JPS61117109A - Preparation of impregnating pitch for electrode - Google Patents

Preparation of impregnating pitch for electrode

Info

Publication number
JPS61117109A
JPS61117109A JP59235229A JP23522984A JPS61117109A JP S61117109 A JPS61117109 A JP S61117109A JP 59235229 A JP59235229 A JP 59235229A JP 23522984 A JP23522984 A JP 23522984A JP S61117109 A JPS61117109 A JP S61117109A
Authority
JP
Japan
Prior art keywords
pitch
electrode
quinoline
filtration
impregnating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP59235229A
Other languages
Japanese (ja)
Inventor
Shosuke Takahashi
高橋 祥介
Toshihide Suzuki
利英 鈴木
Kazuhiro Hasegawa
和広 長谷川
Noriyoshi Fukuda
福田 典良
Takeshi Nagasawa
長沢 健
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP59235229A priority Critical patent/JPS61117109A/en
Publication of JPS61117109A publication Critical patent/JPS61117109A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To prepare an impregnating pitch for electrode having improved impregnability to an electrode and cong. substantially no trace impurities by removing trace amt. of impurity in a pitch freed of quinoline insolubles by filtration, fractional solvent extraction, or centrifuging, etc. CONSTITUTION:Coal tar cong. <0.1% quinoline-insolubles which has been freed of quinoline-insolubles, or pich obtd. from said coal tar is subjected further to the treatment for removing impurities (such as filtration of molten pitch, etc.), thus, purifieid pitch cong. <=0.05% impurity, suitable for impregnating electrode having high bulk density and increasing effect for the strength of the electrode, is obtd.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は電気炉用炭素電極の製造に使用するのに適当な
ピッチ浸透性の改良された電極用含浸ピッチの製造方法
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 impregnated pitch for electrodes with improved pitch permeability suitable for use in producing carbon electrodes for electric furnaces.

(従来の技術) 従来、高品質の人造黒鉛電極を製造する場合には、コー
ルタールまたはコールタールピッチから石炭系針状コー
クスを製造する際に、タールやピッチに含有されている
数パーセントのキノリンネ溶物質を予め除去することが
必要とされ、種々の除去法が開発されている。例えば、
特公昭49−11608号公報にはキノリン不溶分の低
いタールまたはピッチを得る方法として溶剤と混合後、
一工程の遠心分離で効率よく痕跡量または0.4チまで
のキノリン不溶分を除去できることが記載されている。
(Prior art) Conventionally, when producing high-quality artificial graphite electrodes, when producing coal-based needle coke from coal tar or coal tar pitch, a few percent of quinoline coke contained in the tar or pitch was used. It is necessary to remove dissolved substances in advance, and various removal methods have been developed. for example,
Japanese Patent Publication No. 49-11608 describes a method for obtaining tar or pitch with low quinoline insoluble content after mixing with a solvent.
It is described that a trace amount or up to 0.4 inch of insoluble quinoline can be efficiently removed by one step of centrifugation.

特開昭52−78201号公報、には混合溶剤によりキ
ノリン不溶分を含む粒子を粗大化させ、沈降分離する方
法が提案されている。また、特開昭52−28501号
公報には類似の溶剤混合によりキノリン不溶分を除去し
、キノリン不溶分を実質的に痕跡量の0.1%未満にす
ることが提案されている。キノリン不溶分の現行分析法
では、0.1.4未満は分析値として誤差範囲とされて
いる。
JP-A-52-78201 proposes a method in which particles containing insoluble quinoline are coarsened using a mixed solvent and then separated by sedimentation. Furthermore, Japanese Patent Laid-Open No. 52-28501 proposes removing quinoline insolubles by mixing a similar solvent to substantially reduce the quinoline insolubles to less than a trace amount of 0.1%. In the current analytical method for quinoline insoluble matter, a value of less than 0.1.4 is considered to be within the error range as an analytical value.

