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JPH0689418B2 - Continuous magnesium dissolution evaporator - Google Patents

Continuous magnesium dissolution evaporator

Info

Publication number
JPH0689418B2
JPH0689418B2 JP12429789A JP12429789A JPH0689418B2 JP H0689418 B2 JPH0689418 B2 JP H0689418B2 JP 12429789 A JP12429789 A JP 12429789A JP 12429789 A JP12429789 A JP 12429789A JP H0689418 B2 JPH0689418 B2 JP H0689418B2
Authority
JP
Japan
Prior art keywords
magnesium
evaporation
pot
pan
sectional area
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 - Lifetime
Application number
JP12429789A
Other languages
Japanese (ja)
Other versions
JPH02307822A (en
Inventor
文男 長島
哲夫 小田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ube Corp
Original Assignee
Ube Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP12429789A priority Critical patent/JPH0689418B2/en
Publication of JPH02307822A publication Critical patent/JPH02307822A/en
Publication of JPH0689418B2 publication Critical patent/JPH0689418B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F5/00Compounds of magnesium
    • C01F5/02Magnesia
    • C01F5/04Magnesia by oxidation of metallic magnesium

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、微粉末状金属酸化物の製造装置に関するもの
である。さらに詳しくは、気相法によるマグネシウム酸
化物の製造において、連続的にマグネシウムを溶解,蒸
発する装置に関するものである。
TECHNICAL FIELD The present invention relates to an apparatus for producing fine powder metal oxides. More specifically, it relates to an apparatus for continuously dissolving and evaporating magnesium in the production of magnesium oxide by a vapor phase method.

[従来の技術] マグネシウムの溶解,蒸発は一つの鍋にて行なわせる方
法が一般的である。例えば、マグネシア酸化物の製造に
おいては、溶解,蒸発を一つの鍋にて行なう方法が報告
されている(特願昭59−15758号)。
[Prior Art] It is common practice to dissolve and evaporate magnesium in one pot. For example, in the production of magnesia oxide, a method of melting and evaporating in a single pot has been reported (Japanese Patent Application No. 59-15758).

[発明が解決しようとする課題] しかしながら、この従来の一つの鍋にて溶解,蒸発させ
る方法では、安定連続した蒸気の発生が得がたく、工業
生産規模においては問題が出てくる。
[Problems to be Solved by the Invention] However, in the conventional method of melting and evaporating in one pot, it is difficult to generate stable and continuous steam, which causes a problem on an industrial production scale.

すなわち、従来の一つの鍋の方法は回分式であり、生産
性が劣ると共に沸点以上に加熱された高温度の部分にマ
グネシウム塊を投入しなければならないので、マグネシ
ウムのように燃え易い(酸化し易い)金属は、投入時に
鍋内で部分的に燃焼する恐れがある。
In other words, the conventional one-pot method is a batch method, which is inferior in productivity and has to be charged with magnesium lumps in a high-temperature portion heated above the boiling point, so that it burns easily like magnesium (oxidizes. (Easy) metal may partially burn in the pot when thrown.

また、同一鍋内で昇温・溶解を行なわせるので、マグネ
シウム塊投入の際は、溶湯温度が下り、マグネシウム蒸
発速度が減少し変動を起こし安定したマグネシウム蒸発
量が得られず、後工程での製品品質のバラツキなどのト
ラブル発生の原因となる。
Also, since the temperature is raised and melted in the same pot, when the magnesium lump is charged, the molten metal temperature falls, the magnesium evaporation rate decreases, and fluctuations occur, so a stable magnesium evaporation amount cannot be obtained, and in the subsequent process This may cause problems such as variations in product quality.

