JPH03281692A - Preparation of starting powder for carbonaceous material - Google Patents
Preparation of starting powder for carbonaceous materialInfo
- Publication number
- JPH03281692A JPH03281692A JP2084700A JP8470090A JPH03281692A JP H03281692 A JPH03281692 A JP H03281692A JP 2084700 A JP2084700 A JP 2084700A JP 8470090 A JP8470090 A JP 8470090A JP H03281692 A JPH03281692 A JP H03281692A
- Authority
- JP
- Japan
- Prior art keywords
- product
- weight
- raw material
- less
- soluble content
- 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.)
- Granted
Links
- 239000003575 carbonaceous material Substances 0.000 title claims abstract description 15
- 239000000843 powder Substances 0.000 title claims abstract description 13
- 239000002994 raw material Substances 0.000 claims abstract description 21
- 239000011280 coal tar Substances 0.000 claims abstract description 9
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 claims description 12
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 12
- 239000002245 particle Substances 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 238000009760 electrical discharge machining Methods 0.000 abstract description 9
- 238000010438 heat treatment Methods 0.000 abstract description 8
- 238000010298 pulverizing process Methods 0.000 abstract description 3
- 230000000704 physical effect Effects 0.000 abstract description 2
- 239000000047 product Substances 0.000 description 27
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 10
- 238000000034 method Methods 0.000 description 6
- 239000011347 resin Substances 0.000 description 6
- 229920005989 resin Polymers 0.000 description 6
- 229910052786 argon Inorganic materials 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000011305 binder pitch Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000011284 carbonization tar Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011294 coal tar pitch Substances 0.000 description 1
- 238000009694 cold isostatic pressing Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000005087 graphitization Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002931 mesocarbon microbead Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002006 petroleum coke Substances 0.000 description 1
- 239000011295 pitch Substances 0.000 description 1
- 239000006253 pitch coke Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Landscapes
- Carbon And Carbon Compounds (AREA)
- Working-Up Tar And Pitch (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は高密度特殊炭素材用として有用な原料粉の製法
に関するものである。さらに詳しくは高密度でかつ放電
加工特性が良い特殊炭素材用原料粉の製法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing raw material powder useful for high-density special carbon materials. More specifically, the present invention relates to a method for producing raw material powder for special carbon materials that has high density and good electrical discharge machining properties.
従来特殊炭素材はピッチコークス、及び石油コークスを
所定の割合に粒度配合した粒と粉を加熱、混合しながら
バインダーピッチを適当量添加ねつ含酸、成形して製造
される。さらにこの生成形体を焼成、黒鉛化後、加工し
て製品である特殊炭素材を製造している。また、最近ピ
ッチを熱処理後、溶剤で処理して得たメソカーボンマイ
クロビーズを成形して特殊炭素材を製造する方法も報告
されている。Conventionally, special carbon materials are produced by heating and mixing grains and powder of pitch coke and petroleum coke in a predetermined ratio, adding an appropriate amount of binder pitch, adding acid, and forming. Furthermore, this formed body is fired, graphitized, and then processed to produce a special carbon material product. Furthermore, a method has recently been reported in which a special carbon material is produced by molding mesocarbon microbeads obtained by heat-treating pitch and then treating it with a solvent.
これらの方法は製品の嵩密度が低い、強度が低い等製品
の特性が不十分であり、また工程が複雑で製造コストが
高い等の課題があり、低コストで特性の良い特殊炭素材
の出現が望まれていた。These methods have problems such as insufficient product properties such as low bulk density and low strength, and complicated processes and high manufacturing costs.The emergence of special carbon materials with low cost and good properties. was desired.
又近年炭素材は放電加工用電極としての利用が注目され
、需要が急増の傾向にあるが従来の炭素材では放電加工
特性が不十分であり、もっと放電加工特性の良い炭素材
、特に放電加工時の消耗率が低い炭素材が要求されてい
る。またメソカーボンから製造した炭素材では工程が複
雑なためコストが高く、製造コストが低く高特性のもの
が求められている。In recent years, carbon materials have been attracting attention for their use as electrodes for electrical discharge machining, and demand is rapidly increasing. There is a need for carbon materials that have a low wear rate over time. Furthermore, carbon materials manufactured from mesocarbon are expensive due to complicated processes, and there is a demand for materials with low manufacturing costs and high properties.
ciaを解決するための手段〕
そこで、本発明者は、かかる状況に鑑み、高強度でかつ
放電特性の良い特殊炭素材を製造すべく鋭意検討した結
果、コールタール系原料を熱処理しある特性を持つ原料
となし微粉砕して成形後、製品とすると高特性となるこ
とを見出し、本発明に到達した。[Means for solving cia] Therefore, in view of this situation, the present inventor conducted intensive studies to produce a special carbon material with high strength and good discharge characteristics. The present invention was achieved based on the discovery that a product with high properties can be obtained by pulverizing the raw material and molding it into a product.
