JPS6134488B2 - - Google Patents
Info
- Publication number
- JPS6134488B2 JPS6134488B2 JP9752582A JP9752582A JPS6134488B2 JP S6134488 B2 JPS6134488 B2 JP S6134488B2 JP 9752582 A JP9752582 A JP 9752582A JP 9752582 A JP9752582 A JP 9752582A JP S6134488 B2 JPS6134488 B2 JP S6134488B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- plate
- magnesium
- furnace shell
- partition plate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 53
- 229910052749 magnesium Inorganic materials 0.000 claims description 51
- 239000011777 magnesium Substances 0.000 claims description 51
- 238000005192 partition Methods 0.000 claims description 35
- 229910052751 metal Inorganic materials 0.000 claims description 23
- 239000002184 metal Substances 0.000 claims description 23
- 239000011261 inert gas Substances 0.000 claims description 18
- 238000004519 manufacturing process Methods 0.000 claims description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 9
- 229910052799 carbon Inorganic materials 0.000 claims description 7
- 239000000395 magnesium oxide Substances 0.000 claims description 6
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 6
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 4
- 239000003638 chemical reducing agent Substances 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 239000010425 asbestos Substances 0.000 claims description 2
- 210000003298 dental enamel Anatomy 0.000 claims description 2
- 229910002804 graphite Inorganic materials 0.000 claims description 2
- 239000010439 graphite Substances 0.000 claims description 2
- 238000002844 melting Methods 0.000 claims description 2
- 230000008018 melting Effects 0.000 claims description 2
- 239000011226 reinforced ceramic Substances 0.000 claims description 2
- 229910052895 riebeckite Inorganic materials 0.000 claims description 2
- 239000011810 insulating material Substances 0.000 description 10
- 239000002994 raw material Substances 0.000 description 10
- 229910000831 Steel Inorganic materials 0.000 description 9
- 239000010959 steel Substances 0.000 description 9
- 239000011449 brick Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 239000002893 slag Substances 0.000 description 5
- 230000005494 condensation Effects 0.000 description 4
- 238000009833 condensation Methods 0.000 description 4
- 230000006866 deterioration Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000009413 insulation Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000011819 refractory material Substances 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- 229910000519 Ferrosilicon Inorganic materials 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000010459 dolomite Substances 0.000 description 2
- 229910000514 dolomite Inorganic materials 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 239000001095 magnesium carbonate Substances 0.000 description 2
- 235000014380 magnesium carbonate Nutrition 0.000 description 2
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 2
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 2
- 241000272201 Columbiformes Species 0.000 description 1
- 229910001111 Fine metal Inorganic materials 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910021383 artificial graphite Inorganic materials 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
【発明の詳細な説明】
本発明は、金属マグネシウム製造装置に関し、
特に本発明は、密閉式電気炉を含む金属マグネシ
ウム製造装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a metal magnesium manufacturing apparatus,
In particular, the present invention relates to a metal magnesium manufacturing apparatus including a closed electric furnace.
酸化マグネシウム含有物質を溶融スラグ存在下
で還元剤と反応させ減圧下でマグネシウムを製造
する電熱高温還元法によるマグネシウムの製造方
法は既に工業的に実施されており、この方法は他
の方法例えばピジヨン法に比較して高能率な方法
である。 A method for producing magnesium by an electrothermal high-temperature reduction method, in which a substance containing magnesium oxide is reacted with a reducing agent in the presence of molten slag to produce magnesium under reduced pressure, has already been carried out industrially, and this method is similar to other methods such as the Pigeon method. This is a highly efficient method compared to the previous method.
前記電熱高温還元法においては従来密閉式単相
ジロー炉が用いられているが、本発明者らは、密
閉式三相交流浸漬アーク式密閉電気炉を用いるこ
とによる金属マグネシウム製造装置を新規に知見
して特願昭57−69535号により提案した。 In the electrothermal high-temperature reduction method, a closed single-phase Giraud furnace has conventionally been used, but the present inventors have discovered a new metal magnesium production apparatus using a closed three-phase AC immersion arc closed electric furnace. This was proposed in Japanese Patent Application No. 57-69535.