さらに従来は、マグネシウム蒸気が充満している蒸発鍋
内の状態は、加熱温度およびマグネシウム蒸気吹出ノズ
ルから出てくる蒸気の状況により判断していた。内部圧
力が測定できると状態の把握ができるが、圧力検出端へ
のマグネシウム凝固・付着により閉塞が生じ測定が不可
能であった。
Further, conventionally, the state of the inside of the evaporation pan filled with magnesium vapor has been judged by the heating temperature and the state of the vapor coming out from the magnesium vapor blowing nozzle. If the internal pressure can be measured, the state can be grasped, but the measurement is impossible due to blockage due to magnesium coagulation / adhesion to the pressure detection end.

したがって、この発明においては、マグネシウム蒸気を
連続的に安定して供給させ、かつ、鍋内の圧力が計測で
きるようにすることを技術的課題とする。
Therefore, it is a technical object of the present invention to continuously and stably supply magnesium vapor and to measure the pressure in the pan.

[課題を解決するための手段] 上記の技術的課題を解決するために、 まず、第1の発明では、マグネシウム溶解用の溶解鍋
と、マグネシウム蒸発用の蒸発鍋をマグネシウム溶湯の
保持面より下部の部分で互いに溶融マグネシウム金属が
通過可能な接続パイプで連結する。
[Means for Solving the Problems] In order to solve the above technical problems, first, in the first invention, a melting pot for melting magnesium and an evaporation pot for magnesium evaporation are disposed below a holding surface of the molten magnesium. In the portion of, the connection is made by connecting pipes through which molten magnesium metal can pass.

また、第2の発明では、マグネシウム蒸気吹出ノズルお
よび圧力検出端を兼ねた不活性ガス吹き込みノズルを備
えた蓋を蒸発用の蒸発鍋に取り付ける。
Further, in the second aspect of the invention, the lid equipped with the magnesium vapor blowing nozzle and the inert gas blowing nozzle that also serves as the pressure detecting end is attached to the evaporation pot for evaporation.

そして、第3発明では、溶解鍋と蒸発鍋の断面積比(溶
解鍋横断面積/蒸発鍋横断面積)が1以上とする。
Further, in the third invention, the cross-sectional area ratio of the melting pot and the evaporating pot (melting pot cross-sectional area / evaporation pot cross-sectional area) is 1 or more.

そしてまた、第4の発明では、接続パイプの断面積が蒸
発鍋の横断面積に対し1/10〜1/25とする。
Further, in the fourth invention, the cross-sectional area of the connecting pipe is 1/10 to 1/25 of the cross-sectional area of the evaporation pan.

さらに、第5の発明では、蒸発鍋の蓋に取り付けられた
マグネシウム蒸気吹出ノズルの断面積が3cm2以上とす
る。
Further, in the fifth invention, the magnesium vapor blowing nozzle attached to the lid of the evaporation pot has a cross-sectional area of 3 cm 2 or more.

[作用] 上記の技術的手段による構成の装置でマグネシウムを溶
解,蒸発させる時、マグネシウム塊は溶解鍋に投入され
るが、溶解温度以上850℃以下の温度で溶湯が保持され
た状態の溶解鍋に投入されるので、SF6ガス,CO2ガス,
不活性ガス等による溶湯表面カバーによる該知の防燃方
法により、マグネシウムの酸化を防止できる。また、マ
グネシウム塊を溶解鍋に投入する際も、投入前と同じ温
度の溶湯が蒸発鍋に送られるので、蒸発鍋内の定常の状
態は変化せず、蒸発鍋内の温度降下はなく、一定の蒸発
速度が維持される。
[Operation] When magnesium is melted and evaporated by the device having the above-mentioned technical means, the magnesium lump is put into the melting pot, but the melting pot is in a state in which the molten metal is held at a temperature of not less than melting temperature and not more than 850 ° C. since the turned on, SF 6 gas, CO 2 gas,
Oxidation of magnesium can be prevented by the known flameproofing method using a molten metal surface cover with an inert gas or the like. Also, when the magnesium lump is charged into the melting pot, the molten metal at the same temperature as before charging is sent to the evaporation pan, so the steady state inside the evaporation pan does not change, there is no temperature drop inside the evaporation pan, and it is constant. The evaporation rate of is maintained.