他方において、電気デ用炭素電極の製造においては、一
般にカサ密度および強度を向上する目的として、石油系
または石炭系ピッチコークスとバインダーとしてのピッ
チを加熱混線後、成形焼成して電極とする場合に、ピッ
チを軟化溶融し、7〜15に9/cnJの圧力で電極の
気孔に含浸させ、焼成する工程を1〜3回繰返し行って
1tffiにおける気孔率を低め、カサ密度を向上させ
ている。この場合、微小な気孔へ粘度の高い溶融ピッチ
を含浸させる工程では1回の含浸毎に長時間を要するば
かりか、気孔への均一な含浸を達成できない。このため
に、含浸用ピッチとしては気孔に浸透しゃすく、かつ炭
化時の固定炭素分の多い、すなわち、炭化歩りの高いこ
とが要求されている。しかし、この炭化歩りは、一般に
高軟化点ピッチの方が高いが、同時に粘度が高くなるた
めに含浸性が悪くなる。
On the other hand, in the production of carbon electrodes for electrical devices, in order to improve the bulk density and strength, petroleum-based or coal-based pitch coke and pitch as a binder are heated, mixed, and then shaped and fired to form electrodes. The process of softening and melting the pitch, impregnating it into the pores of the electrode at a pressure of 7 to 15 to 9/cnJ, and firing it is repeated 1 to 3 times to lower the porosity at 1 tffi and improve the bulk density. In this case, the step of impregnating the minute pores with the highly viscous molten pitch not only takes a long time for each impregnation process, but also makes it impossible to achieve uniform impregnation of the pores. For this reason, the pitch for impregnation is required to penetrate easily into pores and have a high fixed carbon content during carbonization, that is, to have a high carbonization yield. However, although this carbonization rate is generally higher for high softening point pitches, at the same time, the viscosity increases, resulting in poor impregnating properties.

(発明が解決しようとする問題点) 上述するように従来法によりキノリン不溶分除去処理さ
れたキノリン不溶分0.1%未満のコールタールまたは
ピッチを炭素電極用含浸ピッチとして使用する場合には
、電極に対する含浸性が悪く、電極として満足な密度お
よび強度を得ることができない。それ故、本発明はキノ
リン不溶分除去処理されたキノリン不溶分0.1%未満
のコールタールまたはピッチ(現在、脱QIピッチとし
て商品化されている。商品名rPK−QLJ)の電極に
対する含浸性を向上させることを目的とする。
(Problems to be Solved by the Invention) As described above, when using coal tar or pitch with a quinoline insoluble content of less than 0.1% that has been treated to remove quinoline insoluble content by a conventional method as an impregnated pitch for a carbon electrode, It has poor impregnating properties into electrodes, making it impossible to obtain sufficient density and strength as electrodes. Therefore, the present invention focuses on impregnating electrodes with coal tar or pitch (currently commercialized as QI-free pitch, trade name: rPK-QLJ) with less than 0.1% of quinoline insolubles that has been treated to remove quinoline insolubles. The purpose is to improve

(問題点を解決するための手段) 本発明者らは炭素電極層含浸ピッチの含浸性を改良する
ために幾多の研究の結果、従来法によりキノリン不溶分
除去処理されたキノリン不溶分0.1%未満のコールタ
ールまたはピッチ(脱QIピッチ)中に微量に残存する
物質、すなわち、細孔フィルター(例えば0.22μの
テフロン@フィルター)でP遇した際にP滓として残留
する物質が含浸性を著しく悪くすることを見出し、この
残留物質を除去することにより含浸性が著しく改良され
ることを見出し、本発明に到達したものである。
(Means for Solving the Problems) As a result of numerous studies to improve the impregnation properties of pitch impregnated with a carbon electrode layer, the present inventors found that quinoline insolubles of 0.1 % of coal tar or pitch (de-QI pitch), i.e., the substance that remains as P slag when treated with a pore filter (e.g. 0.22μ Teflon @ filter) is impregnable. It was discovered that the impregnating property was significantly improved by removing this residual substance, and the present invention was achieved based on these findings.