ところで、単相ジロー炉あるいは本発明者らが
提案した製造装置に係る3相電気炉を用いて電熱
高温還元を行なう際、炉内で発生するマグネシウ
ム蒸気が凝縮器へ吸引されると共に、その一部は
電気炉内炉蓋、炉壁ならびに炉床のライニング内
に滲透して次第に蓄積して、ライニングの断熱性
が劣化し、放熱が増大して電力単位が悪くなると
いう現象があつた。 By the way, when electrothermal high-temperature reduction is performed using a single-phase Giraud furnace or a three-phase electric furnace according to the manufacturing apparatus proposed by the present inventors, the magnesium vapor generated in the furnace is sucked into the condenser, and one of the This caused the phenomenon that the heat seeped into the lining of the lid, furnace wall, and hearth in the electric furnace and gradually accumulated, resulting in deterioration of the insulation properties of the lining, increased heat dissipation, and poor power consumption.
本発明は、前記電気炉ライニング内にマグネシ
ウム蒸気が滲透することによる電力原単位の悪化
を防止することのできる電気炉を含む金属マグネ
シウム製造装置を提供することを目的とするもの
であり、特許請求の範囲記載の装置を提供するこ
とによつて前記目的を達成することができる。 An object of the present invention is to provide a metal magnesium manufacturing apparatus including an electric furnace that can prevent deterioration of power consumption rate due to permeation of magnesium vapor into the electric furnace lining. The above objects can be achieved by providing an apparatus according to the scope of the invention.
次に本発明を詳細に説明する。 Next, the present invention will be explained in detail.
特願昭57−69535号により本発明者らが提案し
た金属マグネシウム製造装置に含まれる前記電気
炉は三相交流浸漬アーク式減圧自在の密閉式電気
炉であり;
この電気炉の炉蓋を貫通して3本の電極が炉内
に垂下しており;
前記電極はそれぞれ上部は金属製水冷導管部、
下部は人造黒鉛質部よりなり;
前記電極は電気炉の炉蓋に設けられた貫通孔内
を上下方向に移動自在であり;
前記炉蓋貫通孔を囲繞して炉蓋上に凸設された
炉内への外気侵入防止ならびに電極の上下移動の
際に横振れ防止用筒状体と前記電極の上部金属製
水冷導管部との間には耐熱性パツキングが介装さ
れており;
前記筒状体と電極との隙間には不活性ガスを導
入する導入管が筒状体に連結されている;
ことを特徴とする密閉式電気炉である。 The electric furnace included in the metal magnesium manufacturing apparatus proposed by the present inventors in Japanese Patent Application No. 57-69535 is a three-phase AC immersion arc closed type electric furnace that can freely decompress; three electrodes are suspended in the furnace;
The lower part is made of artificial graphite; the electrode is vertically movable within a through hole provided in the lid of the electric furnace; A heat-resistant packing is interposed between the cylindrical body for preventing outside air from entering the furnace and for preventing lateral vibration during vertical movement of the electrode and the upper metal water-cooling conduit portion of the electrode; This closed electric furnace is characterized in that an inlet pipe for introducing an inert gas is connected to the cylindrical body in the gap between the body and the electrode.
この電気炉のライニング構造は第1図に示す如
く、鋼板製炉殻1の底板上には断熱材が敷設され
ており、その上には耐火断熱煉瓦2、さらにその
上には耐火煉瓦3が築造されており、溶湯と直接
接触する部分にはカーボンブロツク4が内張りさ
れている。また炉殻1の内側面に接して耐熱材2
が、さらにその内側の溶湯接触部にはカーボンブ
ロツク4が、上記溶湯接触部上方は耐火煉瓦3が
内張されている。炉蓋は耐火キヤスタブル煉瓦3
をもつて構築されている。 As shown in Fig. 1, the lining structure of this electric furnace is such that a heat insulating material is laid on the bottom plate of a steel plate furnace shell 1, a fireproof insulation brick 2 is placed on top of the heat insulating material, and a fireproof brick 3 is placed on top of that. The parts that come into direct contact with the molten metal are lined with carbon blocks 4. In addition, a heat-resistant material 2 is placed in contact with the inner surface of the furnace shell 1.
However, a carbon block 4 is lined inside the molten metal contact area, and a refractory brick 3 is lined above the molten metal contact area. The furnace lid is made of refractory castable bricks 3
It is built with.
