JPS58154791A - Manufacture of pitch for high-strength, high-modulus carbon fiber - Google Patents

Manufacture of pitch for high-strength, high-modulus carbon fiber

Info

Publication number
JPS58154791A
JPS58154791A JP57032281A JP3228182A JPS58154791A JP S58154791 A JPS58154791 A JP S58154791A JP 57032281 A JP57032281 A JP 57032281A JP 3228182 A JP3228182 A JP 3228182A JP S58154791 A JPS58154791 A JP S58154791A
Authority
JP
Japan
Prior art keywords
pitch
softening point
organic compound
petroleum
added
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
JP57032281A
Other languages
Japanese (ja)
Other versions
JPS6131156B2 (en
Inventor
Shozo Watanabe
渡辺 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 JP57032281A priority Critical patent/JPS58154791A/en
Publication of JPS58154791A publication Critical patent/JPS58154791A/en
Publication of JPS6131156B2 publication Critical patent/JPS6131156B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To highly efficiently manufacture the titled pitch at a low cost, by melting and mixing a petroleum pitch and an added specified org. compd., and cooling the mixture to separate an inorg. solid in the pitch together with the org. compd. followed by filtering. CONSTITUTION:To a petroleum pitch (A) is added an org. compd. (B) such as phthalic anhydride insoluble in the component A and having softening point higher than that of the component A and <=420 deg.C boiling point at a temp. lower than the softening point of said org. compd. and they are molten and mixed by heating to a temp. higher than the softening point of the component B. An org. solid material in the component A and the component B are separated by cooling the resulting mixture to a temp. lower than the softening point of the component B, and filtered, removing the inorg. solid material in the component A. Then the component B is added to the filtrate and the inorg. solid material in the component A is removed by repeating the above described operation. The obtd. pitch is heated with agitation to 350-450 deg.C under normal or raised pressure in a non-oxidizing gas stream.

Description

【発明の詳細な説明】 本発明は高強度高弾性炭素繊維用原料の製造に係るもの
で、4Iに複合材料の原料として好適な高強度高弾性炭
素繊維を安価に好能率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 relates to the production of raw materials for high-strength, high-modulus carbon fibers, and provides a method for producing high-strength, high-modulus carbon fibers suitable as raw materials for composite materials at low cost and with high efficiency. The purpose is to provide.

もつと詳細に述べると本発明は、減圧軽油の熱接触分解
(FCC) 、あるいはナフサの熱分解によりて副生さ
れる残渣炭素物質の石油系ピッチを加熱温度350℃乃
至450℃で非酸化性気流下攪拌加熱処理しメソフェー
ズピッチ(偏光顕微鏡及びキノリンの溶解試験でキノリ
ンネ溶分として容易に測定するととが出来る。)を含有
するピッチを製造するにわたり、予め原料の石油系ピッ
チに添加する有機化合物の軟化点以下の温度で′に#r
で、原料の石油系ピッチの軟化点以上の軟化点を有し。
More specifically, the present invention aims at converting petroleum pitch, a residual carbon substance produced by thermal catalytic cracking (FCC) of vacuum gas oil or thermal cracking of naphtha, into a non-oxidizing material at a heating temperature of 350°C to 450°C. An organic compound that is added to petroleum-based pitch as a raw material in advance to produce pitch containing mesophase pitch (which can be easily measured as quinoline dissolved content using a polarizing microscope and a quinoline dissolution test) by heat treatment with stirring under a stream of air. #r at a temperature below the softening point of
It has a softening point higher than the softening point of the raw material petroleum pitch.

沸点420℃以下の物性を有する有機化合物を石油系ピ
ッチに添加し、後この混合物を添加有機化合物の軟化点
以上に加温してよく溶解混合し、これを添加有機化合物
の軟化点以下に冷却し原料中に混在する無機質の固形物
を添加肩機物と共に析出せしめて添加有機化合物の軟化
点以下の温度で濾別し、高強度高弾性炭素繊維の原料と
して適したピッチを製造する方法に関する。
An organic compound having physical properties with a boiling point of 420°C or less is added to petroleum-based pitch, then the mixture is heated above the softening point of the added organic compound to thoroughly dissolve and mix, and then cooled to below the softening point of the added organic compound. This invention relates to a method for producing pitch suitable as a raw material for high-strength, high-elastic carbon fibers by precipitating inorganic solids mixed in the raw material together with added shoulder substances and filtering the mixture at a temperature below the softening point of the added organic compound. .

近年航空機、自動車、その他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して特別な物質の組合わ
せからなりそのいくつかの物理的性質が勝れておって且
つ特異性を発揮しうる材料を望む声が大きくなっている
が特に高い強度及び弾性を具備し、同時に軽量で安価な
材料の出現が強く要求されている。しかるに現在の技術
でかかる材料を多量に安定供給することが出来ない。
As a result of the rapid growth of the aircraft, automobile, and other transportation equipment manufacturing industries in recent years, the materials required for these are combinations of special substances that have superior physical properties and can exhibit unique properties. There has been an increasing demand for materials, and there is a strong demand for materials that have particularly high strength and elasticity, and at the same time are lightweight and inexpensive. However, with the current technology, it is not possible to stably supply such materials in large quantities.

