JP2006028423A - Synthetic tar and blockage material for tap hole of molten metal - Google Patents
Synthetic tar and blockage material for tap hole of molten metal Download PDFInfo
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- JP2006028423A JP2006028423A JP2004212179A JP2004212179A JP2006028423A JP 2006028423 A JP2006028423 A JP 2006028423A JP 2004212179 A JP2004212179 A JP 2004212179A JP 2004212179 A JP2004212179 A JP 2004212179A JP 2006028423 A JP2006028423 A JP 2006028423A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D41/00—Casting melt-holding vessels, e.g. ladles, tundishes, cups or the like
- B22D41/14—Closures
- B22D41/44—Consumable closure means, i.e. closure means being used only once
- B22D41/46—Refractory plugging masses
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/66—Monolithic refractories or refractory mortars, including those whether or not containing clay
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C1/00—Working-up tar
- C10C1/005—Working-up tar by mixing two or more coaltar fractions
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C1/00—Working-up tar
- C10C1/02—Removal of water
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C1/00—Working-up tar
- C10C1/04—Working-up tar by distillation
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10C—WORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
- C10C1/00—Working-up tar
- C10C1/04—Working-up tar by distillation
- C10C1/16—Winning of pitch
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- Working-Up Tar And Pitch (AREA)
- Casting Support Devices, Ladles, And Melt Control Thereby (AREA)
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Abstract
Description
本発明は、合成タールおよび溶融金属出湯口用閉塞材(以下「マッド材」という)に関し、さらに詳しくは保管安定性に優れ、粘度の調節が自在である合成タールおよびマッド材の提供を目的とする。 The present invention relates to a synthetic tar and a plugging material for a molten metal outlet (hereinafter referred to as “mud material”), and more specifically, to provide a synthetic tar and a mud material which are excellent in storage stability and whose viscosity can be freely adjusted. To do.
従来、タールを脱水処理して得られる無水タールは、高炉出湯口閉塞材、電気炉出湯口閉塞材などのマッド材のバインダー、塗料のバインダーなどとして使用されている。このような用途のうちで、マッド材は、ロー石、シャモット、アルミナなどの耐火原料と炭素質材料、炭化珪素、窒化珪素および粘土などからなる耐火材料に、さらにタールをバインダーとして製造されてきた。これらのタール系バインダーとして、固定炭素量が高い無水タールを使用することが提案されている(特許文献1)。
上記特許文献1に記載の無水タールは、優れたマッド材を提供するものであるが、該無水タールには揮発成分(主としてナフタリンなど)が含まれており、このような揮発分を含有する無水タールをマッド材のバインダーとして使用した場合には、ナフタリンなどの揮発(昇華)によって、マッド材の組織が粗雑化し、亀裂発生の原因となるという課題があった。また、上記無水タールを保管しておくと、その保管時にもナフタリンなどが揮発し、環境に悪影響を与えるとともに、無水タールの粘度が上昇し、実際の使用時に不都合が発生するという課題が発生している。また、上記無水タールは用途の違いによって用途に適した粘度を有することが好ましいが、粘度の調節が容易とはいえなかった。さらに従来の無水タール中にはフェノールも含まれており、これらのフェノールも環境汚染物質として問題となっている。 The anhydrous tar described in Patent Document 1 provides an excellent mud material. However, the anhydrous tar contains a volatile component (mainly naphthalene and the like), and an anhydrous tar containing such a volatile component. When tar is used as a binder for the mud material, there is a problem that the structure of the mud material becomes rough due to volatilization (sublimation) of naphthalene and the like, which causes cracks. In addition, if the anhydrous tar is stored, naphthalene and the like will volatilize during storage, adversely affecting the environment, increasing the viscosity of the anhydrous tar, and causing problems during actual use. ing. The anhydrous tar preferably has a viscosity suitable for the application depending on the application, but it cannot be said that the adjustment of the viscosity is easy. Furthermore, conventional anhydrous tar contains phenol, and these phenols are also problematic as environmental pollutants.