すなわち、本発明の要旨は、コールタール系原料を熱処
理して得られる生成物であって、粉砕して平均粒度を1
5〜20μとしたものの揮発分(VM)が20重量%以
下で3重量%以上であり、かつトルエン可溶分(TS)
Cr−レジン)が10重量%以下で1重量%以上であり
かつ、キノリン可溶分(QS)とトルエン可溶分(TS
)の差が2重量%以下であるものを微粉砕することを特
徴とする炭素材用原料粉の製法にある。That is, the gist of the present invention is a product obtained by heat-treating a coal tar-based raw material, which is crushed to have an average particle size of 1.
Volatile content (VM) of 5 to 20μ is 20% by weight or less and 3% by weight or more, and toluene soluble content (TS)
Cr-resin) is 10% by weight or less and 1% by weight or more, and the quinoline soluble content (QS) and toluene soluble content (TS
) is pulverized into powder having a difference of 2% by weight or less.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
まず、本発明におけるコールタール系原料は、石炭乾留
時に副生するコールタール又はこれより得られるコール
タールピッチであり、そのVMは30fi量%を超えて
もよいが30重量%を超えると目標の物性に調整する時
間が長く、処理能力が落ち、コストが高くなるので該原
料のVMは30重量%以下が望ましい。First, the coal tar-based raw material in the present invention is coal tar produced as a by-product during coal carbonization or coal tar pitch obtained therefrom, and its VM may exceed 30% by weight, but if it exceeds 30% by weight, the target The VM of the raw material is preferably 30% by weight or less because it takes a long time to adjust the physical properties, reduces processing capacity, and increases cost.
またこれらの原料はアルゴン量が高過ぎると軽沸点留分
が多く融着するために熱処理効率が悪く該原料のアルゴ
ン量は30重量%以下が望ましい。Furthermore, if the amount of argon in these raw materials is too high, a large amount of low-boiling fractions will be fused, resulting in poor heat treatment efficiency, so the amount of argon in these raw materials is preferably 30% by weight or less.
これらのコールタール系原料は通常コールタールをデイ
レードコーカー、オートクレーブ等により350〜48
0℃、1〜72時間程度で熱処理することで作られる。These coal tar-based raw materials are usually heated to 350 to 48
It is produced by heat treatment at 0°C for about 1 to 72 hours.
本発明において、コールタール系原料の熱処理は通常、
200〜350℃、0.5〜48時間程度で行われるが
、処理を均一に行なうために機械的エネルギーを付与し
た方が効果が大きい。機械エネルギーの付与の方法とし
ては撹拌、超音波等が挙げられる。また熱処理は不活性
ガス(アルゴン、窒素等)中、自生圧下で行なってもよ
いが、好適には空気の存在下で行なわれる。In the present invention, the heat treatment of coal tar-based raw materials is usually carried out by
The treatment is carried out at 200 to 350° C. for about 0.5 to 48 hours, but it is more effective to apply mechanical energy to ensure uniform treatment. Examples of methods for applying mechanical energy include stirring and ultrasonic waves. The heat treatment may be performed in an inert gas (argon, nitrogen, etc.) under autogenous pressure, but is preferably performed in the presence of air.
本発明において目的とする熱処理生成物は、粉砕して平
均粒度を15〜2.0μとしたもののVMが20重量%
以下で3重量%以上であり、かつTSが10重量%以下
で1重置%以上であり、かつQSとTSO差(QS−T
S)が2重量%以下である生成物である。The target heat-treated product of the present invention has a VM of 20% by weight after being pulverized to an average particle size of 15 to 2.0μ.
3% by weight or more, and TS is 10% by weight or less and 1% or more by weight, and the difference between QS and TSO (QS-T
S) is less than or equal to 2% by weight.
