爐R內燃燒的燃燒動作,及在另一方的蓄熱式燃燒器1B中,進行使化石燃料G從燃料噴出噴嘴2b噴出
於爐R內之動作停止,且將在爐R內中化石燃料G被燃燒後的燃燒排氣從供/排氣口5b引導至蓄熱部4b且使燃燒排氣的熱蓄熱於收容於蓄熱部4b之蓄熱體3b的蓄熱動作之際,如圖2所示,在任一個蓄熱式燃燒器1A、1B中,均於在開始燃燒動作的時點,首先在使通過收容有蓄熱體3a、3b之蓄熱部4a、4b而加熱的空氣Air從供/排氣口5a、5b噴出於爐R內之後,使化石燃料G從燃料噴出噴嘴2a、2b噴出於爐R內且開始燃燒,另一方面,在開始蓄熱動作的時點,首先在使從燃料噴出噴嘴2a、2b對於爐R內之化石燃料G的噴出停止之後,停止使通過收容有蓄熱體3a、3b之蓄熱部4a、4b而加熱的空氣Air從供/排氣口5a、5b噴出於爐R內的動作,而於從燃料噴出噴嘴2a、2b噴出化石燃料G於爐R內的時候,係以使通過收容有蓄熱體3a、3b的蓄熱部4a、4b而加熱且從供/排氣口5a、5b噴出於爐R內的空氣Air必然不會不足之方式,以抑制燃燒時煤煙的發生。
Furthermore, the above-mentioned patent document 2 discloses the following contents: as shown in FIG. 1, when a fossil fuel G such as hydrocarbon gas is alternately ejected from a
然而,如此一來,在任一個蓄熱式燃燒器1A、1B中都會產生燃燒未被進行的時間,且如圖2所示,在該時點中,會有爐R內的溫度降低,爐R內的溫度變動,無法將被處理物在適當的溫度進行加熱處理的問題。
However, in this case, there will be a time when combustion is not carried out in any of the
[先前技術文獻] [Prior Art Literature]
[專利文獻] [Patent Literature]
專利文獻1:日本特許第4602858號公報 Patent document 1: Japanese Patent No. 4602858
專利文獻2:日本特許第3159606號公報 Patent document 2: Japanese Patent No. 3159606
本發明之目的為解決蓄熱式燃燒設備中之如前所述的問題者,該蓄熱式燃燒設備係構成為進行:燃燒動作,係從燃料噴出噴嘴噴出燃料於爐內,並且使通過收容有蓄熱體之蓄熱部而加熱的空氣從供/排氣口噴出於爐內,而使燃料與空氣混合且使之在爐內燃燒;及蓄熱動作,係將燃料在爐內被燃燒後的燃燒排氣從供/排氣口引導至蓄熱部而使燃燒排氣的熱蓄熱於收容於蓄熱部的蓄熱體。 The purpose of the present invention is to solve the above-mentioned problems in the heat storage type combustion equipment. The heat storage type combustion equipment is configured to perform: combustion action, which is to spray fuel from the fuel spray nozzle into the furnace, and make the air heated by passing through the heat storage part containing the heat storage body spray into the furnace from the supply/exhaust port, so that the fuel and air are mixed and burned in the furnace; and heat storage action, which is to guide the combustion exhaust gas after the fuel is burned in the furnace from the supply/exhaust port to the heat storage part so that the heat of the combustion exhaust gas is stored in the heat storage body contained in the heat storage part.
在本發明的第一蓄熱式氫燃燒設備中,為了解決如前所述的問題,係在使氫噴出於爐內的燃料噴射噴嘴的兩側設置供/排氣口,且進行燃燒動作且另一方面交替地進行蓄熱動作,該燃燒動作係使在收容有蓄熱體之蓄熱部中被加熱後的空氣從一方的供/排氣口噴射於爐內,而使從燃料噴射噴嘴噴射於爐內的氫燃燒;該蓄熱動作係進行將氫在爐內被燃燒之後的燃燒排氣通過另一方的供/排氣口而引導至蓄熱部且使燃燒排氣的熱蓄熱於收容於蓄熱部之蓄熱體。 In the first heat storage hydrogen combustion device of the present invention, in order to solve the above-mentioned problem, air supply/exhaust ports are provided on both sides of the fuel injection nozzle that sprays hydrogen into the furnace, and a combustion action is performed and a heat storage action is performed alternately on the other hand. The combustion action is to spray the air heated in the heat storage part containing the heat storage body into the furnace from the air supply/exhaust port on one side, and to burn the hydrogen sprayed into the furnace from the fuel injection nozzle; the heat storage action is to guide the combustion exhaust gas after the hydrogen is burned in the furnace through the air supply/exhaust port on the other side to the heat storage part, and store the heat of the combustion exhaust gas in the heat storage body contained in the heat storage part.
