JP4405888B2 - Detoxification method of gas to be processed using electric furnace for steelmaking - Google Patents

Detoxification method of gas to be processed using electric furnace for steelmaking Download PDF

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JP4405888B2
JP4405888B2 JP2004281964A JP2004281964A JP4405888B2 JP 4405888 B2 JP4405888 B2 JP 4405888B2 JP 2004281964 A JP2004281964 A JP 2004281964A JP 2004281964 A JP2004281964 A JP 2004281964A JP 4405888 B2 JP4405888 B2 JP 4405888B2
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識生 竹田
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共英製鋼株式会社
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    • YGENERAL 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
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Description

本発明は、冷蔵庫、エアコン等の民生用機器や半導体の製造装置等の産業用機器に冷媒や洗浄剤として使用されていたフロンガス等のHFC化合物等の被処理ガス(本明細書において、単に「被処理ガス」という。)の無害化処理方法に関し、特に、製鋼用電気炉を用いて不要となった被処理ガスを安全に、かつ低コストで分解処理することができる製鋼用電気炉を用いた被処理ガスの無害化処理方法に関するものである。   The present invention relates to a gas to be treated such as an HFC compound such as chlorofluorocarbon gas, which has been used as a refrigerant or a cleaning agent in consumer equipment such as refrigerators and air conditioners and industrial equipment such as semiconductor manufacturing equipment (in this specification, simply “ In particular, a steelmaking electric furnace capable of safely and inexpensively decomposing a gas to be processed that has become unnecessary using a steelmaking electric furnace is used. The present invention relates to a method for detoxifying a gas to be treated.

近年、オゾン層を破壊するフロンガス、具体的には、特定フロンといわれる、フロン11(CClF)、フロン12(CCl)、フロン113(CCl)、フロン22(CHClF)等に関する問題が世界的な規模で提起され、これらのフロンガスの生産が中止となり、事実上使用することができなくなった。 In recent years, chlorofluorocarbon gas that destroys the ozone layer, specifically, chlorofluorocarbon 11 (CCl 3 F), chlorofluorocarbon 12 (CCl 2 F 2 ), chlorofluorocarbon 113 (C 2 Cl 3 F 3 ), chlorofluorocarbon 22 ( Problems with CHClF 2 ), etc. were raised on a global scale, and the production of these chlorofluorocarbons was discontinued and became virtually unusable.

一方、既に各種機器に冷媒や洗浄剤として使用されているフロンガスについては、この規制の対象外となるため、フロンガスが充填された機器がそのまま廃棄されたり、放置されることが多かったが、最近では、この問題が指摘されるに至り、不要となったフロンガスの回収が積極的に行われるようになっている。   On the other hand, chlorofluorocarbons already used as refrigerants and cleaning agents in various equipment are not subject to this regulation, so equipment filled with chlorofluorocarbons was often discarded or left untouched. Then, this problem has been pointed out, and the collection of CFCs that are no longer necessary has been actively carried out.

回収されたフロンガスの無害化処理方法としては、フロンガスを製鋼用電気炉に導入し、製鋼を行う際にアークにより形成される高温雰囲気中でフロンガスを分解する方法が本件出願人により提案されている(特許文献1参照)。
このフロンガスの無害化処理方法は、製鋼を行う際にアークにより形成される高温雰囲気中で、フロンガスを炭酸ガス(CO)、塩化水素(HCl)及びフッ化水素(HF)に分解し、分解ガスを冷却し、苛性ソーダにより中和するとともに、消石灰(Ca(OH))を添加してフッ化カルシウム(CaF)として沈殿、分離できることから、既存の製鋼設備をそのまま利用して、不要となったフロンガスを低コストで分解処理することができる。
As a method for detoxifying the recovered chlorofluorocarbon gas, the present applicant has proposed a method in which chlorofluorocarbon gas is introduced into an electric furnace for steel making and the chlorofluorocarbon gas is decomposed in a high-temperature atmosphere formed by an arc when making the steel. (See Patent Document 1).
This detoxification method of chlorofluorocarbon gas decomposes chlorofluorocarbon gas into carbon dioxide (CO 2 ), hydrogen chloride (HCl), and hydrogen fluoride (HF) in a high temperature atmosphere formed by an arc when steel making. Since the gas can be cooled and neutralized with caustic soda, slaked lime (Ca (OH) 2 ) can be added to precipitate and separate as calcium fluoride (CaF 2 ). The generated chlorofluorocarbon gas can be decomposed at low cost.

