JPS6025364B2 - Method for producing raw material for high-density carbon material - Google Patents
Method for producing raw material for high-density carbon materialInfo
- Publication number
- JPS6025364B2 JPS6025364B2 JP53054943A JP5494378A JPS6025364B2 JP S6025364 B2 JPS6025364 B2 JP S6025364B2 JP 53054943 A JP53054943 A JP 53054943A JP 5494378 A JP5494378 A JP 5494378A JP S6025364 B2 JPS6025364 B2 JP S6025364B2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- temperature
- spherulites
- density
- components
- 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
- 239000002994 raw material Substances 0.000 title claims description 29
- 239000003575 carbonaceous material Substances 0.000 title claims description 22
- 238000004519 manufacturing process Methods 0.000 title claims description 12
- 239000002904 solvent Substances 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 13
- 239000011294 coal tar pitch Substances 0.000 claims description 10
- 239000011295 pitch Substances 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 6
- 239000000047 product Substances 0.000 description 37
- 238000010304 firing Methods 0.000 description 20
- 241000238557 Decapoda Species 0.000 description 9
- 238000005336 cracking Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 238000007796 conventional method Methods 0.000 description 5
- 238000000465 moulding Methods 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 4
- 238000009835 boiling Methods 0.000 description 4
- 229910052698 phosphorus Inorganic materials 0.000 description 4
- 239000011574 phosphorus Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 238000005452 bending Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000005194 fractionation Methods 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000004005 microsphere Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 241000218691 Cupressaceae Species 0.000 description 1
- 241001465382 Physalis alkekengi Species 0.000 description 1
- 241000251539 Vertebrata <Metazoa> Species 0.000 description 1
- FHKPLLOSJHHKNU-INIZCTEOSA-N [(3S)-3-[8-(1-ethyl-5-methylpyrazol-4-yl)-9-methylpurin-6-yl]oxypyrrolidin-1-yl]-(oxan-4-yl)methanone Chemical compound C(C)N1N=CC(=C1C)C=1N(C2=NC=NC(=C2N=1)O[C@@H]1CN(CC1)C(=O)C1CCOCC1)C FHKPLLOSJHHKNU-INIZCTEOSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000010009 beating Methods 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000009760 electrical discharge machining Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000005087 graphitization Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000004020 luminiscence type Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
Landscapes
- Working-Up Tar And Pitch (AREA)
- Ceramic Products (AREA)
- Carbon And Carbon Compounds (AREA)
Description
【発明の詳細な説明】
本発明は高密度炭素材用原料の製造方法に係り、特にコ
ールタールピッチを加熱処理し溶剤分別して得られる光
学的異方性小球体を、不活性雰囲気中で200〜45ぴ
0の温度で股擁した後、バィンダ−を使用せず成形、焼
成さらに黒鉛化する高密度炭素材用原料の製造方法に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a raw material for high-density carbon materials, and in particular, optically anisotropic small spheres obtained by heat-treating coal tar pitch and solvent fractionation are heated at 200 °C in an inert atmosphere. The present invention relates to a method for producing a raw material for a high-density carbon material, which is held at a temperature of ~45 mm, then molded, fired, and graphitized without using a binder.
従釆、高密度炭素材用原料は、放電加工用電極等の電気
化学用、集電体等の電気用、柑禍、ボート材等の冶金用
、シールリング等の機械用、さらに原子炉材等、極め・
て広範囲にわたって利用され、またさらに開発が進めら
れている。しかして、か)る光学的異方性小球体を利用
した高密度炭素材用原料の製造方法は、従来一般に、石
油系重質油やコールタールピッチ等を350〜500o
Cの温度で加熱処理し、生成した光学的異方性小球体、
すなわち球晶を溶剤分別して行なわれてし、た。Raw materials for high-density carbon materials are used for electrochemical purposes such as electrodes for electrical discharge machining, electrical purposes such as current collectors, metallurgical purposes such as lanterns and boat materials, mechanical purposes such as seal rings, and nuclear reactor materials. etc., mastery
It has been widely used and further development is underway. Therefore, in the conventional method for producing raw materials for high-density carbon materials using such optically anisotropic small spheres, petroleum-based heavy oil, coal tar pitch, etc.
optically anisotropic spherules produced by heat treatment at a temperature of C;
That is, it was carried out by separating the spherulites with a solvent.