在此,在前述第一蓄熱式氫燃燒設備中,於從燃料噴射噴嘴噴出於爐內的燃料係使用了氫,故即使從燃料噴射噴嘴噴出於爐內的氫未被完全地燃燒,也不會如習知的化石燃料般發生煤煙,而防止被處理物遭受污損,並且氫的燃燒性極高,故即使產生未燃燒的氫也會被迅速地燃燒。 Here, in the aforementioned first regenerative hydrogen combustion equipment, hydrogen is used as the fuel ejected from the fuel ejection nozzle into the furnace, so even if the hydrogen ejected from the fuel ejection nozzle into the furnace is not completely burned, soot will not be generated like the known fossil fuel, and the treated material will be prevented from being polluted. In addition, hydrogen has extremely high combustibility, so even if unburned hydrogen is generated, it will be burned quickly.
再者,在前述第一蓄熱式氫燃燒設備中,當構成為同時地切換而進行使在收容有蓄熱體的蓄熱部中被加熱後的空氣從一方的供/排氣口噴射於爐內的動作、及通過另一方的供/排氣口而引導至蓄熱部的動作的情形下,即使在切換時,從燃料噴射噴嘴噴出於爐內的氫未被完全地燃燒而殘留,也不會有如前所述發生煤煙的情形,而防止被處理物遭受污損,並且氫的燃燒性極高,故即使產生未燃燒的氫也會被迅速地燃燒。 Furthermore, in the aforementioned first regenerative hydrogen combustion equipment, when the configuration is to switch simultaneously to eject the air heated in the heat storage part containing the heat storage body from one supply/exhaust port into the furnace and to guide the air to the heat storage part through the other supply/exhaust port, even if the hydrogen ejected from the fuel injection nozzle into the furnace is not completely burned and remains during the switching, the situation of soot as described above will not occur, and the treated material will be prevented from being contaminated. Moreover, the combustibility of hydrogen is extremely high, so even if unburned hydrogen is generated, it will be burned quickly.
此外,在本發明的第二蓄熱式氫燃燒設備中,為了解決如前所述的問題,係構成為成對地設置具有燃料噴射噴嘴和供/排氣口的蓄熱式燃燒器,該燃料噴射噴嘴係使氫噴出於爐內;該供/排氣口係進行使在收容有蓄熱體的蓄熱部中被加熱後的空氣噴射於爐內的動作、及將氫在爐內被燃燒後的燃燒排氣引導至蓄熱部且使燃燒排氣的熱蓄熱於收容於蓄熱部之蓄熱體的動作;在一方的蓄熱式燃燒器中,係進行使氫從燃料噴出噴嘴噴出於爐內,並且使通過收容有蓄熱體之蓄熱部而加熱的空氣從供/排氣口噴出於爐內,且使氫與空氣混合且使之在爐內燃燒的燃燒動作,另一方面,在另一方的蓄熱式燃燒器中,係進行使氫從燃料噴出噴嘴噴出於爐內之動作停止,且將氫在爐內被燃燒後的燃燒排氣引導至蓄熱部且使燃燒排氣的熱蓄熱於收容於蓄熱部之蓄熱體的蓄熱動作,在成對的蓄熱式燃燒器中交替地切換而進行燃燒動作和蓄熱動作。 In addition, in the second regenerative hydrogen combustion equipment of the present invention, in order to solve the above-mentioned problem, a regenerative burner having a fuel injection nozzle and a supply/exhaust port is arranged in pairs, the fuel injection nozzle causes hydrogen to be ejected into the furnace; the supply/exhaust port causes the air heated in the heat storage section containing the heat storage body to be ejected into the furnace, and the combustion exhaust gas after the hydrogen is burned in the furnace is guided to the heat storage section and the heat of the combustion exhaust gas is stored in the heat storage body contained in the heat storage section; in the regenerative burner on one side, hydrogen is discharged from the fuel and discharged into the furnace; The ejection nozzle ejects into the furnace, and the air heated by passing through the heat storage part containing the heat storage body is ejected into the furnace from the air supply/exhaust port, and hydrogen is mixed with air and burned in the furnace. On the other hand, in the other regenerative burner, the action of ejecting hydrogen into the furnace from the fuel ejection nozzle is stopped, and the combustion exhaust gas after hydrogen is burned in the furnace is guided to the heat storage part, and the heat of the combustion exhaust gas is stored in the heat storage body contained in the heat storage part. The combustion action and the heat storage action are alternately switched in the paired regenerative burners.