この電気炉を用いて金属マグネシウムを製造す
るとき、操業日数の経過に伴つて炉殻の表面温度
が第2図に示す如く急激に上昇することが判つ
た。本発明者らはこの原因を解明すべく、炉体を
解体して調べたところ、炉体ライニング内の各所
にマグネシウムが凝縮して蓄積されていることを
知見し、かかる蓄積によりライニングの断熱性す
なわち保温性が劣化した結果、炉殻の表面温度が
次第に上昇するに至つたものでありることが判明
した。 It has been found that when producing metallic magnesium using this electric furnace, the surface temperature of the furnace shell rises rapidly as the number of operating days passes, as shown in FIG. In order to elucidate the cause of this, the inventors dismantled the furnace body and investigated it, and found that magnesium was condensed and accumulated in various places within the furnace lining. In other words, it was found that the surface temperature of the furnace shell gradually increased as a result of the deterioration of heat retention.
よつて本発明者らは、第3図に示すように炉体
ライニング層の中間にマグネシウム蒸気が滲透し
ないような耐熱性の隔壁板を設けて、炉内で発生
するマグネシウム蒸気のライニング中への滲透を
隔壁板によつて防止して、外部ライニング層にマ
グネシウム蒸気が滲透しないようにした結果、第
4図に示すように操業経過日数に伴つて炉殻の表
面温度の上昇が比較的緩やかになることが判つた
が、なお十分に炉殻の表面温度の上昇ならびに電
力原単位の上昇を抑制することはできなかつた。
すなわちこの場合においても、炉解体の結果、マ
グネシウムの凝縮、蓄積が隔壁板の外周辺に存在
することが判つた。 Therefore, as shown in Figure 3, the present inventors installed a heat-resistant partition plate in the middle of the furnace lining layer to prevent magnesium vapor from permeating, thereby preventing the magnesium vapor generated in the furnace from entering the lining. As a result of preventing magnesium vapor from seeping into the outer lining layer by preventing seepage with the partition plate, the rise in the surface temperature of the furnace shell becomes relatively gradual as the number of days of operation increases, as shown in Figure 4. However, it was not possible to sufficiently suppress the rise in the surface temperature of the furnace shell and the rise in the electric power consumption rate.
That is, in this case as well, as a result of the furnace dismantling, it was found that magnesium condensation and accumulation existed around the outside of the partition plate.
本発明者らは、前記隔壁板と炉殻との間に不活
性ガスを導入して、このガス圧を密閉式電気炉内
マグネシウム蒸気を含む雰囲気のガス圧を下廻ら
ない圧力とすることにより、マグネシウム蒸気が
隔壁板外周辺ならびに隔壁板外側部へ滲透するこ
とを防止することに想到した。但し上述の如く隔
壁板と炉殻との間の不活性ガス圧を炉内ガス圧よ
り下廻らないようにするためには、相当多量の不
活性ガスを使用しなければならず、かつこれら使
用された不活性ガスが炉内雰囲気中に流入して、
炉内マグネシウム蒸気の濃度を不必要に希薄にす
るに至つた。 The present inventors introduced an inert gas between the partition wall plate and the furnace shell, and set the gas pressure to a pressure that does not fall below the gas pressure of the atmosphere containing magnesium vapor in the closed electric furnace. The inventors have come up with the idea of preventing magnesium vapor from seeping into the outer periphery of the partition plate and the outer part of the partition plate. However, as mentioned above, in order to prevent the inert gas pressure between the bulkhead plate and the furnace shell from falling below the gas pressure in the furnace, it is necessary to use a considerable amount of inert gas, and the use of this gas is necessary. The inert gas that was removed flows into the furnace atmosphere,
This resulted in the concentration of magnesium vapor in the furnace being unnecessarily diluted.
よつて本発明者らは炉殻とこれに対峙する隔壁
板とを1乃至2以上のブロツクに区劃し、各ブロ
ツクに対応する炉殻と隔壁板との間をライニング
を含めて密封し、これら各ブロツク毎に不活性ガ
ス導入管を設けて不活性ガスを導入したところ、
導入されたガスは各ブロツク内に停滞しており、
炉内雰囲気中への漏入を完全に、あるいはほゞ完
全に防止することができることを知見して本発明
を完成した。 Therefore, the present inventors divided the furnace shell and the partition plate facing it into one or more blocks, sealed the space between the furnace shell and the partition plate corresponding to each block including the lining, When an inert gas introduction pipe was installed for each of these blocks and inert gas was introduced,
The introduced gas is stagnant within each block,
The present invention was completed based on the finding that leakage into the furnace atmosphere can be completely or almost completely prevented.