本発明は炭素1框用含浸ピッチとしてキノリン不溶分0
.1−未満のコールタールまたはピッチ(脱Qエピツチ
)中の微量不純物を実質的に含まない含浸ピッチを得る
ことにある。
The present invention has zero quinoline insoluble content as impregnated pitch for carbon 1 frame.
.. The object of the present invention is to obtain an impregnated pitch that is substantially free of coal tar or trace impurities in the pitch (de-Qed epitaxial).

本発明の炭素電極層含浸ピッチの製造方法は脱QIピッ
チ中の微量不純物、すなわち、7滓を濾過、溶剤分割法
、遠心分離法などの適当な除去処理に  □より除去し
、ピッチ中に残存する不純物を実質的に含まないピッチ
を生成することである。また、この除去処理は、ピッチ
製造工程のうちのピッチ蒸留前のタール(ただし脱Q工
後)またはピッチ蒸留後の溶融ピッチに行うことにより
、製品ピッチ中の上記不純物を除去することができる。
The method for producing carbon electrode layer-impregnated pitch of the present invention involves removing trace impurities in the de-QI pitch, that is, 7 slag, through an appropriate removal process such as filtration, solvent division, or centrifugation, and remaining in the pitch. The objective is to produce pitch that is substantially free of impurities. Further, by performing this removal treatment on the tar before pitch distillation (but after the Q removal process) in the pitch manufacturing process or on the molten pitch after pitch distillation, the impurities in the product pitch can be removed.

本発明において炭素電極用含浸ピッチを得るには、上述
する原料ピッチを、例えば200″C〜320’Cの温
度で加熱溶融し、フィルター(平均孔径、例えば0.1
〜40μ)を用い、0.5i9/crl〜5 J9 /
 c++fの圧力で加圧濾過してキノリン不溶分を実質
的に存在しないと認められる分析誤差程度に微量、例え
ば0.05%以下、好ましくは0.02チ以下になるよ
うに濾過する。
In order to obtain impregnated pitch for carbon electrodes in the present invention, the above-mentioned raw material pitch is heated and melted at a temperature of, for example, 200''C to 320'C, and filtered (average pore size, for example, 0.1
~40μ) and 0.5i9/crl~5 J9/
The quinoline is filtered under pressure at a pressure of c++f so that the amount of quinoline insoluble matter is reduced to a trace amount, for example, 0.05% or less, preferably 0.02% or less, to the extent that the analysis error is considered to be substantially absent.

実際上、o、22μのフィルターでF遇する前後のピッ
チは、その分析においてキノリン不溶分が約0.05 
%以下で、濾過前ピッチの値が必ずしも大きいものでな
い。この事から、上記微量(具体的には10(lのピッ
チ当り約50ff+9の7滓が得られた〕の不純物中の
キノリン不溶分それ自体が含浸性を大きく左右するもの
と断定することはむずかしい。その理由は、第3図に示
すように高密度焼成した電極の場合でも、その細孔分布
は10〜100μの気孔を有している一方、キノリン不
溶分の粒径は通常約1μ以下であり、気孔径の大小が直
接の阻害要因とは云い難く、むしろピッチ中のある種の
成分との複合作用が含浸性に大きな影響をもたらすもの
と思われる。
In fact, the pitch before and after filtering with an o, 22 μ filter has a quinoline insoluble content of about 0.05 in the analysis.
% or less, the value of the pitch before filtration is not necessarily large. From this, it is difficult to conclude that the quinoline-insoluble content in the above-mentioned trace amount (specifically, 10 (approximately 50 ff + 9 slag per liter pitch was obtained) of impurities greatly affects impregnating properties. The reason for this is that even in the case of a high-density fired electrode, as shown in Figure 3, the pore distribution has pores of 10 to 100μ, while the particle size of the quinoline-insoluble matter is usually about 1μ or less. Therefore, it is difficult to say that the size of the pore diameter is a direct inhibiting factor, but rather, it is thought that the combined effect with certain components in the pitch has a large effect on the impregnating property.