ところで、このフロンガスの無害化処理方法では、電気炉内の温度が安定しない通電初期などに、酸素バーナー等の補助加熱装置により炉内を加熱するようにしているが、この補助加熱装置は炉内温度が上昇すると停止するため、煤塵が滞留しやすいという問題があった。
また、既存の製鋼用電気炉にフロンガスを導入するためには、フロンガス用ノズルを別途設置する必要があるが、このフロンガス用ノズルは、フロンガスを高温で分解するために、アークが発生する溶鋼付近に配設しなければならず、そのため、ノズルの冷却設備も必要になるなど、設備投資費用がかさむという問題もあった。
特開平11−319484号公報
By the way, in this detoxifying treatment method for chlorofluorocarbon gas, the inside of the furnace is heated by an auxiliary heating device such as an oxygen burner in the initial stage of energization where the temperature in the electric furnace is not stable. Since it stops when the temperature rises, there is a problem that dust tends to stay.
In addition, in order to introduce chlorofluorocarbon into an existing steelmaking electric furnace, it is necessary to install a chlorofluorocarbon gas nozzle separately. This chlorofluorocarbon nozzle is near the molten steel where an arc is generated in order to decompose the chlorofluorocarbon at a high temperature. Therefore, there is a problem that the equipment investment cost is increased, for example, a nozzle cooling facility is required.
JP 11-319484 A

本発明は、上記従来の被処理ガスの無害化処理方法が有する問題点に鑑み、補助加熱装置の煤塵の滞留を防止するとともに、被処理ガス用ノズルやその冷却設備を不要とすることができる製鋼用電気炉を用いた被処理ガスの無害化処理方法を提供することを目的とする。   In view of the problems of the conventional method for detoxifying a gas to be treated, the present invention can prevent the accumulation of dust in the auxiliary heating device, and can eliminate the nozzle for the gas to be treated and its cooling equipment. It aims at providing the detoxification processing method of the to-be-processed gas using the electric furnace for steel manufacture.

上記目的を達成するため、本発明の製鋼用電気炉を用いた被処理ガスの無害化処理方法は、被処理ガスを製鋼用電気炉に導入し、製鋼を行う際にアークにより形成される高温雰囲気中で被処理ガスを分解する製鋼用電気炉を用いた被処理ガスの無害化処理方法において、前記製鋼用電気炉に配設した補助加熱装置に酸素ガスと被処理ガスを選択的に導入し、電気炉内が被処理ガスの分解温度以下の場合に酸素ガスを供給して補助加熱を行い、電気炉内が被処理ガスの分解温度を越える場合に前記酸素ガスの供給を停止して被処理ガスを供給することを特徴とする。 In order to achieve the above object, the method for detoxifying a gas to be treated using the electric steel furnace for steel production according to the present invention is a high temperature formed by an arc when the gas to be treated is introduced into the electric furnace for steel making and steel making is performed. In a method for detoxifying a gas to be treated using an electric furnace for steel making that decomposes the gas to be treated in an atmosphere, oxygen gas and the gas to be treated are selectively introduced into an auxiliary heating device disposed in the electric furnace for steel making. When the inside of the electric furnace is below the decomposition temperature of the gas to be treated , oxygen gas is supplied to perform auxiliary heating, and when the inside of the electric furnace exceeds the decomposition temperature of the gas to be treated , the supply of the oxygen gas is stopped. A gas to be treated is supplied.

この場合、電極棒の外周面を伝わせて製鋼用電気炉内に水を供給することができる。   In this case, water can be supplied into the steelmaking electric furnace along the outer peripheral surface of the electrode rod.