従ってこの要望に答えるため複合瞼質(強化樹脂)の製
造に関する研究が盛んに行なわれている3゜強化樹脂に
使用される最も有望な材料の一つとして高強度高弾性炭
素繊維がある。この材料は前述の産業の急速な成長が始
t6かけた際に現われたもので、この炭素繊維を樹脂と
組合わせると他に全くその例を見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。しかし残念なこ
とでおるが強化樹脂用の高強度高弾性の炭素繊維は現在
極めて高価な為これを使用する強化樹脂が極めて顕著な
特性を発揮するにもかかわらずその需要があまり開拓さ
れていない。
Therefore, in order to meet this demand, research on the production of composite eyelid materials (reinforced resins) is being actively conducted.High-strength, high-modulus carbon fibers are one of the most promising materials for use in 3° reinforced resins. This material appeared at the beginning of the rapid growth of the aforementioned industry, and when this carbon fiber is combined with a resin, it produces a reinforced resin that exhibits properties that are completely unparalleled. I can do it. Unfortunately, however, the high-strength, high-elasticity carbon fibers used for reinforced resins are currently extremely expensive, so even though the reinforced resins that use them exhibit extremely remarkable properties, the demand for them has not been fully exploited. .

現在入手出来る高強度高弾性炭素繊維の原料は特殊な製
造法によって製造されたポリアクリルニトリル繊維が主
であることは公知の事実である。
It is a well-known fact that currently available raw materials for high-strength, high-modulus carbon fibers are mainly polyacrylonitrile fibers manufactured by special manufacturing methods.

このポリアクリルニトリル繊維は、炭素繊維の前駆体と
して高価であるばかりでなく、この前駆体からの炭素繊
維の収率が45 ’J以下で極めて悪い。
This polyacrylonitrile fiber is not only expensive as a carbon fiber precursor, but also the yield of carbon fiber from this precursor is extremely poor at 45'J or less.

この事が優れた物性を有する炭素線維を製造する処理工
程を複雑にし巨大化し、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。
This complicates and enlarges the processing steps for producing carbon fibers with excellent physical properties, thereby increasing the cost of producing the final carbon fiber product.

高強度高弾性炭素繊維を安価に製造する一つの方法とし
て、メソフェーズピッチを含有するピッチから製造する
方法が米国特許願第338,147号に記載され工いる
のでメソフェーズピッチを含有するピッチが高強度高弾
性炭素繊維の原料として極めて優れた原料であることは
公知の事実である。
As one method for producing high-strength, high-modulus carbon fibers at low cost, a method for producing them from pitch containing mesophase pitch is described in U.S. Patent Application No. 338,147. It is a well-known fact that it is an extremely excellent raw material for high modulus carbon fibers.

然るに石油系ピッチは減圧軽油の触媒による熱分解によ
って副生されるものの場合にはその触媒の微小の無Ii
!質の固形物をその中に含んでいる。又ナフサの高温の
熱分解によって副生されるものの場合VCFi高温のた
め反応器の材質の剥離が往々にして生じ、これが微小の
固形物として石油系ピッチに混入している。公知の方法
では無機質の固形物の混入している石油系ピッチを予備
処理することなく、そのまま所定の加熱温度で不活性ガ
ス下に攪拌加熱処理してメソフェーズピッチを含有する
ピッチを製造し、このピッチを溶融紡糸し、不融化後炭
化して長繊維の炭素−維を製造していた。
However, if petroleum pitch is a by-product of the catalytic thermal decomposition of vacuum gas oil, the catalyst's minute non-Ii
! It contains some solid matter. Furthermore, in the case of by-products produced by high-temperature thermal decomposition of naphtha, the reactor material often peels off due to the high temperature of VCFi, and this is mixed into petroleum-based pitch as minute solids. In a known method, petroleum pitch containing inorganic solids is heat-treated with stirring under an inert gas at a predetermined heating temperature without pre-treatment to produce pitch containing mesophase pitch. Pitch was melt-spun, made infusible, and then carbonized to produce long carbon fibers.

本願発明者は上記の石油系ピッチ中に混入している無機
質の固形物は炭素繊維中にボイド(空隙)をつくるがこ
のため及びその他の理由で炭素繊維の強度に極めて大き
な影響を与えることを知ったがこの知見を基にして石油
系ピッチに添加する有機化合物の軟化点以下の温度で石
油系ピッチに難溶で石油系ピッチの軟化点以上の軟化点
を有し。
The inventor of this application has discovered that the inorganic solids mixed in the petroleum-based pitch create voids in the carbon fibers, and for this and other reasons, have an extremely large effect on the strength of the carbon fibers. Based on this knowledge, it is difficult to dissolve in petroleum pitch at a temperature below the softening point of the organic compound added to petroleum pitch, but it has a softening point above the softening point of petroleum pitch.

