JPS58134179A - Preparation of mesophase pitch - Google Patents

Preparation of mesophase pitch

Info

Publication number
JPS58134179A
JPS58134179A JP1552182A JP1552182A JPS58134179A JP S58134179 A JPS58134179 A JP S58134179A JP 1552182 A JP1552182 A JP 1552182A JP 1552182 A JP1552182 A JP 1552182A JP S58134179 A JPS58134179 A JP S58134179A
Authority
JP
Japan
Prior art keywords
pitch
mesophase
layer
heat
men
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
Application number
JP1552182A
Other languages
Japanese (ja)
Other versions
JPH0245669B2 (en
Inventor
Shozo Watabe
渡部 正三
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.)
Kashima Oil Co Ltd
Original Assignee
Kashima Oil Co Ltd
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 Kashima Oil Co Ltd filed Critical Kashima Oil Co Ltd
Priority to JP1552182A priority Critical patent/JPS58134179A/en
Publication of JPS58134179A publication Critical patent/JPS58134179A/en
Publication of JPH0245669B2 publication Critical patent/JPH0245669B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To prepare mesophase pitch, economically, in high efficiency, by heating and stirring a petroleum pitch under specific conditions, leaving the heat- treated pitch at rest to effect the exclusive growth and fusion of the mesophase, and separating the mesophaase from the non-mesophase. CONSTITUTION:A petroleum pitch or tar pitch available at an extremely low cost is heated under stirring preferably at 360-450 deg.C in a non-oxidizing gas flow under atmospheric or positive pressure to develop the mesocomponent in the thermally produced pitch. The pitch is left at rest to effect the exclusive growth and fusion of the mesophase in the thermally produced pitch, and the meso phase is separated from the non-mesophase. A 100% mesophase pitch composed of Q.I component and Q.S component can be obtained by this process. The content of mesophase in the pitch produced by the heating under stirring is preferably 10-50%.

Description

【発明の詳細な説明】 本発明は高強度高弾性炭素繊維用の原料としての100
チメソフエーズのピッチの製造に係るもので、特に複合
材料の原料として好適な高強酸高弾性炭素繊維を高能率
で低摩なコストで製造する方法を提供することを目的と
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention describes the use of 100% carbon fiber as a raw material for high strength and high modulus carbon fiber.
The present invention relates to the production of Chimesophase pitch, and aims to provide a method for producing highly acidic and highly elastic carbon fibers, which are particularly suitable as raw materials for composite materials, with high efficiency and low cost.

本発明は、減圧軽油の熱接触分触(FCC)或はナフサ
の熱分解によって副生された残漬炭素物質の石油系ヒ:
ツチ、石油タールを360″C乃至450″Cの温度で
常圧或は加圧下で非酸化性気流下で攪拌加熱処理し、メ
ソフェーズを101乃至501含有するピッチを製造し
、後2を非酸化性気流下で加熱処理温度より低温290
°C乃至370″Cで静置保持1゜て上層の非メン層と
下層のメン層(偏光顕微晴にて容易に測定出来る)とに
分離“区分し、ion 4メンフエーズピツチを製造す
る方法にある一近年航空機、自動車その他の輸送機製作
工業の急速な成長の結果それに必要な材料と[7て、特
別な物質の組合せからなり、そのいくつかの物理的性質
が極めて傍れておって特異性を発揮しうる材料を望む声
が大きくなっているが特K、高い強奪及び弾性を具備し
、回持に軽量で安価な材料の出現が強く要求されている
。1〜かるに現在の技術で゛か\る要望Kかなった材料
を安定12て供給することが出来ないので、これに答え
るため強含物質(強化樹脂)の製造に関する研究が盛ん
に行われているう 強化樹脂に使用される最も有望な材料の1つとして高強
度高弾性の炭素繊維がある。この材料は前述の産業の急
速な成長が始まりかけた頃から市場に現われたもので、
この炭素繊維を樹脂と組合せて使用すると、他に全くそ
の類例を卵ないような特性を発揮する強化樹脂を製造す
ることが出来る。しかし残念ながら上記の様な強化樹脂
用の高強酸高弾性炭素繊維は価格が極めて高価なため、
これを使用した強化樹脂が極めて顕著な特性を発揮する
にもか\わらずそれの需要があまり開拓されていない。
The present invention deals with petroleum-based carbonization of residual carbon substances produced by thermal catalytic fractionation (FCC) of vacuum gas oil or thermal decomposition of naphtha:
A pitch containing 101 to 501 mesophases was produced by heat-treating petroleum tar at a temperature of 360"C to 450"C under a non-oxidizing gas stream under normal or increased pressure, and the latter 2 was a non-oxidizing pitch. Lower temperature than the heat treatment temperature under a positive air flow290
Separate and separate into an upper non-men layer and a lower men layer (which can be easily measured with a polarized light microscope) by holding still at 1 °C to 370"C to produce an ion 4 men phase pitch. In recent years, the rapid growth of the aircraft, automobile, and other transportation manufacturing industry has resulted in the rapid growth of the industry in manufacturing aircraft, automobiles, and other transportation vehicles. There has been an increasing demand for materials that can exhibit specific properties, and there is a strong demand for materials that have special characteristics, high strength, high elasticity, and are lightweight and inexpensive for recycling. Since it is not possible to stably supply materials that meet certain demands with current technology, research is being actively conducted on the production of highly reinforced materials (reinforced resins) to meet these demands. One of the most promising materials for use in reinforcing resins is high-strength, high-modulus carbon fiber. This material appeared on the market at the beginning of the rapid growth of the aforementioned industries.
When this carbon fiber is used in combination with a resin, it is possible to produce a reinforced resin that exhibits properties that are completely unrivaled by any other similar material. Unfortunately, however, the high strength acid and high modulus carbon fibers for reinforced resins as mentioned above are extremely expensive.
Although the reinforced resin using this material exhibits extremely remarkable properties, the demand for it has not been developed much.