次に本発明を図面について説明する。 Next, the present invention will be explained with reference to the drawings.
第3図において、電気炉は炉殻1が鋼板製で、
前記鋼板製炉殻の底板上には断熱材が敷設されて
おり、その上には耐火断熱煉瓦2、さらにその上
には耐火煉瓦3が築造されており、溶湯と直接接
触する部分にはカーボンブロツク4が内張りされ
ている。また炉殻の側壁板の内側面に接して断熱
材2が、さらにその内側に耐火煉瓦3が内張りさ
れており、その内側にマグネシウム不滲透性隔壁
板6が設けられており、さらにその内側には下部
の溶湯接触部にはカーボンブロツク4が、上部に
は耐火煉瓦が内張りされている。炉蓋は鋼板製炉
殻の内側がキヤスタブル耐火物3で内張りされて
おり、該内張り層のほぼ中間にマグネシウム不滲
透性隔壁板6が設けられている。 In Fig. 3, the electric furnace has a furnace shell 1 made of steel plate,
A heat insulating material is laid on the bottom plate of the steel plate furnace shell, on top of which a fireproof insulation brick 2 is built, and further above that a fireproof brick 3 is built, and the part that comes into direct contact with the molten metal is covered with carbon. Block 4 is lined. In addition, a heat insulating material 2 is provided in contact with the inner surface of the side wall plate of the furnace shell, and a refractory brick 3 is lined inside the heat insulating material 2, and a magnesium impermeable bulkhead plate 6 is provided on the inner side of the heat insulating material 2. The lower molten metal contact area is lined with carbon block 4, and the upper part is lined with refractory bricks. The furnace cover has a steel plate furnace shell lined with a castable refractory material 3, and a magnesium-impermeable partition plate 6 is provided approximately in the middle of the lining layer.
第5図において電気炉は炉殻1が鋼板製で、前
記鋼板製炉殻の底板ならびに側壁板の内側面に接
して耐火断熱材2が内張りされており、その内側
面に接してマグネシウム蒸気不滲透性隔壁板6が
設けられ、前記隔壁板と炉殻との間は炉底部分と
炉側壁部分に分けて密封してある。さらに前記隔
壁板6の内側に耐火材3が築造されており、溶湯
と直接接触する部分にはカーボンブロツク4が内
張りされている。また、前記鋼板製炉殻1の炉蓋
の内側面に接して耐火材3が内張りされており、
その内側にマグネシウム蒸気不滲透性隔壁板6が
設けられ、前記隔壁板と前記炉蓋の炉殻との間は
密封されている。さらに前記隔壁板の内側には耐
火材3が内張りされている。 In FIG. 5, the electric furnace has a furnace shell 1 made of a steel plate, and a refractory heat insulating material 2 is lined in contact with the inner surfaces of the bottom plate and side wall plates of the steel plate furnace shell, and a magnesium vapor insulating material 2 is lined with the inner surface of the steel plate furnace shell. A permeable partition plate 6 is provided, and the space between the partition plate and the furnace shell is sealed separately into a furnace bottom portion and a furnace side wall portion. Further, a refractory material 3 is built inside the partition plate 6, and a carbon block 4 is lined in the portion that comes into direct contact with the molten metal. Further, a refractory material 3 is lined with a refractory material 3 in contact with the inner surface of the furnace lid of the steel plate furnace shell 1,
A magnesium vapor-impermeable partition plate 6 is provided inside thereof, and the space between the partition plate and the furnace shell of the furnace lid is sealed. Further, the inside of the partition plate is lined with a fireproof material 3.
前記炉殻1には、炉殻と隔壁板との間の密封さ
れている部分に不活性ガス導入するための不活性
ガス導入用管7が、炉蓋、炉側壁および炉底にそ
れぞれ配設されている。 In the furnace shell 1, inert gas introduction pipes 7 for introducing inert gas into the sealed portion between the furnace shell and the partition plate are arranged at the furnace lid, furnace side wall, and furnace bottom, respectively. has been done.