従って、本発明の目的は、揮発成分が少なく、長期保管してもその粘度などが変化しない保管安定性に優れ、さらに用途に応じて粘度調整が容易である合成タールを提供することにある。また、本発明の他の目的は、組織が変質したり亀裂が発生しないマッド材を提供することにある。 Accordingly, an object of the present invention is to provide a synthetic tar that has few volatile components, has excellent storage stability that does not change its viscosity even when stored for a long period of time, and can be easily adjusted in viscosity according to the application. Another object of the present invention is to provide a mud material in which the structure is not altered or cracks are not generated.
上記目的は以下の本発明によって達成される。すなわち、本発明は、タール蒸留によって得られた軟ピッチと、タール蒸留によって得られた蒸留油との混合物であって、ナフタリン含有量が1.5質量%以下であることを特徴とする合成タールを提供する。該合成タールにおいては60℃における粘度が100〜2,400mPa・sであること、および/またはフェノール含有量が0.1質量%以下であることが好ましい。 The above object is achieved by the present invention described below. That is, the present invention is a synthetic tar characterized in that it is a mixture of soft pitch obtained by tar distillation and distilled oil obtained by tar distillation, and the naphthalene content is 1.5% by mass or less. I will provide a. The synthetic tar preferably has a viscosity at 60 ° C. of 100 to 2,400 mPa · s and / or a phenol content of 0.1% by mass or less.
また、本発明は、耐火材料とバインダーとからなり、該バインダーが前記本発明の合成タールであることを特徴とするマッド材を提供する。 The present invention also provides a mud material comprising a refractory material and a binder, wherein the binder is the synthetic tar of the present invention.
本発明によれば、揮発成分が少なく、長期保管してもその粘度などが変化しない保管安定性に優れ、さらに用途に応じて粘度調整が容易である無水タールを提供することができる。また、本発明によれば、保管安定性に優れるとともに、組織が変質したり亀裂が発生しにくいマッド材を提供することができる。 ADVANTAGE OF THE INVENTION According to this invention, the anhydrous tar which has few volatile components, is excellent in the storage stability which does not change the viscosity etc. even if it stores for a long period of time, and can adjust viscosity easily according to a use can be provided. Furthermore, according to the present invention, it is possible to provide a mud material that is excellent in storage stability and hardly changes in structure or cracks.
次に発明を実施するための最良の形態を挙げて本発明をさらに詳しく説明する。本発明における「合成タール」とは、タール蒸留によって得られた軟ピッチと、タール蒸留によって得られた蒸留油との混合物である。ここで上記軟ピッチとは、タールを脱水して脱水タール(無水タール)としたものを、さらに常圧蒸留により蒸留し、200〜250℃の留分(ナフタリン油)と230〜280℃の留分(蒸留油、洗浄油、吸収油などと称される)とを留去した後に残った釜残であって、軟化点が70℃未満のものであり、沸点が350℃以上の多くの複雑な高沸点成分と遊離炭素との混合物を意味している。これらの軟ピッチは軟化点が約35〜45℃の範囲にあることが好ましい。 Next, the present invention will be described in more detail with reference to the best mode for carrying out the invention. The “synthetic tar” in the present invention is a mixture of soft pitch obtained by tar distillation and distilled oil obtained by tar distillation. Here, the soft pitch is obtained by dehydrating tar to form dehydrated tar (anhydrous tar), and further distilling by atmospheric distillation to obtain a 200-250 ° C fraction (naphthalene oil) and a 230-280 ° C fraction. Remaining kettle residue after distilling off the water (called distilled oil, washing oil, absorption oil, etc.) with a softening point of less than 70 ° C and a boiling point of 350 ° C or more Meaning a mixture of high-boiling components and free carbon. These soft pitches preferably have a softening point in the range of about 35-45 ° C.
また、蒸留油とは上記の230〜280℃の留分を意味している。本発明の合成タールは、上記の軟ピッチと上記の蒸留油とを混合して得られるもので、この混合物を「合成タール」と称しており、後述するようにナフタリン含有量が1.5質量%以下となる。上記合成タールに対して従来の無水タールは、上記において常圧蒸留される前の脱水タールを意味しており、ナフタリン油などの軽質分が除去されておらず、主としてナフタリンを通常8〜15質量%含有しており、また、フェノールを約0.5〜1.5質量%含有している。 Distilled oil means the above-mentioned fraction of 230 to 280 ° C. The synthetic tar of the present invention is obtained by mixing the above soft pitch and the above distilled oil, and this mixture is referred to as “synthetic tar”, and the naphthalene content is 1.5 mass as described later. % Or less. The conventional anhydrous tar relative to the synthetic tar means dehydrated tar before atmospheric distillation in the above, and light components such as naphthalene oil are not removed, and mainly naphthalene is usually 8 to 15 mass. In addition, phenol is contained in an amount of about 0.5 to 1.5% by mass.