沸点420℃以下の物性を有する有機化合物を石油系ピ
ッチに添加し、この混合物を添加有機化合物の軟化点以
上に加温しよく溶解混合し九後、添加有機物の軟化点以
下に冷却して添加有機化合物を結晶状に析出せしめる場
合1石油系ピッチ中に混在する無機質の固形物が添加有
機化合物の結晶生成の核の効果作用を発揮し1石油系ピ
ッチ中に混在する無機質の固形物が添加有機化合物と共
に析出する。仁の作用を利用して添加有機化合物の軟化
点以下の温度で無機質の固形物と共に析出する添加有機
化合物の結晶を添加有機化合物の軟化点以下の温度で濾
別し、その濾液の石油ピッチを350℃乃至450℃の
温度で常圧或は加圧下で非酸化性ガス気流下攪拌加熱処
理してメソ7エーズピツチを含有するピッチをりくりう
ることを見出した。
An organic compound having physical properties with a boiling point of 420°C or less is added to petroleum-based pitch, and the mixture is heated above the softening point of the added organic compound to dissolve and mix thoroughly. After 90 minutes, the mixture is cooled to below the softening point of the added organic compound and added. When organic compounds are precipitated into crystals, 1. The inorganic solids mixed in the petroleum-based pitch act as nuclei for crystal formation of the added organic compound; 1. The inorganic solids mixed in the petroleum-based pitch act as nuclei for crystal formation Precipitates together with organic compounds. The crystals of the added organic compound, which precipitate together with the inorganic solids at a temperature below the softening point of the added organic compound, are separated by filtration at a temperature below the softening point of the added organic compound, and the filtrate is extracted with petroleum pitch. It has been found that pitch containing meso-7Aze pitch can be diced by heat treatment with stirring in a stream of non-oxidizing gas at a temperature of 350° C. to 450° C. under normal pressure or increased pressure.

上記方法に従って無機質の同形物のないメソフェーズピ
ッチを分離し、これを溶融紡糸し不融化後炭化して高強
度高弾性の炭素繊維を製造しうろことを確めた。
According to the above method, mesophase pitch free of inorganic isomorphs was separated, melt-spun, infusible, and then carbonized to produce high-strength, high-elastic carbon fibers.

石油系ピッチ中に混在している極めて微細な無機質の固
形物を除去する手段として濾過器が採用される。濾過器
として金網の篩、1布式のフィルする無機質の固形物を
除去することは、濾過器を使用する限り不可能である。
A filter is used as a means to remove extremely fine inorganic solids mixed in petroleum pitch. As long as a wire mesh sieve or one-cloth filter is used as a filter, it is impossible to remove inorganic solids.

他の手段で極めて微細な固形物を除去するための手段が
必要である。
Means are needed to remove very fine solids by other means.

濾過器を使用して無機質の固形物(灰分)を0.113
6%含有する減圧軽油の熱接触分解(ycc)の残漬炭
素物質の石油系ピッチ(初留242℃→終貿560℃以
下)を下記の金網を使用して灰分の除去を試みたが、−
の目を通過する微細な固形物を除去することは不可能で
ある。
Use a filter to reduce inorganic solids (ash content) to 0.113
Attempts were made to remove ash from petroleum-based pitch (initial distillation 242°C → final trade 560°C or less), which is the residual carbon material from thermal catalytic cracking (YCC) of vacuum gas oil containing 6%, using the wire mesh shown below. −
It is impossible to remove fine solids that pass through the eyes.

濾過試験 金網篩の目を通過する極めて微細な無機質な固形物も炭
素繊維中に混在するボイド(空Wl)の原因となること
が判明し、より完全に無機質の固形物をより合理的に効
率よく除去する方法を研究した結果2本発明方法を完成
した。即ち本発明方法は原料の石油系ピッチに添加する
有機化合物の軟化点以下の温度で石油系ピッチに難溶で
8石油系ピッチの軟化点以上の軟化点を有し沸点420
℃以下の物性を有する有機化合物を原料に添加し。
Filtration test It was found that the extremely fine inorganic solids that pass through the wire mesh sieve are also the cause of voids (empty Wl) mixed in the carbon fiber, and it is possible to more completely remove inorganic solids in a more rational and efficient manner. As a result of research into methods for effective removal, two methods of the present invention were completed. That is, the method of the present invention uses a compound that is sparingly soluble in petroleum pitch at a temperature below the softening point of the organic compound added to the petroleum pitch as a raw material, has a softening point higher than the softening point of petroleum pitch, and has a boiling point of 420.
An organic compound with physical properties below ℃ is added to the raw material.

後これを添加有機化合物の軟化点以上に加温してよく溶
解混合し、更にこの混合溶液を添加物の軟化点以下に冷
却し、添加有機化合物を結晶状として析出する際、原料
中に混在する無機質の固形物が析出する結晶の核の作用
として効果を発揮させ。
After that, this is heated above the softening point of the additive organic compound to dissolve and mix well, and this mixed solution is further cooled below the softening point of the additive, and when the added organic compound is precipitated as a crystal, it is mixed in the raw material. The effect is exerted as a nucleus of crystals from which inorganic solids precipitate.

無機質の固形物と添加有機化合物と共に析出せしめ添加
有機化合物の軟化点以下の温度で濾別して。
The inorganic solids and the added organic compound are precipitated and separated by filtration at a temperature below the softening point of the added organic compound.