前記隔壁板6は主として金属板が使われるが、
ほかに緻密質な隔壁板としてはマグネシウム蒸気
不滲透性のものであれば良く、緻密質アスベスト
板、ホウロウ板、不滲透性黒鉛板、繊維強化セラ
ミツクス板など、通気度の小さいものが使用でき
る。 The partition wall plate 6 is mainly a metal plate, but
In addition, the dense partition wall board may be made of magnesium vapor impermeable material, and materials with low air permeability such as dense asbestos board, enamel board, impermeable graphite board, fiber-reinforced ceramic board, etc. can be used.
本発明において、前記隔壁板6を設けることに
より保温材中にマグネシウム蒸気が滲透して金属
マグネシウム微粉となつて析出し、保温性能の大
巾劣化をきたすことを防ぐことができる。また、
隔壁板6を鉄板などの金属板とし、前記隔壁板と
炉殻との間を密封することにより、1乃至2以上
のブロツクに区劃して気密室とし、該気密室内の
圧力を電気炉内、すなわち前記隔壁板内側の圧力
よりやす高目に保持しておくように不活性ガスを
前記不活性ガス導入用管7を用いて送気しておく
ことができる。これによつて、例えば長期間の操
業後隔壁板の一部が損傷するようなことがあつた
場合でも、保温層へのマグネシウム蒸気の拡散が
確実に防止され、また、前記気密室内の圧力をチ
エツクすることによつて隔壁板の損傷を確実に知
ることができる。さらに隔壁板の一部に損傷が生
じた場合でも不活性ガスを送入しておくことによ
つて保温材屑を保護できることを知見した。 In the present invention, by providing the partition plate 6, it is possible to prevent magnesium vapor from penetrating into the heat insulating material and precipitating as fine metal magnesium powder, which would cause a significant deterioration of the heat insulating performance. Also,
The partition plate 6 is made of a metal plate such as an iron plate, and the space between the partition plate and the furnace shell is sealed to form an airtight chamber divided into one or more blocks, and the pressure inside the airtight chamber is reduced to within the electric furnace. That is, the inert gas can be supplied using the inert gas introducing pipe 7 so as to keep the pressure higher than the pressure inside the partition plate. As a result, even if, for example, a part of the bulkhead plate is damaged after long-term operation, diffusion of magnesium vapor into the heat insulation layer can be reliably prevented, and the pressure inside the airtight chamber can be reduced. By checking, you can definitely know if the partition plate is damaged. Furthermore, it was discovered that even if a part of the partition plate is damaged, the heat insulating material waste can be protected by supplying inert gas.
本発明のマグネシウム製造用電気炉の保温性能
を保持することは、炉殻からの放熱を減少させ、
電力原単位を向上させることができ、さらに加え
て、電気炉の操業期間を大巾に延長させることが
わかつた。 Maintaining the heat retention performance of the electric furnace for magnesium production of the present invention reduces heat radiation from the furnace shell,
It was found that the electric power consumption rate could be improved and, in addition, the operating period of the electric furnace could be significantly extended.
次に本発明の金属マグネシウム製造装置を用い
て金属マグネシウムを製造する方法の一例につい
て説明し、電気炉のライニング構造による効果を
実施例で説明する。 Next, an example of a method for manufacturing metal magnesium using the metal magnesium manufacturing apparatus of the present invention will be explained, and the effects of the lining structure of the electric furnace will be explained in Examples.
原料は酸化マグネシウム含有物質として焼成ド
ロマイト(2CaO・MgO)と焼成マグネサイト
(MgO)を用い、還元剤としてフエロシリコンア
ルミニウム(Si=50,A=30,Fe=20)を用
いた。焼成ドロマイトと焼成マグネサイトを約3
対1の比率で混合し、該混合物100部に対しフエ
ロシリコンアルミニウムを20〜25部混合したもの
を原料とした。原料粒度は1〜15mm程度とした。 As raw materials, calcined dolomite (2CaO.MgO) and calcined magnesite (MgO) were used as magnesium oxide-containing substances, and ferrosilicon aluminum (Si = 50, A = 30, Fe = 20) was used as a reducing agent. About 3 pieces of calcined dolomite and calcined magnesite
The materials were mixed at a ratio of 1:1, and 20 to 25 parts of ferrosilicon aluminum was mixed with 100 parts of the mixture. The particle size of the raw material was approximately 1 to 15 mm.