すなわち、まず該熱処理生成物のVMが20%を超える
と焼成時の重量減少が大き過ぎ特性が悪化し、一方、3
%未満では焼結性が悪く特性が悪くなる。また該粉砕物
のTS (アルゴン)量が10%以上を超えると焼成時
に成形体が発泡で割れてしまう。1%未満では焼結成分
が少なく特性が悪化する。That is, first of all, if the VM of the heat-treated product exceeds 20%, the weight loss during firing is too large and the properties deteriorate;
If it is less than %, the sinterability will be poor and the properties will deteriorate. Furthermore, if the amount of TS (argon) in the pulverized product exceeds 10% or more, the molded product will foam and crack during firing. If it is less than 1%, the sintered component will be small and the properties will deteriorate.
さらに、QSとTSO差が2重量%を超えると成形体の
組織が不均質となり特性が悪化する。QSとTSの差が
2重量%以下であれば成形体組織は均質になり成形体特
性は良くなる。Furthermore, if the difference between QS and TSO exceeds 2% by weight, the structure of the molded article will become non-uniform and its properties will deteriorate. If the difference between QS and TS is 2% by weight or less, the molded product structure will be homogeneous and the molded product properties will be improved.
本発明においては、このようにして得られた生成物を微
粉砕して原料粉を得る。良好な成形品を得るためには原
料粉の平均粒度は50μ以下が望ましいが製品組織の均
一性をさらに向上させるためには好ましくは30μ以下
、さらに好ましくは20μ以下、最も好ましくは10μ
以下に微粉砕するのが望ましい。In the present invention, the product thus obtained is pulverized to obtain raw material powder. In order to obtain a good molded product, the average particle size of the raw material powder is preferably 50μ or less, but in order to further improve the uniformity of the product structure, it is preferably 30μ or less, more preferably 20μ or less, and most preferably 10μ.
It is preferable to pulverize the powder to a fine powder.
成形体を得るための成形は通常のモールド成形、冷間等
方圧成形等が用いられる。また焼成は不活性ガス中、コ
ークスプリーズ中いずれでも可能であり、800〜10
00℃の温度でなされる。さらに黒鉛化は常法が使用で
き(タンマン炉、アチソン炉、誘導加熱)、通常200
0〜3000℃でなされる。For forming to obtain a molded article, ordinary molding, cold isostatic pressing, etc. are used. Calcining can be done either in an inert gas or in a coke pleat.
It is done at a temperature of 00°C. Furthermore, conventional methods can be used for graphitization (Tammann furnace, Acheson furnace, induction heating), and usually 200
It is made at 0-3000°C.
以下、実施例により本発明の詳細な説明する。 Hereinafter, the present invention will be explained in detail with reference to Examples.
なお実施例中、%とあるのは重量%を意味する。In addition, in the examples, % means weight %.
実施例I
VMが20.5%でかつTレジン量が24.4%のコー
ルタール系原料を空気の存在下で機械エネルギーを付与
しながら230℃、80分で熱処理を行なった。生成物
の平均粒度を16μとした時のVMは15.2%であり
、アルゴン量は5.2%であった。またキノリン可溶分
は6.6%でありQSとTSの差は1.4%であった。Example I A coal tar-based raw material having a VM of 20.5% and a T resin amount of 24.4% was heat-treated at 230° C. for 80 minutes while applying mechanical energy in the presence of air. When the average particle size of the product was 16μ, the VM was 15.2% and the amount of argon was 5.2%. The quinoline soluble content was 6.6%, and the difference between QS and TS was 1.4%.
この微粉砕品をモールドブレスにて成形した。この成形
体を酸化防止のためコークスプリーズ中1000℃まで
焼成後タンマン炉で2800℃まで黒鉛化して製品を得
た。黒鉛成形体の嵩密度は1.88であり、放電加工時
の消耗率は1.2%であった。This finely pulverized product was molded using a mold press. This compact was fired to 1000° C. in a coke shower to prevent oxidation, and then graphitized to 2800° C. in a Tammann furnace to obtain a product. The bulk density of the graphite molded body was 1.88, and the consumption rate during electrical discharge machining was 1.2%.
実施例2
VMが20.6%でγレジンが21.1%の原料を25
0℃、70分で実施例1と同様に熱処理して平均粒度1
7μでのVMが14.9%、γレジン量が5.5%のも
のを得た。この生成物のキノリン可溶分は5.4%であ
り、QSとTSO差は−0,1%であった。この微粉砕
品を実施例1と同様の方法で成形体を製造した。その嵩
密度は1.89、放電加工時の消耗率は0.7%であっ
た。Example 2 25% of raw material with VM of 20.6% and γ resin of 21.1%
Heat treated at 0°C for 70 minutes in the same manner as in Example 1 to obtain an average particle size of 1.
