JPS6362471B2 - - Google Patents
Info
- Publication number
- JPS6362471B2 JPS6362471B2 JP54171553A JP17155379A JPS6362471B2 JP S6362471 B2 JPS6362471 B2 JP S6362471B2 JP 54171553 A JP54171553 A JP 54171553A JP 17155379 A JP17155379 A JP 17155379A JP S6362471 B2 JPS6362471 B2 JP S6362471B2
- Authority
- JP
- Japan
- Prior art keywords
- lime
- cacl
- clinker
- mgcl
- material mixture
- 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
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 29
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 29
- 239000004571 lime Substances 0.000 claims description 29
- 239000000203 mixture Substances 0.000 claims description 23
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 14
- 239000000920 calcium hydroxide Substances 0.000 claims description 14
- 235000011116 calcium hydroxide Nutrition 0.000 claims description 14
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 14
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 12
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 239000002245 particle Substances 0.000 claims description 10
- 239000011230 binding agent Substances 0.000 claims description 9
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 8
- 239000011822 basic refractory Substances 0.000 claims description 7
- 239000010419 fine particle Substances 0.000 claims description 7
- 239000000395 magnesium oxide Substances 0.000 claims description 7
- 239000011819 refractory material Substances 0.000 claims description 6
- 239000000654 additive Substances 0.000 claims description 4
- 230000000996 additive effect Effects 0.000 claims description 4
- 238000006297 dehydration reaction Methods 0.000 claims description 4
- 239000011780 sodium chloride Substances 0.000 claims description 4
- 229910004261 CaF 2 Inorganic materials 0.000 claims description 2
- 229910000514 dolomite Inorganic materials 0.000 claims 1
- 239000010459 dolomite Substances 0.000 claims 1
- 238000009472 formulation Methods 0.000 claims 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 22
- 239000011449 brick Substances 0.000 description 17
- 239000000292 calcium oxide Substances 0.000 description 11
- 235000012255 calcium oxide Nutrition 0.000 description 11
- 239000000463 material Substances 0.000 description 9
- 239000007791 liquid phase Substances 0.000 description 7
- 150000003839 salts Chemical class 0.000 description 7
- 238000002156 mixing Methods 0.000 description 6
- 229910000831 Steel Inorganic materials 0.000 description 5
- 230000005496 eutectics Effects 0.000 description 5
- 238000002844 melting Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 238000000465 moulding Methods 0.000 description 5