現在入手出来る高強度高弾性の炭素繊維の原料は特殊な
製造法及び紡糸法によって製糸されたポリアクリロニト
リル繊維が主であることが知られているが、この、f、
 +)アクリロニ) IJル轍維は炭素繊維の前駆体と
t12で高価であるばかりでなく更にこの前駆体からの
炭素繊維の収率け45幅以、下で極めて悪い。このこと
が優れた炭素錆緯を製造する処理工程を複雑に11、最
終製品の炭素繊維の製造コストを益々高めることになっ
ている。
It is known that the raw materials for currently available high-strength, high-elastic carbon fibers are mainly polyacrylonitrile fibers spun using special manufacturing and spinning methods.
+) Acryloni) IJ rut fibers are not only expensive as a carbon fiber precursor and t12, but also the yield of carbon fiber from this precursor is extremely poor at less than 45%. This complicates the process for producing superior carbon weave11 and increases the cost of producing the final carbon fiber product.

特に安価な炭素繊維用の原料を造り出すために、本発明
の発明者は広はん々研究を′*施1.た。その結果、極
めて安価な石油系及びタール系ピッチを非酸化性気流下
で360°C乃至450°CVC攪拌加熱処理して加熱
生成ピッチ中にメン成分を生成せ17め、後加熱生成ピ
ッチを非酸化性気流下で280°C乃至370°Cに静
置保持し、その温度に充分保持することによってメン成
分が加熱生成ピッチ中で相互に融着巨大化して成長する
様K L、非メンピッチとメン(異方性)ピッチの比重
の差、その他物性の差によって、その静置保持条件下に
於て上層の非メソピッチと下層のメンピッチとに側熱と
区分分離し、100俤のメンピッチを分離製造しうろこ
とを見い出[7本発明を完成した。尚加熱生歳ピッチを
280°C乃至370°Cに保持する場合ピッチ中のメ
ン球の融着巨大化を促進するた込非メン層シメン層との
分離を妨げない穆度でゆるやかに攪拌することもあ抄う
暮。
In order to create a particularly inexpensive raw material for carbon fiber, the inventor of the present invention has conducted extensive research.1. Ta. As a result, extremely inexpensive petroleum-based and tar-based pitches were heat-treated with stirring at 360°C to 450°C in a non-oxidizing air flow to generate meng components in the heated pitch, and the post-heated pitch was non-allocated. By keeping it stationary at 280°C to 370°C under an oxidizing air flow, and keeping it at that temperature sufficiently, the men component fuses with each other in the heated pitch and grows to a large size. Due to the difference in specific gravity and other physical properties of men (anisotropic) pitch, under the conditions of static holding, the upper layer non-meso pitch and the lower layer men pitch are separated from the side heat, and 100 tons of men pitch are separated. Discovered manufacturing scales [7] Completed the present invention. In addition, when the heated raw age pitch is maintained at 280°C to 370°C, it is stirred gently at a level that does not prevent the separation of the folded non-menu layer from the cymene layer, which promotes the fusion and enlargement of the menen balls in the pitch. Kotomoashougure.

