JPH0420495Y2 - - Google Patents
Info
- Publication number
- JPH0420495Y2 JPH0420495Y2 JP1986012614U JP1261486U JPH0420495Y2 JP H0420495 Y2 JPH0420495 Y2 JP H0420495Y2 JP 1986012614 U JP1986012614 U JP 1986012614U JP 1261486 U JP1261486 U JP 1261486U JP H0420495 Y2 JPH0420495 Y2 JP H0420495Y2
- Authority
- JP
- Japan
- Prior art keywords
- rotating shafts
- stirring plates
- pitch
- reactor
- reactor body
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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- Mixers Of The Rotary Stirring Type (AREA)
- Working-Up Tar And Pitch (AREA)
- Inorganic Fibers (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は、高性能ピツチ系炭素繊維の原料とな
るピツチを製造するために使用される熱処理反応
器の改良に関する。[Detailed Description of the Invention] [Industrial Field of Application] The present invention relates to an improvement in a heat treatment reactor used to produce pitch, which is a raw material for high-performance pitch-based carbon fiber.
近年、航空機工業、自動車工業、又はその他の
種々の技術分野の技術進歩に即応し、或いは省エ
ネルギ、省資源の観点から軽量、高強度かつ高弾
性率を有する複合材料の素材として高強度、高弾
性率、高性能のピツチ系炭素繊維の開発が要望さ
れている。こうしたピツチ系炭素繊維は、原料ピ
ツチを加熱して脱アルキル反応と同時に縮合環化
反応を行なつて液晶状態のメソフエーズを多量に
含むピツチを生成し、このピツチを紡糸した後、
このピツチ繊維を不融化処理して不融化繊維と
し、更に炭素化、黒鉛化処理を行なうことにより
製造される。
In recent years, in response to technological advances in the aircraft industry, automobile industry, and various other technical fields, or from the viewpoint of energy and resource conservation, high strength and high There is a need for the development of pitch-based carbon fibers with high elastic modulus and high performance. Such pitch-based carbon fibers are produced by heating the raw material pitch to perform a dealkylation reaction and a condensation cyclization reaction to produce pitch containing a large amount of mesophase in a liquid crystal state, and after spinning this pitch,
It is manufactured by subjecting this pitch fiber to an infusible treatment to obtain an infusible fiber, which is then further subjected to carbonization and graphitization treatment.
ところで、上記ピツチ系炭素繊維の原料である
メソフエーズを含むピツチの製造方法としては、
いかつかの方法が提案されている。しかしなが
ら、これらの方法にあつては長時間の反応を必
要とし、かつ複雑な工程を必要とする、ピツチ
の軟化点が上昇するため紡糸が困難となる、ピ
ツチの軟化点を抑制すると不均質となる等の問題
があつた。 By the way, as a method for producing pitchi containing mesophase, which is the raw material for the pitch carbon fiber,
Several methods have been proposed. However, these methods require a long reaction time and complicated steps, the softening point of the pitch increases, making spinning difficult, and suppressing the softening point of the pitch results in non-uniformity. There were some problems.
このようなことから、前記ピツチの製造方法と
して特開昭55−99646号に開示された方法が提案
されている。この方法は、重質油、タール又はピ
ツチを出発原料としてこれを一つの反応槽に収容
して内部に配置された攪拌羽根により攪拌、混合
しながら380℃程度の温度にて熱分解、重縮合し
てメソフエーズが20〜80%となるようにした後、
該重縮合物を400℃以下に保持しながら静置し、
反応槽の下層に密度の高いメソフエーズピツチを
沈降せしめ、成長熟成させつつ集積して、これを
反応槽上層の非メソフエーズピツチ(メタフエー
ズ)を多く含む部分から分離して取出す方法であ
る。 For this reason, a method disclosed in Japanese Patent Application Laid-Open No. 55-99646 has been proposed as a method for manufacturing the pitch. This method uses heavy oil, tar, or pitch as a starting material, which is placed in a reaction tank and subjected to thermal decomposition and polycondensation at a temperature of approximately 380°C while being stirred and mixed by an internal stirring blade. After adjusting the mesophase concentration to 20-80%,
The polycondensate is allowed to stand still while being maintained at 400°C or below,
This is a method in which high-density mesophase pitches are allowed to settle in the lower layer of the reaction tank, allowed to grow and mature, and then accumulated, and then separated and taken out from the upper layer of the reaction tank, which contains a large amount of non-mesophase pitches (metaphases). .
しかしながら、上記方法では反応槽内で出発原
料であるピツチ等を熱分解、重縮合させる際、該
反応槽内に配置した攪拌羽根により単に攪拌、混
合するため、反応槽の内壁にピツチやコークスが
析出する、いわゆるコーキングを生じる。こうし
たコーキング物が反応槽の内壁に生成すると、次
のような問題を生じる。
However, in the above method, when the starting materials such as pitch are thermally decomposed and polycondensed in the reaction tank, they are simply stirred and mixed using stirring blades placed in the reaction tank, so pitch and coke are deposited on the inner wall of the reaction tank. This causes precipitation, so-called coking. When such coking substances are formed on the inner wall of the reaction tank, the following problems occur.