A product was obtained in which the VM at 7μ was 14.9% and the amount of γ resin was 5.5%. The quinoline soluble content of this product was 5.4%, and the difference between QS and TSO was -0.1%. A molded body was produced from this finely pulverized product in the same manner as in Example 1. Its bulk density was 1.89, and its wear rate during electrical discharge machining was 0.7%.
比較例1
実施例1と同じ原料を熱処理して平均粒度17μでのV
Mが14.6%、γレジン量が6.9%のものを得た。Comparative Example 1 The same raw material as in Example 1 was heat-treated to obtain V with an average particle size of 17μ.
A product was obtained in which M was 14.6% and the amount of γ resin was 6.9%.
この生成物のキノリン可溶分は10.5%であり、QS
とTSの差は3.6%であった。この微粉砕品を実施例
1と同様の方法で成形体を製造した。その嵩密度は1.
77、放電加工時の消耗率は3.8%であった。The quinoline soluble content of this product was 10.5%, QS
The difference between TS and TS was 3.6%. A molded body was produced from this finely pulverized product in the same manner as in Example 1. Its bulk density is 1.
77, the wear rate during electrical discharge machining was 3.8%.
比較例2
実施例2と同じ原料を熱処理して平均粒度16μでのV
Mが14.4%、Tレジン量が7.4%のものを得た。Comparative Example 2 The same raw material as in Example 2 was heat-treated to obtain V at an average particle size of 16μ.
A product containing 14.4% M and 7.4% T resin was obtained.
この生成物のキノリン可溶分は17.9%であり、QS
とTSの差は10.5%であった。The quinoline soluble content of this product was 17.9%, QS
The difference between TS and TS was 10.5%.
この微粉砕品を実施例1と同様の方法で成形体を製造し
た。その嵩密度は1.79、放電加工時の消耗率は9.
7%であった。A molded body was produced from this finely pulverized product in the same manner as in Example 1. Its bulk density is 1.79, and its wear rate during electrical discharge machining is 9.
It was 7%.
比較例3
市販品の嵩密度、放電加工時の消耗率を同時に測定した
らそれぞれ1.84.4.4重量%であった。Comparative Example 3 The bulk density and wear rate during electrical discharge machining of a commercially available product were simultaneously measured and found to be 1.84 and 4.4% by weight, respectively.
本発明の方法による原料粉を用いた炭素材は嵩密度が高
く、放電加工特性が非常に良い(消耗率が低い)。The carbon material using the raw material powder produced by the method of the present invention has a high bulk density and has very good electrical discharge machining characteristics (low wear rate).
Claims (1)
であって、粉砕して平均粒度を15〜20μとしたもの
の揮発分(VM)が20重量%以下で3重量%以上であ
り、トルエン可溶分(TS)が10重量%以下で1重量
%以上であり、かつ、キノリン可溶分(QS)とトルエ
ン可溶分(TS)の差が2重量%以下であるものを微粉
砕することを特徴とする炭素材用原料粉の製法。(1) A product obtained by heat-treating a coal tar-based raw material, which is pulverized to an average particle size of 15 to 20 μm and has a volatile content (VM) of 20% by weight or less and 3% by weight or more, and toluene. The soluble content (TS) is 10% by weight or less and 1% by weight or more, and the difference between the quinoline soluble content (QS) and toluene soluble content (TS) is 2% by weight or less. A method for producing raw material powder for carbon materials, which is characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2084700A JP2808807B2 (en) | 1990-03-30 | 1990-03-30 | Production method of raw material powder for carbon material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2084700A JP2808807B2 (en) | 1990-03-30 | 1990-03-30 | Production method of raw material powder for carbon material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03281692A true JPH03281692A (en) | 1991-12-12 |
JP2808807B2 JP2808807B2 (en) | 1998-10-08 |
Family
ID=13837943
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2084700A Expired - Lifetime JP2808807B2 (en) | 1990-03-30 | 1990-03-30 | Production method of raw material powder for carbon material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2808807B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6392701B2 (en) * | 2015-05-12 | 2018-09-19 | 株式会社神戸製鋼所 | Raw material pitch for carbon fiber production |
-
1990
- 1990-03-30 JP JP2084700A patent/JP2808807B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JP2808807B2 (en) | 1998-10-08 |
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