JPH04310560A - Production of magnesia-carbon brick - Google Patents

Production of magnesia-carbon brick

Info

Publication number
JPH04310560A
JPH04310560A JP3071122A JP7112291A JPH04310560A JP H04310560 A JPH04310560 A JP H04310560A JP 3071122 A JP3071122 A JP 3071122A JP 7112291 A JP7112291 A JP 7112291A JP H04310560 A JPH04310560 A JP H04310560A
Authority
JP
Japan
Prior art keywords
magnesia
raw material
viscosity
phenol resin
resin
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.)
Pending
Application number
JP3071122A
Other languages
Japanese (ja)
Inventor
Takao Okamoto
孝雄 岡本
Norio Kojima
児島 憲生
Kenji Imai
健二 今井
Daijiro Nishimura
西村 大二郎
Kenichi Samejima
鮫島 健一
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.)
DIC Corp
JFE Refractories Corp
Original Assignee
Kawasaki Refractories Co Ltd
Dainippon Ink and Chemicals 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 Kawasaki Refractories Co Ltd, Dainippon Ink and Chemicals Co Ltd filed Critical Kawasaki Refractories Co Ltd
Priority to JP3071122A priority Critical patent/JPH04310560A/en
Publication of JPH04310560A publication Critical patent/JPH04310560A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To produce a magnesia.carbon brick using a novolak type phenolic resin mixable and moldable at normal temperature as a binder without requiring an aging period after kneading. CONSTITUTION:A compound comprising magnesia raw material, a carbonaceous raw material and a metal powder raw material is kneaded with a liquid mixture of a resol type phenol resin and a novolak type phenol resin in a blending ratio of 5/95 to 15/85 as an organic binder to give body, which is molded at normal temperature while reducing pressure.

Description

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

【0001】0001

【産業上の利用分野】本発明は、耐火れんがに関し、特
に不焼成マグネシア・カーボンれんがの製造方法に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to refractory bricks, and more particularly to a method for producing unfired magnesia carbon bricks.

【0002】0002

【従来の技術】マグネシア・カーボンれんがは、マグネ
シア質原料と、例えば黒鉛等の炭素原料に有機結合剤を
添加して混練・成形した後、不焼成品では約200℃程
度の比較的低温の下で乾燥して得られる。こうした不焼
成マグネシア・カーボンれんがは、転炉、電気炉、二次
精錬取鍋等の溶融金属容器の内張り用耐火物として広く
利用され、特にスラグや溶融金属に対する濡れ難さや熱
伝導率の高さといった上記炭素原料が、スラグや溶融金
属の稼働面からの浸透を抑制し、過焼結を防止する作用
を有するところから、優れた耐食性、耐スポーリング性
を備える。
[Prior art] Magnesia carbon bricks are made by adding an organic binder to magnesia raw materials and carbon raw materials such as graphite, kneading and forming them, and then molding them at a relatively low temperature of about 200°C for unfired products. Obtained by drying. These unfired magnesia carbon bricks are widely used as refractories for lining molten metal containers such as converters, electric furnaces, and secondary smelting ladles. The above-mentioned carbon raw material has the effect of suppressing the penetration of slag and molten metal from the working surface and preventing oversintering, and therefore has excellent corrosion resistance and spalling resistance.