反応槽の容積が減少し、所定の反応時間が保
持できなくなる。 The volume of the reaction tank decreases, making it impossible to maintain the predetermined reaction time.
コーキング物が巨大化すると、反応槽内の攪
拌、混合を阻害し、更にコーキング物の生成が
助長されると共に反応物の検出等が困難とな
る。 When the coking material becomes large, it obstructs stirring and mixing in the reaction tank, further promotes the formation of the coking material, and makes it difficult to detect the reactant.
コーキング物の生成により、反応槽の外部に
配置された熱源から反応槽内部のピツチへの熱
伝達効率が低下する。 The formation of coking reduces the efficiency of heat transfer from the heat source located outside the reactor to the pitch inside the reactor.
コーキング物の生成により、温度計、液面計
等の誤指示を生じ易くなり、運転が不可能とな
る。 Due to the formation of caulking materials, thermometers, liquid level gauges, etc. tend to give incorrect readings, making operation impossible.
本考案は、上記従来の課題を解決するためにな
されたもので、軟化点が比較的低いメソフエーズ
を多量に含むピツチが得られることは勿論、重縮
合時のコーキングを防止できると共に出発原料に
対して高収率で前記ピツチを得ることが可能なピ
ツチ製造用熱処理反応器を提供しようとするもの
である。 The present invention was devised to solve the above-mentioned conventional problems, and it not only makes it possible to obtain a pitch containing a large amount of mesophase with a relatively low softening point, but also prevents coking during polycondensation and is effective against starting materials. It is an object of the present invention to provide a heat treatment reactor for producing pitches that can obtain the pitches in high yield.
本考案は、横置き型の反応器本体と、該本体の
長さ方向に互いに平行して配設された同一速度で
回転する複数の回転軸と、これら回転軸に側面が
互いに密接するように軸着され、かつ各回転軸間
において面方向で互いに合致するように配置され
た複数の攪拌板とから構成され、前記各回転軸に
軸着される複数の攪拌板はその中心が回転軸の軸
心に対し回転軸方向に螺旋状の軌跡を描くように
偏心して配置され、かつ面方向で互いに合致する
攪拌板同志はそれらの中心が回転軸の軸心に対し
同一方向、同一距離となるよう偏心されると共に
周面が互いに僅かな間隙をおくかもしくは接触し
て配置され、更に前記反応器本体はその内部に配
置される攪拌板群の回転により描かれる最外端軌
道に等しいかもしくは僅かに大きい断面形状を有
することを特徴とするピツチ製造用熱処理反応器
である。
The present invention consists of a horizontal reactor main body, a plurality of rotating shafts arranged parallel to each other in the length direction of the main body and rotating at the same speed, and a structure in which the side surfaces of these rotating shafts are in close contact with each other. It consists of a plurality of stirring plates that are pivoted and arranged so as to coincide with each other in the plane direction between the respective rotating shafts. Stirring plates that are arranged eccentrically so as to draw a spiral trajectory in the direction of the rotation axis with respect to the axis, and that coincide with each other in the plane direction, have their centers in the same direction and at the same distance from the axis of the rotation axis. The reactor body is eccentrically arranged so that the circumferential surfaces thereof are arranged with a slight gap or in contact with each other, and the reactor body is arranged such that the outermost orbit is equal to or This is a heat treatment reactor for pitch production, characterized by having a slightly larger cross-sectional shape.
本考案の熱分解、重縮合を行なう熱処理反応器
によれば、攪拌板間及び攪拌板と反応器本体の間
でセルフクリーニングがなされるため、前述した
コーキング物の生成を防止でき、熱分解、重縮合
反応の迅速化、熱効率の向上化等を達成できる。
According to the heat treatment reactor for thermal decomposition and polycondensation of the present invention, self-cleaning is performed between the stirring plates and between the stirring plate and the reactor body, so the formation of the above-mentioned coking substances can be prevented, and the thermal decomposition and polycondensation It is possible to speed up the polycondensation reaction and improve thermal efficiency.
以下、本考案の実施例を第1図〜第5図を参照
して説明する。
Embodiments of the present invention will be described below with reference to FIGS. 1 to 5.
図中の1は、熱処理反応器である。この熱処理
反応器1で熱分解、重縮合反応処理されたピツチ
は、配管4aを通して次の工程に供給される。 1 in the figure is a heat treatment reactor. Pitch subjected to thermal decomposition and polycondensation reactions in this heat treatment reactor 1 is supplied to the next step through a pipe 4a.
