JPH058143B2 - - Google Patents

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Publication number
JPH058143B2
JPH058143B2 JP61109299A JP10929986A JPH058143B2 JP H058143 B2 JPH058143 B2 JP H058143B2 JP 61109299 A JP61109299 A JP 61109299A JP 10929986 A JP10929986 A JP 10929986A JP H058143 B2 JPH058143 B2 JP H058143B2
Authority
JP
Japan
Prior art keywords
zirconia
particles
raw material
refractories
oxidation
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
JP61109299A
Other languages
Japanese (ja)
Other versions
JPS62265179A (en
Inventor
Shigeo Endo
Kimio Hirata
Noryuki Igarashi
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.)
Saint Gobain TM KK
Original Assignee
Toshiba Monofrax Co 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 Toshiba Monofrax Co Ltd filed Critical Toshiba Monofrax Co Ltd
Priority to JP61109299A priority Critical patent/JPS62265179A/en
Publication of JPS62265179A publication Critical patent/JPS62265179A/en
Publication of JPH058143B2 publication Critical patent/JPH058143B2/ja
Granted legal-status Critical Current

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  • Compositions Of Oxide Ceramics (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は不飽和酸化物の生成という問題を解消
してジルコニア中の酸素をその化学量論割合(高
い酸化度)に維持する方法を開示するもので、原
料とするジルコニア源の大部分が極めて微細な一
次粒子又はその凝集したものからなり、その比表
面積が極めて大きいものであるジルコニア含有電
鋳耐火物の製造法に関する。 〔従来の技術〕 ジルコニア含有電鋳耐火物は大別してジルコニ
ア(ZrO2)を33〜41%を含有するいわゆるAZS
耐火物と、95%前後のZrO2を含有するZrO2耐火
物の2種類がある。 これ等の耐火物に用いられるZrO2の原料は、
一般に100μm以上の粒状のものが使用されてい
る。即ち天然鉱物であるジルコンサンドやパツデ
レアウト等及び人造鉱物の電融ジルコニアがこれ
に相当するものである。これ等の原料は粒子径が
大きい上、何れも極めて緻密な結晶粒である。ま
れにジルコンサンドにアルカリまたはアルカリ土
類金属酸化物を加えて加熱分解し、それを酸処
理、中和処理等の化学処理を経てつくつた微粉の
ジルコニア源をAZS耐火物の原料として用いら
れたこともあるが、本発明の効果を期待したもの
でもなく、さらに本発明の構成にも属するもので
はなかつた。 AZS耐火物の製法では特公昭36−5375号公報
で開示されたロングアーク法に代表される酸化雰
囲気溶融法が今日では一般化して、酸化度の高い
AZS耐火物が製造されている。 また、さらに特開昭58−179536号公報に開示さ
れた酸化性鋳型を併用すると、高い酸化度を確実
に維持することができる。(鋳造後の還元を防止
し得る) 一方、ZrO2耐火物は前述酸化雰囲気溶融法で
も十分に高い酸化度を保ち得ず、しかも黒鉛型に
鋳造するため還元を受けて灰黒色の製品となる。 一般に、ZrO2は高温でも極めて安定な酸化物
であると思われているが、その融点に近い高温で
は炭素や一酸化炭素に接するとその一部の酸素を
失つて不飽和酸化物となり易い。 前述の酸化雰囲気溶融法は、これを防止する一
方法ではあるが、酸化の程度が溶融毎に少しづつ
異なり、製品のバラツキが生じ易い。また、
ZrO2耐火物の場合には余りにも多量のZrO2を含
有しており、酸化雰囲気溶融法では十分な酸化状
態を保つことができない。 このように黒の着色した還元状態の耐火物は、
ガラス溶融窯に用いられて溶融ガラスと接したと
きガラスを還元しながらガラス中へ泡を放出す
る。 黒く着色した還元状態の耐火物を、一たん酸化
雰囲気中で熱処理(例えば1450℃)すると、通常
明るい褐色または黄色に変り、溶融ガラスに接し
ても泡を発生させることはない。前述の酸化雰囲
気溶融−酸化性鋳型によるAZS耐火物は前述の
熱処理品と同等の性質を有する。 〔発明が解決しようとする課題〕 本発明は上述の還元即ち不飽和酸化物の生成と
いう問題を解消し、ジルコニア中の酸素をその化
学量論割合(高い酸化度)に維持する方法を提供
するものである。 〔課題を解決するための手段〕 本発明は、ジルコニア原料粒子を含む溶融鋳造
してジルコニア含有電鋳耐火物を製造する方法に
おいて、平均一次粒子径が1μm以下の微粒子ま
たはこれ等が凝集した顆粒状のものであつて、そ
の比表面積が1平方メートル/グラム以上である
ジルコニア原料粒子を全ジルコニア原料の90%以
上用いて、ジルコニア原料粒子の表面に酸化性ガ
スを吸着させ溶融に際して酸化雰囲気を形成し電
鋳耐火物を酸化度の高い白色または黄色または褐
色にすることを特徴とするジルコニア含有電鋳耐
火物の製造法を要旨としている。 〔作用〕 本発明はジルコニア源の大部分を個々の一次粒
子が極めて微細な粒子よりなり、その比表面積が
大きいものとするものである。このような微粒子
の表面には空気中の酸素或いは酸化剤として添加
される副原料である硝酸塩の分解により生じた硝
酸等の酸化性ガスを吸着し、溶融に際して酸化雰
囲気を形成する。これ等の微粒子は断熱性が優れ
ているため溶融に先立つて予熱を受けて吸着ガス
を放出する機会が少なく吸着ガスが有効に作用す
る。 本発明で使用するジルコニア源微粒子の径は、
およそ1μm以下のものである。好ましくはこれ