この製鋼用電気炉を用いた被処理ガスの無害化処理方法は、被処理ガスを製鋼用電気炉に導入し、製鋼を行う際にアークにより形成される高温雰囲気中で被処理ガスを分解する製鋼用電気炉を用いた被処理ガスの無害化処理方法において、前記製鋼用電気炉に配設した補助加熱装置に酸素ガスと被処理ガスを選択的に導入し、電気炉内が被処理ガスの分解温度以下の場合に酸素ガスを供給して補助加熱を行い、電気炉内が被処理ガスの分解温度を越える場合に前記酸素ガスの供給を停止して被処理ガスを供給することから、炉内温度が上昇した段階で停止する補助加熱装置を利用して被処理ガスを炉内に供給することができ、これにより、従来の被処理ガス用ノズルやその冷却設備を不要としながら、被処理ガスを高温の溶鋼付近に導入するとともに、供給される被処理ガスによって補助加熱装置を清掃し煤塵の滞留を防止することができる。 In this method of detoxifying a gas to be treated using an electric furnace for steelmaking, the gas to be treated is introduced into the electric furnace for steelmaking, and the gas to be treated is decomposed in a high-temperature atmosphere formed by an arc when steelmaking is performed. In the method for detoxifying a gas to be treated using an electric furnace for steel making, oxygen gas and the gas to be treated are selectively introduced into an auxiliary heating device disposed in the electric furnace for steel making, and the inside of the electric furnace is the gas to be treated. When oxygen gas is supplied below, the auxiliary heating is performed by supplying oxygen gas, and when the inside of the electric furnace exceeds the decomposition temperature of the gas to be processed, the supply of the oxygen gas is stopped and the gas to be processed is supplied. A gas to be treated can be supplied into the furnace by using an auxiliary heating device that stops when the temperature in the furnace rises. This eliminates the need for the conventional gas nozzle and its cooling equipment. Introduce treatment gas near hot molten steel Together, it is possible to clean the auxiliary heating device by the processed gas to be supplied to prevent the accumulation of dust.

この場合、電極棒の外周面を伝わせて製鋼用電気炉内に水を供給することにより、電極棒の冷却を行うとともに、被処理ガスの分解物質となる水分を炉内に供給することができる。   In this case, by supplying water into the electric steel furnace for steelmaking along the outer peripheral surface of the electrode rod, the electrode rod can be cooled and moisture as a decomposition substance of the gas to be treated can be supplied into the furnace. it can.

以下、本発明の製鋼用電気炉を用いた被処理ガスの無害化処理方法の実施の形態を、図面に基づいて説明する。   Embodiments of a detoxification method for a gas to be processed using the electric furnace for steel making according to the present invention will be described below with reference to the drawings.

図1〜図4に、本発明の製鋼用電気炉を用いた被処理ガスの無害化処理方法の一実施例を示す。   1 to 4 show an embodiment of a method for detoxifying a gas to be processed using the electric furnace for steel making of the present invention.

この製鋼用電気炉を用いた被処理ガスの無害化処理方法は、被処理ガスとしてのフロンガスを製鋼用電気炉1に導入し、製鋼を行う際にアーク12により形成される高温雰囲気中でフロンガスを分解するものであり、前記製鋼用電気炉1に配設した酸素バーナー2に酸素ガスとフロンガスを選択的に導入し、電気炉内が所定温度、具体的には、被処理ガスの分解温度以下の場合に酸素ガスを供給して補助加熱を行い、電気炉内が所定温度、具体的には、被処理ガスの分解温度を越える場合に前記酸素ガスの供給を停止してフロンガスを供給するようにしている。 The detoxification treatment method of the gas to be treated using the electric furnace for steelmaking introduces chlorofluorocarbon in the high-temperature atmosphere formed by the arc 12 when the chlorofluorocarbon gas as the gas to be treated is introduced into the electric furnace 1 for steelmaking. And oxygen gas and chlorofluorocarbon gas are selectively introduced into the oxygen burner 2 disposed in the steelmaking electric furnace 1, and the electric furnace has a predetermined temperature , specifically, the decomposition temperature of the gas to be treated. In the following cases, oxygen gas is supplied and auxiliary heating is performed. When the inside of the electric furnace exceeds a predetermined temperature , specifically, the decomposition temperature of the gas to be processed, the supply of the oxygen gas is stopped and the chlorofluorocarbon gas is supplied. I am doing so.