在此,在第二蓄熱式氫燃燒設備中,亦與前述第一蓄熱式氫燃燒設備同樣地,係於從燃料噴射噴嘴噴出於爐內的燃料中使用了氫,故即使從燃料噴射噴嘴噴出於爐內的氫未被完全地燃燒,也不會有如習知的 化石燃料般發生煤煙的情形,而防止被處理物遭受污損,並且氫的燃燒性極高,故即使產生未燃燒的氫也會被迅速地燃燒。 Here, in the second regenerative hydrogen combustion equipment, similarly to the first regenerative hydrogen combustion equipment, hydrogen is used in the fuel ejected from the fuel ejection nozzle into the furnace, so even if the hydrogen ejected from the fuel ejection nozzle into the furnace is not completely burned, there will be no soot as in the known fossil fuels, and the treated material will be prevented from being contaminated. Furthermore, hydrogen has extremely high combustibility, so even if unburned hydrogen is generated, it will be burned quickly.
再者,當構成為在前述第二蓄熱式氫燃燒設備中,在切換成對之蓄熱式燃燒器中之燃燒動作和蓄熱動作之際,同時地切換而進行使在收容有蓄熱體的蓄熱部中被加熱後的空氣從一方的供/排氣口噴射於爐內的動作、及通過另一方的供/排氣口而引導至蓄熱部的動作的情形下,即使在切換時,從燃燒狀態下之燃料噴射噴嘴噴出於爐內的氫未被完全地燃燒而殘留,也不會有如前所述發生煤煙的情形,而防止被處理物遭受污損,並且氫的燃燒性極高,故即使產生未燃燒的氫,也將藉由另一方之蓄熱式燃燒器中的燃燒動作而被迅速地燃燒。 Furthermore, when the second regenerative hydrogen combustion device is configured such that, when switching between the combustion action and the heat storage action in the paired regenerative burner, the action of ejecting the air heated in the heat storage part containing the heat storage body from the air supply/exhaust port on one side into the furnace and the action of guiding the air heated in the heat storage part through the air supply/exhaust port on the other side are performed simultaneously, In this case, even if the hydrogen ejected from the burning fuel injection nozzle into the furnace is not completely burned and remains during switching, there will be no soot as mentioned above, thus preventing the treated material from being contaminated. In addition, hydrogen has a very high combustibility, so even if unburned hydrogen is produced, it will be quickly burned by the combustion action in the other regenerative burner.
此外,在前述第二蓄熱式氫燃燒設備中,較佳為設置用於切換氫對於前述燃料噴射噴嘴之供給和停止的燃料切換閥,並且設置對於前述燃料噴射噴嘴供給惰性氣體的惰性氣體供給管,且從前述惰性氣體供給管供給惰性氣體至藉由前述燃料切換閥停止氫之供給的燃料噴射噴嘴。如此一來,惰性氣體被供給至已停止燃燒動作的燃料噴射噴嘴內,而防止爐內的空氣流入於前述燃料噴射噴嘴內,且當將氫供給至該燃料噴射噴嘴內而進行燃燒動作時,可防止氫與燃料噴射噴嘴內的空氣混合,而在燃料噴射噴嘴內發生爆炸。 In addition, in the aforementioned second heat storage type hydrogen combustion equipment, it is preferred to provide a fuel switching valve for switching the supply and stop of hydrogen to the aforementioned fuel injection nozzle, and to provide an inert gas supply pipe for supplying inert gas to the aforementioned fuel injection nozzle, and to supply inert gas from the aforementioned inert gas supply pipe to the fuel injection nozzle where the supply of hydrogen is stopped by the aforementioned fuel switching valve. In this way, inert gas is supplied to the fuel injection nozzle that has stopped burning, preventing the air in the furnace from flowing into the aforementioned fuel injection nozzle, and when hydrogen is supplied to the fuel injection nozzle to perform combustion, it can prevent hydrogen from mixing with the air in the fuel injection nozzle and causing an explosion in the fuel injection nozzle.
此外,在前述第二蓄熱式氫燃燒設備中,較佳為將切換對於前述燃料噴射噴嘴停止和供給氫的燃料切換閥設置於前述燃料噴射噴嘴中之噴出口的附近。如此,若將前述燃料切換閥設於燃料噴射噴嘴中之噴出口的附近,當關閉前述燃料切換閥時,已使燃燒動作停止的燃料噴射噴嘴 與燃料切換閥之間的空間變小,可使爐內的空氣流入於燃料噴射噴嘴內的量減為極少,且當對於該燃料噴射噴嘴內供給氫而進行燃燒動作時,可抑制氫與燃料噴射噴嘴內的空氣混合,而於燃料噴射噴嘴內發生爆炸。 Furthermore, in the second regenerative hydrogen combustion device, it is preferred that a fuel switching valve for switching between stopping and supplying hydrogen to the fuel injection nozzle be provided near an injection port in the fuel injection nozzle. In this way, if the aforementioned fuel switching valve is arranged near the injection port in the fuel injection nozzle, when the aforementioned fuel switching valve is closed, the space between the fuel injection nozzle which has stopped the combustion action and the fuel switching valve becomes smaller, so that the amount of air in the furnace flowing into the fuel injection nozzle can be reduced to a minimum, and when hydrogen is supplied to the fuel injection nozzle to perform the combustion action, the hydrogen can be suppressed from mixing with the air in the fuel injection nozzle, and an explosion can be suppressed from occurring in the fuel injection nozzle.