【0003】さらに、上記マグネシア・カーボンれんが
に耐酸化性を付与するために、例えばAl粉末や、特公
昭61−303号公報で開示されたMg−Al合金を原
料中に添加することが行われている。また、上記有機結
合剤としてはフェノール樹脂が汎用されており、原料に
所定の粘度を付与し、成形を行いやすくするとともに、
炉の稼働時に受ける熱で揮発分が消失して組織内に炭素
成分を残留させて上記炭素質原料の作用を補完する役割
も果たす。このような有機結合剤としてフェノール樹脂
を用いる場合、残炭率、すなわち組織内に残留する炭素
成分の重量比率を40%程度として、添加量は外掛け3
.5〜4.0重量%とするのが一般的である。このよう
なフェノール樹脂としては熱硬化性を有するとともに常
温で比較的低い粘度のレゾール型と、常温下で粘度が高
く、そのために原料を加熱しながら混練が行われるノボ
ラック型の2種類がある。
Furthermore, in order to impart oxidation resistance to the above-mentioned magnesia carbon bricks, for example, Al powder or the Mg-Al alloy disclosed in Japanese Patent Publication No. 61-303 is added to the raw materials. ing. In addition, phenolic resin is commonly used as the organic binder, and it imparts a predetermined viscosity to the raw material, making it easier to mold, and
The heat received during operation of the furnace causes the volatile matter to disappear, leaving carbon components remaining in the structure, which also plays the role of supplementing the action of the carbonaceous raw material. When using phenolic resin as such an organic binder, the residual carbon content, that is, the weight ratio of the carbon component remaining in the structure, is set to be about 40%, and the amount added is the external multiplication factor of 3.
.. The content is generally 5 to 4.0% by weight. There are two types of such phenolic resins: resol type, which has thermosetting properties and a relatively low viscosity at room temperature, and novolac type, which has high viscosity at room temperature and is therefore kneaded while heating the raw materials.

【0004】0004

【発明が解決しようとする課題】ところで、上記レゾー
ル型のフェノール樹脂の常温下における粘度は低いが、
混練後の坏土中にあっては原料中のMg又はFeと該フ
ェノール樹脂との間でキレート反応が起こり、該坏土の
粘性は混練後からの時間の経過とともに次第に上昇する
。従って、混練直後に成形を行った場合では、原料の粘
性が低過ぎて成形時にラミネーションが発生する恐れが
ある一方で、混練後、時間が経ちすぎると、坏土は乾い
た状態(バインダーの粘性が上がりすぎて、外観上バイ
ンダー不足の状態)を呈するところから、坏土が混練後
から成形に適した状態となるまでの時間(熟成時間)を
適切に設定する必要がある。この熟成時間は採用したレ
ゾール型のフェノール樹脂の個々の特性、使用時の気温
及び湿度、ミキサーからの排出された坏土温度等の種々
のファクターに左右され、このようなファクターを勘案
して最適な熟成時間を算出・設定するという、煩雑さが
求められる。
[Problems to be Solved by the Invention] By the way, although the viscosity of the above-mentioned resol type phenolic resin at room temperature is low,
In the clay after kneading, a chelate reaction occurs between Mg or Fe in the raw materials and the phenol resin, and the viscosity of the clay gradually increases with the passage of time after kneading. Therefore, if molding is performed immediately after kneading, the viscosity of the raw materials may be too low and lamination may occur during molding. On the other hand, if too much time has passed after kneading, the clay will be in a dry state (the viscosity of the binder The time (ripening time) required for the clay to reach a state suitable for molding after kneading must be appropriately set to prevent the appearance of a binder shortage due to excessive increase in the amount of binder. This aging time depends on various factors such as the individual characteristics of the resol-type phenolic resin used, the temperature and humidity during use, and the temperature of the clay discharged from the mixer, and is determined optimally by taking these factors into consideration. The complexity of calculating and setting the appropriate ripening time is required.

【0005】さらにレゾール型のフェノール樹脂は熱硬
化性を有するため、該レゾール型のフェノール樹脂の製
造に際しては厳密な温度管理が要求されるとともに、保
管に際しても例えば15℃以下に保たれた保冷室内で保
管する必要があり、その上、25℃程度の条件で保管さ
れた場合でも可使用期間は、通常1カ月程度と短かかっ
た。
Furthermore, since resol-type phenolic resins have thermosetting properties, strict temperature control is required when producing the resol-type phenolic resins, and storage in a cold storage room kept at 15°C or lower is also necessary. Furthermore, even when stored at a temperature of about 25°C, the usable life was usually as short as about one month.