フロンガスの無害化処理を行う設備は、基本的には既存の製鋼設備をそのまま利用したものであり、製鋼を行う際に、電気炉1の電極棒11の先端から発生するアーク12は、通常、5000〜6000℃という高温に達しており、このアーク12により形成される溶鋼13付近の略1600℃の高温雰囲気中で、フロンガスを分解するようにしている。   The facility that performs the detoxification treatment of the chlorofluorocarbon gas is basically an existing steel making facility, and the arc 12 generated from the tip of the electrode rod 11 of the electric furnace 1 is usually used when making steel. The high temperature reaches 5000 to 6000 ° C., and the CFC gas is decomposed in a high temperature atmosphere of about 1600 ° C. near the molten steel 13 formed by the arc 12.

分解に供するフロンガスは、冷蔵庫、エアコン等の民生用機器や半導体の製造装置等の産業用機器に冷媒や洗浄剤として使用され、不要となって回収されたフロンガスであり、具体的には、特定フロンといわれる、フロン11(CClF)、フロン12(CCl)、フロン113(CCl)、フロン22(CHClF)等のオゾン層を破壊するフロンガスが対象となる。 Fluorocarbons used for decomposition are chlorofluorocarbons that are used as refrigerants and cleaning agents in consumer equipment such as refrigerators and air conditioners, and industrial equipment such as semiconductor manufacturing equipment. Freon gas that destroys the ozone layer such as Freon 11 (CCl 3 F), Freon 12 (CCl 2 F 2 ), Freon 113 (C 2 Cl 3 F 3 ), and Freon 22 (CHClF 2 ), which is called Freon, is targeted. .

一方、酸素バーナー2は、図3に示すように、補助加熱装置として製鋼用電気炉1を等分するように3基設けられている。
各酸素バーナー2は、図2に示すように、燃料噴射ノズル21と、該燃料噴射ノズル21の液体燃料を霧状にするための圧搾空気噴射ノズル22と、火力調節用の酸素噴射ノズル23とを備え、酸素噴射ノズル23の先端部には、供給された酸素ガスに旋回流を付与して噴射する旋回流リブ24が形成されている。
また、酸素バーナー2の外周部には水冷ジャケット25が設けられており、給水口25aから供給された冷却水が内部を循環して排水口25bから排出されることにより、酸素バーナー2を冷却することができる。
On the other hand, as shown in FIG. 3, three oxygen burners 2 are provided so as to equally divide the steelmaking electric furnace 1 as an auxiliary heating device.
As shown in FIG. 2, each oxygen burner 2 includes a fuel injection nozzle 21, a compressed air injection nozzle 22 for atomizing the liquid fuel in the fuel injection nozzle 21, and an oxygen injection nozzle 23 for adjusting the thermal power. And a swirl flow rib 24 is formed at the tip of the oxygen injection nozzle 23 to impart a swirl flow to the supplied oxygen gas.
Further, a water cooling jacket 25 is provided on the outer peripheral portion of the oxygen burner 2, and the cooling water supplied from the water supply port 25a circulates inside and is discharged from the drain port 25b, thereby cooling the oxygen burner 2. be able to.