炭素繊維用の安価な原料の製法は特公昭48−36 、
160、特公昭48−122.122及び特公昭昭−6
5,425等その他多くの特許出願公報に報告されてい
Aoこれらの製法では石油系及びタール系ピッチを温度
380°C乃至440°Cに加熱処理;7てメソフェー
ズを40チ乃至90憾好ま1.〈はM憾乃至6憾含有す
るピッチを製造し、これをそのま\炭素横維用の原料と
している。従ってこのピッチは非メソピッチを多く含有
し、高強度高弾性の炭素繊維用の原料として要求される
100チメソフエーズピツチとは云えずその特性を充分
具備していない、更らに本質上100 %のメソフェー
ズを含有するビツアを製造する□方法カ5%−昭54−
55.625(7)公報に報告されている。即ち婢万性
ピッチに9素、アルゴン、キセノン、ヘリウム、水蒸気
等の不活性ガスを原料麺当り少なくとも877分以上極
めて多量に圧入L7、強く攪拌1.つ\380°C乃至
430″Cで5時間乃至44時間も加熱して単−相の系
に変換されるまで加熱処理して、所謂100係のメソフ
ェーズのピッチの製造を試みている。I7かるに原料の
等方性ピッチは所謂巨大分子で複雑で純粋な化合物でな
く、不純物も含有し、エマルジョンを形成していて如何
に長時間不活性がスをW人して強く攪拌し処理゛しつぐ
しても該エマルジョンを完全に単一化することは不可能
で、如何に(2ても未反応の等方性ピッチの混在を完全
に無くすることは出来ない、従って得られるものは純粋
に1001メソフエーズ七は云えない。
The manufacturing method of inexpensive raw materials for carbon fiber was published in the Japanese Patent Publication No. 48-36.
160, Special Publication Showa 48-122.122 and Special Publication Publication Showa-6
In these production methods, petroleum-based and tar-based pitches are heat-treated to a temperature of 380°C to 440°C; 〈 produces pitch containing M≧6≦, which is directly used as a raw material for carbon fibers. Therefore, this pitch contains a large amount of non-meso pitch, and cannot be said to be the 100-chimeso phase pitch required as a raw material for high-strength, high-elastic carbon fibers, and does not have the characteristics sufficiently, and furthermore, it is essentially 100%. □Method for producing bitsea containing mesophase of 5% - 1972-
55.625(7). That is, a very large amount of inert gas such as 9 elements, argon, xenon, helium, and water vapor is press-injected into the flexible pitch for at least 877 minutes per raw noodle L7, and vigorously stirred 1. We are attempting to produce a so-called 100 mesophase pitch by heating it at 380°C to 430"C for 5 to 44 hours until it converts to a single-phase system. Isotropic pitch, which is a raw material, is a so-called macromolecule and is not a complex and pure compound, but also contains impurities and forms an emulsion. Even if the emulsion is mixed, it is impossible to completely unify the emulsion, and no matter how much (2) I can't say 1001 mesophases 7.

減圧軽油の熱接触分解(FCC)によって副生された残
渣炭素物質を常圧下非酸゛化性気流下で必要に応じて予
備加熱処理して前駆体をつくり、この前駆体を温度35
0 ”C”乃至450°c、でダ)分乃至308S間で
攪拌処理して加熱生成ピッチ中のメンフェーズの含有量
がlOチ乃至50%になる様々加熱処理をする好唾しく
は攪拌加熱処理条件を合理化するため加熱温度380°
C乃至440″C1反応時間1時間乃至6時間の条件を
選んで加熱処理することによってメソフェーズを20係
乃至40%含有する加熱生成ピッチを製造できる。この
加熱生成ピッチを非酸イヒ性気流下で加熱処理温度より
低温の280″C乃至370°Cで2時間乃至(イ)時
間静置保持(7てメンフェーズの部分を融着成長させ巨
大仕させ加熱生成ピンチを非メソ層とメン層とに側熱と
区分で^る。
Residual carbon substances produced by thermal catalytic cracking (FCC) of vacuum gas oil are preheated as necessary under normal pressure and non-oxidizing gas to create a precursor.
0 ``C'' to 450°C, stirring treatment for 5 minutes to 308 seconds to achieve a content of menphase in the heated pitch of 10 to 50%. Heating temperature 380° to streamline processing conditions
C to 440"C1 By selecting heat treatment conditions for a reaction time of 1 to 6 hours, heat-generated pitch containing 20% to 40% mesophase can be produced. This heat-generated pitch is heated under a non-acidic gas flow. Hold at 280"C to 370°C, which is lower than the heat treatment temperature, for 2 hours to (a) (7) The menphase part is fused and grown to form a large size, and the heat-generated pinch is separated into a non-meso layer and a menslayer. It is classified as side heat.

尚静置加温々度が280°C以下では加熱中広ピッチを
非メン層とメソ層とに区分分離することけ出来ない。加
熱処理する時並JtC茄熱牛成ピッチを非メン層とメソ
層とに分離する時に使用す非酸化性気流ガスと17て使
用し得るものはメタン、エタン、グロ/!?ン、ブタン
等炭素数の少ない炭化★素、沸点の低く\重質化、lL
ないナフサ留分を挙げることができる。しかしニガから
経済的は最もすぐれているガスは原料を加色処理して副
生ずるドライガス(主として炭素数少1ない炭化水素の
混合物)である。
If the heating temperature is 280° C. or lower, the wide pitch during heating cannot be separated into a non-menu layer and a meso layer. 17 Non-oxidizing gases used during heat treatment and when separating JtC boiled beef pitch into non-menu layer and meso layer include methane, ethane, and gros/! ? Carbohydrates with a small number of carbon atoms such as carbon, butane, low boiling points\heavy, 1L
The naphtha fraction that does not have any However, the most economical gas from bittern is the dry gas (mainly a mixture of hydrocarbons with a small number of carbon atoms) produced by coloring the raw material.