在本發明的第一和第二蓄熱式氫燃燒設備中,如前所述係於從燃料噴射噴嘴噴出於爐內的燃料中使用了氫,故即使從燃料噴射噴嘴噴出於爐內的氫未被完全地燃燒,也不會有發生煤煙的情形,而防止被處理物遭受污損,並且氫的燃燒性極高,故即使產生未燃燒的氫也會被迅速地燃燒。 In the first and second regenerative hydrogen combustion devices of the present invention, as mentioned above, hydrogen is used in the fuel ejected from the fuel ejection nozzle into the furnace, so even if the hydrogen ejected from the fuel ejection nozzle into the furnace is not completely burned, there will be no soot, and the treated material will be prevented from being contaminated. In addition, hydrogen has extremely high combustibility, so even if unburned hydrogen is generated, it will be quickly burned.
藉此,在切換燃燒動作和蓄熱動作時,可消除爐內溫度的變動。 This can eliminate temperature fluctuations in the furnace when switching between combustion and heat storage.
10,50a,50b:燃料噴射噴嘴 10,50a,50b: fuel injection nozzle
11,51a,51b:燃料供給管 11,51a,51b: fuel supply pipe
12,52a,52b:燃料切換閥 12,52a,52b: Fuel switching valve
13,53a,53b:噴出口 13,53a,53b: Spray outlet
20a,20b:供/排氣口 20a, 20b: air supply/exhaust port
21,61:送風鼓風機 21,61: Air blower
22,64:吸引鼓風機 22,64: Suction blower
31,62:空氣供給管 31,62: Air supply pipe
32a,32b,63a,63b:供給閥 32a,32b,63a,63b: Supply valve
33a,33b,42a,42b:蓄熱部 33a, 33b, 42a, 42b: heat storage part
34a,34b,43a,43b:蓄熱體 34a,34b,43a,43b: heat storage body
35,65:排氣管 35,65: Exhaust pipe
36,67:排氣塔 36,67: Exhaust tower
36a,36b,66a,66b:排氣閥 36a,36b,66a,66b: Exhaust valve
40A,40B:蓄熱式燃燒器 40A, 40B: Regenerative burner
41a,41b:供/排氣口 41a,41b: air supply/exhaust port
54a,54b:惰性氣體供給管 54a, 54b: Inert gas supply pipe
55a,55b:開閉閥 55a,55b: Open/Close valve
Air:空氣 Air: Air
H2:氫 H 2 : Hydrogen
N2:氮(惰性氣體) N2 : Nitrogen (inert gas)
R1,R2:爐 R1, R2: Furnace
圖1係顯示習知之蓄熱式燃燒設備的概略剖面說明圖。 Figure 1 is a schematic cross-sectional view of a known regenerative combustion device.
圖2係顯示在習知之蓄熱式燃燒設備中之一對蓄熱式燃燒器1A、1B中,要使化石燃料從燃料噴出噴嘴噴出於爐內的時間點、與要使空氣從供/排氣口噴出於爐內的時間點的關係;要停止使化石燃料從燃料噴出噴嘴噴出於爐內的時間點、與要停止使空氣從供/排氣口噴出於爐內的時間點的關係;及爐內之溫度的變化的圖。
FIG2 shows the relationship between the time when fossil fuel is ejected from the fuel ejection nozzle into the furnace and the time when air is ejected from the supply/exhaust port into the furnace in a pair of
圖3係顯示本發明之實施型態1之蓄熱式氫燃燒設備的概略剖面說明圖。
Figure 3 is a schematic cross-sectional view of the heat storage hydrogen combustion equipment of
圖4係顯示本發明之實施型態2之蓄熱式氫燃燒設備的概略剖面說明圖。 FIG4 is a schematic cross-sectional view showing the heat storage hydrogen combustion equipment of embodiment 2 of the present invention.