フロンガスは、図1に示すように、ガスボンベ3から導管31を介し、前記した3基のうちの1基の酸素バーナー2’の圧搾空気噴射ノズル22に導入されている。
これにより、圧搾空気噴射ノズル22には、圧搾空気とフロンガスとが、制御用電磁弁32の切替によって選択的に供給されるようになっている。
また、フロンガスは、圧搾空気噴射ノズル22の代わりに酸素噴射ノズル23に導入することも可能であり、この場合は、酸素ガスとフロンガスが、この酸素噴射ノズル23に制御用電磁弁32によって選択的に供給される。
ところで、フロンガスは、図4に示すように、炉内が分解温度以上であるときに供給することが好ましいが、逆に、酸素バーナー2は、通電初期や溶鋼材料の追装時など、炉内が分解温度に満たないときに補助加熱運転を行い、炉内が分解温度以上に上昇したときには運転を停止する。
本発明は、この酸素バーナー2の運転のタイミングを利用するもので、炉内温度が上昇したときに停止する酸素バーナー2からフロンガスを炉内に供給することにより、従来のフロンガス用ノズルやその冷却設備を不要としながら、フロンガスを高温の溶鋼13付近に導入するとともに、供給されるフロンガスによって酸素バーナー2を清掃し煤塵の滞留を防止することができる。
As shown in FIG. 1, the chlorofluorocarbon gas is introduced from a gas cylinder 3 through a conduit 31 into a compressed air injection nozzle 22 of one of the three oxygen burners 2 ′.
Thereby, the compressed air and the chlorofluorocarbon gas are selectively supplied to the compressed air injection nozzle 22 by switching the control solenoid valve 32.
Further, the chlorofluorocarbon gas can be introduced into the oxygen injection nozzle 23 instead of the compressed air injection nozzle 22. In this case, the oxygen gas and the chlorofluorocarbon gas are selectively supplied to the oxygen injection nozzle 23 by the control solenoid valve 32. To be supplied.
By the way, as shown in FIG. 4, it is preferable to supply the chlorofluorocarbon gas when the inside of the furnace is at or above the decomposition temperature, but conversely, the oxygen burner 2 is used in the furnace at the beginning of energization or during the addition of molten steel material. When the temperature is below the decomposition temperature, auxiliary heating operation is performed, and when the inside of the furnace rises above the decomposition temperature, the operation is stopped.
The present invention uses the operation timing of the oxygen burner 2, and by supplying flon gas into the furnace from the oxygen burner 2 that stops when the furnace temperature rises, the conventional flon gas nozzle and its cooling While eliminating the need for equipment, it is possible to introduce chlorofluorocarbon gas into the vicinity of the high-temperature molten steel 13 and to clean the oxygen burner 2 with the chlorofluorocarbon gas supplied to prevent dust from staying.

一方、フロンガスの分解物質となる水分(HO)は、図3(a)に示すように、水流量計を備えた水供給装置14から、製鋼用電気炉1の電極棒11の外周面を伝わせて炉内に供給されており、これにより、電極棒11の冷却を行うとともに、フロンガスの分解物質となる水分を炉内に供給するようにしている。
製鋼用電気炉1に導入されたフロンガス及び水分(HO)等の分解物質からなる混合ガスは、溶鋼13付近の略1600℃の高温雰囲気中で、炭酸ガス(CO)、塩化水素(HCl)及びフッ化水素(HF)に分解され、製鋼用電気炉1から排出される。
On the other hand, as shown in FIG. 3A, moisture (H 2 O), which is a decomposed substance of chlorofluorocarbon gas, flows from the water supply device 14 equipped with a water flow meter to the outer peripheral surface of the electrode rod 11 of the steelmaking electric furnace 1. In this way, the electrode rod 11 is cooled, and moisture as a decomposing substance of CFC gas is supplied into the furnace.
A mixed gas composed of a decomposition material such as chlorofluorocarbon gas and moisture (H 2 O) introduced into the steelmaking electric furnace 1 is carbon dioxide (CO 2 ), hydrogen chloride ( HCl) and hydrogen fluoride (HF) and discharged from the steelmaking electric furnace 1.

この排気ガスは、図1に示すように、必要に応じて燃焼塔4に導入され、燃焼塔4を、例えば、800〜1200℃程度の温度に保持することにより、未分解のフロンガスを確実に分解するようにする。
フロンガスの分解で生じた、炭酸ガス(CO)、塩化水素(HCl)及びフッ化水素(HF)からなる分解ガスは、分解ガスに含まれる粉塵をバグフィルタ5において分離した後、スプレータワー6を通過することにより冷却される。
このスプレータワー6においては、苛性ソーダ水溶液をスプレーすることにより、分解ガスと反応させ、有害な塩化水素(HCl)及びフッ化水素(HF)を中和して塩化ナトリウム(NaCl)及びフッ化ソーダ(NaF)にする。
As shown in FIG. 1, this exhaust gas is introduced into the combustion tower 4 as necessary, and the combustion tower 4 is maintained at a temperature of, for example, about 800 to 1200 ° C., so that undecomposed chlorofluorocarbon gas is surely obtained. Try to disassemble.
The cracked gas composed of carbon dioxide (CO 2 ), hydrogen chloride (HCl), and hydrogen fluoride (HF) generated by the decomposition of the freon gas is separated from the dust contained in the cracked gas by the bag filter 5 and then spray tower 6 It is cooled by passing through.
In this spray tower 6, by spraying an aqueous solution of caustic soda, it reacts with the cracked gas, neutralizes harmful hydrogen chloride (HCl) and hydrogen fluoride (HF), and sodium chloride (NaCl) and sodium fluoride ( NaF).