- 239000010959 steel Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 230000029087 digestion Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000011159 matrix material Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 229910010413 TiO 2 Inorganic materials 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000001079 digestive effect Effects 0.000 description 2
- 239000011451 fired brick Substances 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 230000036571 hydration Effects 0.000 description 2
- 238000006703 hydration reaction Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000011882 ultra-fine particle Substances 0.000 description 2
- 239000011452 unfired brick Substances 0.000 description 2
- -1 CaCl 2 Chemical class 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 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
- 239000010426 asphalt Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 235000010216 calcium carbonate Nutrition 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 235000011148 calcium chloride Nutrition 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000011295 pitch Substances 0.000 description 1
- 239000011802 pulverized particle Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Compositions Of Oxide Ceramics (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Description
本発明は、微粒部分の成分として特に安定な状
態で石灰を含有するCaO質又はCaO−MgO系の
塩基性耐火物の製造方法に係るものである。
塩基性耐火材料であるCaO(石灰)は、その溶
融温度が2500℃以上の高温であると共に、解離酸
素圧及び蒸気圧が低く、真空中でも安定であるた
め耐火物としては有用性の高い材料である。そし
てこれを主体とする石灰系耐火物は、特に鉄鋼の
製錬において、低酸素、低黄黄、低燐の鋼、又は
鋼中介在物の少ないいわゆるクリーンステイール
を溶製するための炉材として優れた特性を示すこ
とはよく知られている。
このように、耐火物として優れた性質を有する
石灰も、CaOが本質的に水和反応性が強く、空気
中の湿分とでも容易に反応して水酸化物となるい
わゆる消化現象のため、その製造工程、製品の貯
蔵手段、使用面等における困難性が大きく、工業
的規模での生産並びに使用については実用化に達
していなかつたのである。
そこでその欠点を補うために、石灰に例えば
Fe2O3、TiO2、Al2O3、SiO2等の焼結剤を1〜10
%程度添加して耐水和性クリンカーを得ようとす
る試みが種々行なわれている。また、高純度石灰
クリンカーを高温で焼成することにより、結晶成
長を促進させて耐消化性を増すことも試みられて
いる。しかしこれらの在来手段においては、前者
の方法は、組成的には石灰煉瓦に対する不純物を
添加することになるので耐火物の耐火性、耐蝕性
を損う欠点を助長することになり、また、前者、
後者いずれにしてもそのクリンカーを機械的に微
粉砕して使用するという製造技術上の問題があ
る。
すなわち、石灰質系耐火物を製造するにあたつ
ては、原料のクリンカーを粉砕して粒度調合し、
それにピツチ、タール、アスフアルト、パラフイ
ン、ワツクス、油又は樹脂等の非水系有機質バイ
ンダーを少量添加して、混練し、成形し不焼成煉
瓦又は焼成煉瓦の形で製品とされるのが通常であ
り、そしてこの場合充填性がよく緻密な煉瓦組織
を得るためには粒径が0.044mm以下の微粒子を10
〜40%程度の配合となすことが必要とされてい
る。
しかし、ある程度の不純物を加えたり、高温焼
成されたものを使用するとしても、石灰クリンカ
ーを上記のように微粉砕すると、その比表面積が
大きくなるために消化反応速度が著しく速くな
り、その保存性が低くなる傾向が顕著に見られた
のである。そして一部消化した微粒子を配合に含
む場合には、焼成煉瓦においては成形体の焼成中
に、又不焼成煉瓦においては使用中に、消化した
石灰粒子が脱水反応し水蒸気の生成、蒸散により
煉瓦に亀裂を生じたり組織を劣化させることとな
るのである。それを防止すべく比較的粗い微粒
子、たとえば0.3mm以下、又は1mm以上程度の比
表面積の小さな粉砕物を微粒子として配合した場
合には、当然に成形充填性が悪いため、密充填さ
れた煉瓦組織は得られないのである。
上記のような欠点を回避するため、耐火物の微
粒子部分に消化反応を生じないマグネシアを用い
