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JPS5843353B2 - How to fire magnesia - Google Patents
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JPS5843353B2 - How to fire magnesia - Google Patents

How to fire magnesia

Info

Publication number
JPS5843353B2
JPS5843353B2 JP54104018A JP10401879A JPS5843353B2 JP S5843353 B2 JPS5843353 B2 JP S5843353B2 JP 54104018 A JP54104018 A JP 54104018A JP 10401879 A JP10401879 A JP 10401879A JP S5843353 B2 JPS5843353 B2 JP S5843353B2
Authority
JP
Japan
Prior art keywords
magnesia
water vapor
firing
temperature
weight
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
Application number
JP54104018A
Other languages
Japanese (ja)
Other versions
JPS5632322A (en
Inventor
陽一 高宮
康義 小田
隆生 福田
康生 鈴木
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.)
Shin Nihon Kagaku Kogyo KK
Original Assignee
Shin Nihon Kagaku Kogyo KK
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 Shin Nihon Kagaku Kogyo KK filed Critical Shin Nihon Kagaku Kogyo KK
Priority to JP54104018A priority Critical patent/JPS5843353B2/en
Publication of JPS5632322A publication Critical patent/JPS5632322A/en
Publication of JPS5843353B2 publication Critical patent/JPS5843353B2/en
Expired legal-status Critical Current

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  • Compositions Of Oxide Ceramics (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Description

【発明の詳細な説明】 本発明は高密度でなおかつ結晶の十分に発達したマグネ
シアを焼成する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for firing magnesia having high density and sufficiently developed crystals.

マグネシアはアルミナと同様に最も大量に用いられる酸
化物のひとつであり、現在塩基性製鋼炉用材料として広
く用いられているほか、その秀れた特性を利用する分野
、例えば金属溶解ルツボ、光学用、電子材料、MHD発
電用などの耐火材料への利用が期待されている。
Magnesia, like alumina, is one of the most widely used oxides, and is currently widely used as a material for basic steelmaking furnaces, as well as in fields that utilize its excellent properties, such as metal melting crucibles and optical applications. It is expected to be used as a refractory material for electronic materials, MHD power generation, etc.

製鋼炉の耐火物としてのマグネシア耐火物の品質改良な
らびにマグネシアの用途を拡大するひとつの方向として
、マグネシア焼結体の密度を上げ、またその結晶粒子の
大きさを大きくすることが示唆されている。
It has been suggested that one way to improve the quality of magnesia refractories as refractories in steelmaking furnaces and to expand the uses of magnesia is to increase the density of magnesia sintered bodies and the size of their crystal grains. .

すなわち焼結体の密度を高めることはスラグ侵蝕を抑え
、強度を向上させ、電気的特性を改善するなどの効果が
期待でき、結晶粒子を大きくすることtiミスラグ蝕を
抑え、高温でのクリープ特性を改善するなどの効果が期
待できる。
In other words, increasing the density of the sintered body can be expected to have effects such as suppressing slag corrosion, improving strength, and improving electrical properties, while enlarging crystal grains suppresses slag corrosion and improves creep characteristics at high temperatures. It can be expected to have effects such as improving

高密度でかつ大きな結晶粒子をもつマグネシア焼結体の
製造方法としてはホットプレス法、電融マグネシアから
切り出す方法などが知られているが、これらの方法はい
づれもコストがかさみなおかつ得られる形状が限られる
、壁間による強度低下が著しいなどの欠陥を有するため
、マグネシア焼結体の改良を行えるのは極く限られた場
合とみられていた。
Hot pressing methods and methods of cutting magnesia from fused magnesia are known as methods for producing magnesia sintered bodies with high density and large crystal grains, but these methods are both expensive and difficult to obtain. It was thought that improvements to magnesia sintered bodies could only be made in very limited cases due to defects such as limited strength and a significant decrease in strength between walls.

勿論、従来のマグネシアの焼結方法たとえば軽焼マグネ
シアを成形しロータリーキルン、シャフトキルン等で焼
成する方法において焼結体の密度を上げる様々な努力、
たとえば焼結促進剤の添加、不純物組成の調整、焼成雰
囲気の変化などがとられている。
Of course, various efforts have been made to increase the density of the sintered body in conventional magnesia sintering methods, such as molding light sintered magnesia and firing it in a rotary kiln, shaft kiln, etc.
For example, the addition of sintering accelerators, adjustment of impurity composition, and changes in the firing atmosphere have been taken.