等が顆粒状で凝集したものがよい。微粒子のみで
はアークの衝撃により飛散し、原料の歩留りが低
下し作業環境を悪化させる。この原料の比表面積
は少なくとも1平方メートル/グラムであるべき
である。好ましくは5平方メートル/グラム以上
であれば常に安定した酸化状態が得られる。 これ等のジルコニア源はジルコニア単味でも、
シリカ或いはアルミナを結合、または混合したも
のでも差支えない。 微粒子の形成方法は化学薬品の如き化学的処理
に経由しても、ボールミルの如き機械的方法によ
つても良いが、好ましくは前者の方法がよい。
(大きな比表面積を得る上で)好ましくは、全て
のジルコニア源を上述の微粒子の原料とすべきで
あるが、機械的粉砕法による場合や経済的理由な
ども考慮して10%程度のより粗い粒子、またはよ
り小さい比表面積の粒子の混入も可能である。こ
れが10%を超えると還元を受けた灰色のジルコニ
ア耐火物が生成する。 〔実施例〕 本発明の実施例について説明する。 実施例 次の如き粒子径および比表面積の原料を使用し
た。 Γ微粒ジルコニア A;新日本金属化学社製Z−999 二次粒子径:2μm 一次粒子径:0.1μm 比評面積:15m2/g B;南アフリカ産バツデイアイト鉱を特開昭56
−32385号により塩化精製処理後、微粉砕し
たもの 粒子径:1μm 比表面積:1.7m2/g Γジルコンサンド(オーストラリア産) 粒子径:100μm以上 比表面積:0.01m2/g以下 Γアルミナ C;住友化学工業社製A−21 二次粒子径:40μm 一次粒子径:3μm 比表面積:0.6m2/g D;住友化学工業社製A−HPS30 一次粒子径:0.3μm 中心粒子径:0.4μm 比表面積:6m2/g 表−1の如き原料を配合し、300KVAアーク炉
で溶融し、黒鉛型に鋳造した。鋳造後30分後に離
型し、アルミナ粉中に徐冷した。2日後鋳造体を
取り出し切断して試料を得た。 微粉ジルコニア源を全ジルコニア源の90%以上
とした場合(実施例1〜3)に酸化度の高いジル
コニア耐火物を得た。その試料の色調は熱処理に
よつても変らなかつた。 逆に10%以上の粗粒で、比表面積の小さいジル
コニア源を用いると(参考例)灰色になり熱処理
して初めて本来の純白色に変つた。
[Industrial Application Field] The present invention discloses a method for solving the problem of the formation of unsaturated oxides and maintaining oxygen in zirconia at its stoichiometric ratio (high oxidation degree). The present invention relates to a method for producing a zirconia-containing electrocast refractory in which most of the zirconia source is composed of extremely fine primary particles or aggregates thereof and has an extremely large specific surface area. [Prior art] Zirconia-containing electrocast refractories are broadly classified into so-called AZS containing 33 to 41% zirconia (ZrO 2 ).
There are two types: refractories and ZrO 2 refractories containing around 95% ZrO 2 . The raw material for ZrO 2 used in these refractories is
Generally, particles with a size of 100 μm or more are used. That is, natural minerals such as zircon sand and patudereout, and artificial minerals such as fused zirconia correspond to this. These raw materials have large particle sizes and all have extremely dense crystal grains. In rare cases, a fine powder zirconia source produced by adding an alkali or alkaline earth metal oxide to zircon sand, thermally decomposing it, and then chemically treating it with acid and neutralization is used as a raw material for AZS refractories. However, the effect of the present invention was not expected, and furthermore, it did not belong to the structure of the present invention. In the production of AZS refractories, the oxidizing atmosphere melting method, represented by the long arc method disclosed in Japanese Patent Publication No. 36-5375, has become commonplace today, resulting in a high degree of oxidation.