マグネシウム塊の溶解鍋への投入時以外は、溶解鍋から
蒸発鍋へのマグネシウム溶湯の流れは、蒸発鍋で蒸発し
た量が、溶解鍋と蒸発鍋の溶湯のヘッド差により、自然
に、連続的に行なわれる。
The flow of magnesium melt from the melting pan to the evaporating pan is natural and continuous except when the magnesium lump is put into the melting pan, due to the difference in head volume between the melting pan and the evaporating pan. To be done.

マグネシウム塊投入時の、塊の顕熱・溶解熱による湯温
降下および溶湯の急激な蒸発鍋への流入をできる限り防
止するためには、蒸発鍋の蒸発速度に応じたマグネシウ
ム塊量を連続的に溶解鍋に投入していくことが望まし
い。
In order to prevent the temperature of the molten metal from dropping due to the sensible heat and the heat of dissolution of the lump of magnesium and the sudden inflow of the molten metal into the evaporating pan as much as possible, the amount of magnesium lump according to the evaporation rate of the evaporating pan should be set continuously. It is desirable to add it to a melting pot.

しかし、このような操作は作業上非常に困難であるの
で、溶解鍋と蒸発鍋の断面積比(溶解鍋横断面積/蒸発
鍋横断面積)をできる限り大きくし、溶湯保持量に差を
持たせ、マグネシウム塊の溶解鍋への投入時の、溶解鍋
から蒸発鍋への急激な溶湯の流入を防ぐ。蒸発鍋の蒸発
速度およびマグネシウム塊投入インターバル等を総合し
て考え、上記断面積比が1以上あれば、蒸発鍋内蒸発速
度に影響を与えずマグネシウム塊を投入できる。
However, such an operation is extremely difficult in terms of work, so make the cross-sectional area ratio (melting pan cross-sectional area / evaporation pan cross-sectional area) between the melting pot and the evaporation pan as large as possible to make the difference in molten metal holding amount. Prevents the rapid inflow of molten metal from the melting pot to the evaporation pot when the magnesium mass is put into the melting pot. Considering the evaporation rate of the evaporating pan and the magnesium lump introduction interval, etc., if the cross-sectional area ratio is 1 or more, the magnesium lump can be injected without affecting the evaporation rate in the evaporating pan.

また、溶解鍋と蒸発鍋を連結する接続パイプの断面積
は、蒸発鍋横断面積の1/25より小さいと閉塞の原因とな
り、1/10より大きいと蒸発鍋から溶解鍋への熱拡散の要
因となり、適当な断面積が必要となる。
In addition, if the cross-sectional area of the connecting pipe that connects the melting pot and the evaporation pot is smaller than 1/25 of the cross-sectional area of the evaporation pot, it causes blockage, and if it is larger than 1/10, the factor of heat diffusion from the evaporation pot to the melting pot. Therefore, an appropriate cross sectional area is required.

よって、接続パイプの断面積は、蒸発鍋横断面積の1/10
〜1/25の範囲内が好ましい。
Therefore, the cross-sectional area of the connecting pipe is 1/10 of the cross-sectional area of the evaporation pot.
It is preferably within the range of to 1/25.

蒸発鍋の内圧測定は、この装置の運転上必要である。圧
力が低い運転は問題がないが、高い圧力になると蒸発鍋
内湯面が下り溶解鍋内湯面が上昇する。蒸発鍋内湯面が
接続パイプより下面にくると、マグネシウム蒸気が溶解
鍋内側に吹き抜ける現象が起こる。この危険な状態を生
じさせないためには、蒸発鍋内の圧力を測定し、蒸発鍋
内の湯面が下り過ぎないようにしなければならない。
Measurement of the internal pressure of the evaporation pan is necessary for the operation of this device. There is no problem in low pressure operation, but when the pressure becomes high, the surface of the liquid inside the evaporation pan goes down and the surface of the liquid inside the melting pan rises. When the surface of the water in the evaporation pot comes below the connection pipe, magnesium vapor blows into the melting pot. In order to prevent this dangerous condition, the pressure inside the evaporation pan must be measured so that the surface of the liquid inside the evaporation pan does not go down too much.