る例もあるが、この手段によるときは、石灰煉瓦
のマトリツクス組成といわれる石灰の微粒子部分
を欠くために、該微粒子部分で強く生起する鉄鋼
精錬時の脱硫、脱燐反応等が行なわれず、そのよ
うな微粒子部分をMgOとするので、石灰煉瓦に
おけるような冶金学的効果を減少させる結果とな
る。
本発明は斯かる現況に鑑がみなされたもので、
石灰質系煉瓦のマトリツクス部分を組成する石灰
の消化を抑止した、性状の優れた石灰煉瓦となす
手段を提案せんとするもので、具体的には石灰質
系煉瓦のマトリツクス組成部分に消石灰を使用
し、
Ca(OH)2→CaO+H2O
なる脱水反応が生ずる580℃以上の温度に配合材
料を加熱し、その温度条件を保ちながら直接、配
材料を成形することにより、在来技術が逢着して
いた問題点を解消した石灰質系煉瓦の製造方法の
提供を目的としている。
以下本発明の方法の一例につき詳述すると、
TiO2、Al2O3、Fe2O3のごとき焼結剤を予め少量
添加して製造された石灰クリンカー又は高温焼成
された高純度の石灰クリンカーを粉砕して、例え
ば粗粒子として4〜1mm径、中間粒子としては1
mm径以下が存在するように篩分けした後、これに
10〜50%の消石灰を混合する。
次いで、CaCl2、MgCl2、Ca(NO3)2等の塩を
添加対象の1〜15%の範囲で、上記のクリンカー
と消石灰との混合体に添加結合剤として、混合し
た後、580〜800℃の加熱状態で成形を行なう。
在来技術にあつては、石灰にCaCl2を少量添加
して、400〜800℃の熱間状態でCaCl2の液相転移
を利用して適度の可塑性を与え、圧縮、押し出
し、遠心力法等により成形して水和抵抗性をもた
らさんとする石灰耐火物の製造方法は知られてい
るが、この手段による場合には適度の可塑性を具
現し得る温度域が高く、その温度域での取扱作業
に見合う設備が必要となる等の困難性があつたの
である。
本発明では、混合材料の微粒構成分として消石
灰を用い、混合材料を加熱しその状態において直
接、成形をすると共に、この間における上記のご
とき添加結合剤成分に共融点を下げる物質を組合
わせることにより、それらの液相生成温度を下
げ、所要の成形を行ない得る可塑性を、実質上有
利な低温域にてもたらされるようになしている。
すなわち、例えばCaCl2単独では772℃に達し
なければ液相が生成し始めないため、それ以下の
温度ではCaO−CaCl2の混合物が可塑性を示すこ
とはできないが、CaCl2にその共融点を下げる物
質である。NaCl、Ca(NO3)2、CaCO3、KCl、
BaCl2、MgCl2、CaSO4、CaF2等の1種又は2種
以上を組合わせて共存させることにより、その液
相生成温度を実質的に下げ、熱間での材料の取扱
いをきわめて容易としたのである。
CaCl2と各塩類とを共存させた場合の液相の生
成温度は第1表に示すとおりであり、例えば
CaCl2にNaClを添加することにより、その融点
を500℃にまで下げることができる。第1表に示
す温度はその系の最も低い溶融温度であり、組成
比率はその状態を示すときの比率であつて、本発
明における添加割合はこれに限定する要はなく、
772℃よりも低いものであればよく、特に消石灰
の脱水温度580℃に上寄りより近似する共融点と
なる混合比を選ぶことが望ましい。
液相生成温度の低下は、材料混合物の加熱温度
を下げることになるので、製品化のための成形機
の金型の熱膨張を小さくしたり、製品の精度を向
上させたり、その他秤量関係の取扱いがきわめて
容易となる等の熱収支の面から省エネルギーに資
するところ大なる効果と共に多大の利点を生ずる
のである。これらのCaCl2と組合わされる塩類
は、消石灰と予備混合してもよいし、骨材粒子と
直接混合してもよく、いずれの場合も同効を達し
得る。
本発明の方法における、温度変化による各組成
体の挙動についてみれば、所定温度に達すると先
づ消石灰が脱水して生石灰CaOに変化する。この
とき生成するCaOは消石灰の超微粒子から出発し
ているので粒子径が1〜2μ程度のきわめて微細
で活性な状態となつている。前記のごとく石灰ク
リンカーを機械的に粉砕しようとすると粉砕限界
があつて、全体を数μ径以下にすることは至難で
あるが、本発明の方法においては、加熱を必要条
件として消石灰より生成する微細な生石灰超品微
粒子を含む状態となつており、そのような微細な
生石灰粒子を大量に配合するのと同様の効果が得
られ、しかもそのような超微粉粒子石灰が消化す
る懸念はないのである。
煉瓦微粒子部分がCaOとなると同時に、添加し
てある塩も溶融して液相が生成するため混合材料
に適当な可塑性を与えることになり、その温度の
まま加圧等により成形すると充填性の良好な緻密
な煉瓦組織が得られるのである。こうして得られ
た耐火物は微粒子部分にCaOを含むにもかかわら
ず、緻密で気孔率が低いため比表面積が小さく、
大気中の湿分の侵入に対しても抵抗性が著しく大
となり安定な性状を保持する。
本発明による製造方法において使用される結合
剤成分はCaCl2又はCaCl2とその共融物を形成す
る物質に限定されることはなく、MgCl2若しくは
Ca(NO3)2の単独又はそれらと共融点を下げる物
質を組合わせた塩の使用によつても、微粒部分に
石灰を含有する塩基性耐火物を安定な性状のもの
として得られるのである。これらの場合の塩の融
点は同じく第1表に例示するとおりである。
実施例 1
第2表に示す化学組成の石灰クリンカーを粉砕
して、4〜1mm径及び1mm径以下の粒度に篩い分
けて骨材とする。これとは別に第3表のNo.1〜11
に示す塩類を0.3mm径以下にして消石灰と共に第
3表に示す配合比にて混合する。この混合物に先
の4〜1mm径及び1mm径以下の石灰クリンカーよ
りなる骨材を加えて混合し、その最終混混合物を
それぞれ第3表に示す温度まで昇温し、全体が均
一な状態となるよう3時間保持した。
成形して得られたものについてみれば、本発明
のNo.1〜9は従来品と比較して第4表に示すよう
に、よく緻密化された煉瓦が得られているが、No.
11のように消石灰配合比が少なかつたり、逆りNo.