尚メソ層は偏光顕微鏡で1004メンフエーズであるこ
とは容易に確Vすることが出来る。静ti持条件を合理
化するため、静置温度300°C乃至340で、保持時
間5時間乃至15時間の静電保持条件を選んで非メン層
とメソ層とに分離することが好ましい。
It should be noted that the meso layer can be easily confirmed to be 1004 memphase using a polarizing microscope. In order to rationalize the static holding conditions, it is preferable to select electrostatic holding conditions of a standing temperature of 300° C. to 340° C. and a holding time of 5 hours to 15 hours to separate the non-meso layer and the meso layer.

更に本発明の発明者は区分分離されたメン層けQ、■、
(キノリンネ溶分、130”Cでキノリン抽出によって
測定する)とOoS、 (キノリン溶解分)との2つの
メン成分によって構成され、しかもこの100チメンフ
エーズをQ、 1.成分のみならずQ、、S、成分によ
っても構成させることにより、このメソフェーズの紡糸
性を良くすることを見付けた。
Furthermore, the inventor of the present invention has developed a segmented men layer Q, ■,
It is composed of two main components: (quinoline soluble content, measured by quinoline extraction at 130"C) and OoS, (quinoline soluble content), and this 100-time phase is not only Q, 1. component, but also Q,,S We have found that the spinnability of this mesophase can be improved by configuring it with other components.

本発明の特徴は100チメンフエーズを製造すると同時
にこのメンフェーズはQ、Lメン成分とQ、S。
The feature of the present invention is that 100 chimen phase is produced, and at the same time, this men phase contains Q, L men components and Q, S men.

メン成分とによって構成させることにある、この100
 %メンフェーズを紡糸した炭素繊維を製造する1例を
挙げると次の如くである。紡糸温li 320″C粘度
聞ボイズ(紡糸温間にて)、紡糸速度10t)1111
/分で紡糸して得られた糸を300°Cで15分間空気
で不融化(架橋化)し、後昇温速度10°C/分で最終
温度1.400″Cで15分間炭化して長amの高強度
高弾性の炭素繊維を製造することが出来冬。
This 100 is composed of
An example of producing carbon fiber by spinning % menphase is as follows. Spinning temperature li 320″C viscosity (at spinning temperature), spinning speed 10t) 1111
The yarn obtained by spinning at 300°C/min was infusible (crosslinked) with air at 300°C for 15 minutes, and then carbonized at a final temperature of 1.400″C for 15 minutes at a heating rate of 10°C/min. In winter, we were able to produce long-lasting, high-strength, high-elastic carbon fiber.

実施例1 減圧軽油の熱接触分解(FCC) [よって副生される
残漬炭素物質を非酸化性気流下で400°rで2時間加
熱処理して前駆体ピッチを製造17会。
Example 1 Thermal catalytic cracking (FCC) of vacuum gas oil [Thus, the residual carbon material produced as a by-product was heat treated at 400°r for 2 hours under a non-oxidizing air flow to produce precursor pitch.

前駆体の収率54係前駆体の軟化点(RAB相当)67
°Cであった。
Precursor yield: 54 Precursor softening point (RAB equivalent): 67
It was °C.

この前駆体を次の加熱処理条件で処理し7、その後加熱
生成ピッチを300 ”CでU時間静置保持して非メン
層とメソ層とに区分分1111 L、た。尚非酸化性気
流として加熱処理反応に於て生成するドライガスな循環
させたものを使用した、 実施例2 実施例1の実験番号2によって生成された加熱生成ピッ
チを生成後直接法の如き静置保持条件でメン層の分岐試
験を実施した。
This precursor was treated under the following heat treatment conditions7, and then the heated pitch was left standing at 300"C for U hours to divide it into a non-menu layer and a meso layer. Example 2 The heat-generated pitch produced in Experiment No. 2 of Example 1 was maintained under static holding conditions such as the direct method after generation. Layer bifurcation tests were conducted.

実験番号6の静電保持条件では、非メン層とメン層との
2層に刺然と分離せず3つの層にやつと区分が出来る程
度で、静電保持条件として不充分なものであった。
Under the electrostatic holding conditions of Experiment No. 6, the electrostatic holding conditions were not sufficient as the electrostatic holding conditions were not sharply separated into two layers, the non-men layer and the men layer, but could be divided into three layers. Ta.

実施例3 ナフサの熱分解によって副生されるB、P、 200°
C以上の残漬炭素物質をメタンガスの非酸化性気流下で
次の加熱処理条件で処理した。
Example 3 B, P, by-produced by pyrolysis of naphtha at 200°
The residual carbon material of C or higher was treated under the following heat treatment conditions under a non-oxidizing stream of methane gas.