しかしこれらの努力にもかかわらずマグネシアの特性を
高度に備えた高純度のマグネシアの場合、従来の方法に
おいては2000℃という高温度焼成を行っても嵩比重
は3.4どまり、結晶粒子経30〜40μが限度とみら
れていた。
However, despite these efforts, in the case of high-purity magnesia that has the characteristics of magnesia to a high degree, the bulk specific gravity is only 3.4 even if it is fired at a high temperature of 2000°C in the conventional method, and the crystal grain size is 30. ~40μ was considered to be the limit.

本発明は従来のマグネシアの焼成方法に改善を加えるこ
とにより、従来の方法では得られない高密度で大きな結
晶粒子をもつマグネシアを焼成することができるばかり
でなく、焼成温度も従来のような2000℃という高温
度を要しない方法を見出したものである。
By improving the conventional magnesia firing method, the present invention not only makes it possible to fire magnesia with high density and large crystal grains that cannot be obtained with the conventional method, but also lowers the firing temperature to 2,000 yen as in the conventional method. They discovered a method that does not require high temperatures of ℃.

本発明の方法によればホットプレスなどの複雑な焼結方
法によらず1500℃の焼成温度で嵩比重3.5以上結
晶粒子経60μ程度のマグネシア焼結体を容易に得るこ
とができる。
According to the method of the present invention, a magnesia sintered body having a bulk specific gravity of 3.5 or more and a crystal grain size of approximately 60 μm can be easily obtained at a sintering temperature of 1500° C. without using a complicated sintering method such as hot pressing.

本発明は、酸化マグネシウムの成形体を総圧200 m
mHg以上で水蒸気を25vo1%以上含み、かつ水蒸
気分圧と炭酸ガス分圧との比(H20/C02)が1.
7以上である雰囲気中で焼成することを特徴とするマグ
ネシアの焼成方法。
In the present invention, a molded body of magnesium oxide is formed under a total pressure of 200 m
mHg or higher, contains 25 vol% or more of water vapor, and has a ratio of water vapor partial pressure to carbon dioxide gas partial pressure (H20/C02) of 1.
A method for firing magnesia, characterized by firing in an atmosphere having a temperature of 7 or higher.

マグネシアの焼成に於ける水蒸気の影響については既に
P −J 、Anderson他Trans、 Far
adySoc、Vo160(5)930−937(64
):East−man他J 、Am Soram、Vo
l 49(10’) 526〜530(66)らの研究
者による報告が提出されている。
Regarding the influence of water vapor on the firing of magnesia, P-J, Anderson et al., Trans., Far
adySoc, Vo160(5)930-937(64
): East-man et al. J, Am Soram, Vo.
Reports have been submitted by researchers such as 49(10') 526-530(66).

しかしながら、これら研究においては主として初期焼結
の過程が扱われており、また水蒸気を含むガス組成につ
いても十分な検討が行われているとはいえない。
However, these studies mainly deal with the initial sintering process, and it cannot be said that sufficient consideration has been given to the gas composition including water vapor.

従来のマグネシアの焼結は実際にはかなり水蒸気分圧を
有する雰囲気中で行なわれている。
Conventional sintering of magnesia is actually carried out in an atmosphere having a significant partial pressure of water vapor.

すなわち、マグネシアを焼成するに用いる燃料としては
重油天然ガス等の炭化水素を用いることが多く、これら
の炭化水素を燃焼させれば当然のことながら水蒸気が生
成する。
That is, hydrocarbons such as heavy oil and natural gas are often used as fuels for firing magnesia, and as a matter of course, steam is produced when these hydrocarbons are combusted.

本発明は水蒸気と炭酸ガスの組成比が1.7を越えると
マグネシアの焼結が急速に進み、しかも結晶粒子の太き
さも増大してくることを見出したものであり、このよう
な雰囲気は電気炉ならびに炭化水素を燃焼させる炉に水
蒸気を可及的高温度で噴霧することにより得られる。
The present invention has discovered that when the composition ratio of water vapor and carbon dioxide gas exceeds 1.7, sintering of magnesia proceeds rapidly and the thickness of the crystal grains also increases. It is obtained by spraying steam at the highest possible temperature into an electric furnace or a furnace that burns hydrocarbons.