圖5係顯示在前述實施型態2之蓄熱式氫燃燒設備中之一對蓄熱式燃燒器40A、40B中,要使氫從燃料噴出噴嘴噴出於爐內的時間點、與要使空氣從供/排氣口噴出於爐內的時間點的關係;要停止使氫從燃料噴出噴嘴噴出於爐內的時間點、與要停止使空氣從供/排氣口噴出於爐內的時間點的關係;及爐內之溫度的變化的圖。
FIG5 shows the relationship between the time when hydrogen is ejected from the fuel ejection nozzle into the furnace and the time when air is ejected from the supply/exhaust port into the furnace in a pair of
圖6係顯示前述實施型態2之蓄熱式氫燃燒設備的變更例,且顯示將燃料切換閥設置在燃料噴射噴嘴中之噴出口的附近之狀態的概略剖面說明圖,該燃料切換閥係切換氫對於燃料噴射噴嘴之供給和停止。 FIG6 is a schematic cross-sectional view showing a modification of the heat storage hydrogen combustion equipment of the aforementioned embodiment 2, and showing a state in which a fuel switching valve is set near the injection port in the fuel injection nozzle, and the fuel switching valve switches the supply and stop of hydrogen to the fuel injection nozzle.
以下根據所附圖式具體地說明本發明之實施型態的蓄熱式氫燃燒設備。另外,本發明的蓄熱式氫燃燒設備係不限定於下述實施型態所示者,在不變更發明之要旨的範圍內,亦可適當地變更而實施。 The following specifically describes the thermal storage hydrogen combustion equipment of the embodiment of the present invention according to the attached drawings. In addition, the thermal storage hydrogen combustion equipment of the present invention is not limited to the embodiment shown below, and can be appropriately modified and implemented within the scope of not changing the gist of the invention.
(實施型態1) (Implementation Type 1)
在實施型態1的蓄熱式燃燒設備中,如圖3所示,係構成為開啟設在供給氫H2之燃料供給管11的燃料切換閥12,通過燃料供給管11將氫H2引導至燃料噴射噴嘴10,且從該燃料噴射噴嘴10前端的噴出口13噴出氫H2至爐R1內。在此,關於前述的燃料切換閥12或後述的各種閥,係以反白顯示開啟的狀態,且以塗黑顯示關閉的狀態。
In the regenerative combustion equipment of the
此外,以位於設在爐R1之前述燃料噴射噴嘴10前端之噴出口13之兩側之方式設有二個供/排氣口20a、20b。
In addition, two air supply/
再者,在一方的供/排氣口20a側中,如圖3所示,係構成為進行藉由送風鼓風機21將空氣Air供給至空氣供給管31,且開啟設在前述空氣供給管31之一方的供給閥32a,而將空氣Air引導至一方的蓄熱部33a,且使前述空氣Air藉由該蓄熱部33a內被加熱的蓄熱體34a加熱,且使加熱後的空氣Air從一方的供/排氣口20a噴射於爐R1內,而使從前述燃料噴射噴嘴10噴射於爐R1內的氫H2燃燒的燃燒動作。另外,在以此方式使空氣Air供給至蓄熱部33a內且使氫H2燃燒的燃燒動作中,係關閉了設在使燃燒排氣從前述蓄熱部33a內排出之排氣管35之一方的排氣閥36a。
Furthermore, on the side of the air supply/
另一方面,在另一方的供/排氣口20b側,如圖3所示,係構成為進行了關閉設於前述空氣供給管31之另一方之供給閥32b,使得空氣Air不會被引導至另一方的蓄熱部33b,另一方面,開啟設在使燃燒排氣從前述蓄熱部33b內排出之排氣管35的排氣閥36b,藉由吸引鼓風機22吸引,而使燃燒過氫H2後的燃燒排氣從爐R1內通過前述供/排氣口20b而引導至另一方的蓄熱部33b,且使燃燒排氣的熱蓄熱於該蓄熱部33b內之蓄熱體34b的蓄熱動作之後,使前述燃燒排氣通過前述排氣管35而引導至排氣塔36而使之排氣。
On the other hand, on the other side of the air supply/
再者,在此實施型態1的蓄熱式燃燒設備中,係如前所述構成為一面從燃料噴射噴嘴10噴出氫H2於爐R1內,一面同時地交替地切
換而進行前述一方之供/排氣口20a側的燃燒動作、和另一方之供/排氣口20b側的蓄熱動作。
Furthermore, in the regenerative combustion equipment of this
在此,在此實施型態1的蓄熱式燃燒設備中,係如前所述構成為使氫H2從燃料噴射噴嘴10噴出於爐R1內且使之燃燒,故在切換前述一方之供/排氣口20a側的燃燒動作、和另一方之供/排氣口20b側的蓄熱動作時,即使空氣暫時地不足,氫H2未完全地燃燒,而殘留氫H2的一部分,也不會有如習知的化石燃料般發生煤煙,而使被處理物(未圖示)遭受污損的情形,而且因為氫H2燃燒性極高,故即使產生未燃燒的氫H2,亦將在切換後,藉由從供/排氣口20a、20b噴射於爐R1內的空氣Air而被迅速地燃燒。