圧力測定は、蒸発鍋蓋に取り付けてある不活性ガス吹き
込みノズルを検出端とし、不活性ガス配管の冷間部にて
圧力を検出し、配管圧損を考慮し蒸発鍋内の圧力を推定
する。不活性ガスを流し、不活性ガス吹き込みノズル部
のパイプをマグネシウム蒸気が凝固しない温度以上に加
熱すれば、圧力検出端の閉塞は防ぐことができる。
For pressure measurement, the inert gas blowing nozzle attached to the lid of the evaporation pan is used as the detection end, the pressure is detected in the cold part of the inert gas pipe, and the pressure in the evaporation pan is estimated in consideration of the pipe pressure loss. If an inert gas is flown and the pipe of the nozzle for blowing the inert gas is heated to a temperature at which magnesium vapor does not solidify, the pressure detection end can be prevented from being blocked.

また、蒸発蒸気吹き出しノズルも、酸化物・窒化物等の
付着で閉塞の恐れがあるが、断面積が3cm2以上あれ
ば、充分な加熱により付着もほとんどなく、閉塞による
蒸発鍋内圧の急激な上昇もなく、安定した運転ができ
る。
Also, the evaporative vapor blowing nozzle may be clogged due to the adhesion of oxides and nitrides, but if the cross-sectional area is 3 cm 2 or more, there will be almost no adhesion due to sufficient heating, and the evaporating pot internal pressure due to the clog will be sharp. There is no rise and stable operation is possible.

[実施例] 第1図はこの発明の一実施例を示すもので、本図に示す
装置にてマグネシウムを溶解,蒸発させる。
[Embodiment] FIG. 1 shows an embodiment of the present invention. Magnesium is dissolved and evaporated in the apparatus shown in this figure.

あらかじめマグネシウム地金を溶解鍋1にて溶解させ、
接続パイプ2を通じて溶融マグネシウムを蒸発鍋3に充
満させ、その後に溶解鍋1の部分を850℃、接続パイプ
2の部分を900℃、蒸発鍋3の部分を1200℃にする。昇
温加熱は加熱炉7にて行なう。
Dissolve the magnesium metal in the melting pan 1 beforehand,
Molten magnesium is filled in the evaporation pan 3 through the connection pipe 2, and then the melting pan 1 part is heated to 850 ° C., the connection pipe 2 part is heated to 900 ° C., and the evaporation pan 3 part is heated to 1200 ° C. The heating by heating is performed in the heating furnace 7.

不活性ガス吹き込みノズル5からは、アルゴンガスを0.
2Nm3/H常時流す。定常になると、マグネシウム蒸気吹出
ノズル4よりマグネシウム蒸気が吹き出し、空気中の酸
素により燃焼する。
From the inert gas blowing nozzle 5, an argon gas of 0.
2Nm 3 / H Always flow. At a steady state, magnesium vapor is blown out from the magnesium vapor blowing nozzle 4 and burned by oxygen in the air.

蒸発が進むと、系内のマグネシウム量が減少し、溶解鍋
1の湯面が降下してくる。マグネシウム蒸気の蒸発速度
は、マグネシウム蒸気吹出ノズル4から吹き出し酸化燃
焼した酸化マグネシウムの量を計量することにより確認
できる。この蒸発量に応じたマグネシウム金属塊を定期
的に溶解鍋1に投入することにより、蒸発速度を一定に
保つことができる。
As the evaporation proceeds, the amount of magnesium in the system decreases and the molten metal level of the melting pot 1 drops. The evaporation rate of magnesium vapor can be confirmed by measuring the amount of magnesium oxide blown out from the magnesium vapor blowing nozzle 4 and oxidized and burned. It is possible to keep the evaporation rate constant by periodically charging the melting pot 1 with a magnesium metal mass corresponding to this evaporation amount.