常圧加熱処理結果 R&B相当軟化点の測定法はJI8に−2531に依る
The method for measuring the R&B equivalent softening point as a result of normal pressure heat treatment is based on JI8-2531.

実験番号11によって生成された加熱生成ピッチを生成
後直接メタンガスの″非酸化性気流下で次の如き静電保
持条件でメン層の分離試験を実施した。
After the heated pitch produced in Experiment No. 11 was produced, a men layer separation test was conducted directly under the non-oxidizing flow of methane gas under the following electrostatic holding conditions.

メン層の分離試験結果 出願人: 渡  部  正  三 ””’−1 代理人:升埋士佐々井彌太部・  ; □1 (SJか 1名) 1収辷 手続補正書 ;印紙j         昭和57年8月し8日ニー
、−19,11,−111,: 特許庁長官  若 杉 和 夫  殿 (特許庁審判長          殿)(特許庁審査
官          殿)1、事件の表示  昭和5
7年特許願第 15521  号2、発明の名称  メ
ンフェーズピッチの製造法3、補正をする者 事件との関係  特許出願人 fE  l!Ii  j4L )Ra h &区鳥円寺
45−18−2氏   名  渡   部   止  
三          [相]4、代理人 住   所  〒160  東京都新宿区新宿2丁目8
番1号新宿セブンビル608号室 (6601)氏名弁理土佐々井彌太部’、@(電話35
4−1285&す〜6)  l−5、補正命令の日付 
自発袖IE 6、補正により増加する発明の数 増加せず8、補正の
内容 以下の通シ (1)特許Bpi求の範囲の記載を次の様に変更する。
Men's layer separation test results Applicant: Shozo Watanabe""'-1 Agent: Yatabe Sasai; August 8th, -19, 11, -111: Mr. Kazuo Wakasugi, Commissioner of the Patent Office (Mr. Chief Adjudicator of the Patent Office) (Mr. Examiner of the Patent Office) 1, Display of the case 1932
7 Year Patent Application No. 15521 2, Title of Invention Method for Manufacturing Menphase Pitch 3, Relationship with Amendment Case Patent Applicant fE l! Ii j4L) Rah & 45-18-2 Torienji, Ward Name: Watanabe Tome
3 [Phase] 4, Agent address: 2-8 Shinjuku, Shinjuku-ku, Tokyo 160
No. 1 Shinjuku Seven Building Room 608 (6601) Name Patent Attorney Yata Tosasai', @ (Telephone 35
4-1285 & 6) l-5, date of amendment order
Spontaneous Sleeve IE 6. The number of inventions increased by the amendment No increase 8. Contents of the amendment The following circular (1) The description of the scope of the patent Bpi request will be changed as follows.

1)石油系ピッチを常圧或は加圧下で非酸化性気流下で
攪拌加熱処理し、後2を静置保持して加熱生成ピッチ中
のメンフェーズのみを成長#l111着させ非メン層と
メン層とに区分分離することを%倣とするζ、1.成分
とQ、s、成分のみによって構成されている100%メ
ンフェーズピッチを製造する方法。
1) Petroleum-based pitch is stirred and heat-treated in a non-oxidizing air flow under normal pressure or pressurization, and the latter is held stationary to grow only the men phase in the pitch produced by heating and deposit #l111, forming a non-men layer. ζ, 1. A method for manufacturing 100% menphase pitch consisting only of components Q, s, and components.

2)石油系ピッチを360℃乃至450℃の温度で常圧
或は加圧下で非酸化性気流下で攪拌加熱処理して生成す
るピンチ中にメソフェーズの含有蓋を10傷乃至50嗟
にし、これを静置保持して非メン層とメン層とに区分分
離することをtf!f徴とする。  Q、i、成分とQ
、S、成分のみによって構成されている100傷メンフ
エーズピツチを製造する方法。
2) The mesophase-containing lid is made 10 to 50 scratches in the pinch produced by stirring and heating petroleum pitch at a temperature of 360 ° C to 450 ° C under normal pressure or under pressure in a non-oxidizing gas flow. tf! It is assumed to be f-symptom. Q, i, component and Q
, S. A method for producing 100-wound Memphaze pitches composed only of ingredients.

3)前述の加熱生成ピッチを加熱処理条件より全く別の
処理条件−非酸化性気流下で加熱処理温度より低温の2
80℃乃至350℃の温ター理し1 度で加熱生成ピッチ中のメンフェーズのみが成長融着し
で加熱生成ピッチが非メソ層とメることを特徴とするQ
、1.成分とQ、s、成分のみに′よって構成されてい
る100%メンフェーズピッチを製造する方法。
3) The above-mentioned heat-generated pitch was treated under completely different treatment conditions than the heat treatment conditions - under a non-oxidizing air flow and at a lower temperature than the heat treatment temperature.
Q characterized in that only the menphase in the heat-generated pitch grows and fuses after one degree of temperature treatment at 80°C to 350°C, and the heat-generated pitch becomes a non-meso layer.
, 1. A method for manufacturing 100% menphase pitch composed only of the components Q, s, and the component '.