Here, in the regenerative combustion equipment of this
(實施型態2) (Implementation Type 2)
在實施型態2的蓄熱式氫燃燒設備中,如圖4所示,係將成對的蓄熱式燃燒器40A、40B設置為朝向爐R2的內部相對向。
In the regenerative hydrogen combustion equipment of embodiment 2, as shown in FIG4 , a pair of
再者,在前述成對的各蓄熱式燃燒器40A、40B中,係構成為開啟設在分別供給氫H2之各燃料供給管51a、51b的各燃料切換閥52a、52b,通過各燃料供給管51a、51b將氫H2引導至各燃料噴射噴嘴50a、50b,且從各燃料噴射噴嘴50a、50b之前端的噴出口53a、53b分別噴出氫H2於爐R2內。另外,關於前述的燃料切換閥52a、52b或後述的各種閥,係與前述實施型態1同樣地,以反白顯示開啟的狀態,以塗黑顯示關閉的狀態。
Furthermore, in the aforementioned paired
此外,構成為相對於前述燃料噴射噴嘴50a、50b,分別設置供給惰性氣體之氮N2的惰性氣體供給管54a、54b,並且在各惰性氣體供
給管54a、54b分別設置開閉閥55a、55b,藉由開閉閥55a、55b的開閉,而進行對於各燃料噴射噴嘴50a、50b供給和停止氮N2。
In addition, inert
再者,在實施型態2的蓄熱式燃燒設備中,係構成為藉由送風鼓風機61將空氣Air供給至空氣供給管62,且在前述空氣供給管62以對應各蓄熱式燃燒器40A、40B中之各蓄熱部42a、42b之方式分別設置供給閥63a、63b,且開閉前述供給閥63a、63b而切換對於各蓄熱部42a、42b供給和停止空氣Air,且通過各蓄熱部42a、42b而使空氣Air從各蓄熱式燃燒器40A、40B中的各供/排氣口41a、41b噴射於爐R2內。
Furthermore, in the regenerative combustion equipment of the second embodiment, the air Air is supplied to the
此外,構成為以藉由吸引鼓風機64吸引在爐R2內氫H2被燃燒後的燃燒排氣,且通過各蓄熱式燃燒器40A、40B中的各供/排氣口41a、41b而引導至前述各蓄熱部42a、42b,且將被引導至各蓄熱部42a、42b的燃燒排氣引導至排氣管65;且開啟設於排氣管65的排氣閥66a、66b,而使前述燃燒排氣從各蓄熱部42a、42b通過排氣管65引導至排氣塔67而使之排氣。
In addition, the exhaust gas after the hydrogen H2 is burned in the furnace R2 is sucked by the
再者,在一方的蓄熱式燃燒器40A中,係構成為以下列方式進行燃燒動作:藉由送風鼓風機61將空氣Air供給至空氣供給管62,且開啟設於空氣供給管62之一方的供給閥63a,而將空氣Air引導至該蓄熱式燃燒器40A中的蓄熱部42a,且將前述空氣Air藉由蓄熱部42a內之被加熱後的蓄熱體43a加熱,且使加熱後的空氣Air從該蓄熱式燃燒器40A中的供/排氣口41a噴射於爐R2內,並且開啟設於前述燃料供給管51a的燃料切換閥52a,將氫H2供給至前述燃料噴射噴嘴50a,且從該燃料噴射噴嘴50a前端的噴出口53a噴出氫H2於爐R1內,而使氫H2燃燒。
Furthermore, in the
在此,在以此方式使通過蓄熱部42a而加熱的空氣Air從供/排氣口41a噴射於爐R2內,而進行使氫H2燃燒的燃燒動作之一方的蓄熱式燃燒器40A中,係構成為關閉設在使氫H2在爐R2內燃燒後的燃燒排氣從前述蓄熱部42a內排出之排氣管65之一方的排氣閥66a,並且關閉設在前述惰性氣體供給管54a的開閉閥55a,而不使惰性氣體的氮N2供給至燃料噴射噴嘴50a內。
Here, in the
另一方面,在不進行燃燒動作之另一方的蓄熱式燃燒器40B中,係構成為以在進行了關閉設在前述燃料供給管51b的燃料切換閥52b,而不使氫H2供給至前述燃料噴射噴嘴50b,並且關閉設在前述空氣供給管62的供給閥63b,不將空氣Air引導至該蓄熱式燃燒器40B中的蓄熱部42b,在該狀態下,開啟設在從前述蓄熱部42b內排出燃燒排氣之排氣管65的排氣閥66b,且藉由吸引鼓風機64吸引在爐R2內氫H2被燃燒後的燃燒排氣,且通過蓄熱式燃燒器40B中的供/排氣口41b而引導至前述蓄熱部42b,且使燃燒排氣的熱蓄熱於收容在該蓄熱部42b內之蓄熱體43b的蓄熱動作之後,使前述燃燒排氣通過前述排氣管65而引導至排氣塔67使之排氣。
On the other hand, in the other
在此,在如前所述進行不使氫H2供給至燃料噴射噴嘴50b,將爐R2內的燃燒排氣引導至前述蓄熱部42b,且使燃燒排氣的熱蓄熱於收容於該蓄熱部42b內之蓄熱體43b的蓄熱動作之另一方的蓄熱式燃燒器40B中,係構成為開啟設在前述惰性氣體供給管54b的開閉閥55b,而使惰性氣體的氮N2微少地供給至前述燃料噴射噴嘴50b。
Here, in the
如此一來,在關閉燃料切換閥52b時使殘留於燃料噴射噴嘴50b內的氫H2噴出於爐R2內而加以逐出,將可防止回火。
In this way, when the
此外,可防止在爐R2內的空氣Air流入於前述燃料噴射噴嘴50b內,且在此另一方的蓄熱式燃燒器40B中,當對於前述燃料噴射噴嘴50b供給氫H2而進行燃燒動作時,可防止供給至燃料噴射噴嘴50b的氫H2與流入於燃料噴射噴嘴50b內的空氣Air混合,而在燃料噴射噴嘴50b內產生爆炸。