AZS refractories are manufactured. In addition, when the oxidizing template disclosed in JP-A-58-179536 is used in combination, a high degree of oxidation can be reliably maintained. (Reduction after casting can be prevented.) On the other hand, ZrO 2 refractories cannot maintain a sufficiently high degree of oxidation even with the oxidizing atmosphere melting method mentioned above, and furthermore, because they are cast into graphite molds, they undergo reduction and become gray-black products. . Generally, ZrO 2 is considered to be an extremely stable oxide even at high temperatures, but when it comes into contact with carbon or carbon monoxide at high temperatures close to its melting point, it tends to lose some of its oxygen and become an unsaturated oxide. The aforementioned oxidizing atmosphere melting method is one way to prevent this, but the degree of oxidation differs slightly each time it is melted, and product variations are likely to occur. Also,
In the case of ZrO 2 refractories, they contain too much ZrO 2 and cannot maintain a sufficient oxidation state using the oxidizing atmosphere melting method. In this way, the black-colored refractory in the reduced state is
When used in glass melting kilns, when it comes into contact with molten glass, it reduces the glass and releases bubbles into the glass. Once a black-colored refractory in a reduced state is heat-treated in an oxidizing atmosphere (for example, at 1,450°C), it usually turns light brown or yellow, and does not generate bubbles when it comes into contact with molten glass. The AZS refractory manufactured by the above-mentioned oxidizing atmosphere melting-oxidizing mold has properties equivalent to the above-mentioned heat-treated products. [Problems to be Solved by the Invention] The present invention solves the above-mentioned problem of reduction, that is, the formation of unsaturated oxides, and provides a method for maintaining oxygen in zirconia at its stoichiometric ratio (high degree of oxidation). It is something. [Means for Solving the Problems] The present invention provides a method for producing zirconia-containing electrocast refractories by melt casting containing zirconia raw material particles, and in which fine particles having an average primary particle size of 1 μm or less or granules in which these are aggregated are used. Using 90% or more of the total zirconia raw material, zirconia raw material particles having a specific surface area of 1 square meter/gram or more are used to adsorb oxidizing gas on the surface of the zirconia raw material particles to form an oxidizing atmosphere during melting. The gist of this paper is a method for producing zirconia-containing electrocast refractories, which is characterized by making the electrocast refractories white, yellow, or brown with a high degree of oxidation. [Function] In the present invention, most of the zirconia source is made up of extremely fine individual primary particles and has a large specific surface area. The surface of such fine particles adsorbs oxygen in the air or oxidizing gas such as nitric acid generated by decomposition of nitrate, which is an auxiliary raw material added as an oxidizing agent, and forms an oxidizing atmosphere during melting. Since these fine particles have excellent heat insulating properties, there is little chance of releasing the adsorbed gas through preheating prior to melting, allowing the adsorbed gas to act effectively. The diameter of the zirconia source fine particles used in the present invention is