炭酸ガス以外の気体の影響は炭酸ガスのように顕著では
ないが、それでも若干の悪影響が認められるので、でき
る限り少いことが望ましい。
Although the influence of gases other than carbon dioxide is not as pronounced as carbon dioxide, some adverse effects are still observed, so it is desirable to minimize the influence.

水蒸気の含有率が総圧200mtHg以下で25vo1
%以下になった場合には他のガ入組成によらず本発明の
効果は得られなかった。
Water vapor content is 25vol at total pressure 200mtHg or less
% or less, the effect of the present invention could not be obtained regardless of other gas content compositions.

水蒸気の含有率は50vo1%以上がとくに望ましい。It is particularly desirable that the water vapor content be 50vol% or more.

本発明の方法によればマグネシアの焼成温度を大巾に引
き下げることができる。
According to the method of the present invention, the firing temperature of magnesia can be significantly lowered.

すなわち本発明の方法によれば1400℃以上の温度で
焼成を行えば従来の方法で2000℃程度の焼成温度に
匹敵するものが得られるようになった。
That is, according to the method of the present invention, when firing is performed at a temperature of 1400°C or higher, it is possible to obtain a product comparable to the firing temperature of about 2000°C in the conventional method.

マグネシア焼成においては焼成法に適した組成というも
のが存在する。
In magnesia firing, there is a composition suitable for the firing method.

本発明の場合にはCa00.03%以下5in20.0
9〜0.20%B2030.05%以下の組成のマグネ
シアがとくに良い焼結性状を示した。
In the case of the present invention, Ca00.03% or less5in20.0
Magnesia with a composition of 9 to 0.20%B2030.05% or less showed particularly good sintering properties.

本発明の実施の態様を示すと次の通りである。The embodiments of the present invention are as follows.

マグネシアの原料としては炭酸マグネシウム水酸化マグ
ネシウム等の未分解の原料も用いうるが、成形物中のM
gO分の密度が1.3g/i以上有ると焼結が急速に進
行する傾向が認められるので、軽焼マグネシアを出発原
料とするのが特に有利となる。
Undecomposed raw materials such as magnesium carbonate and magnesium hydroxide can also be used as raw materials for magnesia, but M
If the gO density is 1.3 g/i or more, sintering tends to proceed rapidly, so it is particularly advantageous to use light sintered magnesia as a starting material.

軽焼マグネシアを用いる場合あまり高い温度で分解した
ものは活性がなくなるので、軽焼マグネシアの結晶子の
大きさは0.1μ以下が望ましい。
When light burnt magnesia is used, it is desirable that the crystallite size of the light burnt magnesia is 0.1 μm or less because if it decomposes at too high a temperature, it will lose its activity.

マグネシア原料はダブルロール、打錠機鋳込みなどの方
法で成形されたのち上記雰囲気中で焼成する。
The magnesia raw material is formed by a method such as double roll or tablet casting, and then fired in the above atmosphere.

更に詳しく述べるならば、成形体を焼成炉に送入し、加
熱とはゾ同時に水蒸気を含んだ気体を送入し、その水蒸
気分圧を保ちながら1400℃以上に昇温する。
More specifically, the molded body is fed into a firing furnace, and at the same time as heating, a gas containing water vapor is fed, and the temperature is raised to 1400° C. or higher while maintaining the partial pressure of the water vapor.

所定温度に達した後世くともその水蒸気分圧下で1時間
以上保持することが望ましい、この際の昇温速度は40
0°C/Hr以下が望ましく急激な昇温をさける。
After reaching the specified temperature, it is desirable to hold the temperature under that water vapor partial pressure for at least 1 hour.
It is desirable to keep the temperature below 0°C/Hr and avoid rapid temperature rise.

水蒸気を同伴するガスは通常空気で良いが、特に望1し
くはN2.Arの如き不活性ガスの方が良い。
The gas entrained with water vapor may normally be air, but preferably N2. An inert gas such as Ar is better.