本発明の合成タールは、前記軟ピッチと蒸留油とを混合して得られ、軟ピッチと蒸留油との混合比を変更することで任意の粘度を有する混合物(合成タール)が得られるという利点を有する。合成タールの好ましい粘度は60℃において100〜2,400mPa・sの範囲である。このような粘度の調整は前記軟ピッチ(A)と蒸留油(B)とを質量比でA:B=74〜90:26〜10の比率で混合することによって得られる。前記60℃における粘度が100mPa・s未満であるとバインダーとしての粘着性が不足するとともに、固定炭素が減少するため、耐用性が低下するなどの不都合が生じる場合がある。一方、前記60℃における粘度が2,400mPa・sを超えると必要とする充填性を得るためのタール量が増加するために、気孔率が増大し耐用性が低下するなどの不都合が生じる場合がある。参考のために合成タール中の蒸留油の含有量と合成タールの粘度との関係を図1に示す。図示するように本発明の合成タールはその蒸留油の含有量を変更することによって、その粘度を目的に応じて任意にかつ容易に変更することができる。 The synthetic tar of the present invention is obtained by mixing the soft pitch and the distilled oil, and an advantage that a mixture (synthetic tar) having an arbitrary viscosity can be obtained by changing the mixing ratio of the soft pitch and the distilled oil. Have The preferred viscosity of the synthetic tar is in the range of 100 to 2,400 mPa · s at 60 ° C. Such a viscosity adjustment is obtained by mixing the soft pitch (A) and the distilled oil (B) in a mass ratio of A: B = 74 to 90: 26-10. When the viscosity at 60 ° C. is less than 100 mPa · s, the adhesiveness as a binder is insufficient, and fixed carbon is reduced, which may cause inconveniences such as reduced durability. On the other hand, when the viscosity at 60 ° C. exceeds 2,400 mPa · s, the amount of tar for obtaining the required filling property increases, which may cause inconveniences such as increased porosity and reduced durability. is there. For reference, the relationship between the content of distilled oil in synthetic tar and the viscosity of synthetic tar is shown in FIG. As shown in the figure, the viscosity of the synthetic tar of the present invention can be arbitrarily and easily changed according to the purpose by changing the content of the distilled oil.
また、本発明の合成タールは、そのナフタリン含有量が1.5質量%以下であることを特徴としている。合成タール中のナフタリン含有量が1.5質量%を超えると前記本発明の課題の解決が困難になる。該合成タール中のナフタリン含有量を1.5質量%以下にする方法としては、特別な方法は不要であり、前記の通りナフタリンなどの軽質分を含有したままの無水タールを蒸留してナフタリンなどの軽質分を留去し、さらに蒸留を続けて無水タールを蒸留油と軟ピッチに分けた後、該蒸留油と軟ピッチとを前記の混合比で混合(合成)する方法が好ましい。この際使用する蒸留油と軟ピッチのいずれもがナフタリン含有量が低いことから、得られる合成タールのナフタリン含有量は1.5質量%以下となる。 The synthetic tar of the present invention is characterized in that the naphthalene content is 1.5% by mass or less. When the naphthalene content in the synthetic tar exceeds 1.5% by mass, it becomes difficult to solve the problem of the present invention. As a method for reducing the naphthalene content in the synthetic tar to 1.5% by mass or less, a special method is unnecessary, and as described above, an anhydrous tar containing light components such as naphthalene is distilled to obtain naphthalene or the like. A method of distilling off the light components and further distilling to separate anhydrous tar into distilled oil and soft pitch, and then mixing (synthesizing) the distilled oil and soft pitch in the above-mentioned mixing ratio is preferable. Since both the distilled oil and soft pitch used in this case have a low naphthalene content, the naphthalene content of the resulting synthetic tar is 1.5% by mass or less.