原料の石油系ピッチより無機質の固形物をより完全に除
去し、これを高強度高弾性炭素繊維の原料製造用に供す
るピッチの製造方法である。
This method removes inorganic solids more completely from petroleum-based pitch as a raw material, and uses the pitch for producing raw material for high-strength, high-elastic carbon fibers.

これをよりくわしく説明すると、原料の石油系ピッチに
添加する有機化合物の軟化点以下の温度で石油系ピッチ
に難溶で、且つ原料の軟化点以上の軟化点を有し、沸点
420℃以下の物性を有する有機化合物は極めて多くあ
るが、結晶性がよく。
To explain this in more detail, it is poorly soluble in petroleum pitch at a temperature below the softening point of the organic compound added to the petroleum pitch raw material, has a softening point above the softening point of the raw material, and has a boiling point of 420°C or below. There are many organic compounds that have physical properties, but they have good crystallinity.

混合物よりも純粋な化合物が取シ扱い易く、加温して溶
解混合する操作を考慮すると軟化点40℃以上の芳香族
の有横酸、芳香族の酸化物、芳香族のハロゲン化合物、
パラフィンワックス等が挙げられるが、よく使用される
有機化合物は無水フタール酸、ナフトール、クロールナ
フタリン等がある。更に原料中に混在している微細な無
機質の固形物の粒の大きさに差異があるため、添加有機
物を石油系ピッチ中で結晶状に析出する場合、結晶速度
、生成する結晶の大きさに差異を生じ、無機:質の固形
物の濾別に不手際を生ずることもありうるので1石油系
ピッチ中に混在する無機質の固形物のより完全な除去を
期するため、予め鰹式の濾過器で濾過することによシ、
無機質の固形物粒の大きさを篩の目を通過する程度に均
一化し、添加有機化合物の結晶速度、生成する結晶の大
きさを出来るだけ均一化して0石油系ピッチ中に混在す
る無機質の固形物の除去の完全を期することも有効であ
る。
Pure compounds are easier to handle than mixtures, and considering the operation of heating and dissolving and mixing, aromatic hydroxy acids, aromatic oxides, aromatic halogen compounds with a softening point of 40°C or higher,
Examples include paraffin wax, and commonly used organic compounds include phthalic anhydride, naphthol, and chlornaphthalene. Furthermore, since there are differences in the size of the fine inorganic solid particles mixed in the raw materials, when the added organic matter is precipitated in the form of crystals in petroleum-based pitch, the crystallization rate and the size of the formed crystals will vary. In order to remove the inorganic solids mixed in the petroleum pitch more completely, we used a bonito-type filter in advance. By filtering,
The size of the inorganic solid particles is made uniform to the extent that they can pass through a sieve, and the crystallization speed of the added organic compound and the size of the crystals formed are made as uniform as possible. It is also effective to ensure complete removal of objects.

石油系ピッチ中の混入する無機質の固形物を前述の如く
本発明の方法によって除去した石油系ピッチを350℃
乃至450℃の温度で常圧あるいは加圧下で非酸化性ガ
ス気流下攪拌処理してメソフェーズピッチを含有するピ
ッチをつ〈シ出しこれからメソフェーズピッチを分離し
て製造することも本発明の別の一面でありかくして得ら
れたメソフェーズピッチを溶融紡糸、不融化後炭化して
極めて物性のすぐれた高強度、高弾性の長繊維の炭素繊
維を製造することが出来る。。
The petroleum pitch from which the inorganic solids mixed in the petroleum pitch have been removed by the method of the present invention as described above is heated at 350°C.
Another aspect of the present invention is to produce a pitch containing mesophase pitch by stirring under a stream of non-oxidizing gas at a temperature of 450°C to 450° C. under normal pressure or increased pressure, and then separating the mesophase pitch from the pitch. The mesophase pitch thus obtained can be melt-spun, infusible, and then carbonized to produce long-fiber carbon fibers with excellent physical properties, high strength, and high elasticity. .

尚非酸化性ガスとして使用出来るものは、メタン、エタ
ン、プロパン勢炭素数の少ない炭化水素。
Hydrocarbons with a small number of carbon atoms such as methane, ethane, and propane can be used as non-oxidizing gases.

沸点が低く重質化しないナフサ留分、そして経済的に最
もすぐれているガスとしては、原料を加熱処理して副生
ずるドライガス(主として炭素数の少ない炭化水素の混
合ガス)を挙けることが出来る。
The naphtha fraction has a low boiling point and does not become heavy, and the most economical gas is dry gas (mainly a mixed gas of hydrocarbons with a small number of carbon atoms) produced as a by-product when heat treating raw materials. I can do it.