なぜならば不活性ガスの方が水蒸気含有率が低くても結
晶の生長が大きいからである。
This is because crystal growth is greater with inert gas even if the water vapor content is lower.

いずれの場合にも水蒸気含有率は50vo1%以上が特
に好ましい。
In any case, the water vapor content is particularly preferably 50vol% or more.

水蒸気の送入開始温度は焼成物の温度が低い時の方が望
ましいが1000℃程度までは大差がなく、1260℃
以上に達つしてから送入しても効果がない。
The temperature at which steam starts to be fed is preferably when the temperature of the fired product is low, but there is no big difference up to about 1000℃, and it is 1260℃.
Even if it is sent after reaching the above limit, it will have no effect.

前述の如くマグネシアは、重油あるいは天然ガスを燃料
として焼成されることが多いがこの際生成水蒸気により
燃焼ガスの水蒸気含有率は空気を用いた時10〜20
vo1%、純酸素を用いた場合では理論的には水蒸気含
有率が40〜50vo1%になり得る。
As mentioned above, magnesia is often fired using heavy oil or natural gas as fuel, but due to the steam produced at this time, the steam content of the combustion gas is 10 to 20 when air is used.
If pure oxygen is used, the water vapor content can theoretically be 40 to 50 vol.

しかし炭化水素燃料を用いた場合には1500℃程度の
焼成で結晶粒子の大きさはわずか数μ程度!どするにす
ぎず水蒸気分圧が高いにもかかわらず結晶の生長が進み
難い。
However, when hydrocarbon fuel is used, the crystal grain size is only a few microns when fired at about 1500℃! It is difficult for the crystal to grow even though the partial pressure of water vapor is high.

これらについて本発明者らは焼成ガス中の炭酸ガス分圧
と水蒸気分圧との関係を検討した結果水蒸気の分圧が炭
酸ガス分圧の少くとも1.7倍以上、即ちN2CO2−
N20の系で水蒸気含有率が25 vo 1%以上占め
かつ炭酸ガスの分圧の1.7倍以上である時本発明の効
果が有る事を認めた。
Regarding these, the present inventors investigated the relationship between the partial pressure of carbon dioxide gas in the firing gas and the partial pressure of water vapor, and found that the partial pressure of water vapor was at least 1.7 times the partial pressure of carbon dioxide gas, that is, N2CO2-
It was confirmed that the present invention is effective when the water vapor content is 25 vo 1% or more and is 1.7 times or more the partial pressure of carbon dioxide gas in an N20 system.

以下実施例によって本発明を説明する。The present invention will be explained below with reference to Examples.

実施例 1 海水と消石灰を反応させて生成した水酸化マグネシウム
を精製し組成を調整して仮焼物換算で下。
Example 1 Magnesium hydroxide produced by reacting seawater with slaked lime was purified, its composition was adjusted, and the composition was converted into calcined material.

記表−1の原料記号Aの試料を得た。A sample of raw material symbol A in Table-1 was obtained.

ャ 上記水酸化マグネシウムを仮焼炉で軽焼し、X線半
価巾法による結晶子のサイズを350Aに調節した。
The above magnesium hydroxide was lightly calcined in a calcining furnace, and the crystallite size was adjusted to 350A by the X-ray half width method.

この軽焼マグネシアを成形機で成形し嵩比重1.85の
成形体とした。
This lightly calcined magnesia was molded using a molding machine to form a molded body having a bulk specific gravity of 1.85.

成形体をマグネシア製台板に乗せ環状型電気炉に送入し
、初め100℃/Hrの昇温速度で800℃まで昇温し
、500°Cに到達した時蒸気発生器で調節した蒸気を
送入した。
The molded body was placed on a magnesia base plate and sent into an annular electric furnace. Initially, the temperature was raised to 800°C at a rate of 100°C/Hr, and when it reached 500°C, steam regulated by a steam generator was released. Sent.

800℃から200°C/Hrの昇温速度で昇温し、所
定温度に達つした後0.5〜4Hr保持した。
The temperature was raised from 800°C at a rate of 200°C/Hr, and after reaching a predetermined temperature, it was maintained for 0.5 to 4Hr.