しかしてこうして得られた炭素材原料、すなわち上記の
球晶を用いて成形、焼成し次いで黒鉛化して最終製品に
するのである。しかしながら、このような従来の方法で
は、前記球晶を分離する工程にて多量の溶剤を使用し、
何回も溶剤の分別を行なわなければならない。The carbon material raw material thus obtained, that is, the above-mentioned spherulites, is then molded, fired, and then graphitized to produce a final product. However, in such conventional methods, a large amount of solvent is used in the step of separating the spherulites,
The solvent must be separated many times.
しかも、このようにして得られた球晶もまだなお若干の
ピッチ分(例えば8レジン等)や溶剤が残存し易く、こ
れを原料として成形した成形品はその焼成の工程におい
て、残存するピッチ分(例えば8レジン等)や溶剤に起
因する割れや膨れの現象が起り良品を得にくい欠点があ
り、工業的製造方法として可成り問題があった。本発明
者等は、上記の欠点に鑑み、前記の球晶からの高密度炭
素材用原料の製造方法につき鋭意研究の結果、前記球晶
を溶剤分別の後に不活性雰囲気中で200〜4500C
の温度にて澱焼することによって、これを用いた後の競
成工程における割れや膨れの現象を起さない優れた結果
が得られる高密度炭素材用原料の製造方法を見出した。Moreover, the spherulites obtained in this way still tend to have some residual pitch (e.g. 8 resin) and solvent, and molded products made from this raw material are subject to residual pitch during the firing process. (For example, 8 resin, etc.) and solvents can cause cracking and blistering phenomena, making it difficult to obtain good products, and this poses considerable problems as an industrial manufacturing method. In view of the above-mentioned drawbacks, the present inventors conducted extensive research into a method for producing a raw material for high-density carbon materials from the spherulites, and found that the spherulites were separated at 200 to 4,500 C in an inert atmosphere after solvent fractionation.
We have found a method for producing a raw material for high-density carbon material, which produces excellent results that do not cause cracking or blistering in the competitive formation process after starch firing at a temperature of .
すなわち、本発明は、コールタールピッチを350〜5
0000の温度にて加熱処理し、該加熱処理工程で生成
した光学的異方性小球体をピッチ中のB成分と共に溶剤
分別した後、溶剤や3成分の残存する前記光学的異方性
小球体を、次いでさらに不活性雰囲気中において200
〜45ぴ○の温度で蝦暁する高密度炭素材用原料の製造
方法である。That is, the present invention has a coal tar pitch of 350 to 5
After heat treatment at a temperature of 0,000 °C and solvent separation of the optically anisotropic microspheres produced in the heat treatment process together with the B component in the pitch, the optically anisotropic microspheres with the solvent and three components remaining. and then an additional 200 min in an inert atmosphere.
This is a method for producing a raw material for high-density carbon material, which is produced at a temperature of ~45 pi.
さらに詳細に説明すれば、コールタールピッチを350
〜500℃の温度で加熱処理して液相(ピッチ)中に中
間相の球晶を生成させ、溶剤で分別し、これを炉別して
球晶を得る。To explain in more detail, coal tar pitch is 350
A heat treatment is performed at a temperature of ~500° C. to generate intermediate phase spherulites in the liquid phase (pitch), which are fractionated with a solvent and separated in a furnace to obtain spherulites.
かくして得られた球晶は、相当量のピッチ分(例えば8
成分等)や溶剤が残存しており、これを次いで不活性雰
囲気中で200〜450午Cの温度で2〜1畑時間股焼
して球晶中に残存する竪質分を除去し、同時に8成分等
の童質分をキノリン不溶分(QI)に変える。この結果
、y成分やB成分の少ないB1(ベンゼン不溶分)およ
びQIが略々一定の値を有する球晶の蝦焼品が得られる
。この蝦焼品を次いで成形、焼成および黒鉛化して高密
度炭素材を製造することができる。The thus obtained spherulites contain a considerable amount of pitch (e.g. 8
This is then burned in an inert atmosphere at a temperature of 200 to 450 pm for 2 to 1 hour to remove the vertebrates remaining in the spherulites, and at the same time. Converts components such as 8 components into quinoline insoluble components (QI). As a result, a spherulite-fired product having B1 (benzene insoluble content) with a small amount of y component and B component and QI of approximately constant values is obtained. This fired product can then be shaped, fired, and graphitized to produce a high-density carbon material.