スプレータワー6からの排気は、建屋ファン7及び建屋バグフィルタ8を介して、液体及び固体成分を完全に除去した後、大気中へ放出される。
一方、スプレータワー6からの廃液は、排水口から水処理槽61に導入し、水処理槽61で消石灰(Ca(OH))を添加してフッ化カルシウム(CaF)として沈殿、分離する。
この最終生成物のフッ化カルシウム(CaF)は、製鋼の際に用いる脱硫剤として有効利用することができ、これにより、廃棄物の量を低減することができる。
Exhaust air from the spray tower 6 is discharged into the atmosphere after completely removing liquid and solid components through the building fan 7 and the building bag filter 8.
On the other hand, the waste liquid from the spray tower 6 is introduced into the water treatment tank 61 from the drain outlet, and slaked lime (Ca (OH) 2 ) is added in the water treatment tank 61 to precipitate and separate as calcium fluoride (CaF 2 ). .
This final product, calcium fluoride (CaF 2 ), can be effectively used as a desulfurization agent used in steelmaking, and thus the amount of waste can be reduced.

なお、本発明の製鋼用電気炉を用いたフロンガスの無害化処理方法を、フロン12(CCl)及びフロン113(CCl)を例にして示すと次のとおりとなる。 It is to be noted that the detoxification treatment method for chlorofluorocarbon using the electric furnace for steel making of the present invention is as follows, using chlorofluorocarbon 12 (CCl 2 F 2 ) and chlorofluorocarbon 113 (C 2 Cl 3 F 3 ) as examples. .

(1)フロン12(CCl)及びフロン113(CCl)並びに分解物質としての水分(HO)及び酸素ガス(O)からなる混合ガスは、製鋼用電気炉1に導入され、製鋼を行う際にアーク12により形成される高温雰囲気中で分解されて、炭酸ガス(CO)、塩化水素(HCl)及びフッ化水素(HF)になる。
CCl+2HO→CO+2HCl+2HF
2CCl+6HO+O→4CO+6HCl+6HF
(1) A mixed gas composed of Freon 12 (CCl 2 F 2 ) and Freon 113 (C 2 Cl 3 F 3 ) and moisture (H 2 O) and oxygen gas (O 2 ) as decomposition substances is used in an electric furnace for steelmaking. 1 is decomposed in a high-temperature atmosphere formed by the arc 12 when steelmaking, and becomes carbon dioxide (CO 2 ), hydrogen chloride (HCl), and hydrogen fluoride (HF).
CCl 2 F 2 + 2H 2 O → CO 2 + 2HCl + 2HF
2C 2 Cl 3 F 3 + 6H 2 O + O 2 → 4CO 2 + 6HCl + 6HF

(2)塩化水素(HCl)は、スプレータワー7において、苛性ソーダ水溶液をスプレーされることにより、中和されて塩化ナトリウム(NaCl)となる。
HCl+NaOH→NaCl+H
(2) Hydrogen chloride (HCl) is neutralized into sodium chloride (NaCl) by spraying a caustic soda aqueous solution in the spray tower 7.
HCl + NaOH → NaCl + H 2 O

(3)フッ化水素(HF)は、スプレータワー7において、苛性ソーダ水溶液をスプレーされることにより、中和されてフッ化ソーダ(NaF)となり、さらに、水処理槽で消石灰(Ca(OH))を添加されてフッ化カルシウム(CaF)として沈殿、分離される。
HF+NaOH→NaF+H
2NaF+Ca(OH)→CaF+2NaOH
(NaF+Ca(OH)+HSO→CaF+NaSO+HO)
(3) Hydrogen fluoride (HF) is neutralized to become sodium fluoride (NaF) by spraying a caustic soda aqueous solution in the spray tower 7, and further slaked lime (Ca (OH) 2 in a water treatment tank). ) Is added and precipitated and separated as calcium fluoride (CaF 2 ).
HF + NaOH → NaF + H 2 O
2NaF + Ca (OH) 2 → CaF 2 + 2NaOH
(NaF + Ca (OH) 2 + H 2 SO 4 → CaF 2 + Na 2 SO 4 + H 2 O)