蒸発鍋3内の圧力は一定に保たれ、マグネシウム蒸気が
溶解鍋1へ吹き抜ける現象は起きない。
The pressure in the evaporation pot 3 is kept constant, and the phenomenon that magnesium vapor blows through the melting pot 1 does not occur.

溶解鍋1表面には酸化防止用としてSF6ガスを少量、コ
ンスタントに流し続ける。運転後、溶解鍋1底部に沈ん
でいるスラッジ(マグネシウム酸化物)は、ほとんどな
い状態である。
A small amount of SF 6 gas is continuously flowed on the surface of the melting pot 1 as an antioxidant. After the operation, there is almost no sludge (magnesium oxide) sinking at the bottom of the melting pot 1.

[発明の効果] 本発明は以下に記載されるような効果を奏する。[Advantages of the Invention] The present invention has the advantages described below.

マグネシウムを溶解,蒸発させる際、溶解部と蒸発部の
二つの部分に機能を分けたため、酸化燃焼のロスがな
く、連続的に、溶解,蒸発できる。
When melting and evaporating magnesium, the functions are divided into two parts, a melting part and an evaporating part, so that there is no loss of oxidative combustion and continuous melting and evaporation is possible.

また、溶解鍋を蒸発鍋に対して大きくすることと、溶解
鍋と蒸発鍋の接続パイプの断面積を蒸発鍋の横断面積の
1/10〜1/25にとることにより、マグネシウム塊を溶解鍋
に投入する際の温度降下が蒸発鍋内の蒸発速度に大きな
影響を与えることを防ぐことができ、連続・安定したマ
グネシウム蒸気の発生が得られる。
Also, make the melting pot larger than the evaporation pot, and change the cross-sectional area of the connecting pipe between the melting pot and the evaporation pot to the cross-sectional area of the evaporation pot.
By setting it to 1/10 to 1/25, it is possible to prevent the temperature drop when charging the magnesium lump into the melting pot from having a large effect on the evaporation rate in the evaporation pot, and to ensure continuous and stable magnesium vapor. Occurrence is obtained.

さらに、蒸発鍋内部の圧力を検出できることにより、マ
グネシウム沸騰状態の把握ができる。
Furthermore, since the pressure inside the evaporation pan can be detected, the state of boiling magnesium can be grasped.