また、不純物の除去において、除去工程を上述するピッ
チ製造工程に適用することができ、この場合、望ましく
はピッチ蒸留工程後の陰融ピッチに対して濾過などの不
純物除去工程を設けることによって十分に除去すること
ができ、この外の手段としてキノリン不溶分除去後でピ
ッチ蒸留前の工程に濾過などの不純物除去工程を設けて
も実用上十分な効果を得ることができる。
In addition, in removing impurities, the removal step can be applied to the pitch production process described above, and in this case, it is preferable that the impurity removal step such as filtration be performed on the sintered pitch after the pitch distillation step. Alternatively, an impurity removal step such as filtration may be provided in the step after removing the quinoline insoluble matter and before the pitch distillation to obtain a sufficient practical effect.

本発明における不純物除去での濾過に使用するフィルタ
ーの平均孔径について、0.1〜40μの範囲の平均孔
径を実験的に用いたが、特に微粒子を十分に捕捉できる
7紙として0.22μを便宜的に使用したもので、本発
明において例示する7紙の平均孔径は特定の範囲に制限
するものではない。
Regarding the average pore size of the filter used for filtration in removing impurities in the present invention, an average pore size in the range of 0.1 to 40μ was experimentally used, but 0.22μ was particularly convenient as a paper that can sufficiently capture fine particles. The average pore diameter of the seven papers exemplified in the present invention is not limited to a specific range.

平均孔径0.22μおよび10μのフィルターでの濾過
後のピッチの含浸性が著しく向上することを実施例1お
よび2で具体的に説明する。
Examples 1 and 2 specifically illustrate that the impregnating properties of pitch are significantly improved after filtering with filters having average pore sizes of 0.22μ and 10μ.

(発明の効果) 上述するように、本発明においては従来法によりキノリ
ン不溶分除去処理されたキノリン不溶分0.1%未満の
コールタールまたはピッチを濾過の如き除去処理を行う
ことによりタールまたはピッチ中に残存する不純物、す
なわち、7滓を除去して0.05%以下の不純物を含む
電極用含浸ピッチを得たことにより、ピッチの電極に対
する含浸性を向上させ、電極のカサ密度および強度を高
めることができた。
(Effects of the Invention) As described above, in the present invention, coal tar or pitch containing less than 0.1% of quinoline insolubles, which has been treated to remove quinoline insolubles by a conventional method, is removed by a removal process such as filtration. By removing the remaining impurities, i.e., 7 slag, to obtain an impregnated pitch for electrodes containing impurities of 0.05% or less, the impregnation of the pitch into the electrode is improved, and the bulk density and strength of the electrode are improved. I was able to increase it.

(実施例1) 商品名「PK−QLJの脱QIピッチ100gを210
℃で溶融し、0.22μのフィルターを用い、219 
/ c++Jで加圧濾過したところ、第1図に示すよう
に時間の経過と共に、濾過速度は著しく低下し、50■
(0,05% )のF滓を得た。次いで、この濾過後の
ピッチを用い、同一条件で濾過したところ、第1図の上
段の曲線で示すように濾過速度の低下は軽微であった。
(Example 1) Product name “PK-QLJ de-QI pitch 100g to 210g”
Melt at 219°C using a 0.22μ filter.
When pressure filtration was performed using /c++J, the filtration rate decreased significantly over time as shown in Figure 1.
(0.05%) of F slag was obtained. Next, when this filtered pitch was used to perform filtration under the same conditions, as shown by the upper curve in FIG. 1, the decrease in filtration rate was slight.

更に、実際に使用されている電極の低密度焼成品(人廃
品)および高密度焼成品(B廃品)から得た濾過板を用
いて上記濾過前ピッチおよび0.22μフイルターでの
濾過後のピッチについての一過試験を行った。この結果
は表1に示すように浸透性が著しく向上していることが
わかる(生ピッチの濾過速度を1とした)。なお、P滓
除去前後とも、ピッチのqI成分含量は約0.On〜0
.05%であった。
Furthermore, using filter plates obtained from low-density fired products (human waste) and high-density fired products (B-waste) of electrodes actually used, the pitch before filtration and the pitch after filtration with a 0.22 μ filter were measured. A transient test was conducted on As shown in Table 1, the results show that the permeability was significantly improved (the filtration rate of raw pitch was set at 1). Note that the qI component content of pitch is approximately 0.0% before and after P slag removal. On~0
.. It was 0.5%.