かくして、本実施例の製鋼用電気炉を用いた被処理ガスの無害化処理方法は、被処理ガスとしてのフロンガスを製鋼用電気炉1に導入し、製鋼を行う際にアーク12により形成される高温雰囲気中でフロンガスを分解するフロンガスの無害化処理方法において、前記製鋼用電気炉1に配設した酸素バーナー2に酸素ガスとフロンガスを選択的に導入し、電気炉内が所定温度以下の場合に酸素ガスを供給して補助加熱を行い、電気炉内が所定温度を越える場合に前記酸素ガスの供給を停止してフロンガスを供給することから、炉内温度が上昇した段階で停止する酸素バーナー2を利用してフロンガスを炉内に供給することができ、これにより、従来のフロンガス用ノズルやその冷却設備を不要としながら、フロンガスを高温の溶鋼13付近に導入するとともに、供給されるフロンガスによって酸素バーナー2を清掃し煤塵の滞留を防止することができる。
この場合、電極棒11の外周面を伝わせて製鋼用電気炉1内に水を供給することにより、電極棒11の冷却を行うとともに、フロンガスの分解物質となる水分を炉内に供給することができる。
Thus, the detoxification method of the gas to be treated using the steelmaking electric furnace of the present embodiment is formed by the arc 12 when the freon gas as the gas to be treated is introduced into the steelmaking electric furnace 1 and steelmaking is performed. In the detoxification treatment method for CFCs that decomposes CFCs in a high-temperature atmosphere, oxygen gas and CFCs are selectively introduced into an oxygen burner 2 disposed in the steelmaking electric furnace 1, and the temperature in the electric furnace is below a predetermined temperature. Oxygen gas is supplied to the auxiliary heater, and when the inside of the electric furnace exceeds a predetermined temperature, the supply of the oxygen gas is stopped and the chlorofluorocarbon gas is supplied. Therefore, the oxygen burner is stopped when the temperature in the furnace rises. 2 can be used to supply chlorofluorocarbon gas into the furnace. This eliminates the need for conventional chlorofluorocarbon gas nozzles and cooling equipment, and introduces chlorofluorocarbon gas to the vicinity of the hot molten steel 13. As well as, it is possible to clean the oxygen burner 2 by chlorofluorocarbons supplied to prevent the accumulation of dust.
In this case, the electrode rod 11 is cooled by supplying water into the steelmaking electric furnace 1 along the outer peripheral surface of the electrode rod 11, and moisture serving as a decomposing substance of chlorofluorocarbon gas is supplied into the furnace. Can do.

以上、本発明の製鋼用電気炉を用いた被処理ガスの無害化処理方法について、フロンガスを処理する場合について説明したが、本発明は上記実施例に記載した構成に限定されるものではなく、また、被処理ガスの対象もフロンガス等のHFC化合物のほか、ハロンガス等の化合物にも適用できる等、その趣旨を逸脱しない範囲において適宜その構成を変更することができるものである。   As described above, the detoxification treatment method for the gas to be treated using the electric furnace for steel making according to the present invention has been described for the case of treating flon gas, but the present invention is not limited to the configuration described in the above embodiment, In addition, the configuration of the gas to be treated can be changed as appropriate without departing from the scope of the present invention, for example, applicable to not only HFC compounds such as chlorofluorocarbon gas but also compounds such as halon gas.

本発明の製鋼用電気炉を用いた被処理ガスの無害化処理方法は、炉内温度が上昇した段階で停止する補助加熱装置を利用して被処理ガスを炉内に供給することができ、従来の被処理ガス用ノズルやその冷却設備を不要としながら、被処理ガスを高温の溶鋼付近に導入するとともに、供給される被処理ガスによって補助加熱装置を清掃し煤塵の滞留を防止するという特性を有していることから、既存の製鋼用電気炉を利用して被処理ガスを低コストで安全に無害化処理する用途に好適に用いることができる。   The process gas detoxification method using the electric furnace for steel making of the present invention can supply the process gas into the furnace using an auxiliary heating device that stops when the furnace temperature rises, The characteristic of introducing the gas to be treated in the vicinity of high-temperature molten steel while cleaning the auxiliary heating device with the gas to be treated to prevent the accumulation of soot and dust while eliminating the need for the conventional gas to be treated and its cooling equipment Therefore, it can be suitably used for the purpose of safely detoxifying the gas to be treated at low cost using an existing electric furnace for steelmaking.