前記股焼品は低沸点成分が非常に少ないため、これらの
存在に起因する焼成工程時の割れや膨れの現象を起さず
に良好な結果が得られ、さらに黒鉛化工程を経て高密度
黒鉛材を製造することが可能となる。注目すべきことは
、焼成工程において、200〜45000の間の股焼で
得られる炭素材用原料の高密度を最大なものになし得る
焼成温度が存在し、この温度はコールタールピッチの種
類および球晶の製造条件によってそれぞれ特有の値とな
ること、さらに8成分を多く含む球晶ほど不活性雰囲気
下での股焼によってより高密度の炭素材が得られること
である。なお、前記股焼工程における股焼温度は200
℃より低いと十分な揮発成分の輝教や3成分等からのQ
I生成が行なわれないため効果が得られず、一方450
00を越えると蝦燈品の粘結性が失なわれるため、後の
成形工程にて成形ができなくなる欠点が生ずる。Since the above-mentioned crotch-fired product has very few low-boiling point components, good results can be obtained without cracking or blistering during the firing process due to the presence of these components. It becomes possible to manufacture materials. What should be noted is that in the firing process, there is a firing temperature between 200 and 45,000 that can maximize the density of the raw material for carbon material obtained by firing, and this temperature varies depending on the type of coal tar pitch and The value is unique depending on the manufacturing conditions of the spherulites, and the more the spherulites contain the eight components, the higher the density of carbon material can be obtained by firing the spherulites in an inert atmosphere. In addition, the searing temperature in the searing process is 200℃.
When the temperature is lower than ℃, there is sufficient Q from volatile components such as luminescence and three components.
No effect is obtained because I is not generated, and on the other hand, 450
If it exceeds 00, the caking property of the lamp product will be lost, resulting in the disadvantage that it will not be possible to mold it in the subsequent molding process.
このように本発明は、コールタールピッチを加熱処理し
て得られる球晶を不活性雰囲気下で200〜45000
の温度で蝦焼することによって、前記球品に残存したピ
ッチ分(例えば8レジン等)や溶剤に起因する揮発成分
の蒸発、3成分の重縮合によるQI化を行ない、成形性
の優れた、焼成工程における割れや膨れの現象を生じな
い、しかもより高密度の炭素材を与える股暁球晶を製造
する方法である。In this way, the present invention produces spherulites obtained by heat-treating coal tar pitch under an inert atmosphere.
By firing the shrimp at a temperature of , the pitch (e.g., 8 resin) remaining in the ball product and the volatile components caused by the solvent are evaporated, and QI is created by polycondensation of the three components, resulting in excellent moldability. This is a method for producing spherulite that does not cause cracking or blistering during the firing process and provides a carbon material with higher density.
従来方法に見られた焼成工程における割れや膨れの現象
を解消するのみでなく、溶剤分別をより簡略化でき、経
済的にも廉価な、しかも従来品よりさらに高密度の炭素
材を製造し得るものである。本発明の奏する効果および
応用分野は次の通りである。This method not only eliminates the cracking and blistering phenomena seen in conventional methods during the firing process, but also simplifies solvent separation, makes it possible to produce carbon materials that are economically cheaper and have even higher density than conventional products. It is something. The effects and fields of application of the present invention are as follows.
すなわち、従釆の方法によれば、球晶中に残存する低沸
点ピッテ分や溶剤に起因する焼成工程での割れや膨れの
現象を防止しようとして、溶剤分別操作を繰返しても、
このような低沸点油分は完全に除去できず、焼成時に割
れや膨れの発生する確率は大きかつた。In other words, according to the conventional method, even if the solvent separation operation is repeated in an attempt to prevent cracking and blistering during the firing process caused by the low-boiling point content and solvent remaining in the spherulites,
Such low boiling point oil cannot be completely removed, and there is a high probability that cracks and blisters will occur during firing.
しかるに、本発明方法によれば、不活性雰囲気下で20
0〜450qoの温度において蝦競処理を施して、球晶
中に残存する低沸点のピッチ分(例えば8レジン等)や
溶剤による低輝発分を除き、原料コ−ルタールピッチの
性状、球晶の製造条件、適合した蝦焼条件を選べば、最
大級の高密度を有する焼成品や黒鉛化品を得ることがで
きる。However, according to the method of the present invention, 20
A shrimp competition treatment is performed at a temperature of 0 to 450 qo to remove low boiling point pitch components (e.g. 8 resin) remaining in the spherulites and low brightness components due to solvents, and evaluate the properties of the raw coal tar pitch and the spherulite properties. By selecting manufacturing conditions and suitable firing conditions, fired products and graphitized products with the highest density can be obtained.