10のように消石灰配合比が50%を超えると充填性
が悪くなり緻密な耐火物が得られない。
さらにNo.1〜9のものは大気中に放置した場合
は2週間、ブリキ缶内にて保持する場合は3ケ月
間消化することなく、搬送、保管による影響はな
く実用に供するための充分な安定性が確認せられ
た。また、No.2の煉瓦を製鋼工場の大型取鍋で張
り合せテストをしたところ在来品の使用に勝る耐
用性を示し、Al2O385%の高アルミナ質煉瓦を同
等以上の使用実績を示した。
実施例 2
実施例1で用いた石灰クリンカーの全部又は一
部を第2表に示す組成のマグネシアクリンカーと
置換し、実施例1と全く同様の工程で煉瓦を試作
した。この例における配合割合とその得られたも
のの物性値は第5表に示すとおりであり、MgO
を添加することにより純石灰系のものよりも耐食
性が増大した。
The present invention relates to a method for producing a CaO-based or CaO-MgO-based basic refractory that contains lime in a particularly stable state as a component of the fine particulate portion. CaO (lime), a basic refractory material, has a high melting temperature of over 2500℃, low dissociated oxygen pressure and vapor pressure, and is stable even in vacuum, making it a highly useful material as a refractory. be. Lime-based refractories based on this are used as furnace materials for melting low-oxygen, low-yellow, low-phosphorus steel, or so-called clean steel with few inclusions, especially in steel smelting. It is well known that it exhibits excellent properties. In this way, even though lime has excellent properties as a refractory, CaO is inherently highly hydration-reactive and easily reacts with moisture in the air to form hydroxides, a so-called digestion phenomenon. There were great difficulties in the manufacturing process, product storage means, use, etc., and production and use on an industrial scale had not yet been put to practical use. Therefore, in order to compensate for this drawback, for example, lime
1 to 10 sintering agents such as Fe 2 O 3 , TiO 2 , Al 2 O 3 , SiO 2 etc.
Various attempts have been made to obtain a hydration-resistant clinker by adding about %. Furthermore, attempts have been made to increase the digestion resistance by accelerating crystal growth by firing high-purity lime clinker at high temperatures. However, in these conventional methods, the former method adds impurities to the lime brick composition, which exacerbates the drawback of impairing the fire resistance and corrosion resistance of the refractory. former,
In either case, there is a problem in manufacturing technology that the clinker must be mechanically pulverized before use. In other words, when producing calcareous refractories, the raw material clinker is ground and the particle size is adjusted.
Usually, a small amount of non-aqueous organic binder such as pitch, tar, asphalt, paraffin, wax, oil, or resin is added to the mixture, and the product is kneaded and shaped into unfired bricks or fired bricks. In this case, in order to obtain a dense brick structure with good filling properties, fine particles with a particle size of 0.044 mm or less are added to
It is necessary to have a blend of about ~40%. However, even if a certain amount of impurities is added or a product calcined at a high temperature is used, when lime clinker is finely pulverized as described above, its specific surface area becomes large, so the digestion reaction rate becomes significantly faster, and its preservability increases. There was a noticeable tendency for the value to decrease. When partially digested fine particles are included in the mixture, the digested lime particles undergo a dehydration reaction during the firing of the molded body for fired bricks, or during use for unfired bricks, producing water vapor and evaporating, causing the bricks to form. This can lead to cracks in the structure and deterioration of the structure. In order to prevent this, if relatively coarse particles, such as pulverized particles with a small specific surface area of 0.3 mm or less or 1 mm or more, are blended as fine particles, the moldability will naturally be poor, resulting in a densely packed brick structure. cannot be obtained. In order to avoid the above-mentioned disadvantages, there are cases where magnesia, which does not cause a digestive reaction, is used in the particulate part of the refractory, but when this method is used, it is difficult to use magnesia, which does not cause a digestive reaction, because it lacks the particulate part of lime, which is said to be the matrix composition of lime bricks. Since the desulfurization and dephosphorization reactions that occur strongly in the fine particle portion during steel refining are not carried out, and the fine particle portion is converted into MgO, the metallurgical effect as in lime bricks is reduced. The present invention was created in consideration of the current situation,
The purpose of this project is to propose a method for making lime bricks with excellent properties by suppressing the digestion of the lime that makes up the matrix of calcareous bricks.Specifically, using slaked lime in the matrix composition of calcareous bricks, Conventional technology was applied by heating the compounded material to a temperature of 580°C or higher, where the dehydration reaction of Ca(OH) 2 →CaO+H 2 O occurs, and directly molding the compounded material while maintaining that temperature condition. The purpose is to provide a method for manufacturing calcareous bricks that eliminates problems. An example of the method of the present invention will be described in detail below.