(2)発明の詳細な説明の項に於いて次の補正をする。(2) The following amendments will be made in the detailed description of the invention.

(1)3頁上よ99行目の 「ピッチ、石油タールを」を 「ピッチを」に変更する。(1) Page 3 top, line 99 "Pitch, petroleum tar" Change the pitch to "Pitch".

411 3真下より8行目の 「290℃」を「280℃」に 「370℃」を「350℃」に変更する。411 8th line from directly below 3 "290℃" to "280℃" Change "370℃" to "350℃".

(III)  3頁下より6行目の 「分し、」と「100傷」の間に 「Q、i、成分) Q、8.成分のみによって構成され
ている。」を入れる。
(III) In the 6th line from the bottom of page 3, insert "Consisted only of Q, i, component) Q, 8. component" between "divided," and "100 scratches."

11V)  3頁下より5行目の 「フェースピッチ」と「を製造」との間に「(偏光顕微
鏡によって容易に確認することが、できる」を入れる。
11V) In the 5th line from the bottom of page 3, insert "(can be easily confirmed with a polarizing microscope)" between "face pitch" and "manufactured".

(v)5頁上より10行目の 「細糸及びタール系ピッチ」を 「細糸ピソナ」に変更する。(v) 10th line from the top of page 5 "Fine threads and tar-based pitch" Change to "Hoisito Pisona".

6/1)  5頁下より8行目の 「流下で」と「280℃」の間に 「加熱処理温度よυ低温の」を入れる。6/1) 8th line from the bottom of page 5 Between “flowing down” and “280℃” Enter "heat treatment temperature υ low temperature".

−5真下より7行目の 「370℃」を「350℃」K変更する。-5 7th line from directly below Change "370℃" to "350℃".

(V−)δ貴下より6行目の 「つて」と「メン」の間に 「のみ始めて、」を入れる。(V-)δ 6th line from you Between “Tsute” and “Men” Insert "Only begin."

(IX) 5頁下より5行目の 「る様にし、」をi″ることか可能となり、」に変更す
る。
(IX) In the 5th line from the bottom of page 5, change ``Rusama nishi,'' to ``i''.

(→ 5頁下より1行目の 「離し、」と1100価」の間に 「Q、i、成分とQ、8.成分のみによって構成されで
いる」を入れる。
(→ In the first line from the bottom of page 5, insert ``It is composed only of Q, i, component and Q, 8. component'' between ``Release,'' and 1100 valence.''

(XI)  6負上上92行目の 1370℃」を「350℃」に変更する。(XI) 6 negative upper 92nd line Change "1370℃" to "350℃".

@ 6頁下より6行目の 「成分」と「が加熱」とのト11に「のみ」を入れる。@6th line from the bottom of page 6 Put "Only" in box 11 of "Ingredients" and "Heating".

kil)  6頁下より4行目の 「物性」と「の」との間に 「例えば粘度)」を入れる。kil) 4th line from the bottom of page 6 Between “physical properties” and “no” Enter "e.g. viscosity)".

04ν)7頁下より4行目の 「350℃」を「360℃」に変更する。04ν) 4th line from the bottom of page 7 Change "350℃" to "360℃".

(ハ)8頁上より6行目の 「370℃Jを「350℃」に、「2時間」を「5時間
」に、「60時間」を「30時間Jに変更する。
(c) In the 6th line from the top of page 8, change "370°C J to "350°C,""2hours" to "5 hours," and "60 hours" to "30 hours J."

鉤1)8貞上より7行目の [−ズの部分]を「−ズのみ」に変更する。Hook 1) 7th line from 8 Sadaka Change [-z part] to "-z only".

(膚11)9頁上より3行目の 「15時間」を「25時間」に変更する。(Skin 11) 3rd line from the top of page 9 Change "15 hours" to "25 hours".

(洩−)9N4上より6行目の 「者は」と「区分」の間に 「上記のf19置保持条件を設定することに:す」を入
れる。   中 体国 9頁上より10・行目から11行目迄の[メン7
エーズをQ、i、成分のみならずQ、6.成分によって
も]を「メソフェーズtiQ、i、成分が75儂乃至8
マチ及びJS、成分が13饅乃至2Φ 俤によって」に
変更する。
(Leak-) 9N4 In the 6th line from the top, insert "I will set the above f19 position holding conditions:" between "person" and "category". Medial country From line 10 to line 11 from the top of page 9 [Men 7
AIDS as Q, i, not only the components but also Q, 6. [depending on the component] is defined as "Mesophase tiQ,i, the component is 75 to 8
Machi and JS, the ingredients will be changed to 13 饅~2Φ 俤.