また、蝦燐により高密度を調節することが可能であるの
で、従来のような成形圧力だけで炭素材の高密度を制御
しようとする方法に比較して、前記の澱焼条件と成形圧
力との任意かつ適当な組合わせによってより広範囲の物
性を有する炭素材を、容易に得ることが可能となり、炭
素材の用途をさらに拡大することができる。さらにまた
、本発明によれば、驚くべきことには、a成分を多く含
む球晶ほど適切な蝦焼処理を施すことによって、より高
密度の炭素材が得られることが明らかとなり、同時に8
成分をQI化し炭素材として有効に利用する結果原料コ
ールタールピッチに対する球晶を主体とした炭素材用原
料の収率は著しく向上した。In addition, since it is possible to adjust the high density using shrimp phosphorus, compared to the conventional method of controlling the high density of carbon materials using only molding pressure, it is possible to control the high density of carbon materials by adjusting the starch conditions and molding pressure described above. By arbitrarily and appropriately combining these, it becomes possible to easily obtain a carbon material having a wider range of physical properties, and the uses of the carbon material can be further expanded. Furthermore, according to the present invention, it has been surprisingly revealed that the more a-component-containing spherulites are subjected to an appropriate firing treatment, the more dense the carbon material can be obtained.
As a result of converting the components into QI and effectively using them as carbon materials, the yield of raw materials for carbon materials mainly consisting of spherulites compared to raw material coal tar pitch was significantly improved.
これらのことは、石油系重質油を出発原料とする球晶に
ついても同様である。次に実施例についてさらに説明す
る。The same applies to spherulites using petroleum heavy oil as a starting material. Next, examples will be further described.
実施例 1
B成分をそれぞれ6.6重量%、3.5重量%含有する
球晶A,Bを不活性雰囲気下で2時間股焼して股競品を
得た。Example 1 Spherulites A and B containing 6.6% by weight and 3.5% by weight of component B, respectively, were calcined in an inert atmosphere for 2 hours to obtain a spherulite.
蝦競温度は各々250〜65000の間で100oo間
隔で行なった。椴焼品の分析値の一例として35000
の椴蛾のものを表一1に示す。本実施例1で述べる、蝦
焼を行なわないとは、抽出後、アセトンで洗浄後、90
00、3時間で減圧乾燥を行なっているのは当然である
。表−1 350℃殴り1,品の分析値この椴焼
品と股燐を行わない原料球晶A,Bについて、それぞれ
円筒状の直径5伍舷0の金型を用い、1.5ton/汝
の圧力で加圧成形し、次いで2000/hの昇温速度で
1000ooまで昇温し、さらに2時間この温度に維持
し焼成して焼成品を得、これを260000の温度にて
黒鉛化した。The temperature of each shrimp competition was between 250 and 65,000 at intervals of 100 oo. An example of the analysis value of Shuba-yaki products is 35,000.
Table 1 shows the results of the cypress moth. In this Example 1, not performing shrimp roasting means that after extraction, after washing with acetone,
It is natural that the vacuum drying is carried out for 3 hours. Table 1: 350°C beating 1, analysis value of the product For this ceramic-fired product and the raw material spherulites A and B that are not phosphorized, a cylindrical mold with a diameter of 5 m2 was used, and 1.5 ton/you The molded product was press-molded at a pressure of 2,000 mm/h, and then heated to 1,000 oo degrees at a heating rate of 2,000 mm/h, and then maintained at this temperature for 2 hours to obtain a fired product, which was graphitized at a temperature of 260,000 mm.
このようにして得られた焼成品および黒鉛化品をそれぞ
れについて測定した特性値と蝦暁温度との関係を、特性
別に第1図には高密度、第2図には曲げ強度、第3図に
は固有抵抗についてそれぞれ示した。Figure 1 shows high density, Figure 2 shows bending strength, Figure 3 shows the relationship between the characteristic values measured for the fired products and graphitized products obtained in this way and the temperature of the shrimp. shows the specific resistance.
第1図から明らかなように、8成分を多く含むAを原料
としたものは3500○、8成分の少ないBを原料とし
たものは250COの椴暁温度のものが最大の高密度を
示し、かつ8成分の多いAを原料としたものの方がより
高い高密度を示した。As is clear from Fig. 1, the highest density is shown at 3500° for the material made from A, which contains many 8 components, and 250 CO for the material made from B, which contains less 8 components. In addition, the material made from A, which contains many 8 components, exhibited higher density.