表1 、(実施例2) 実施例1と同一ロットの試料を月い、10μフイルター
での一過試験を行った。この結果は第2図に示すように
生ピッチの濾過速度は著しく低下し、−過後のピッチは
その低下が殆んど観察されず、実施例1と同じ傾向を示
しており、−過後のピッチの再−過速度は著しく大であ
った。
Table 1 (Example 2) Samples from the same lot as in Example 1 were subjected to a transient test using a 10μ filter. As shown in Fig. 2, the filtration rate of the raw pitch decreased significantly, and the decrease was hardly observed in the pitch after the filtration, showing the same tendency as in Example 1. The re-overspeed was significantly large.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の方法による0、22μフイルターによ
り濾過処理して得たピッチの濾過特性を示すグラフ、 第2図は本発明の方法による10μフイルターにより濾
過処理して得たピッチの一過特性を示すグラフ、および 第3図は電極材から採取した濾過板の気孔径分布を示す
グラフである。 第1図 第2図 f通時間
Figure 1 is a graph showing the filtration characteristics of pitch obtained by filtering with a 0 and 22μ filter according to the method of the present invention. Figure 2 is a graph showing the filtration characteristics of pitch obtained by filtering with a 10μ filter according to the method of the present invention. A graph showing the characteristics, and FIG. 3 is a graph showing the pore size distribution of the filter plate taken from the electrode material. Fig. 1 Fig. 2 Fig. f Running time

Claims (1)

【特許請求の範囲】[Claims] 1、キノリン不溶分除去処理したキノリン不溶分0.1
%未満のコールタールまたはこれから得たピッチを不純
物除去処理して0.05%以下の不純物を含むピッチを
得ることを特徴とする電極用含浸ピッチの製造方法。
1. Quinoline insoluble content removed by quinoline insoluble content 0.1
1. A method for producing impregnated pitch for electrodes, characterized in that pitch containing less than 0.05% of impurities is obtained by removing impurities from coal tar or pitch obtained therefrom.
JP59235229A 1984-11-09 1984-11-09 Preparation of impregnating pitch for electrode Pending JPS61117109A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59235229A JPS61117109A (en) 1984-11-09 1984-11-09 Preparation of impregnating pitch for electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59235229A JPS61117109A (en) 1984-11-09 1984-11-09 Preparation of impregnating pitch for electrode

Publications (1)

Publication Number Publication Date
JPS61117109A true JPS61117109A (en) 1986-06-04

Family

ID=16982990

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59235229A Pending JPS61117109A (en) 1984-11-09 1984-11-09 Preparation of impregnating pitch for electrode

Country Status (1)

Country Link
JP (1) JPS61117109A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5199588A (en) * 1988-04-01 1993-04-06 Yoshino Kogyosho Co., Ltd. Biaxially blow-molded bottle-shaped container having pressure responsive walls
JP2007176506A (en) * 2005-12-27 2007-07-12 Yoshino Kogyosho Co Ltd Synthetic resin square bottle
JP2007290718A (en) * 2006-03-30 2007-11-08 Yoshino Kogyosho Co Ltd Synthetic resin square bottle body
US8739995B2 (en) 2005-08-31 2014-06-03 Yoshino Kogyosho Co., Ltd. Synthetic resin bottle

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5199588A (en) * 1988-04-01 1993-04-06 Yoshino Kogyosho Co., Ltd. Biaxially blow-molded bottle-shaped container having pressure responsive walls
US8739995B2 (en) 2005-08-31 2014-06-03 Yoshino Kogyosho Co., Ltd. Synthetic resin bottle
JP2007176506A (en) * 2005-12-27 2007-07-12 Yoshino Kogyosho Co Ltd Synthetic resin square bottle
JP2007290718A (en) * 2006-03-30 2007-11-08 Yoshino Kogyosho Co Ltd Synthetic resin square bottle body

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