(ハ) 9頁下より9行目の 「性を」と「良く」の間に「極めて」を入れる。(c) 9th line from the bottom of page 9 Insert "extremely" between "sexually" and "good."

6oC1)  g貴下より6行目の 「成分と」と「によって」の間に「のみ」を入れる。6oC1) 6th line from you Insert "only" between "ingredients" and "by".

炊11)15頁表の7欄の i 2,96 Jをl’296Jに変更する。Cooking 11) Column 7 of the table on page 15 Change i2,96J to l'296J.

発+yH名称に作哨者の打つ:句4 2・4・1・・′[・・+’7 ;Rv’j ・1.i
z 1iij・−記・成された発明の数3ZJIF入V
代理入り”4’51111j;y、ゴ、γ、 4−、 
、(、7に1−ii−B。
The sentinel writes the name of the letter: Phrase 4 2・4・1・・′[・・+'7;Rv'j ・1. i
z 1iij・-Number of inventions recorded/made 3ZJIF entry V
Substituted” 4'51111j;y, go, γ, 4-,
, (1-ii-B in ,7.

lχ I収入1 手続補正書 j印紙1          昭和57年 9月lo日
:、−1.21.−0.−1.−1: 特許庁長官  若 杉 和 夫  殿 (特許庁審判長          殿)(特許庁審査
官          殿)1、事件の表示  昭和5
7年特許願第 15521  号2、発明の名称 メソ
フェーズピッチの仮這法3、補正をする者 事件との関係  特許出願人 住 所 束永郁杉並区高円寺南5−18−2氏   名
   渡   部   正   三         
   J4、代理人 住   所  〒160  東京都新宿区新宿2丁目8
番1号新宿セブンビル608号室 (6601)氏名弁理土佐々井彌太部        
  [相](電話354−1285■〜6) 5、補正命令の日付 自発補正 6、補正により増加する発明の数 増加せf(1)特許
請求の範囲の記載を次の様に変更する1゜1)石油系ピ
ッチを常圧或は加圧下で非酸化性気流下で攪拌加熱処理
し、後2を静置保持して加熱生成ピッチ中のメソフェー
ズのみを成長融層させ非メン層とメソI−とに区分分離
することを特徴とするQ、1.成分とQ、8.成分のみ
によって構成されている100%メンツエーズビッチを
製造する方法。
lχ I Revenue 1 Procedural Amendment j Stamp 1 September 1981 lo date:, -1.21. -0. -1. -1: Mr. Kazuo Wakasugi, Commissioner of the Patent Office (Mr. Chief Adjudicator of the Patent Office) (Mr. Examiner of the Patent Office) 1. Display of the case 1937
Patent Application No. 15521, filed in 2007 2, Title of the invention: Mesophase pitch tentative propagation method 3, Relationship with the case of the person making the amendment Patent applicant Address: Iku Tsukanaga 5-18-2 Koenji Minami, Suginami-ku Name: Tadashi Watanabe three
J4, agent address 2-8 Shinjuku, Shinjuku-ku, Tokyo 160
No. 1 Shinjuku Seven Building Room 608 (6601) Name Patent Attorney Yata Tosasai Department
[Phase] (Telephone: 354-1285 - 6) 5. Date of amendment order Voluntary amendment 6. Number of inventions increased by amendment Increase f (1) Change the description of the scope of claims as follows 1゜1) Petroleum-based pitch is stirred and heat-treated in a non-oxidizing air flow under normal pressure or pressurization, and the latter is held stationary to grow and melt only the mesophase in the heated pitch, forming a non-menu layer and a mesophase I. -Q characterized by segmentation into 1. Ingredients and Q, 8. A method for producing 100% Menzez Bich, which is composed only of ingredients.

2)上記の攪拌加勢処理条件が石油系ピッチを360℃
乃至450℃の温度で常圧或は加圧下で非酸化性気流下
で攪拌加熱処理して生成するピッチ中にメソフェーズの
含有量を10嗟乃至50饅に\\する特許請求の範囲1
の方法3)上記の静置保持条件がMiJ述の加熱生成ピ
ッチの加熱処理条件より全く別の処理条件であって非酸
化性気流下でυ11熱処熱処理上り低温の280℃乃至
3.5’ o℃の温度で加熱生成ピッチ中のメソフェー
ズのみが成長融着して加熱生成ピッチが非メン層とメン
層とに側熱と区分させメン層を区分分離するものである
特許請求の範囲1の方法 昭不1157年8月18日付補正畳中で次の補正をする
2) The above stirring and force treatment conditions are applied to petroleum pitch at 360°C.
Claim 1: The content of mesophase in the pitch produced by stirring and heating treatment in a non-oxidizing gas flow at a temperature of 450° C. to 450° C. under normal pressure or increased pressure is 10 to 50.
Method 3) The above-mentioned static holding conditions are completely different from the heat treatment conditions for the heat-generated pitch described in MiJ, and the υ11 heat treatment is performed at a low temperature of 280°C to 3.5' under a non-oxidizing air flow. Claim 1, wherein only the mesophase in the heat-generated pitch grows and fuses at a temperature of 0°C, and the heat-generated pitch separates the non-men layer and the men layer from the side heat, and separates the men layer. Method The following amendments are made in the amendment dated August 18, 1157.