Lime clinker manufactured by adding a small amount of sintering agent such as TiO 2 , Al 2 O 3 , Fe 2 O 3 in advance or high purity lime clinker calcined at high temperature is pulverized into coarse particles of 4 to 1 mm, for example. diameter, as an intermediate particle 1
After sieving so that there is a diameter of mm or less, this
Mix 10-50% slaked lime. Next, salts such as CaCl 2 , MgCl 2 , and Ca(NO 3 ) 2 are added to the above mixture of clinker and slaked lime as an additive binder in a range of 1 to 15% of the amount to be added. Molding is carried out under heating conditions of 800℃. In conventional technology, a small amount of CaCl 2 is added to lime to give it appropriate plasticity by utilizing the liquid phase transition of CaCl 2 in a hot state of 400 to 800 degrees Celsius, and compression, extrusion, and centrifugal force methods are used. There is a known method for producing lime refractories that is molded using methods such as molding methods to provide hydration resistance. There were difficulties, such as the need for equipment suitable for the handling work. In the present invention, slaked lime is used as a particulate component of the mixed material, the mixed material is heated and molded directly in that state, and a substance that lowers the eutectic point is combined with the above-mentioned additive binder component during this time. , their liquid phase formation temperature is lowered so that the plasticity that allows for the required shaping is achieved in a substantially advantageous low temperature range. That is, for example, CaCl 2 alone does not begin to form a liquid phase until the temperature reaches 772 °C, so below that temperature the CaO−CaCl 2 mixture cannot exhibit plasticity, but CaCl 2 lowers its eutectic point. It is a substance. NaCl, Ca( NO3 ) 2 , CaCO3 , KCl,
By coexisting one type or a combination of two or more of BaCl 2 , MgCl 2 , CaSO 4 , CaF 2 , etc., the liquid phase formation temperature can be substantially lowered, making handling of the material extremely easy. That's what I did. The formation temperature of the liquid phase when CaCl 2 and each salt coexist is as shown in Table 1. For example,
By adding NaCl to CaCl2 , its melting point can be lowered to 500 °C. The temperature shown in Table 1 is the lowest melting temperature of the system, and the composition ratio is the ratio that indicates the state, and the addition ratio in the present invention does not need to be limited to this.
It may be lower than 772°C, and it is particularly desirable to select a mixing ratio that provides a eutectic point that is closer to the dehydration temperature of slaked lime, 580°C. Lowering the liquid phase formation temperature lowers the heating temperature of the material mixture, which can be used to reduce the thermal expansion of molds in molding machines for commercialization, improve product accuracy, and other weighing-related matters. It contributes to energy saving in terms of heat balance, such as being extremely easy to handle, and has great benefits as well as great effects. These salts combined with CaCl 2 may be premixed with slaked lime or mixed directly with aggregate particles, and in both cases the same effect can be achieved. Looking at the behavior of each composition due to temperature changes in the method of the present invention, when a predetermined temperature is reached, slaked lime first dehydrates and changes to quicklime CaO. Since the CaO produced at this time starts from ultrafine particles of slaked lime, it is in an extremely fine and active state with a particle size of about 1 to 2 μm. As mentioned above, if you try to mechanically crush lime clinker, there is a crushing limit and it is extremely difficult to reduce the entire size to less than a few microns in diameter. However, in the method of the present invention, heating is a necessary condition and it is produced from slaked lime. It contains ultra-fine particles of quicklime, and the same effect as mixing large amounts of such fine quicklime particles can be obtained, and there is no concern that such ultra-fine lime particles will be digested. be. At the same time that the brick particulate part becomes CaO, the added salt also melts and a liquid phase is generated, giving the mixed material appropriate plasticity.If it is molded under pressure at that temperature, it has good filling properties. This results in a dense brick structure. Although the refractories obtained in this way contain CaO in the fine particles, they are dense and have low porosity, so they have a small specific surface area.