また、蒸気吹き出しノズルの断面積を3m2以上にするこ
とにより、吹き出しノズルのつまりが防止され蒸発鍋内
部圧力の上昇をふせぎ、溶解鍋部へのマグネシウム蒸気
の吹き抜けを防止することができる。
Further, by setting the cross-sectional area of the steam blowing nozzle to 3 m 2 or more, the clogging of the blowing nozzle is prevented, the rise of the internal pressure of the evaporation pot is suppressed, and the blowout of magnesium vapor to the melting pot part can be prevented.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の連続式マグネシウム溶解,蒸発装置の
一実施例を示す縦断面図である。 1…溶解鍋、2…接続パイプ、 3…蒸発鍋、 4…マグネシウム蒸気吹出ノズル、 5…不活性ガス吹き込みノズル、 6…マグネシウム塊投入口、 7…加熱炉。
FIG. 1 is a vertical cross-sectional view showing an embodiment of a continuous magnesium melting / evaporating apparatus of the present invention. DESCRIPTION OF SYMBOLS 1 ... Melting pan, 2 ... Connection pipe, 3 ... Evaporating pan, 4 ... Magnesium vapor blowing nozzle, 5 ... Inert gas blowing nozzle, 6 ... Magnesium lump injection port, 7 ... Heating furnace.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】マグネシウム溶解用の溶解鍋と、マグネシ
ウム蒸発用の蒸発鍋をマグネシウム溶湯の保持面より下
部の部分で互いに溶融マグネシウム金属が通過可能な接
続パイプで連結したことを特徴とする連続マグネシウム
溶解蒸発装置。
1. A continuous magnesium characterized in that a melting pot for melting magnesium and an evaporation pot for vaporizing magnesium are connected to each other by a connecting pipe through which molten magnesium metal can pass at a portion below a holding surface of the molten magnesium. Dissolution evaporation device.
【請求項2】マグネシウム蒸気吹出ノズルおよび圧力検
出端を兼ねた不活性ガス吹き込みノズルを備えた蓋を蒸
発鍋に取り付けたことを特徴とする請求項1記載の連続
マグネシウム溶解蒸発装置。
2. A continuous magnesium dissolving / evaporating apparatus according to claim 1, wherein a lid equipped with a magnesium vapor blowing nozzle and an inert gas blowing nozzle which also serves as a pressure detecting end is attached to the evaporation pot.
【請求項3】溶解鍋と蒸発鍋の断面積比(溶解鍋横断面
積/蒸発鍋横断面積)が1以上を特徴とする請求項1ま
たは2記載の連続マグネシウム溶解蒸発装置。
3. The continuous magnesium dissolution / evaporation apparatus according to claim 1, wherein the sectional area ratio (dissolving pan cross-sectional area / evaporating pan cross-sectional area) of the melting pan and the evaporation pan is 1 or more.
【請求項4】接続パイプの断面積が蒸発鍋の横断面積に
対し、1/10〜1/25であることを特徴とする請求項1ない
し3のいずれか一つに記載の連続マグネシウム溶解蒸発
装置。
4. The continuous magnesium dissolution evaporation according to claim 1, wherein the cross-sectional area of the connecting pipe is 1/10 to 1/25 of the cross-sectional area of the evaporation pan. apparatus.
【請求項5】蒸発鍋の蓋に取り付けられたマグネシウム
蒸気吹出用ノズルの断面積が3cm2以上であることを特
徴とする請求項1ないし4のいずれか一つに記載の連続
マグネシウム溶解蒸発装置。
5. The continuous magnesium dissolving / evaporating apparatus according to claim 1, wherein the magnesium vapor blowing nozzle attached to the lid of the evaporation pot has a cross-sectional area of 3 cm 2 or more. .
JP12429789A 1989-05-19 1989-05-19 Continuous magnesium dissolution evaporator Expired - Lifetime JPH0689418B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12429789A JPH0689418B2 (en) 1989-05-19 1989-05-19 Continuous magnesium dissolution evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12429789A JPH0689418B2 (en) 1989-05-19 1989-05-19 Continuous magnesium dissolution evaporator

Publications (2)

Publication Number Publication Date
JPH02307822A JPH02307822A (en) 1990-12-21
JPH0689418B2 true JPH0689418B2 (en) 1994-11-09

Family

ID=14881848

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12429789A Expired - Lifetime JPH0689418B2 (en) 1989-05-19 1989-05-19 Continuous magnesium dissolution evaporator

Country Status (1)

Country Link
JP (1) JPH0689418B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009030172A (en) * 2008-08-25 2009-02-12 Ube Material Industries Ltd Metal magnesium melting/evaporating device, and method for producing high purity magnesium oxide fine powder using the same

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08269696A (en) * 1995-03-28 1996-10-15 Nisshin Steel Co Ltd Method for vaporizing mg
JP4195278B2 (en) * 2002-12-02 2008-12-10 宇部マテリアルズ株式会社 Metallic magnesium melt evaporation apparatus and method for producing high-purity magnesium oxide fine powder using the same
JP4949340B2 (en) * 2008-08-25 2012-06-06 宇部マテリアルズ株式会社 High purity magnesium oxide fine powder production apparatus and high purity magnesium oxide fine powder production method using the same
KR101704757B1 (en) 2014-11-25 2017-02-08 전남대학교산학협력단 Manufacturing method of high purity mesoporous inorganic oxides and high purity mesoporous inorganic oxides made by the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009030172A (en) * 2008-08-25 2009-02-12 Ube Material Industries Ltd Metal magnesium melting/evaporating device, and method for producing high purity magnesium oxide fine powder using the same

Also Published As

Publication number Publication date
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