この間炉端から蒸気を逃し他の炉端から常時炉内通過速
度2CrIL/5ec(常温換算)で新しい蒸気を供給
した。
During this time, steam was released from the hearth and new steam was constantly supplied from the other hearth at a furnace passing rate of 2 CrIL/5 ec (converted to room temperature).

焼成体は常法により嵩比重を測定し、また、反射顕微鏡
で撮影した写真からペリクレース結晶粒子の大きさをフ
ルマン法で結晶粒界200ケ所以上を計数し平均粒子経
とした。
The bulk specific gravity of the fired body was measured by a conventional method, and the size of the periclase crystal grains was determined by the Fullman method from a photograph taken with a reflection microscope, and 200 or more grain boundaries were counted to obtain the average grain diameter.

表−2はこの結果を示す。Table 2 shows the results.

比較例 1 実施例1と同様に製した水酸化マグネシウムを組成調整
して仮焼物換算で下記表 B、Cの試料を得た。
Comparative Example 1 The composition of magnesium hydroxide produced in the same manner as in Example 1 was adjusted to obtain samples shown in Tables B and C below in terms of calcined product.

3の原料記号 肴上記水酸化マグネシウムを仮焼炉で軽焼し、X線半価
巾法による結晶子のサイズを300〜350人に調節し
た。
The above magnesium hydroxide was lightly calcined in a calcining furnace, and the crystallite size was adjusted to 300 to 350 by the X-ray half width method.

この軽焼マグネシアを実施例1と同様の操作により焼成
並びに測定した。
This lightly calcined magnesia was calcined and measured in the same manner as in Example 1.

表−4はこの結果を示す。Table 4 shows the results.

実施例 2 実施例1の原料記号の試料を実施例1と同様の操作で成
形体を作成し、プロパン炉で焼成した。
Example 2 A molded body was prepared using a sample having the raw material code of Example 1 in the same manner as in Example 1, and fired in a propane furnace.

ガス組成の調整は流量計によりプロパン1molに対し
空気24molの割合で燃焼させ、一方蒸気発生器に3
.3molの割合で水を供給して発生させた180℃〜
200℃の蒸気を炉内に送入した。
To adjust the gas composition, 1 mol of propane is combusted using a flowmeter at a ratio of 24 mol of air, while a steam generator is charged with 3 mol of air.
.. 180℃~ generated by supplying water at a ratio of 3 mol
Steam at 200°C was introduced into the furnace.

昇温速度は燃料ガスの量で調節したが同時に空気水蒸気
の送入量を上記割合で変化させた。
The temperature increase rate was adjusted by the amount of fuel gas, and at the same time, the amount of air and steam fed was varied at the above rate.

昇温速度は約300°C/Hrであった。The temperature increase rate was approximately 300°C/Hr.

所定温度到達後IHr同温度で保持した。After reaching a predetermined temperature, the IHr was maintained at the same temperature.

焼結体の測定は実施例1と同一の方法で行った。Measurement of the sintered body was performed in the same manner as in Example 1.

表−5にこの結果を示す。比較例 2 実施例1の原料記号Aの試料を実施例1と同様の操作で
成形体を作威し、プロパン炉で焼成した。
Table 5 shows the results. Comparative Example 2 A molded body was prepared from a sample of raw material code A of Example 1 in the same manner as in Example 1, and fired in a propane furnace.

実施例2と同様な燃料の送入方法で行ったが、水蒸気の
送入は行わない。
The same fuel feeding method as in Example 2 was used, but water vapor was not fed.

** 昇温速度は燃料ガスの
量で調節し、昇温速度は約300℃/Hrであった。
** The temperature increase rate was adjusted by the amount of fuel gas, and was approximately 300° C./Hr.

所定温度到達後IHr同温度で保持した。After reaching a predetermined temperature, the IHr was maintained at the same temperature.

焼結体の測定は実施例1と同一の方法で行った。Measurement of the sintered body was performed in the same manner as in Example 1.

表−6にこの結果を示す。Table 6 shows the results.