実施例1 無機質の固形物(灰分)を0.1136−含有する減圧
軽油の熱接触分解(ycc)の残漬炭素物質の石油系ピ
ッチ(初留242℃→終留560℃以下)K無水フタノ
ール酸を0.4%(重量)添加し、約150℃に加温し
、よく攪拌して溶解し、@4a℃に徐冷し添加物の無水
フタノール酸の結晶を生長卓せこれを40℃で濾過除去
し、その濾液を減圧蒸留して初留404℃→終留560
℃以上の留分を非酸化性ガス化で400℃で2時間加熱
処理して前駆体ピッチを製造した。
Example 1 Petroleum-based pitch (initial distillation 242°C → final distillation 560°C or less) of residual carbon material from thermal catalytic cracking (YCC) of vacuum gas oil containing 0.1136% of inorganic solids (ash content) K anhydrous phthanol Add 0.4% (by weight) of acid, heat to about 150°C, stir well to dissolve, and slowly cool to 4a°C to grow crystals of phthanolic anhydride as an additive. The filtrate was distilled under reduced pressure to reduce the initial distillation temperature from 404°C to the final distillation temperature at 560°C.
A precursor pitch was produced by heating the fraction at 400°C for 2 hours using non-oxidizing gasification.

前駆体の収率54−1前駆体の軟化点(R4B相幽)6
7℃この前駆体ピッチを下記の実験番号の加熱処理条件
で処理した。
Precursor yield 54-1 Precursor softening point (R4B phase) 6
This precursor pitch was treated at 7°C under the heat treatment conditions of the experiment number below.

第1表 常圧加熱処理の結果 実験番号(1)の加熱条件で処理してメソフェーズピッ
チ含有のピッチをつ<)、これよりメソピッチを分離し
、メソピッチを下記の紡糸条件で紡糸し。
Table 1 Results of normal pressure heat treatment A pitch containing mesophase pitch was obtained by treatment under the heating conditions of experiment number (1), from which meso pitch was separated, and the meso pitch was spun under the following spinning conditions.

後不融化炭化して炭素繊維をりくり、それの品位をフィ
ラメント試験法で試験した。
After infusibility and carbonization, the carbon fibers were cut out and their quality was tested using the filament test method.

紡糸条件;温度320℃紡糸孔径0,3!11/II紡
糸速度22 Q m/l1lin 不融化条件; (空気中で)不融−維の収率10マ、6
−〇℃→280℃昇温速度 5℃/分 280℃にて20分間保持 炭化条件; (アルゴンガス中で)#!素繊維の収率8
6.2チ 0℃→1.500℃(10℃/分昇温)。
Spinning conditions: Temperature: 320°C Spinning hole diameter: 0.3!11/II Spinning speed: 22 Q m/l1lin Infusibility conditions: Yield of infusible fibers (in air): 10 mm, 6
-〇℃→280℃ Temperature increase rate 5℃/min Hold at 280℃ for 20 minutes Carbonization conditions: (in argon gas) #! Yield of elementary fiber 8
6.2chi 0℃ → 1.500℃ (temperature increase 10℃/min).

後1,500℃→500℃(10℃/分冷却)・無処理
ピッチよりのものは1本発明法によらず、無処理のピッ
チを原料としC同じ熱処理。
After 1,500℃ → 500℃ (cooling at 10℃/min)・Things from untreated pitch 1 The method of the present invention was not applied, but untreated pitch was used as the raw material and C was subjected to the same heat treatment.

同じ紡糸、炭化条件で製作した繊維ズある。There are fibers produced under the same spinning and carbonization conditions.

実施例2 実施例1の石油系ピッチを前述の濾過試験の0.2μの
篩を使って濾過し、その濾液にβ−クロールナフタリン
(軟化点56℃)を0.2tlkC重量)を添加し、約
80℃に加温し、よく攪拌して溶解し、後40℃に徐冷
し、添加物のクロールナフタリンの結晶を生長させ、こ
れを40℃で濾過除去し。
Example 2 The petroleum pitch of Example 1 was filtered using the 0.2 μ sieve of the above-mentioned filtration test, and β-chlornaphthalene (softening point 56°C) (0.2 tlkC weight) was added to the filtrate. The mixture was heated to about 80°C, stirred well to dissolve, and then slowly cooled to 40°C to grow crystals of chlornaphthalene, an additive, which were filtered off at 40°C.

その濾液を減圧蒸留して初留404℃→終留560℃以
上の留分を非酸化性ガス下で400℃で2時間加熱処理
して前駆体ピッチを製造した。
The filtrate was distilled under reduced pressure, and the fraction with an initial distillation of 404°C and a final distillation of 560°C or higher was heat-treated at 400°C for 2 hours under non-oxidizing gas to produce a precursor pitch.

前躯体の収率54−前駆体の軟化点(RAB相当)67
℃この前躯体ピッチを前述の第1表の実験番号(2)の
加熱条件で処理してメソフェーズピッチヲ含有するピッ
チをつ<シ、これからメンピッチを分離し。
Precursor yield 54 - Precursor softening point (RAB equivalent) 67
℃ This precursor pitch was treated under the heating conditions of Experiment No. (2) in Table 1 above to obtain pitch containing mesophase pitch, from which men pitch was separated.

これを実施例1の紡糸条件で紡糸し、この原糸を実施例
1と同じ条件で不融化、炭化して炭素繊維をつくり、そ
れの品位をフラメント試験法にて試験した。
This was spun under the spinning conditions of Example 1, and the raw yarn was made infusible and carbonized under the same conditions as Example 1 to produce carbon fibers, and the quality of the fibers was tested using the filament test method.