【0006】一方、ノボラック型のフェノール樹脂は、
熱可塑性であるため、加熱混練が可能であるが、一般に
液状であっても硬化剤としてヘキサミンを添加して40
%の残炭率とするためには必然的に常温での粘性が高く
なり、上記のようにミキサー等の混練手段に加熱装置を
設ける必要がある。また、上記特公昭61−303号公
報で開示されたように、酸化防止剤として特に活性なM
gを含むMg−Al合金の引火点は535℃と、従来の
Al粉末単体の引火点650℃に比べて低いために加熱
混練を行った場合には引火する危険があった。
On the other hand, novolac type phenolic resins are
Because it is thermoplastic, it can be heated and kneaded, but even if it is liquid, it is generally mixed with hexamine as a hardening agent.
%, the viscosity at room temperature inevitably increases, and as mentioned above, it is necessary to provide a heating device to the kneading means such as a mixer. In addition, as disclosed in the above-mentioned Japanese Patent Publication No. 61-303, M, which is particularly active as an antioxidant,
The flash point of the Mg-Al alloy containing g is 535° C., which is lower than the flash point of conventional Al powder alone, 650° C., so there is a risk of ignition when heated and kneaded.

【0007】さらに上記ノボラック型のフェノール樹脂
を結合剤とする不焼成マグネシア・カーボンれんがの成
形時には、坏土中に存在する空気を排出するためにプレ
ス等の加圧・成形手段にも坏土を加熱して粘性を低くす
るための加熱装置を備える必要があった。このような事
情から発明者らは、種々の実験の結果、常温で混練可能
なマグネシア・カーボンれんがの製造に用いられるノボ
ラック型フェノールレジンの具備すべき条件として、粘
度      1000〜2000  cps  (2
5℃)不揮発分  70±2% 残炭率    40±2% とすることが望ましいとの知見を得たが、粘度を低下さ
せようとすると最終製品の耐火物の強度特性を確保する
ための不揮発分、残炭率までが上記範囲未満の値にまで
低下し、実用に適さないこととなってしまう。
Furthermore, when molding unfired magnesia carbon bricks using the above novolac type phenolic resin as a binder, the clay is also used in the pressurizing/forming means such as a press in order to exhaust the air present in the clay. It was necessary to provide a heating device to heat the product and lower its viscosity. Under these circumstances, as a result of various experiments, the inventors determined that the novolac type phenol resin used for producing magnesia carbon bricks, which can be kneaded at room temperature, should have a viscosity of 1000 to 2000 cps (2
5°C) It was found that it is desirable to set the non-volatile content to 70 ± 2% and the residual carbon content to 40 ± 2%, but when trying to lower the viscosity, it is necessary to The residual carbon content and the residual carbon content decrease to a value below the above-mentioned range, making it unsuitable for practical use.

【0008】本発明は上記の事情に鑑みて提案されたも
のであって、混練後の熟成期間を必要とすることなく、
常温下で混練・成形を行うことのできるノボラック型の
フェノール樹脂を結合剤とした不焼成マグネシア・カー
ボンれんがの製造方法を提供することを目的とする。
The present invention was proposed in view of the above circumstances, and does not require a maturing period after kneading.
The object of the present invention is to provide a method for producing unfired magnesia carbon bricks using a novolac type phenolic resin as a binder, which can be kneaded and molded at room temperature.

【0009】[0009]

【課題を解決するための手段】上記の目的を達成するた
めに本発明は以下の手段を採用する。すなわち、マグネ
シア質原料、炭素質原料、金属粉末原料からなる組成物
に、有機結合剤として混合比が5/95〜15/85の
範囲にあるレゾール型フェノール樹脂とノボラック型の
フェノール樹脂の液状混合物を添加して、混練し、得ら
れた坏土を減圧を行いながら常温下で成形を行う構成と
する。
[Means for Solving the Problems] In order to achieve the above object, the present invention employs the following means. That is, a liquid mixture of a resol type phenolic resin and a novolac type phenolic resin in a mixing ratio of 5/95 to 15/85 as an organic binder is added to a composition consisting of a magnesia raw material, a carbonaceous raw material, and a metal powder raw material. is added, kneaded, and the resulting clay is molded at room temperature while applying reduced pressure.