5頁下から4行目 [(X11)  6負下よ、す6行目の」を((xll
)  5頁下より6行目に」5頁下から1行目 r (x+ii)  6頁下より4行目の」をr (x
ii+)  5貞Fより4行目の」に補正する。
4th line from the bottom of page 5 [(X11) 6 negative bottom, 6th line” ((xll
) 6th line from the bottom of page 5 r (x+ii) 1st line from the bottom of page 5 r (x+ii) 4th line from the bottom of page 6 r (x
ii+) Correct to `` from the 5th F on the 4th line.

Claims (1)

【特許請求の範囲】 1)石油系及びタール系ピッチを常圧或は力9圧下で非
酸化性気流下で攪拌加熱処理し、後2を静置保持して加
熱生成ピッチ中のイソフェーズを成長融着させ非メン層
とメン層とに区分分離することを特色とする100係メ
ソフエーズピツチを製造する方法。 2)石油系及びタール系ピッチを350°C乃至450
°Cの温度で常IEtは加田下で非酸化性気流下7攪拌
加熱竺理1テて生成する″チ中にメソフェーズの含有量
を10係乃至51Mに12.2f″を静置保持[・て非
メ子層と12層とに区分分離することを特徴と大る、1
00%メソフェーズピッチを製造する方法。 加熱処理温度より低温の280″C乃至370 ’C(
D温度で加熱生成ピッチ中のメツフェーズが成険融着し
て加熱生成ピッチが非メン層とメソ層とに側熱と区分さ
せメン層を区分分離することを特徴とする100 %メ
ソフェーズピッチを製造する方法つ
[Scope of Claims] 1) Petroleum-based and tar-based pitches are stirred and heat-treated under a non-oxidizing air flow at normal pressure or 9 pressures, and the remaining 2 is kept stationary to remove isophase in the heated pitch. A method for manufacturing a 100-layer mesophase pitch characterized by growing and fusing it and separating it into a non-men layer and a men layer. 2) Petroleum-based and tar-based pitches at 350°C to 450°C
At a temperature of °C, the IEt is heated under a non-oxidizing gas stream with stirring for 7 hours to produce a mesophase content of 10 to 51M and kept at 12.2f. The main feature is that the layer is divided into a non-meko layer and 12 layers.
A method of manufacturing 00% mesophase pitch. 280''C to 370'C (lower than the heat treatment temperature)
Production of 100% mesophase pitch characterized in that the mesophase in the heat-generated pitch is successfully fused at temperature D, and the heat-generated pitch separates the meso layer into a non-men layer and a meso layer, and separates the meso layer. One way to do it
JP1552182A 1982-02-04 1982-02-04 Preparation of mesophase pitch Granted JPS58134179A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1552182A JPS58134179A (en) 1982-02-04 1982-02-04 Preparation of mesophase pitch

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1552182A JPS58134179A (en) 1982-02-04 1982-02-04 Preparation of mesophase pitch

Publications (2)

Publication Number Publication Date
JPS58134179A true JPS58134179A (en) 1983-08-10
JPH0245669B2 JPH0245669B2 (en) 1990-10-11

Family

ID=11891112

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1552182A Granted JPS58134179A (en) 1982-02-04 1982-02-04 Preparation of mesophase pitch

Country Status (1)

Country Link
JP (1) JPS58134179A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57119984A (en) * 1980-07-21 1982-07-26 Toa Nenryo Kogyo Kk Preparation of meso-phase pitch

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5238855A (en) * 1975-09-22 1977-03-25 Nec Corp Error correcting unit
JPS5386717A (en) * 1973-12-11 1978-07-31 Union Carbide Corp Manufacture of mesoophase pitch by using inert gas
US4303631A (en) * 1980-06-26 1981-12-01 Union Carbide Corporation Process for producing carbon fibers

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5386717A (en) * 1973-12-11 1978-07-31 Union Carbide Corp Manufacture of mesoophase pitch by using inert gas
JPS5238855A (en) * 1975-09-22 1977-03-25 Nec Corp Error correcting unit
US4303631A (en) * 1980-06-26 1981-12-01 Union Carbide Corporation Process for producing carbon fibers

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57119984A (en) * 1980-07-21 1982-07-26 Toa Nenryo Kogyo Kk Preparation of meso-phase pitch
JPS6138755B2 (en) * 1980-07-21 1986-08-30 Toa Nenryo Kogyo Kk

Also Published As

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JPH0245669B2 (en) 1990-10-11

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