炭素線維の強度試験結果 :印紙1         昭和s7年3月2SBし、
、−−−−−、−j 特許庁長官  島 1)春 樹  殿 (特許庁審判長          殿)(特許庁審査
官          殿)1、事件の表示  昭和b
フ年特許願第−322J’/  号2、 発明の名称 
高強度高弾性炭素−雑用ピッチの製法3、補正をする者 事件との関係  特許出願人 住  所 東京都杉並区高円寺南5丁目1Bの2氏  
名   渡  部  正  三          の
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 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 増加せず7、補正の
対象  明細書の発明の詳細な説明の項8、補正の内容
別紙の通シ ロ負11行目〜14行目 「本―発明者は・・・・・・の強度に」を「本鵬発明者
Fi種々研究した結果上記の石油系ピッチ中に混合して
いる無機質の固形−が炭素軌線の1性41に強度及び弾
性率Kl変更する。
Carbon fiber strength test results: Stamp 1 March 1939 2SB,
, ------, -j Director General of the Patent Office Shima 1) Mr. Haruki (Mr. Chief Adjudicator of the Patent Office) (Mr. Examiner of the Patent Office) 1. Indication of the case Showa b
Patent Application No.-322J'/No. 2, Title of Invention
High-strength, high-elastic carbon - Manufacturing method for miscellaneous pitch 3, relationship with the amended case Patent applicant address: Mr. 2, 5-1B Koenji Minami, Suginami-ku, Tokyo
Name Shozo Watabe 4, Agent Address 2-8 Shinjuku, Shinjuku-ku, Tokyo 160
No. 1 Shinjuku Seven Building 608 Room 5, Date of amendment order Voluntary amendment 6, Number of inventions increased by amendment No increase 7, Subject of amendment Detailed explanation of the invention in the specification Section 8, Contents of amendment attached Lines 11 to 14 of the negative line ``This invention - the strength of...'' is changed to ``The inventor Fi, as a result of various studies, found that the inorganic material mixed in the above petroleum-based pitch The solid state changes the strength and modulus of elasticity Kl to 1 property of the carbon trajectory.

8頁下から3〜2行目 「炭素繊維中に混在するボイド(空1ll)の原因とな
る」を 「炭素IIII維の物性4IK強度及び弾性率に大きな
影譬を与えるjに変更する。
In the 3rd to 2nd lines from the bottom of page 8, "Causes voids (1ll of voids) mixed in carbon fibers" is changed to "j that has a large influence on the physical properties 4IK strength and elastic modulus of carbon III fibers."

12頁6〜7行目 「560℃以上の留分を非酸化性ガス化で」を「560
℃以下の留分を非酸化性ガス下で」に変更する。
Page 12, lines 6 to 7, "Non-oxidizing gasification of fractions at 560°C or higher" is changed to "560
℃ or less under non-oxidizing gas.

14頁12行目 「以上の留分」を「以下の留分」に変更する。Page 14, line 12 Change "distillate above" to "distillate below".

a辷 手続補正書 1印紙1          昭和5フ年8月1日し一
−−−−−−−H−−−−’ 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b
フ年特許願第3■81 号3、補正をする者 事件との関係  特許出願人 住  所 東京都杉並区高円寺南6丁目18の2氏  
  名    A ! 】ヒ ニ          
         の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 (1)明細書の特許請求の範囲の記載を次の橡に変更す
る。
a. Procedural Amendment 1 Stamp 1 August 1, 1930 - H-----' Commissioner of the Patent Office Mr. Kazuo Wakasugi (Mr. Patent Office Chief Adjudicator) (Mr. Patent Office Examiner) ) 1.Display of the incident Showa b
Patent Application No. 3, 81, No. 3, 2013, Relationship with the Amendment Case Patent Applicant Address: Mr. 2, 6-18 Koenji Minami, Suginami-ku, Tokyo
Name A! 】Hi Ni
4. Agent address: 2-8 Shinjuku, Shinjuku-ku, Tokyo 160
No. 1 Shinjuku Seven Building Room 608 (1) The claims in the specification are changed to the following.