また、本発明の合成タールのフェノール含有量は0.1質量%以下であることが好ましい。本発明の合成タール中のフェノール含有量を0.1質量%以下にする方法は、上記のナフタリン含有量の調整と同様である。
以上の本発明の合成タールはマッド材、耐火物、炭素材料用含浸材、特炭素用バインダー、塗料バインダーなどの多数の用途に有用である。以下マッド材用としての用途を代表例として説明する。
Moreover, it is preferable that the phenol content of the synthetic tar of this invention is 0.1 mass% or less. The method for adjusting the phenol content in the synthetic tar of the present invention to 0.1% by mass or less is the same as the adjustment of the naphthalene content.
The synthetic tar of the present invention is useful for many applications such as mud materials, refractories, carbon material impregnation materials, special carbon binders, paint binders and the like. Hereinafter, the use as a mud material will be described as a representative example.
本発明のマッド材は、耐火材料とバインダーとからなり、該バインダーが前記本発明の合成タールであることを特徴としている。上記耐火材料としては、従来公知のマッド材用の耐火材料がいずれも使用でき、例えば、ロー石、シャモット、アルミナなどの耐火原料と、炭素質材料、炭化珪素、窒化珪素および粘土からなる耐火材料が挙げられる。本発明のマッド材は、上記耐火材料(A)100質量部に対して本発明の合成タール(B)を10〜25質量部の比率で混合して得られる。合成タールの使用量が上記範囲よりも少ないと潤滑性が低下するために、必要量を充填することができなくなるなどの不都合が生じる場合がある。一方、合成タールの使用量が上記範囲よりも多いと気孔率が増大し、耐用性が低下したり、未乾燥による開孔中のガス吹きが発生するなどの不都合が生じる場合がある。 The mud material of the present invention comprises a refractory material and a binder, and the binder is the synthetic tar of the present invention. As the refractory material, any conventionally known refractory material for mud materials can be used, for example, a refractory material such as rholite, chamotte, alumina and the like, and a refractory material made of carbonaceous material, silicon carbide, silicon nitride and clay. Is mentioned. The mud material of the present invention is obtained by mixing the synthetic tar (B) of the present invention at a ratio of 10 to 25 parts by mass with respect to 100 parts by mass of the refractory material (A). If the amount of the synthetic tar used is less than the above range, the lubricity is lowered, and there may be a disadvantage that the necessary amount cannot be filled. On the other hand, when the amount of the synthetic tar used is larger than the above range, the porosity may increase, the durability may be lowered, and there may be inconveniences such as the occurrence of gas blowing during the opening due to undried.
上記のマッド材の特徴は、前記本発明の合成タールと同様に、得られるマッド材の保管安定性に優れるという点である。すなわち、本発明の上記マッド材を長期間保管しておいてもマッド材の性質、例えば、マッド材の柔らかさ(硬度)などに変化が生じることがなく、また、揮発分が少ないことから作業環境などに悪影響を与えることがない。これに対して従来の無水タールをバインダーとして使用したマッド材は、特に製鉄所や製鋼所において高い雰囲気温度に曝された場合、ナフタレンなどの揮発成分の揮発などによりその柔らかさが失われ、使用困難となる場合があり、また、作業環境を悪化させる畏れがあった。このような畏れのためにマッド材を一度に多量に製造しておくことが困難であったが、本発明のマッド材はこのような畏れがなく、従って作業性が向上するという利点がある。 The characteristic of said mud material is that it is excellent in storage stability of the obtained mud material, like the synthetic tar of the present invention. That is, even if the mud material of the present invention is stored for a long period of time, the property of the mud material, for example, the softness (hardness) of the mud material does not change, and the volatile content is low. Does not adversely affect the environment. In contrast, conventional mud materials using anhydrous tar as a binder lose their softness due to volatilization of volatile components such as naphthalene, especially when exposed to high atmospheric temperatures in steelworks and steelworks. In some cases, it may become difficult and the working environment may be deteriorated. Although it has been difficult to manufacture a large amount of mud material at a time due to such curling, the mud material of the present invention does not have such curling and therefore has an advantage of improving workability.