It has extremely high resistance to the intrusion of atmospheric moisture and maintains stable properties. The binder component used in the production method according to the invention is not limited to CaCl 2 or substances forming a eutectic thereof with CaCl 2 , but includes MgCl 2 or
By using salts such as Ca(NO 3 ) 2 alone or in combination with substances that lower the eutectic point, basic refractories containing lime in the fine grains can be obtained with stable properties. . The melting points of the salts in these cases are also as illustrated in Table 1. Example 1 Lime clinker having the chemical composition shown in Table 2 is crushed and sieved into particles with a diameter of 4 to 1 mm and a diameter of 1 mm or less to obtain aggregate. Apart from this, Nos. 1 to 11 in Table 3
The salts shown in the table below are mixed in a diameter of 0.3 mm or less with slaked lime at the mixing ratio shown in Table 3. Add and mix the lime clinker aggregates with a diameter of 4 to 1 mm and less than 1 mm to this mixture, and the final mixed mixture is heated to the temperature shown in Table 3, so that the whole becomes uniform. It was held for 3 hours. Looking at the products obtained by molding, as shown in Table 4, bricks No. 1 to No. 9 of the present invention were well densified compared to the conventional products, but No.
If the slaked lime blending ratio is low as in No. 11, or the opposite No.
When the slaked lime blending ratio exceeds 50%, as in No. 10, the filling properties deteriorate and a dense refractory cannot be obtained. In addition, Nos. 1 to 9 will remain undigested for two weeks if left in the atmosphere, and for three months if kept in a tin can, and will not be affected by transportation or storage, and will be sufficient for practical use. Stability was confirmed. In addition, when No. 2 bricks were laminated in a large ladle at a steel factory and tested, they showed superior durability to conventional bricks, and the use of high alumina bricks with 85% Al 2 O 3 was equivalent or better. showed that. Example 2 Bricks were trial-produced in exactly the same manner as in Example 1, except that all or part of the lime clinker used in Example 1 was replaced with magnesia clinker having the composition shown in Table 2. The blending ratio in this example and the physical properties of the obtained product are shown in Table 5, and the MgO
By adding , the corrosion resistance was increased compared to that of pure lime.
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】
本発明においては、添加結合剤成分を調整する
ことにより、作業温度の低域化と工程の迅速化を
通じて生産性を向上せしめつつ、安定な製品供給
を可能としたものであり、本発明の趣旨に従えば
上記の諸実施例に限定されるものではなく、それ
から導かれる応用、転用等はすべての本発明の技
術的範囲に包合されるものであることはいうまで
もない。[Table] In the present invention, by adjusting the additive binder component, it is possible to improve productivity by lowering the working temperature range and speeding up the process, while also enabling stable product supply. It goes without saying that in accordance with the spirit of the invention, the invention is not limited to the above embodiments, and any applications, diversions, etc. derived therefrom are encompassed within the technical scope of the invention.
Claims (1)
マグネシアクリンカーの1種若しくは2種以上を
粉砕して適宜粒度分布に調整したものを骨材とし
て、これに10〜15%の消石灰を加え、さらに添加
結合剤としてCaCl2、MgCl2又はCa(NO3)2を1
〜15%混合し、得られる材料混合物を580〜800℃
の加熱状態に保持して配合組成中の消石灰の脱水
反応を終らせた後、その温度域にてこの混合物を
加圧成形して製品を得るようにしたことを特徴と
する微粒部分に石灰を含有する塩基性耐火物の製
造方法。 2 材料混合物中の添加結合剤成分を、CaCl2又
はCaCl2にNaCl、Ca(NO3)2、CaCO3、KCl、
BaCl2、MgCl2、CaSO4、CaF2の1種若しくは2
種以上を組合わせたものとなしたことを特徴とす
る特許請求の範囲第1項記載の微粒部分に石灰を
含有する塩基性耐火物の製造方法。 3 材料混合物中の添加結合剤成分を、MgCl2又
はMgCl2にKCl、NaCl、BaCl2の1種若しくは2
種以上を組合わせたものとなしたことを特徴とす
る特許請求の範囲第1項記載の微粒部分に石灰を
含有する塩基性耐火物の製造方法。 4 材料混合物中の添加結合剤成分を、Ca
(NO3)2又はCa(NO3)2にBaCl2を組合わせたもの
となしたことを特徴とする特許請求の範囲第1項
記載の微粒部分に石灰を含有する塩基性耐火物の
製造方法。[Scope of Claims] 1. One or more types of lime clinker, dolomite clinker, or magnesia clinker are crushed and adjusted to have an appropriate particle size distribution as aggregate, and 10 to 15% of slaked lime is added to this, and Addition of 1 part of CaCl 2 , MgCl 2 or Ca(NO 3 ) 2 as a binder
Mix ~15% and heat the resulting material mixture to 580~800℃
After the dehydration reaction of the slaked lime in the formulation is completed by holding it in a heated state of A method for producing a basic refractory containing the same. 2 Add binder components in the material mixture to CaCl 2 or CaCl 2 with NaCl, Ca(NO 3 ) 2 , CaCO 3 , KCl,
One or two of BaCl 2 , MgCl 2 , CaSO 4 , CaF 2
2. A method for producing a basic refractory containing lime in the fine particulate portion according to claim 1, characterized in that it is a combination of two or more kinds of refractories. 3 Add binder component in the material mixture to MgCl 2 or MgCl 2 with one or more of KCl, NaCl, BaCl 2 .