100KVAの本発明に係る三相交流密閉式電気炉
により溶融還元を実施するに当り電気炉内を不活
性ガス雰囲気とし、前記原料を投入しながら通電
して原料を溶解した。つぎに、電気炉内の圧力を
30―50Terrの範囲内に減圧し、そのままに保つ
た。各電極の電力のバランスが良くなるように電
極を上下して調節する。電極の上下は各電極の負
荷に応じて自動調節又は手動で行なつた。 When melting and reduction was performed using a 100 KVA three-phase AC closed type electric furnace according to the present invention, the inside of the electric furnace was made into an inert gas atmosphere, and electricity was applied while the raw materials were introduced to melt the raw materials. Next, the pressure inside the electric furnace is
The pressure was reduced to within 30-50 Terr and maintained there. Adjust the electrodes by raising and lowering them so that the power of each electrode is well balanced. The electrodes were raised and lowered automatically or manually depending on the load on each electrode.
電力を65KWの負荷としたのち、前記原料を逐
次投入した。原料投入を開始すると、酸化マグネ
シウムが還元されて金属マグネシウムとなり、該
金属マグネシウムはマグネシウム蒸気となる。そ
のマグネシウム蒸気は電気炉のマグネシウム蒸気
排出口を通り、電気炉に接続されたマグネシウム
蒸気凝縮器に導入され、液体マグネシウムとして
集められた。 After setting the electric power to a load of 65 KW, the raw materials were sequentially introduced. When raw material input is started, magnesium oxide is reduced to metal magnesium, and the metal magnesium turns into magnesium vapor. The magnesium vapor passed through the magnesium vapor outlet of the electric furnace, was introduced into a magnesium vapor condenser connected to the electric furnace, and was collected as liquid magnesium.
操業中、溶湯温度は約1600℃を保つように、ま
た電気炉内の原料が完全に溶解するように、電極
先端位置、電圧を調節した。また炉蓋の電極貫通
孔や原料投入口から一定のガス流量で不活性ガス
を流し、該部分へのマグネシウム蒸気の凝縮によ
る閉塞や電気的トラブルを防止した。 During operation, the electrode tip position and voltage were adjusted to maintain the molten metal temperature at approximately 1,600°C and to ensure that the raw materials in the electric furnace were completely melted. In addition, inert gas was flowed at a constant gas flow rate from the electrode through holes in the furnace cover and the raw material inlet to prevent blockages and electrical troubles caused by condensation of magnesium vapor in these areas.
一定時間操業して、電気炉内にスラグおよび副
生メダルが、されにマグネシウム凝縮器に液体マ
グネシウムが一定量蓄積したとき、原料投入を一
時中断し、電気炉負荷を下げ、電気炉内の圧力を
不活性ガスで常圧に戻してから、電気炉のスラグ
排出口からスラグを排出し、マグネシウム凝縮器
から液体マグネシウムを取り出した。 After operating for a certain period of time, when slag and by-product medals accumulate in the electric furnace, and a certain amount of liquid magnesium accumulates in the magnesium condenser, raw material input is temporarily suspended, the electric furnace load is reduced, and the pressure inside the electric furnace is reduced. After returning to normal pressure with inert gas, the slag was discharged from the slag discharge port of the electric furnace, and liquid magnesium was taken out from the magnesium condenser.
この際電気炉を常圧に戻したとき、炉内粉塵排
出口から炉内ガスおよび粉塵を吸引し、原料投入
口や電極貫通部の閉塞、汚染を防止した。 At this time, when the electric furnace was returned to normal pressure, the furnace gas and dust were sucked through the furnace dust outlet to prevent clogging and contamination of the raw material input port and the electrode penetration part.
電気炉内のスラグおよび副生メタル、またはマ
グネシウム凝縮器の液体マグネシウムの排出が終
つたら、直ちに電気炉内の圧力を30―50Torrに
戻して操業を続けた。 As soon as the slag and by-product metal in the electric furnace or the liquid magnesium in the magnesium condenser was discharged, the pressure in the electric furnace was returned to 30-50 Torr and operation continued.