次に実施例、比較例および評価例を挙げて本発明をさらに具体的に説明する。なお、文中の「部」および「%」は特に断りのない限り質量基準である。
実施例1
原料タール100部を脱水塔において約150℃で0.5時間加熱処理して脱水タール(無水タール)97部を得た。該脱水タール97部を常圧蒸留により蒸留し、留分200〜250℃のナフタリン油19部と留分230〜280℃の蒸留油4部と、軟ピッチである釜残74部を得た。以上の原料タール、脱水タール、蒸留油および軟ピッチの性状は下記表1の通りであった。
Next, the present invention will be described more specifically with reference to examples, comparative examples and evaluation examples. In the text, “part” and “%” are based on mass unless otherwise specified.
Example 1
100 parts of raw material tar was heat-treated at about 150 ° C. for 0.5 hours in a dehydration tower to obtain 97 parts of dehydrated tar (anhydrous tar). 97 parts of the dehydrated tar was distilled by atmospheric distillation to obtain 19 parts of naphthalene oil having a fraction of 200 to 250 ° C., 4 parts of distilled oil having a fraction of 230 to 280 ° C., and 74 parts of a residue remaining as a soft pitch. The properties of the raw material tar, dehydrated tar, distilled oil and soft pitch are shown in Table 1 below.
[粘度の測定条件]
JIS Z 8803(1991)液体の粘度−測定方法に準拠してブルックフィールドB型回転粘度計を使用して測定した。
[軟化点の測定条件]
JIS K 2425(1983)6.タールピッチの軟化点測定方法(環球法)に準拠して測定した。
[固定炭素の測定条件]
JIS K 2425(1983)9.固定炭素分定量方法に準拠して電気炉を使用して測定した。
[水分の測定条件]
JIS K 0068(2001)に準拠して容量滴定によりカールフィッシャー法により測定した。
[ナフタリン含有量の測定条件]
ガスクロマトグラフィーにより測定し、内部標準法にて定量を行なった。
[Measurement conditions for viscosity]
According to JIS Z 8803 (1991) liquid viscosity-measurement method, it was measured using a Brookfield B-type rotational viscometer.
[Measurement conditions for softening point]
JIS K 2425 (1983) 6. The tar pitch was measured according to the softening point measurement method (ring ball method).
[Measurement conditions for fixed carbon]
JIS K 2425 (1983) 9. It measured using the electric furnace based on the fixed carbon content determination method.
[Moisture measurement conditions]
It was measured by Karl Fischer method by volumetric titration in accordance with JIS K 0068 (2001).
[Measurement conditions for naphthalene content]
Measured by gas chromatography and quantified by an internal standard method.
上記で得られた蒸留油と軟ピッチとを下記表2に記載の割合で混合して本発明の合成タールを得た。それらの性状も表2に示した。
実施例2
アルミナ、シリカ、炭化珪素、窒化珪素および炭素などからなる粉末耐火材料100部に対し、実施例1の合成タール1の18部を添加して良く混合し本発明のマッド材1を調製した。同様に合成タール5、および合成タール10を用いて本発明のマッド材2およびマッド材3を調製した。
The above-obtained distilled oil and soft pitch were mixed at the ratio shown in Table 2 below to obtain the synthetic tar of the present invention. Their properties are also shown in Table 2.
Example 2
The mud material 1 of the present invention was prepared by adding 18 parts of the synthetic tar 1 of Example 1 to 100 parts of a powder refractory material made of alumina, silica, silicon carbide, silicon nitride, carbon, and the like and mixing them well. Similarly, the mud material 2 and the mud material 3 of the present invention were prepared using the
比較例1
原料タールを加熱釜中において24時間をかけて235℃まで加熱して脱水して比較例の無水タールを製造した。この無水タールの60℃における粘度は280mPa・s、固定炭素は32%、水分0.1%、ナフタリン含有量10.9%であった。この無水タールを用いて実施例2と同様にして比較例のマッド材を得た。
Comparative Example 1
The raw material tar was heated to 235 ° C. in a heating kettle over 24 hours and dehydrated to produce a comparative anhydrous tar. The anhydrous tar had a viscosity at 60 ° C. of 280 mPa · s, fixed carbon of 32%, moisture of 0.1%, and naphthalene content of 10.9%. Using this anhydrous tar, a comparative mud material was obtained in the same manner as in Example 2.