(1)石油系ピッチに添加する有機化合物の軟化点以下
の温度で石油系ピッチに難溶で1石油系ピッチの軟化点
以上の軟化点を有し、沸点420℃以下の物性を有する
有機化合物を石油系ピッチに添加し、この混合物を添加
有機化合物の軟化点以上に加温してよく溶解混合し、後
添加有機化合物の軟化点以下に冷却して石油系ピッチp
に混在する無機質の固形物を添加有機化合物と共に析出
せしめて、添加有機化合物の軟化点以下の温度で炉別し
て9石油系ピッチ中に混在する無機質の固形物を除去す
るか又は石油系ピッチ中に混在する無機質の固形物を濾
過器で一過し、そのF*に前述の有機化合物を添加し、
得られた混合物を添加有機化合物の軟化点以上に加温し
てよく溶解混合し、後添加有機化合物の軟化点以下に冷
却し、F液中に尚混在する無機質の固形物を添加有機化
合物と共に析出せしめて添加有機化合物の軟化点以下の
温度で炉別して1石油系ピッチ中に混在する無機質の固
形物を除去する方法。
(1) An organic compound that is sparingly soluble in petroleum pitch at a temperature below the softening point of the organic compound added to petroleum pitch, has a softening point above the softening point of petroleum pitch, and has physical properties with a boiling point of 420°C or below. is added to petroleum-based pitch, the mixture is heated above the softening point of the added organic compound, thoroughly dissolved and mixed, and then cooled below the softening point of the added organic compound to form petroleum-based pitch P.
The inorganic solids mixed in the petroleum pitch are precipitated together with the added organic compound, and separated in a furnace at a temperature below the softening point of the added organic compound to remove the inorganic solids mixed in the petroleum pitch. The mixed inorganic solids are passed through a filter, and the above-mentioned organic compound is added to the F*,
The resulting mixture is heated above the softening point of the added organic compound to dissolve and mix well, and then cooled below the softening point of the added organic compound to remove inorganic solids still present in the F solution together with the added organic compound. A method of removing inorganic solids mixed in petroleum pitch by precipitating and separating in a furnace at a temperature below the softening point of the added organic compound.

(2)  石油系ピッチ中に混入する無機質の固形物を
前述の有機化合物を添加し、前述の処111によって。
(2) The above-mentioned organic compound is added to the inorganic solids mixed in the petroleum-based pitch, and the above-mentioned process 111 is carried out.

除去した石油系ピッチを31SO℃乃至4!SO℃の温
度で常圧あるいは加圧下で、非酸化性ガスの気流下で攪
拌しながら加熱魁珊して高強度高弾性縦索繊維用の原料
のメソフェーズを含有するピッチを製造する方法。
The removed petroleum pitch is heated to 31SO℃ to 4! A method for producing mesophase-containing pitch, which is a raw material for high-strength and high-elastic longitudinal fibers, by heating it under normal pressure or increased pressure at a temperature of SO° C. with stirring under a stream of non-oxidizing gas.

(2)  明細書の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 section of the specification.

(1)3jl上から10行目の 「−ズピツチ(偏」を「−ズ(偏」に変更する。(1) 3jl 10th line from the top Change "-zupituchi (biased)" to "-zu (biased)."

(15頁下から1行目の 「−ズビツチを會」を 「−ズを含」に変更する。(1st line from the bottom of page 15 “-Zubitschi wo meeting” Change it to "-".

(2))5貴下から5行目の 「−ズビツチを含」を「−ズを含」に変更する。(2)) 5th line from you Change "Includes -Zbit" to "Includes -Z".

−6買上から8行目の 「−ズビツチを含」を「−ズを含」に変更する。-8th line from 6 purchase Change "Includes -Zbit" to "Includes -Z".

(v)6真下から10行目の 「省は」と「上記の°」の間に 「種々研究した結果」を入れる。(v) 10th line from directly below 6 Between “Ministry” and “above °” Insert "results of various studies".

611)63i下から9行目から下から1行目迄の[は
炭素繊維中にボイド(空隙)t−りくるがこのため及び
その他の理由で縦索僚維の強度」を「が縦索繊維の物性
%に強度及び弾性率」に変更する。
611) 63i From the 9th line from the bottom to the 1st line from the bottom, there are voids in the carbon fibers, but for this and other reasons, the strength of the longitudinal fibers is Change the physical properties of the fiber to % strength and elastic modulus.

&ゆ フ真下から6行目の 1−−ズビツチを分」をr−ズを分」に変更する。& Yufu 6th line from the bottom 1. Change "Zbitchi to Minutes" to "Rss to Minutes."

(幡 8j[下から3行目から下から2行目迄の「炭素
繊維中Kll在するボイド(空隙)の原因となる」を「
炭素―錐の物性41に強度及び弾性率に大き愈影響を与
える」に変更する。
(Hata 8j [From the third line from the bottom to the second line from the bottom, "Causes voids present in carbon fiber"]
Carbon - has a large influence on the strength and elastic modulus of the physical properties 41 of cones.''

(IX) 11買上から1行目の 「−ズビツチを含」を「−ズを含」に変更する。(IX) 1st line from 11 purchase Change "Includes -Zbit" to "Includes -Z".

(→ 11真上から6行目の 「−ズビツチを含」を「−ズを含JKI更する。(→ 6th line from directly above 11 Change "-Zubitschi included" to "-Z included JKI."

6$ 11買上から1行目の 「−ズピッチな含」を「−ズを書」に変更する。1st line from 6$11 purchase Change "-zu pitch na inclusion" to "-zu wo writing."

@ 12買上から5行目の 「560℃以上」を1560℃以下jK賓更する。@ 5th line from 12 purchase Change "560℃ or higher" to 1560℃ or lower.

6dl)lft真上から6行目の 「ガス化で」をrガス下でjに変更する。6dl) lft 6th line from the top Change "by gasification" to "j" under r gas.