上記の如き操業を続た結果、従来のライニング
構造(第1図)による電気炉では、第2図に示し
たように操業日数の経過とともに炉殻表面温度が
かなり急激に上昇した。この場合8日間の操業
後、電気炉を解体してライニング内部を調査した
ところ1図に示す如くライニング層中に金属マグ
ネシウム凝縮析出部分4が観察された。 As a result of continued operation as described above, in the electric furnace with the conventional lining structure (FIG. 1), the furnace shell surface temperature rose quite rapidly as the number of days of operation progressed, as shown in FIG. In this case, after 8 days of operation, the electric furnace was dismantled and the inside of the lining was investigated, and as shown in Figure 1, metallic magnesium condensation deposits 4 were observed in the lining layer.
また、ライニング層中に隔壁板を設けた構造と
した電気炉(第3図)では、第4図に示したよう
に操業日数の経過にともなう炉殻表面温度の上昇
は比較的緩やかになつたが、25日間操業後ライニ
ング解体調査を行つた結果、第3図に示した如く
隔壁板の裏側にまで金属マグネシウム凝縮析出部
分が観察された。 Furthermore, in an electric furnace with a structure in which a partition plate is provided in the lining layer (Figure 3), the rise in the furnace shell surface temperature as the number of operating days passes is relatively gradual, as shown in Figure 4. However, when the lining was dismantled and investigated after 25 days of operation, metallic magnesium condensation was observed on the back side of the partition wall plate as shown in Figure 3.
つぎに本発明のライニング構造である炉壁と隔
壁板の間を密閉型とした電気炉(第5図)では、
第6図に示したように炉殻表面温度の急激な上昇
はまつたく見られず、54日間の操業継続中も前記
炉殻表面温度は150℃前後を保持し続け、さらに
操業が継続できる状態であつた。また前記隔壁板
と炉壁との間の気密室の圧力は電気炉の炉内圧力
30―50Torrに対して約50―60Torrと若干庫目に
保持した。 Next, in the electric furnace (Fig. 5) in which the lining structure of the present invention is a closed type between the furnace wall and the partition plate,
As shown in Figure 6, there was no sudden rise in the furnace shell surface temperature, and the furnace shell surface temperature continued to be maintained at around 150°C during the 54 days of continuous operation, making it possible to continue operation. It was hot. In addition, the pressure in the airtight chamber between the partition plate and the furnace wall is the internal pressure of the electric furnace.
Compared to 30-50 Torr, the temperature was maintained at about 50-60 Torr.
以上の如く、本発明の電気炉ライニング構造に
よれば、従来のライニング構造の場合と異なり、
炉蓋、炉壁ならびに炉床ライニング層にマグネシ
ウム蒸気が滲透することがなく、そのためにライ
ニングの損傷が少なく、また電気炉の保温性も長
期にわたつて保持されることにより長期間の連続
操業が可能となり、金属マグネシウムの工業生産
上多大の進歩がもたらされるものと期待される。 As described above, according to the electric furnace lining structure of the present invention, unlike the conventional lining structure,
Magnesium vapor does not seep into the furnace lid, furnace walls, or hearth lining layer, so there is little damage to the lining, and the electric furnace maintains its heat retention properties over a long period of time, allowing for long-term continuous operation. It is expected that this will lead to great progress in the industrial production of magnesium metal.