2. A method for producing a basic refractory containing lime in the fine particulate portion according to claim 1, characterized in that it is a combination of two or more kinds of refractories. 4 The additive binder component in the material mixture is
(NO 3 ) 2 or Ca(NO 3 ) 2 in combination with BaCl 2. The production of a basic refractory containing lime in the fine particles as set forth in claim 1. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17155379A JPS5692159A (en) | 1979-12-27 | 1979-12-27 | Manufacture of basic refractories containing lime in fine grain portion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17155379A JPS5692159A (en) | 1979-12-27 | 1979-12-27 | Manufacture of basic refractories containing lime in fine grain portion |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5692159A JPS5692159A (en) | 1981-07-25 |
| JPS6362471B2 true JPS6362471B2 (en) | 1988-12-02 |
Family
ID=15925258
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17155379A Granted JPS5692159A (en) | 1979-12-27 | 1979-12-27 | Manufacture of basic refractories containing lime in fine grain portion |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5692159A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62241866A (en) * | 1986-04-15 | 1987-10-22 | 三井造船株式会社 | High strength calcia-base refractory composition |
| JP2629730B2 (en) * | 1987-09-17 | 1997-07-16 | 旭硝子株式会社 | Block for tundish weir |
-
1979
- 1979-12-27 JP JP17155379A patent/JPS5692159A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5692159A (en) | 1981-07-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2412132C2 (en) | Coarse-ceramic refractory material and refractory article made therefrom | |
| EP0544913B1 (en) | Process for producing silica brick | |
| US4473654A (en) | Low temperature bonding of refractory aggregates and refractory products of improved cold strength | |
| US2805167A (en) | Synthetic spinel refractory products | |
| US2621131A (en) | Method of consolidating refractory materials | |
| US6548436B2 (en) | Cristobalite-free mullite grain having reduced reactivity to molten aluminum and method of producing the same | |
| US2572688A (en) | Magnesia refractory and method of | |
| CA1037503A (en) | Carbon composition and shaped article made therefrom | |
| US5496780A (en) | Method for producing silica brick | |
| JPS6362471B2 (en) | ||
| US4366257A (en) | Process for producing a calcia clinker | |
| CN101367626B (en) | White portland cement | |
| US3429723A (en) | Process for the manufacture of refractory magnesia-chrome and chromemagnesia products | |
| JP2000302536A (en) | Method for producing high density hydrate resistant lime sintered product | |
| US4383044A (en) | Slaking-resistant calcia refractory | |
| SU1289845A1 (en) | Raw mixture for producing porous aggregate | |
| KR100328072B1 (en) | Synthetic Slag Manufacturing Method | |
| US3377177A (en) | Metallurgical furnace lining | |
| US2238428A (en) | Method of making basic refractories | |
| US1230430A (en) | Furnace-lining and method of making same. | |
| US1238020A (en) | Refractory material and process of making the same. | |
| US3864136A (en) | Direct bonded refractory brick having improved hot strength and its method of manufacture | |
| JPS6112871B2 (en) | ||
| RU1796600C (en) | Raw materials mixture for clinker production | |
| US2287455A (en) | Corrected basic refractory |