It is approximately 1 μm or less. Preferably, these are aggregated in granular form. If only fine particles are used, they will be scattered by the impact of the arc, reducing the yield of raw materials and deteriorating the working environment. The specific surface area of this raw material should be at least 1 square meter/gram. Preferably, a stable oxidation state can be obtained at 5 square meters/gram or more. These zirconia sources can be made of zirconia alone,
A combination or mixture of silica or alumina may also be used. The fine particles may be formed by a chemical treatment such as using chemicals or by a mechanical method such as a ball mill, but the former method is preferred.
Preferably, all the zirconia sources should be used as raw materials for the above-mentioned fine particles (in order to obtain a large specific surface area), but if mechanical grinding is used or for economic reasons, coarser particles of about 10% should be used. The incorporation of particles or particles of smaller specific surface area is also possible. When this exceeds 10%, a gray zirconia refractory is produced after undergoing reduction. [Example] An example of the present invention will be described. Examples Raw materials having the following particle diameters and specific surface areas were used. Γ fine-grained zirconia A: Z-999 manufactured by Nippon Metal Chemical Co., Ltd. Secondary particle size: 2 μm Primary particle size: 0.1 μm Relative area: 15 m 2 /g B: South African batdayite ore, published in 1983
- Finely ground after chlorination purification according to No. 32385 Particle size: 1 μm Specific surface area: 1.7 m 2 /g Γ Zircon Sand (produced in Australia) Particle size: 100 μm or more Specific surface area: 0.01 m 2 /g or less Γ Alumina C; Sumitomo Chemical Co., Ltd. A-21 Secondary particle size: 40 μm Primary particle size: 3 μm Specific surface area: 0.6 m 2 /g D; Sumitomo Chemical Co., Ltd. A-HPS30 Primary particle size: 0.3 μm Center particle size: 0.4 μm Ratio Surface area: 6 m 2 /g The raw materials shown in Table 1 were blended, melted in a 300 KVA arc furnace, and cast into a graphite mold. The mold was released 30 minutes after casting and slowly cooled in alumina powder. Two days later, the cast body was taken out and cut to obtain a sample. Zirconia refractories with a high degree of oxidation were obtained when the fine powder zirconia source accounted for 90% or more of the total zirconia source (Examples 1 to 3). The color tone of the sample remained unchanged by heat treatment. On the other hand, when a zirconia source with coarse grains of 10% or more and a small specific surface area was used (reference example), it turned gray and only changed to its original pure white color after heat treatment.