【0010】0010

【作  用】上記本発明の構成によれば、ノボラック型
のフェノール樹脂をベースとして、5〜15重量%のレ
ゾール型のフェノール樹脂を配合することにより、不揮
発分、固定炭素を低下させることなく、粘度を低下させ
ることができる。この場合、レゾール型及びノボラック
型のフェノール樹脂、各々の粘度、不揮発分、残炭率は
下記の表1に示す条件とすることが望ましい。尚、表1
においてノボラック型のフェノール樹脂の残炭率は硬化
剤としてヘキサミンを添加した状態での値を示し、例え
ばヘキサミンを該ノボラック型のフェノール樹脂に対し
て7重量%添加した状態で表記範囲の残炭率が得られる
[Function] According to the above structure of the present invention, by blending 5 to 15% by weight of resol type phenol resin with novolac type phenol resin as a base, the nonvolatile content and fixed carbon are not reduced. Can reduce viscosity. In this case, it is desirable that the viscosity, nonvolatile content, and residual carbon content of the resol type and novolac type phenolic resins be as shown in Table 1 below. Furthermore, Table 1
The residual carbon percentage of a novolac type phenolic resin is the value when hexamine is added as a curing agent.For example, when 7% by weight of hexamine is added to the novolac type phenolic resin, the residual carbon percentage within the stated range is is obtained.

【0011】[0011]

【表1】[Table 1]

【0012】又、レゾール型のフェノール樹脂とノボラ
ック型のフェノール樹脂との混合比は5/95〜15/
85であることが望ましく、レゾール型のフェノール樹
脂が上記範囲よりも過多となると、該レゾール型のフェ
ノール樹脂の欠点が表れて、ミキサーから排出した後、
時間の経過と共に坏土の乾きが顕著であり、熟成時間の
設定が必要となり、上記範囲よりも過少であると粘度の
低下が顕れず本発明の所期の効果が発揮されない。
[0012] Furthermore, the mixing ratio of resol type phenolic resin and novolak type phenolic resin is 5/95 to 15/
85 is desirable, and if the amount of resol type phenolic resin exceeds the above range, the drawbacks of the resol type phenolic resin will appear, and after discharging from the mixer,
As time passes, the clay noticeably dries out, making it necessary to set a ripening time.If the maturing time is less than the above range, the viscosity will not decrease and the desired effect of the present invention will not be exhibited.

【0013】さらに上記特性を有する本発明にかかる不
焼成マグネシア・カーボンれんがの成形時には、坏土の
中へ巻き込んだ空気を抜きながら成形することにより、
低気孔率の緻密な成形体を得ることができる。この場合
、成形手段としては例えば真空脱気式プレスを使用する
ことが最も望ましい。
Furthermore, when molding the unfired magnesia carbon brick according to the present invention having the above-mentioned characteristics, by molding while removing air trapped in the clay,
A dense molded body with low porosity can be obtained. In this case, it is most desirable to use, for example, a vacuum degassing press as the molding means.

【0014】[0014]

【実施例】以下、本発明に関し実施例をもとに説明する
。 =実施例1= 表2に示す配合で不焼成マグネシア・カーボンれんがの
試料を作成した。表2において、マグネシアクリンカー
の微粒、Mg−Al合金粉末、ヘキサメチレンテトラミ
ンと共に添加量が少量なので各々秤量したものを合わせ
て予め予備混合して混練した。
EXAMPLES The present invention will be explained below based on examples. =Example 1= Samples of unfired magnesia carbon bricks were prepared using the formulations shown in Table 2. In Table 2, since the amounts added together with magnesia clinker fine particles, Mg-Al alloy powder, and hexamethylenetetramine were small, the respective weights were combined, premixed, and kneaded.