(XIV) 12頁第1表第3欄の [1中ヤリヤーガスi o、e I O061Jを「I
I?ヤリャーガス16161Jに変更する。   −W
XZ頁下から1行目の 「キャリヤーガス」を 「キャリヤーガス メタンガス(1)/原料C−)×(
分)」に変更する。
(XIV) In column 3 of Table 1 on page 12, replace Yariyagas i o, e I O061J with “I
I? Change to Yaryagasu 16161J. -W
"Carrier gas" in the first line from the bottom of page XZ is "Carrier gas methane gas (1) / Raw material C-) x (
minutes)”.

kVl)13買上から1行目から上から2行目迄の「−
ズピツチ含有」を「−ズ含有」に変更する。
kVl) 13 Purchase from the first line to the second line from the top "-
Change "Zupitzchi Contains" to "-ZZ Contains".

6411Dll真上から2行目の 「メンピッチ」を「メソフェーズ」に変更する。6411Dll 2nd row from the top Change "Menpitch" to "Mesophase".

6@11114)j下から9行目の 「以上の」を「以下の」に変更する。6@11114)j 9th line from the bottom Change "more than" to "less than".

(XIV)  14頁下から4行目の(XIV) Page 14, 4th line from the bottom

Claims (2)

【特許請求の範囲】[Claims] (1)  石油系ピッチに銖加する有機化合物の軟化点
以下の温度で石油系ピッチに難溶で1石油系ピッチの軟
化点以上の軟化点を有し、沸点420℃以下の物性を有
する有機化合物を石油系ピッチに添加し、この混合物を
添加有機化合物の軟化点以上に加温してよく溶解混合し
、後添加有機化合物の軟化点以下に冷却して石油系ピッ
チに混在する無機質の固形物を添加有機化合物と共rc
析出せしめて。 添加有機化合物の軟化点以下の温度で1別して。 石油系ピッチ中に混在する無機質の固形物を除去するか
又は石油系ピッチ中に混在する無機質の同形物を濾過器
で蝋過し、その1液に前述の有機化。 合物を添加し、得られた混合物を添加有機化合物の軟化
点以上に加温してよく溶解混合し、後添加有機化合物の
軟化点以下に冷却し、濾液中に尚混在する無機質の固形
物を添加有機化合物と共に析出せしめて添加有機化合物
の軟化点以下の温度で1別して1石油系ピッチ中に混在
する無機質の同形物を除去する方法。
(1) An organic compound that is poorly soluble in petroleum pitch at a temperature below the softening point of the organic compound to be added to petroleum pitch, has a softening point above the softening point of petroleum pitch, and has physical properties with a boiling point of 420°C or below. The compound is added to petroleum-based pitch, the mixture is heated above the softening point of the added organic compound to dissolve and mix well, and then cooled below the softening point of the added organic compound to form the inorganic solids mixed in the petroleum-based pitch. rc with added organic compounds
Let it precipitate. Separate at a temperature below the softening point of the added organic compound. The inorganic solids mixed in the petroleum-based pitch are removed, or the inorganic isomorphic substances mixed in the petroleum-based pitch are waxed through a filter, and the above-mentioned organic compound is added to the first liquid. The resulting mixture is heated above the softening point of the added organic compound to dissolve and mix well, and then cooled below the softening point of the added organic compound to remove any inorganic solids still present in the filtrate. A method for removing inorganic isomorphic substances mixed in petroleum-based pitch by precipitating it together with an added organic compound and separating it at a temperature below the softening point of the added organic compound.
(2)  石油系ピッチ中に混入する無機質の同形物を
前述の有機化合物を添加し、前述の処理によって。 除去した石油系ピッチを350℃乃至450℃の温度で
常圧あるいは加圧下で、非鹸化性ガスの気流下で攪拌し
ながら加熱処理して高強度高弾性炭素縁雑用の原料のメ
ンフエーズビチチを含有するピッチを製造する方法。
(2) Add the above-mentioned organic compound to the inorganic isomorphic substance mixed in the petroleum-based pitch, and perform the above-mentioned treatment. The removed petroleum pitch is heat-treated at a temperature of 350°C to 450°C under normal pressure or pressure, with stirring under a stream of non-saponifiable gas, to produce high-strength, high-elastic carbon rimming raw material. A method of producing pitch containing.
JP57032281A 1982-03-03 1982-03-03 Manufacture of pitch for high-strength, high-modulus carbon fiber Granted JPS58154791A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57032281A JPS58154791A (en) 1982-03-03 1982-03-03 Manufacture of pitch for high-strength, high-modulus carbon fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57032281A JPS58154791A (en) 1982-03-03 1982-03-03 Manufacture of pitch for high-strength, high-modulus carbon fiber

Publications (2)

Publication Number Publication Date
JPS58154791A true JPS58154791A (en) 1983-09-14
JPS6131156B2 JPS6131156B2 (en) 1986-07-18

Family

ID=12354586

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57032281A Granted JPS58154791A (en) 1982-03-03 1982-03-03 Manufacture of pitch for high-strength, high-modulus carbon fiber

Country Status (1)

Country Link
JP (1) JPS58154791A (en)

Also Published As

Publication number Publication date
JPS6131156B2 (en) 1986-07-18

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