本発明の製鋼用電気炉を用いた被処理ガスの無害化処理方法を実施するために用いる設備の一例を示す説明図である。It is explanatory drawing which shows an example of the equipment used in order to implement the detoxification processing method of the to-be-processed gas using the electric furnace for steelmaking of this invention. 酸素バーナーを示し、(a)はその断面図、(b)は背面図である。An oxygen burner is shown, (a) is a sectional view thereof, and (b) is a rear view. 製鋼用電気炉を示し、(a)はその縦断面図、(b)は横断面図である。An electric furnace for steel making is shown, (a) is a longitudinal sectional view thereof, and (b) is a transverse sectional view thereof. 酸素バーナーの補助加熱運転と被処理ガスとしてのフロンガスの供給のタイミングを示す説明図である。It is explanatory drawing which shows the timing of the auxiliary | assistant heating operation of an oxygen burner, and the supply of the fluorocarbon gas as to-be-processed gas.

1 製鋼用電気炉
11 電極棒
12 アーク
13 溶鋼
14 水供給装置
2 酸素バーナー(補助加熱装置)
21 燃料噴射ノズル
22 圧搾空気噴射ノズル
23 酸素噴射ノズル
24 旋回流リブ
25 水冷ジャケット
3 ガスボンベ
31 導管
32 制御用電磁弁
4 燃焼塔
5 バグフィルタ
6 スプレータワー
61 水処理槽
7 建屋ファン
8 建屋バグフィルタ
DESCRIPTION OF SYMBOLS 1 Electric furnace for steel making 11 Electrode rod 12 Arc 13 Molten steel 14 Water supply apparatus 2 Oxygen burner (auxiliary heating apparatus)
DESCRIPTION OF SYMBOLS 21 Fuel injection nozzle 22 Compressed air injection nozzle 23 Oxygen injection nozzle 24 Swirling flow rib 25 Water cooling jacket 3 Gas cylinder 31 Conduit 32 Control solenoid valve 4 Combustion tower 5 Bag filter 6 Spray tower 61 Water treatment tank 7 Building fan 8 Building bug filter

Claims (2)

被処理ガスを製鋼用電気炉に導入し、製鋼を行う際にアークにより形成される高温雰囲気中で被処理ガスを分解する製鋼用電気炉を用いた被処理ガスの無害化処理方法において、前記製鋼用電気炉に配設した補助加熱装置に酸素ガスと被処理ガスを選択的に導入し、電気炉内が被処理ガスの分解温度以下の場合に酸素ガスを供給して補助加熱を行い、電気炉内が被処理ガスの分解温度を越える場合に前記酸素ガスの供給を停止して被処理ガスを供給することを特徴とする製鋼用電気炉を用いた被処理ガスの無害化処理方法。 In the detoxification treatment method of a gas to be treated using an electric furnace for steel making, wherein the gas to be treated is introduced into an electric furnace for steel making and the gas to be treated is decomposed in a high temperature atmosphere formed by an arc when steel making is performed, Oxygen gas and gas to be treated are selectively introduced into an auxiliary heating device disposed in an electric furnace for steel making, and when the inside of the electric furnace is below the decomposition temperature of the gas to be treated , oxygen gas is supplied and auxiliary heating is performed. A process gas detoxification method using an electric furnace for steel making, characterized in that when the inside of an electric furnace exceeds a decomposition temperature of the process gas, the supply of the oxygen gas is stopped and the process gas is supplied. 電極棒の外周面を伝わせて製鋼用電気炉内に水を供給することを特徴とする請求項1記載の製鋼用電気炉を用いた被処理ガスの無害化処理方法。   The method for detoxifying a gas to be treated using an electric furnace for steelmaking according to claim 1, wherein water is supplied into the electric furnace for steelmaking along the outer peripheral surface of the electrode rod.
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