【0015】また、有機結合剤として添加したフェノー
ル樹脂は本発明の適用品ではレゾール型とノボラック型
の混合割合を10/90とし、該ノボラック型のフェノ
ール樹脂に対して約11%のヘキサメチレンテトラミン
を添加した。一方、従来品では100%レゾール型のフ
ェノール樹脂を採用した。このような配合の従来品では
混練の後の熟成時間を4時間、24時間、48時間とし
て成形を行ったが、従来品では熟成時間が4時間ではラ
ミネーションが発生し、48時間では坏土が硬化してと
もに成形することができなかった。また、本発明の適用
品では熟成時間を4時間、24時間として真空脱気式プ
レスを使用し、減圧条件60トールで成形を行った。
In addition, the phenol resin added as an organic binder has a mixing ratio of resol type and novolac type in the product of the present invention of 10/90, and about 11% hexamethylenetetramine with respect to the novolak type phenol resin. was added. On the other hand, the conventional product uses 100% resol type phenolic resin. Conventional products with such a composition were molded with aging times of 4 hours, 24 hours, and 48 hours after kneading, but with conventional products, lamination occurred when the aging time was 4 hours, and the clay formed after 48 hours. It hardened and could not be molded together. In addition, in the products to which the present invention was applied, the aging time was 4 hours and 24 hours, and a vacuum degassing press was used and molding was performed under reduced pressure conditions of 60 torr.

【0016】表3は、本発明の適用品(熟成時間4、2
4時間)と従来品(熟成時間24時間)の成形体の各物
性の測定値を示す。表3に見られる通り本発明の適用品
と従来品との間に顕著な差異は認められず、特に真空式
脱気プレスを使用したために圧縮強さ、曲げ強さは本発
明の適用品がやや高い値を示している。また、従来品と
本発明の適用品を40t容量の取鍋のスラグラインに張
り合わせ使用したところ、20チャージの操業後で両者
の間に残厚の差はみられなかった。
Table 3 shows the products to which the present invention is applied (aging times 4, 2
4 hours) and the conventional product (aging time 24 hours) are shown below. As seen in Table 3, there was no noticeable difference between the products to which the present invention was applied and the conventional products, and in particular, due to the use of a vacuum degassing press, the products to which the present invention was applied had lower compressive strength and bending strength. It shows a slightly high value. Further, when the conventional product and the product to which the present invention was applied were laminated together on a slag line of a ladle with a capacity of 40 tons, no difference in residual thickness was observed between the two after 20 charges of operation.

【0017】[0017]

【表2】[Table 2]

【0018】[0018]

【表3】[Table 3]

【0019】=実施例2= 実施例1で用いた本発明の適用品、及び従来品で使用し
たフェノール樹脂(初期粘度300cps)を50℃の
恒温槽に入れてその粘度の経時変化を測定したところ、
本発明に係るレゾール型とノボラック型を混合したフェ
ノール樹脂では4ヶ月間粘度変化がなかったのに対し、
従来のレゾール型単体のフェノール樹脂では2週間後に
既に3000cpsにまで粘度が上昇し、不焼成マグネ
シア・カーボンれんがの有機結合剤として適用できる限
界を逸脱していた。
= Example 2 = The applied product of the present invention used in Example 1 and the phenol resin (initial viscosity 300 cps) used in the conventional product were placed in a constant temperature bath at 50°C and the change in viscosity over time was measured. However,
Whereas the phenol resin, which is a mixture of resol type and novolac type according to the present invention, did not exhibit any viscosity change for 4 months,
The viscosity of the conventional resol-type single phenol resin had already increased to 3000 cps after two weeks, which exceeded the limit of its applicability as an organic binder for unfired magnesia carbon bricks.

【0020】[0020]

【発明の効果】以上のように本発明によると、常温での
混練が可能であるので、引火性、爆発性の強い酸化防止
剤(例Mg−Al合金)も安全に混練でき、レゾール型
のフェノール樹脂を適用した場合に必要とされた煩雑な
熟成時間の設定が不要となるばかりか、混練直後にも成
形が可能であるのでリードタイムを短縮することができ
る。この場合の減圧しながら成形を行うとより緻密な耐
火物を製造することができる。
As described above, according to the present invention, it is possible to knead at room temperature, so even highly flammable and explosive antioxidants (e.g. Mg-Al alloy) can be safely kneaded. Not only is it unnecessary to set a complicated aging time that is required when phenolic resin is used, but also molding can be performed immediately after kneading, so lead time can be shortened. In this case, if the molding is performed under reduced pressure, a denser refractory can be manufactured.