In addition, the air Air in the furnace R2 can be prevented from flowing into the aforementioned
此外,藉由流動常溫的氮N2,可防止細小之燃料噴射噴嘴50b內的過度升溫,且可防止燃料噴射噴嘴50b因為熱而變形。
Furthermore, by flowing nitrogen N 2 at room temperature, excessive temperature rise in the small
此外,在實施型態2的蓄熱式燃燒設備中,亦由於在燃料中使用了氫H2,故在切換燃燒動作和蓄熱動作時,即使氫H2未完全地燃燒,而殘留了氫H2的一部分,也不會有如習知的化石燃料般發生煤煙,而使被處理物(未圖示)遭受污損的情形,此外,由於氫H2的燃燒性極高,故即使產生未燃燒的氫H2,也會在切換後,藉由從前述供/排氣口41a、41b噴射於爐R2內的空氣Air而被被迅速地燃燒。
Furthermore, in the regenerative combustion equipment of the second embodiment, since hydrogen H2 is used as fuel, even if hydrogen H2 is not completely burned and a part of hydrogen H2 remains when switching between the combustion operation and the regenerative operation, there is no possibility of generating soot as in the conventional fossil fuels, thereby causing the treated material (not shown) to be polluted. Furthermore, since hydrogen H2 has an extremely high combustibility, even if unburned hydrogen H2 is generated, it will be quickly burned by the air Air injected into the furnace R2 from the aforementioned air supply/
如此一來,在實施型態2的蓄熱式氫燃燒設備中,當在前述成對的蓄熱式燃燒器40A、40B中,切換如前所述之燃燒動作和蓄熱動作而交替進行之際,係使燃燒動作和蓄熱動作的切換同時進行,如圖5所示,可使藉由前述燃料切換閥52a、52b切換氫H2從燃料噴射噴嘴50a、50b對於爐R2內之供給和停止的時間點、和藉由設於空氣供給管62的前述供給閥63a、63b而切換從各蓄熱式燃燒器40A、40B中之各供/排氣口41a、41b對於爐R2內供給和停止空氣Air的時間點成為同時。結果,如圖5所
示,爐R2內的溫度將保持為固定,在爐R2內中,將可用穩定的溫度處理被處理物(未圖示)。
Thus, in the regenerative hydrogen combustion device of the second embodiment, when the combustion operation and the regenerative heat operation are switched alternately in the pair of
此外,在此實施型態2的蓄熱式氫燃燒設備中,如前所述,雖構成為爐R2內的空氣Air流入於已停止燃燒動作的燃料噴射噴嘴50a、50b內而進行燃燒動作的時候,為了防止供給至燃料噴射噴嘴50a、50b的氫H2與流入於燃料噴射噴嘴50a、50b內的空氣Air混合,而在燃料噴射噴嘴50a、50b內發生爆炸,故使惰性氣體的氮N2從惰性氣體供給管54a、54b供給至已停止燃燒動作的燃料噴射噴嘴50a、50b,然而,未必要使惰性氣體的氮N2從惰性氣體供給管54a、54b供給至燃料噴射噴嘴50a、50b。
In addition, in the regenerative hydrogen combustion equipment of this embodiment 2, as described above, although it is configured that the air Air in the furnace R2 flows into the
例如,如圖6所示,可將切換氫H2對於燃料噴射噴嘴50a、50b之供給和停止的燃料切換閥52a、52b設在前述燃料噴射噴嘴50a、50b中的噴出口53a、53b附近,減少爐R2內中的空氣Air流入至已停止燃燒動作之燃料噴射噴嘴50a、50b內的容積。
For example, as shown in FIG. 6 ,
如此一來,從爐R2內流入至燃料噴射噴嘴50a、50b內之空氣Air的量變得極少,當進行燃燒動作時,將可抑制供給至燃料噴射噴嘴50a、50b的氫H2在燃料噴射噴嘴50a、50b內爆炸。
In this way, the amount of air Air flowing from the furnace R2 into the
40A,40B:蓄熱式燃燒器 40A, 40B: Regenerative burner
41a,41b:供/排氣口 41a,41b: air supply/exhaust port
42a,42b:蓄熱部 42a, 42b: heat storage part
43a,43b:蓄熱體 43a,43b: Heat storage body
50a,50b:燃料噴射噴嘴 50a, 50b: fuel injection nozzle