評価例1
実施例1における製造直後の合成タール1、合成タール7、合成タール10および比較例1の脱水後25℃に冷却した直後の無水タールのそれぞれをビーカー中に20gを入れ、35℃の雰囲気に1週間放置後のナフタリン含有量と粘度を測定し下記表3の結果を得た。
Evaluation Example 1
20 g of each of synthetic tar 1, synthetic tar 7,
評価例2
実施例2において調製したマッド材1〜3および比較例のマッド材の原料組成を表4に示す。また、各1kgを35℃で1週間放置した後のそれぞれのマッド材の硬度(柔らかさ)を測定し下記表4の結果を得た。なお、各マッド材の製造直後の硬度も測定して表4に記載した。
Evaluation example 2
Table 4 shows the raw material compositions of the mud materials 1 to 3 prepared in Example 2 and the mud material of the comparative example. Further, the hardness (softness) of each mud material after 1 kg of each was left at 35 ° C. for 1 week was measured, and the results shown in Table 4 below were obtained. In addition, the hardness immediately after manufacture of each mud material was also measured and listed in Table 4.
上記表における硬度の測定方法は以下の通りである。
[硬度の測定方法]
マッド材を70℃で5時間保温した後、針侵入式硬度計(大起理化工業(株)製クラスト硬度計)を用いて測定した。
The method for measuring hardness in the above table is as follows.
[Measurement method of hardness]
After the mud material was kept at 70 ° C. for 5 hours, the mud material was measured using a needle penetration type hardness meter (Crust hardness meter manufactured by Dairika Kogyo Co., Ltd.).
以上の表1〜4に示す結果から明らかな通り、本発明によれば、揮発成分が少なく、長期保管してもその粘度などが変化しない保管安定性に優れ、さらに用途に応じて粘度調整が容易である合成タールを提供することができる。また、本発明によれば、保管安定性に優れるとともに、組織が変質したり亀裂が発生しにくいマッド材を提供することができる。 As is clear from the results shown in Tables 1 to 4 above, according to the present invention, there are few volatile components, the storage stability does not change even when stored for a long time, and the viscosity can be adjusted according to the application. Synthetic tars that are easy can be provided. Furthermore, according to the present invention, it is possible to provide a mud material that is excellent in storage stability and hardly changes in structure or cracks.
Claims (4)
A plug for a molten metal tap, comprising a refractory material and a binder, wherein the binder is the synthetic tar according to any one of claims 1 to 3.
Priority Applications (5)
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JP2004212179A JP4769435B2 (en) | 2004-07-20 | 2004-07-20 | Synthetic tar, plugging material for molten metal outlet, and method for producing the same |
PCT/JP2005/013204 WO2006009128A1 (en) | 2004-07-20 | 2005-07-11 | Coal tar blend and plug for outlet for molten metal |
KR1020067008696A KR100768384B1 (en) | 2004-07-20 | 2005-07-11 | Coal tar blend and plug for outlet for molten metal |
CNA2005800012915A CN1898360A (en) | 2004-07-20 | 2005-07-11 | Coal tar blend and plug for outlet for molten metal |
TW094124469A TWI271433B (en) | 2004-07-20 | 2005-07-20 | Coal tar blend and plug for outlet for molten metal |
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JP2004212179A JP4769435B2 (en) | 2004-07-20 | 2004-07-20 | Synthetic tar, plugging material for molten metal outlet, and method for producing the same |
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JP (1) | JP4769435B2 (en) |
KR (1) | KR100768384B1 (en) |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006151718A (en) * | 2004-11-26 | 2006-06-15 | Shinagawa Refract Co Ltd | Plugging material for molten metal tapping hole |
JP5215861B2 (en) * | 2006-10-20 | 2013-06-19 | 黒崎播磨株式会社 | Mud |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
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TWI501935B (en) * | 2014-01-10 | 2015-10-01 | China Steel Corp | Mud composition of tap hole of blast furnace |