【0021】さらに本発明の有機結合剤では保存性が向
上し、保管に特別の注意は不要となる効果を有するなど
、その産業上の利用価値は大いに高まる。
Furthermore, the organic binder of the present invention has the effect of improving storage stability and requiring no special precautions during storage, greatly increasing its industrial utility value.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】  マグネシア質原料、炭素質原料、金属
粉末原料からなる組成物に、有機結合剤として混合比が
5/95〜15/85の範囲にあるレゾール型のフェノ
ール樹脂とノボラック型のフェノール樹脂との液状混合
物を添加して、混練し、得られた坏土を減圧を行いなが
ら常温下で成形することを特徴とするマグネシア・カー
ボンれんがの製造方法。
Claim 1: A composition consisting of a magnesia raw material, a carbonaceous raw material, and a metal powder raw material, and a resol type phenol resin and a novolac type phenol as organic binders in a mixing ratio of 5/95 to 15/85. A method for producing magnesia carbon bricks, which comprises adding a liquid mixture with a resin, kneading the mixture, and molding the resulting clay at room temperature while applying reduced pressure.
【請求項2】  硬化剤としてヘキサミンを添加した上
記ノボラック型フェノール樹脂の25℃での粘度が30
000〜50000cps、不揮発分が70±2%、固
定炭素が40±2%であり、レゾール型フェノール樹脂
の25℃での粘度が250〜350cps、不揮発分が
70±2%、固定炭素が40±2%としたことを特徴と
する請求項1に記載のマグネシア・カーボンれんがの製
造方法。
[Claim 2] The viscosity at 25° C. of the novolac type phenolic resin to which hexamine is added as a curing agent is 30.
000 to 50,000 cps, non-volatile content is 70 ± 2%, and fixed carbon is 40 ± 2%, and the viscosity of the resol type phenol resin at 25°C is 250 to 350 cps, non-volatile content is 70 ± 2%, and fixed carbon is 40 ± 2. The method for producing magnesia carbon bricks according to claim 1, wherein the magnesia carbon brick is 2%.
JP3071122A 1991-04-03 1991-04-03 Production of magnesia-carbon brick Pending JPH04310560A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3071122A JPH04310560A (en) 1991-04-03 1991-04-03 Production of magnesia-carbon brick

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3071122A JPH04310560A (en) 1991-04-03 1991-04-03 Production of magnesia-carbon brick

Publications (1)

Publication Number Publication Date
JPH04310560A true JPH04310560A (en) 1992-11-02

Family

ID=13451452

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3071122A Pending JPH04310560A (en) 1991-04-03 1991-04-03 Production of magnesia-carbon brick

Country Status (1)

Country Link
JP (1) JPH04310560A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011506257A (en) * 2007-12-17 2011-03-03 エボニック デグサ ゲーエムベーハー Formulations and refractories with high hydration resistance produced therefrom
CN102219526A (en) * 2011-03-11 2011-10-19 山东圣泉化工股份有限公司 Phenolic resin for magnesia carbon brick and preparation method thereof
JP5097861B1 (en) * 2012-03-05 2012-12-12 品川リフラクトリーズ株式会社 Magnesia-carbon brick
CN109851373A (en) * 2018-12-29 2019-06-07 海城利尔麦格西塔材料有限公司 A kind of modified phenolic resin magnesia carbon brick and preparation method thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011506257A (en) * 2007-12-17 2011-03-03 エボニック デグサ ゲーエムベーハー Formulations and refractories with high hydration resistance produced therefrom
CN102219526A (en) * 2011-03-11 2011-10-19 山东圣泉化工股份有限公司 Phenolic resin for magnesia carbon brick and preparation method thereof
JP5097861B1 (en) * 2012-03-05 2012-12-12 品川リフラクトリーズ株式会社 Magnesia-carbon brick
CN109851373A (en) * 2018-12-29 2019-06-07 海城利尔麦格西塔材料有限公司 A kind of modified phenolic resin magnesia carbon brick and preparation method thereof

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