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

第1図は実施例1の実験/I65のベリクレーズ結晶粒
子経を反射顕微鏡で観察した写真。 第2図は比較例1の実験層12のペリクレーズ結晶粒子
経を反射顕微鏡で観察した写真。 第3図は、実施例1の実験/I67のベリクレーズ結晶
粒子経の粒界を鮮明にするため硝酸で強度にエツチング
し、走査電子顕微鏡で観察した写真であり、焼成体内部
の代表的部分を示し、第4図は、比較例1の実験層15
のペリクレーズ結晶粒子経の粒界を鮮明にするため硝酸
で強度にエツチングし、走査型電子顕微鏡で観察した写
真であり、焼成体内部の代表的部分を示す。
FIG. 1 is a photograph of the Vericlese crystal grain size of Experiment I65 in Example 1 observed with a reflection microscope. FIG. 2 is a photograph of the periclase crystal grain size of the experimental layer 12 of Comparative Example 1 observed with a reflection microscope. Figure 3 is a photograph taken with a scanning electron microscope after intense etching with nitric acid to clarify the grain boundaries of the Vericlese crystal grains of I67 in the experiment of Example 1. 4 shows the experimental layer 15 of Comparative Example 1.
This photograph was taken with a scanning electron microscope after it was strongly etched with nitric acid to make the grain boundaries of the periclase crystal grains clearer, and shows a representative part of the inside of the fired product.

Claims (1)

【特許請求の範囲】 1 酸化マグネシウムの成形体を総圧200 mmHg
以上で水蒸気を25vo1%以上含み、かつ水蒸気分圧
と炭酸ガス分圧との比(H20/C02)が1.7以上
である雰囲気中で焼成することを特徴とするマグネシア
の焼成方法。 2 焼成温度を1400℃以上とすることを特徴とする
特許請求範囲第1項記載のマグネシアの焼成古島 3 5102 t Cab、およびB2O3の含有率が
各々0.04〜0.30重量%、0.35重量%以下、
および0.1重量%以下であり、かつMgOの含有率が
99、3 重量%以上であるマグネシア成形体を用いる
ことを特徴とする特許請求範囲第1項および第2項記載
のマグネシアの焼成方法。 4 成形体の嵩比重が1.3以上であることを特徴とす
る特許請求の範囲第1項、第2項及び第3項記載のマグ
ネシアの焼成古島
[Claims] 1. A molded body of magnesium oxide is heated to a total pressure of 200 mmHg.
A method for firing magnesia, which comprises firing in an atmosphere containing 25 vol % or more of water vapor and having a ratio of water vapor partial pressure to carbon dioxide gas partial pressure (H20/C02) of 1.7 or more. 2. The fired magnesia old island 3 5102 t Cab and B2O3 content of 0.04 to 0.30% by weight and 0.2% by weight, respectively, as set forth in claim 1, characterized in that the firing temperature is 1400°C or higher. 35% by weight or less,
and 0.1% by weight or less, and a magnesia molded body having an MgO content of 99.3% by weight or more. . 4. The calcined old island of magnesia according to claims 1, 2, and 3, characterized in that the bulk specific gravity of the compact is 1.3 or more.
JP54104018A 1979-08-17 1979-08-17 How to fire magnesia Expired JPS5843353B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54104018A JPS5843353B2 (en) 1979-08-17 1979-08-17 How to fire magnesia

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54104018A JPS5843353B2 (en) 1979-08-17 1979-08-17 How to fire magnesia

Publications (2)

Publication Number Publication Date
JPS5632322A JPS5632322A (en) 1981-04-01
JPS5843353B2 true JPS5843353B2 (en) 1983-09-26

Family

ID=14369511

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Application Number Title Priority Date Filing Date
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Country Link
JP (1) JPS5843353B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59190218A (en) * 1983-04-12 1984-10-29 Ube Kagaku Kogyo Kk High-density magnesia clinker and its preparation
JPS59190217A (en) * 1983-04-12 1984-10-29 Ube Kagaku Kogyo Kk High purity magnesium hydroxide and high-density magnesia clinker having coarse crystal size, and their preparation thereof
US4681863A (en) * 1985-07-17 1987-07-21 Ube Chemical Industries Co., Ltd. High-density magnesia-calcia clinker and process for production thereof
JPH068169B2 (en) * 1991-03-30 1994-02-02 宇部化学工業株式会社 High density coarse grain magnesia clinker

Also Published As

Publication number Publication date
JPS5632322A (en) 1981-04-01

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