51a,51b:燃料供給管 51a, 51b: fuel supply pipe
52a,52b:燃料切換閥 52a,52b: fuel switching valve
53a,53b:噴出口 53a,53b: Spray outlet
54a,54b:惰性氣體供給管 54a, 54b: Inert gas supply pipe
55a,55b:開閉閥 55a,55b: Open/Close valve
61:送風鼓風機 61: Air blower
62:空氣供給管 62: Air supply pipe
63a,63b:供給閥 63a,63b: Supply valve
64:吸引鼓風機 64: Suction blower
65:排氣管 65: Exhaust pipe
66a,66b:排氣閥 66a,66b: Exhaust valve
67:排氣塔 67: Exhaust tower
Air:空氣 Air: Air
H2:氫 H 2 : Hydrogen
N2:氮(惰性氣體) N2 : Nitrogen (inert gas)
R2:爐 R2: Furnace
Claims (5)
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| CN204084339U (en) * | 2014-09-25 | 2015-01-07 | 河北钢铁股份有限公司唐山分公司 | A kind of heat-accumulating burner that can realize coal gas and burn completely |
| TW201833505A (en) * | 2017-03-03 | 2018-09-16 | 日商中外爐工業股份有限公司 | Regenerative burner system |
| CN116085760A (en) * | 2022-11-06 | 2023-05-09 | 北京工大环能科技有限公司 | A supplementary combustion thermoelectric decoupling system for gas and steam power generation and its working mechanism |
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| JPS462858Y1 (en) | 1968-10-29 | 1971-02-01 | ||
| JP2571556Y2 (en) * | 1992-11-30 | 1998-05-18 | 中外炉工業株式会社 | Heat storage regeneration burner |
| JPH11286719A (en) * | 1998-04-02 | 1999-10-19 | Toho Gas Co Ltd | Non-oxidative heat treatment method and apparatus |
| JP2002181324A (en) * | 2000-12-08 | 2002-06-26 | Kawasaki Steel Corp | Explosion-proof gas heating apparatus and explosion-proof gas heating method |
| JP3159606U (en) | 2010-03-08 | 2010-05-27 | アイテック株式会社 | Knife |
| US10059615B2 (en) * | 2015-10-29 | 2018-08-28 | Praxair Technology, Inc. | Thermochemical regeneration and heat recovery in glass furnaces |
| JP6855917B2 (en) * | 2017-05-16 | 2021-04-07 | 三浦工業株式会社 | Hydrogen combustion boiler |
| WO2018216331A1 (en) * | 2017-05-26 | 2018-11-29 | 三浦工業株式会社 | Hydrogen combustion boiler |
| CN114395421A (en) * | 2021-12-03 | 2022-04-26 | 上海柯来浦能源科技有限公司 | Double-molten pool heating gasification furnace |
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| CN204084339U (en) * | 2014-09-25 | 2015-01-07 | 河北钢铁股份有限公司唐山分公司 | A kind of heat-accumulating burner that can realize coal gas and burn completely |
| TW201833505A (en) * | 2017-03-03 | 2018-09-16 | 日商中外爐工業股份有限公司 | Regenerative burner system |
| CN116085760A (en) * | 2022-11-06 | 2023-05-09 | 北京工大环能科技有限公司 | A supplementary combustion thermoelectric decoupling system for gas and steam power generation and its working mechanism |
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