また、250〜4500Cの間の蝦焼温度にて得られた
蝦焼品についてはすべて良好な成形性を有しかつ焼成時
における割れや膨れが皆無であったが、500C○以上
の脇焼品は粘絹性が低下し成形が困難となり良好な成形
品が得られず、焼成、黒鉛化ができなかった。一方、前
記の股燐を施さない原料A,Bを焼成したものは、割れ
や膨れの発生する確率が大きかつた。In addition, all of the shrimp-fired products obtained at a firing temperature of 250 to 4,500C had good formability and had no cracks or blisters during firing, but side-fired products of 500C or higher The viscosity decreased and molding became difficult, and a good molded product could not be obtained, and firing and graphitization could not be performed. On the other hand, when raw materials A and B were fired without being phosphoroused, there was a high probability that cracks and blisters would occur.
実施例 2
8成分を27.$重量%含有する球晶Cを原料とし、こ
のCと、このCを不活性雰囲気中で35000の温度で
1餌時間股競を行なった蝦競品を前記実施例1と同様に
それぞれ成形し、焼成した。Example 2 8 ingredients were mixed into 27. Using spherulite C containing $% by weight as a raw material, shrimp competition products were molded in the same manner as in Example 1, in which this C and this C were competed for one feeding time at a temperature of 35,000 °C in an inert atmosphere. , fired.
この結果、股競品からは第5図a,bに示すように割れ
や膨れのない嵩密度1.73夕/地、曲げ強度960k
9/仇を有する良好な焼成品が得られたが、股焼を施さ
ないCからのものは第6図a,bに示すように割れや膨
れが発生した。As a result, as shown in Figure 5 a and b, the product had a bulk density of 1.73 mm/ground without cracks or blisters, and a bending strength of 960 k.
Although a good fired product having a 9/2 degree of heat was obtained, cracks and blisters occurred in the product from C, which was not subjected to cross-firing, as shown in FIGS. 6a and 6b.
なお、股焼品の分析値は表−2に示す通りであつた。The analytical values of the roasted product were as shown in Table 2.
表−2 350,℃■酸燐Mの分析値本実施例2で
述べる、蝦燐を行なわないとは、抽出後、アセトンで洗
浄後、90oo、3時間で減圧乾燥を行なっているのは
当然である。Table 2 350,℃ ■Analysis value of acid phosphorus M As mentioned in this Example 2, not performing phosphorus means that after extraction, washing with acetone, drying under reduced pressure at 90oo for 3 hours is natural. It is.
実施例 3
同じ原料コールタールピッチから試作したそれぞれ異な
った8成分量を含有する球晶A,B,D,EおよびFを
原料として、不活性雰囲気中において、各原料について
それぞれの成形焼成品が最高の嵩密度を示す最適の蝦鱗
条件で股焼を行なつた。Example 3 Using spherulites A, B, D, E, and F, each containing different amounts of eight components, which were trial-produced from the same raw material coal tar pitch, as raw materials, molded and fired products were produced for each raw material in an inert atmosphere. Roasting was carried out under optimal shrimp scale conditions that gave the highest bulk density.
次いで得られた股蛭品をそれぞれ前記実施例1と同様に
成形焼成を行ない、焼成中に割れや膨れの現象を生じる
ことなく良好な焼成品を得た。Next, each of the obtained crotch products was molded and fired in the same manner as in Example 1, and a good fired product was obtained without any cracking or blistering phenomena during firing.
かくして得られた焼成品の高密度と原料球晶中の8成分
含有量との関係を第4図に示す。すなわち、第4図は横
軸に股暁前における8−レジン量%を、縦軸に焼成品の
嵩密度夕/洲を表わす。図中の記号A,B,C,D,E
およびFは、それぞれ該焼成品に対応する原料球晶の種
類を、数値は原料球晶の3成分含有量を示す。第4図か
ら明らかなように、原料球晶中の8成分含有量が多いも
のほど、蝦鱗処理を行なって成形、焼成して得られる焼
成品の嵩密度は高くなっており、高密度炭素材用原料向
けとして好ましいことが判る。FIG. 4 shows the relationship between the high density of the fired product thus obtained and the content of eight components in the raw material spherulites. That is, in FIG. 4, the horizontal axis represents the amount of 8-resin before dawn, and the vertical axis represents the bulk density of the fired product. Symbols A, B, C, D, E in the diagram
and F indicate the type of raw material spherulite corresponding to the fired product, and the numerical values indicate the three component contents of the raw material spherulite. As is clear from Figure 4, the higher the content of the eight components in the raw material spherulite, the higher the bulk density of the fired product obtained by molding and firing after the shrimp scale treatment. It is found that it is preferable as a raw material for raw materials.