CN105001892B (en) * | 2015-07-17 | 2017-05-24 | 程志宇 | Method for co-production of refined maltha through fixed bed-based coal-tar hydrogenation process |
TWI745848B (en) * | 2020-02-03 | 2021-11-11 | 中國鋼鐵股份有限公司 | Coal tar binder and method of fabricating same |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5959787A (en) * | 1982-09-30 | 1984-04-05 | Nippon Steel Chem Co Ltd | Dehydration of coal tar |
JPS617385A (en) * | 1984-06-22 | 1986-01-14 | Nippon Steel Chem Co Ltd | Hydrogenation treatment of coal tar pitch |
JPS63130696A (en) * | 1986-11-20 | 1988-06-02 | Nippon Steel Chem Co Ltd | Hydrogenation of pitch |
JPH026593A (en) * | 1988-06-27 | 1990-01-10 | Nippon Steel Corp | Production of binder pitch with low ash content |
JPH02194088A (en) * | 1988-12-05 | 1990-07-31 | Ruhrkohle Ag | Method for treating crude tar |
JPH05132675A (en) * | 1991-11-12 | 1993-05-28 | Osaka Gas Co Ltd | Production of pitch |
JPH10324576A (en) * | 1997-05-26 | 1998-12-08 | Shinagawa Refract Co Ltd | Molten metal tapping hole-closing material |
JPH11278949A (en) * | 1998-03-30 | 1999-10-12 | Shinagawa Refract Co Ltd | Closing material for molten metal tap hole |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5413533A (en) * | 1977-07-04 | 1979-02-01 | Kawatetsu Kagaku Kk | Method of reducing 3*4 benzpyrene in coal tar pitch |
JPS60123585A (en) * | 1983-12-07 | 1985-07-02 | Kawasaki Steel Corp | Manufacture of soft pitch |
JPH09151383A (en) * | 1995-11-30 | 1997-06-10 | Kawasaki Steel Corp | Production of binder pitch for carbon material |
-
2004
- 2004-07-20 JP JP2004212179A patent/JP4769435B2/en active Active
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2005
- 2005-07-11 KR KR1020067008696A patent/KR100768384B1/en active IP Right Grant
- 2005-07-11 CN CNA2005800012915A patent/CN1898360A/en active Pending
- 2005-07-11 WO PCT/JP2005/013204 patent/WO2006009128A1/en active Application Filing
- 2005-07-20 TW TW094124469A patent/TWI271433B/en active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5959787A (en) * | 1982-09-30 | 1984-04-05 | Nippon Steel Chem Co Ltd | Dehydration of coal tar |
JPS617385A (en) * | 1984-06-22 | 1986-01-14 | Nippon Steel Chem Co Ltd | Hydrogenation treatment of coal tar pitch |
JPS63130696A (en) * | 1986-11-20 | 1988-06-02 | Nippon Steel Chem Co Ltd | Hydrogenation of pitch |
JPH026593A (en) * | 1988-06-27 | 1990-01-10 | Nippon Steel Corp | Production of binder pitch with low ash content |
JPH02194088A (en) * | 1988-12-05 | 1990-07-31 | Ruhrkohle Ag | Method for treating crude tar |
JPH05132675A (en) * | 1991-11-12 | 1993-05-28 | Osaka Gas Co Ltd | Production of pitch |
JPH10324576A (en) * | 1997-05-26 | 1998-12-08 | Shinagawa Refract Co Ltd | Molten metal tapping hole-closing material |
JPH11278949A (en) * | 1998-03-30 | 1999-10-12 | Shinagawa Refract Co Ltd | Closing material for molten metal tap hole |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006151718A (en) * | 2004-11-26 | 2006-06-15 | Shinagawa Refract Co Ltd | Plugging material for molten metal tapping hole |
JP5215861B2 (en) * | 2006-10-20 | 2013-06-19 | 黒崎播磨株式会社 | Mud |
Also Published As
Publication number | Publication date |
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WO2006009128A1 (en) | 2006-01-26 |
TWI271433B (en) | 2007-01-21 |
KR100768384B1 (en) | 2007-10-18 |
KR20060085940A (en) | 2006-07-28 |
TW200617154A (en) | 2006-06-01 |
CN1898360A (en) | 2007-01-17 |
JP4769435B2 (en) | 2011-09-07 |
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