第1図はマグネシウム製造用密閉式電気炉の従
来のライニング構造の縦断面図、第2図は前記電
炉による操業日数と炉殻表面温度の関係を示す
図、第3図はライニング層の中間に隔壁板を設け
たライニング構造の縦断面図、第4図は該電気炉
による操業日数と炉殻表面温度の関係を示す図、
第5図は前記隔壁板と炉殻の間を密封型にしたラ
イニング構造の縦断面図、第6図は該電気炉によ
る操業日数と炉殻表面温度の関係を示す図であ
る。
1…鋼板製炉殻、2…シヤモツト系断熱材、3
…アルミナ系耐火煉瓦、4…カーボンブロツク、
5…ライニング中のマグネシウム析出部分、6…
隔壁板、7…不活性ガス導入用管。
Figure 1 is a vertical cross-sectional view of the conventional lining structure of a closed electric furnace for producing magnesium, Figure 2 is a diagram showing the relationship between the number of operating days of the electric furnace and the surface temperature of the furnace shell, and Figure 3 is a diagram showing the relationship between the number of operating days of the electric furnace and the surface temperature of the furnace shell. A vertical cross-sectional view of a lining structure provided with a partition plate, FIG. 4 is a diagram showing the relationship between the number of operating days of the electric furnace and the furnace shell surface temperature,
FIG. 5 is a longitudinal sectional view of a lining structure in which the space between the partition plate and the furnace shell is sealed, and FIG. 6 is a diagram showing the relationship between the number of operating days of the electric furnace and the surface temperature of the furnace shell. 1...Steel plate furnace shell, 2...Shamototsu-based insulation material, 3
...Alumina firebrick, 4...Carbon block,
5...Magnesium precipitated part in the lining, 6...
Partition plate, 7...Inert gas introduction pipe.
Claims (1)
を用いて溶融還元する密閉式電気炉を含む金属マ
グネシウム製造装置において、前記電気炉の炉殻
の内側に施されたライニング層中に炉殻に沿つて
マグネシウム蒸気がライニングを滲透して炉殻に
至るのを防止するためのマグネシウム蒸気不滲透
性隔壁板を設け、かつ炉殻と隔壁板との間の圧力
を制御するための不活性ガス導入用導管を炉殻に
設けてなることを特徴とる金属マグネシウム製造
装置。 2 前記電気炉の炉殻と隔壁板との間は、炉殻と
それに対峙する隔壁板とを必要により1乃至2以
上のブロツクに区劃してそれぞれのブロツクの炉
殻に不活性ガス導入用導管を設けてなることを特
徴とする特許請求の範囲第1項記載の装置。 3 前記隔壁板を構成するマグネシウム蒸気不滲
透用隔壁板は、金属板、緻密なアスベスト板、ホ
ウロウ板、不滲透黒鉛板、炭素繊維強化セラミツ
クス板の何れかであることを特徴とする特許請求
の範囲第1、2項の何れかに記載の装置。[Scope of Claims] 1. In a metal magnesium production apparatus including a closed electric furnace for melting and reducing a magnesium oxide-containing substance using a reducing agent under reduced pressure, a lining layer provided inside the furnace shell of the electric furnace is provided. A magnesium vapor-impermeable bulkhead plate is provided along the furnace shell to prevent magnesium vapor from permeating the lining and reaching the furnace shell, and the pressure between the furnace shell and the bulkhead plate is controlled. A metal magnesium production device characterized by having an inert gas introduction conduit installed in the furnace shell. 2. Between the furnace shell and the partition plate of the electric furnace, the furnace shell and the partition plate facing it are divided into one or more blocks as necessary, and an inert gas is introduced into the furnace shell of each block. 2. Device according to claim 1, characterized in that it is provided with a conduit. 3. The magnesium vapor impermeable partition plate constituting the partition plate is any one of a metal plate, a dense asbestos plate, an enamel plate, an impermeable graphite plate, and a carbon fiber-reinforced ceramic plate. The device according to any one of scope 1 and 2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9752582A JPS58217650A (en) | 1982-06-09 | 1982-06-09 | Apparatus for preparing metallic magnesium |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9752582A JPS58217650A (en) | 1982-06-09 | 1982-06-09 | Apparatus for preparing metallic magnesium |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58217650A JPS58217650A (en) | 1983-12-17 |
| JPS6134488B2 true JPS6134488B2 (en) | 1986-08-08 |
Family
ID=14194665
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9752582A Granted JPS58217650A (en) | 1982-06-09 | 1982-06-09 | Apparatus for preparing metallic magnesium |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58217650A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101063798B1 (en) | 2008-12-23 | 2011-09-08 | 주식회사 포스코 | Magnesium production apparatus and magnesium production method using the same |
| JP7244000B2 (en) * | 2018-10-25 | 2023-03-22 | 株式会社アクセル技研 | Furnace wall structure of holding furnace for molten metal |
-
1982
- 1982-06-09 JP JP9752582A patent/JPS58217650A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58217650A (en) | 1983-12-17 |
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