【表】【table】

〔発明の効果〕〔Effect of the invention〕

本発明の方法によると高い酸化度(ZrO2の化
学量論割合の酸素を含む)のジルコニア含有電鋳
耐火物を得ることができる。 酸化物(状態)は試料の色により容易に判断す
ることができる。Fe、Ti、Cu、Cr、Mn等の不
純物の酸化物の総量が0.05%以下であり、高い酸
化度であれば純白色であり、還元を受けた場合灰
色になる。灰色の試料は空気中で熱処理して酸化
すると純白色に変る。 前述の不純物をより多く含み還元されたZrO2
耐火物は灰色に呈し、酸化状態のものは明るい黄
色ないし褐色となる。高い酸化度の耐火物は、酸
化熱処理によつて色調に大きな変化はない。灰色
ないし黒色の耐火物は溶融ガラスに接するとガラ
スを還元してガラス中に発泡する欠点を持つが本
発明によりこの欠点が解消された。
According to the method of the present invention, a zirconia-containing electrocast refractory with a high degree of oxidation (containing oxygen in a stoichiometric proportion of ZrO 2 ) can be obtained. The oxide (state) can be easily determined by the color of the sample. The total amount of oxides of impurities such as Fe, Ti, Cu, Cr, Mn, etc. is 0.05% or less, and if the degree of oxidation is high, the color is pure white, and if it is reduced, it becomes gray. When a gray sample is heat-treated and oxidized in air, it turns pure white. Reduced ZrO 2 containing more of the aforementioned impurities
Refractories appear gray, while those in an oxidized state become bright yellow to brown. Refractories with a high degree of oxidation do not undergo significant changes in color tone through oxidation heat treatment. Gray or black refractories have the disadvantage that when they come into contact with molten glass, they reduce the glass and cause bubbles to form in the glass, but this disadvantage has been overcome by the present invention.

Claims (1)

【特許請求の範囲】[Claims] 1 ジルコニア原料粒子を含む原料を溶融鋳造し
てジルコニア含有電鋳耐火物を製造する方法にお
いて、平均一次粒子径が1μm以下の微粒子また
はこれ等が凝集した顆粒状のものであつて、その
比表面積が1平行メートル/グラム以上であるジ
ルコニア原料粒子を全ジルコニア原料の90%以上
用いて、ジルコニア原料粒子の表面に酸化性ガス
を吸着させ、溶融に際して酸化雰囲気を形成し、
電鋳耐火物を酸化度の高い白色または黄色または
褐色にすることを特徴とするジルコニア含有電鋳
耐火物の製造法。
1. In the method of manufacturing zirconia-containing electrocast refractories by melting and casting raw materials containing zirconia raw material particles, fine particles with an average primary particle size of 1 μm or less or granular aggregates of these particles, whose specific surface area Using 90% or more of all zirconia raw materials, zirconia raw material particles having a diameter of 1 parallel meter/gram or more, adsorbing an oxidizing gas on the surface of the zirconia raw material particles, and forming an oxidizing atmosphere during melting,
A method for producing a zirconia-containing electrocast refractory, which is characterized by making the electrocast refractory white, yellow, or brown with a high degree of oxidation.
JP61109299A 1986-05-12 1986-05-12 Manufacture of zirconia-containing electrocast refractories Granted JPS62265179A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61109299A JPS62265179A (en) 1986-05-12 1986-05-12 Manufacture of zirconia-containing electrocast refractories

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61109299A JPS62265179A (en) 1986-05-12 1986-05-12 Manufacture of zirconia-containing electrocast refractories

Publications (2)

Publication Number Publication Date
JPS62265179A JPS62265179A (en) 1987-11-18
JPH058143B2 true JPH058143B2 (en) 1993-02-01

Family

ID=14506662

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61109299A Granted JPS62265179A (en) 1986-05-12 1986-05-12 Manufacture of zirconia-containing electrocast refractories

Country Status (1)

Country Link
JP (1) JPS62265179A (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5912619B2 (en) * 1980-03-18 1984-03-24 旭硝子株式会社 High zirconia hot melt refractories
JPS6051663A (en) * 1983-08-29 1985-03-23 東芝モノフラツクス株式会社 Thermal impact resistant zirconia electroforming refractories
JPS60103035A (en) * 1983-11-04 1985-06-07 Nippon Mining Co Ltd Manufacture of fine zirconium oxide powder

Also Published As

Publication number Publication date
JPS62265179A (en) 1987-11-18

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