また、次の表−3には、原料D(B成分4.6重量%)
、原料E(3成分14.7重量%)それぞれの股暁後の
分析値を示す。In addition, in the following Table 3, raw material D (B component 4.6% by weight)
, shows the analytical values of raw material E (three components 14.7% by weight) after dawn.
表−3 殿焼品の分析値Table-3 Analysis values of Tonoyaki products
第1図は本発明の実施例1における焼成品並びに黒鉛化
品について股競温度と高密度との関係を示す線図、第2
図は同じくその股嬢温度と曲げ強さとの関係を示す線図
、第3図は同じくその蝦燐温度と固有抵抗との関係を示
す線図、第4図は本発明に係る原料球晶の8成分含有量
と股暁後の焼成品の高密度との関係を示す線図、第5図
a,bは本発明の実施例2における焼成品(蝦競工程を
経てもの)の外観を示すそれぞれ平面図および側面図、
および第6図a,bは第5図に比較するため暇暁工程を
経ない原料球晶からの焼成品を示すそれぞれ平面図およ
び側面図である。
第1図
第2図
第3図
第5図
第4図
第6図FIG. 1 is a diagram showing the relationship between temperature and high density for fired products and graphitized products in Example 1 of the present invention, and FIG.
Figure 3 is a diagram showing the relationship between crotch temperature and bending strength, Figure 3 is a diagram showing the relationship between phosphorus temperature and specific resistance, and Figure 4 is a diagram showing the relationship between spherulite temperature and specific resistance. A diagram showing the relationship between the content of 8 components and the high density of the fired product after baking, FIGS. plan and side views, respectively;
6a and 6b are a plan view and a side view, respectively, showing a fired product made from raw material spherulites that do not undergo the aging process, for comparison with FIG. 5. Figure 1 Figure 2 Figure 3 Figure 5 Figure 4 Figure 6
Claims (1)
加熱処理し、該加熱処理工程で生成した光学的異方性小
球体をピツチ中のβ成分と共に溶剤分別した後、溶剤や
β成分の残存する前記光学的異方性小球体を、次いでさ
らに不活性雰囲気中において200〜450℃の温度で
■焼することを特徴とする高密度炭素材用原料の製造方
法。1 Coal tar pitch is heat-treated at a temperature of 350 to 500°C, and after the optically anisotropic spherules generated in the heat treatment process are separated from the solvent together with the β component in the pitch, the solvent and β component remain. A method for producing a raw material for a high-density carbon material, characterized in that the optically anisotropic small spheres are then further baked at a temperature of 200 to 450°C in an inert atmosphere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53054943A JPS6025364B2 (en) | 1978-05-11 | 1978-05-11 | Method for producing raw material for high-density carbon material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53054943A JPS6025364B2 (en) | 1978-05-11 | 1978-05-11 | Method for producing raw material for high-density carbon material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54157791A JPS54157791A (en) | 1979-12-12 |
| JPS6025364B2 true JPS6025364B2 (en) | 1985-06-18 |
Family
ID=12984719
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53054943A Expired JPS6025364B2 (en) | 1978-05-11 | 1978-05-11 | Method for producing raw material for high-density carbon material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6025364B2 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59164604A (en) * | 1983-03-11 | 1984-09-17 | Koa Sekiyu Kk | Manufacture of isotropic carbonaceous material of high density |
| JPS6016806A (en) * | 1983-07-06 | 1985-01-28 | Koa Sekiyu Kk | Manufacture of formed carbon |
| JPS60200816A (en) * | 1984-03-26 | 1985-10-11 | Kawasaki Steel Corp | Production of carbonaceous material |
| JPS62108767A (en) * | 1985-11-06 | 1987-05-20 | 川崎製鉄株式会社 | Manufacture of high oxidation resistance isotropic high density high strength carbon material |
| JPH0645504B2 (en) * | 1986-11-28 | 1994-06-15 | 川崎製鉄株式会社 | High-density and high-strength carbon material manufacturing method |
| JP2782193B2 (en) * | 1988-02-17 | 1998-07-30 | 大阪瓦斯株式会社 | How to dry mesocarbon microbeads |
-
1978
- 1978-05-11 JP JP53054943A patent/JPS6025364B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54157791A (en) | 1979-12-12 |
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