前記熱処理反応器1は、第2図〜第5図に示す
構造となつている。即ち、図中の11は第4図及
び第5図に示すように内部に配置される後記攪拌
板群の回転により描かれる最外端軌道に等しい断
面が円を2つ連結した形状の筒体状反応器本体で
ある。この本体11の左端上部及び右端下部に
は、夫々ピツチの入口12、出口13が設けられ
ている。前記本体11の外周には、楕円筒体状の
ジヤケツト14が配設されており、該ジヤケツト
14の左端上部及び右端下部には夫々熱媒体の入
口15、出口16が設けられている。前記本体1
1の長さ方向には、同一速度で回転する複数、例
えば2本の回転軸17,18が互いに平行して貫
通されている。これら回転軸17,18は、前記
本体11の両側壁に配設された軸受19〜22に
軸支されている。前記各回転軸17,18には、
複数の円板状の攪拌板23…,24…がそれらの
側面が互いに接触するように、かつ各回転軸1
7,18間において面方向で合致するように軸着
されている。前記各回転軸17,18に軸着され
る攪拌板23…,24…は、第2図〜第5図に示
すように中心が前記回転軸17,18の軸心に対
して回転軸方向に螺旋状の軌跡を描くように偏心
し配置されている。具体的には、第4図及び第5
図に示すように同一回転軸(例えば17)の隣接
した攪拌板23,23間においてそれら中心A1,
A2は回転軸17の軸心Oに対して同一距離でか
つ互いに60°の周角度ずれるように偏心して配置
されている。また、前記各回転軸17,18間に
おいて面方向で合致する攪拌板23,24同志
は、第4図に示すようにそれらの中心A1,B1と
回転軸17,18の軸心O,Pとの関係におい
て、同一方向、同一距離となるように偏心される
と共に、それらの円周面が互いに接触するように
配置されている。つまり、回転軸17,18を図
示しない駆動機構により同一速度で回転させた場
合、それらの軸17,18に軸着された複数の攪
拌板23…,24…からなる攪拌板群は最外端軌
道が2つの円を連結した形状に回転し、かつ相互
に接触すると共に自動運動が妨げられないように
構成されている。 The heat treatment reactor 1 has a structure shown in FIGS. 2 to 5. That is, 11 in the figure is a cylindrical body whose cross section is equal to the outermost orbit drawn by the rotation of the stirring plate group described later arranged inside as shown in FIGS. 4 and 5, and has a shape in which two circles are connected. This is the reactor body. An inlet 12 and an outlet 13 of the pitch are provided at the upper left end and lower right end of the main body 11, respectively. An oval cylindrical jacket 14 is disposed around the outer periphery of the main body 11, and an inlet 15 and an outlet 16 for the heat medium are provided at the upper left end and lower right end of the jacket 14, respectively. The main body 1
A plurality of, for example two, rotating shafts 17 and 18 that rotate at the same speed pass through the lengthwise direction of the shaft 1 in parallel with each other. These rotating shafts 17 and 18 are supported by bearings 19 to 22 provided on both side walls of the main body 11. Each of the rotating shafts 17 and 18 includes
A plurality of disk-shaped stirring plates 23..., 24... are arranged so that their side surfaces are in contact with each other, and each rotating shaft 1
7 and 18 are pivoted so that they coincide in the plane direction. The stirring plates 23..., 24... which are pivotally attached to each of the rotating shafts 17, 18 have their centers oriented in the direction of the rotating shaft with respect to the axes of the rotating shafts 17, 18, as shown in FIGS. 2 to 5. They are arranged eccentrically so as to draw a spiral trajectory. Specifically, Figures 4 and 5
As shown in the figure, between adjacent stirring plates 23, 23 of the same rotating shaft (for example 17), their centers A 1 ,
A 2 is eccentrically arranged at the same distance from the axis O of the rotating shaft 17 and offset from each other by a circumferential angle of 60°. In addition, the stirring plates 23 and 24 that coincide with each other in the plane direction between the rotating shafts 17 and 18 have their centers A 1 and B 1 and the axes O and O of the rotating shafts 17 and 18, as shown in FIG. In relation to P, they are eccentrically arranged in the same direction and at the same distance, and are arranged so that their circumferential surfaces are in contact with each other. In other words, when the rotating shafts 17, 18 are rotated at the same speed by a drive mechanism (not shown), the stirring plate group consisting of the plurality of stirring plates 23..., 24... attached to the shafts 17, 18 is at the outermost end. The orbits rotate in the shape of two connected circles, contact each other, and are configured so that automatic movement is not hindered.
次に、上述したピツチ製造用熱処理反応器の作
用を説明する。 Next, the operation of the heat treatment reactor for pitch production described above will be explained.
まず、熱処理反応器1の反応器本体11内に入
口12より出発原料であるピツチを処定量供給す
ると共に、熱媒体入口15から所定温度の熱媒体
を供給して本体11内の温度を例えば450℃に設
定した状態で回転軸17,18を同一速度、同一
方向に回転させると、各回転軸17,18に軸支
された複数の攪拌板23…,24…の中心は回転
軸17,18方向に螺旋状の軌跡を描くように回
転軸17,18の軸心に対して偏心されているた
め、それら攪拌板23…,24…からなる攪拌板
群が断続的なスクリユーを形成し、本体11内に
供給されたピツチに強力な送り作用が生じる。こ
うした作用により、本体11内のピツチは攪拌板
23…,24…により攪拌されながらピツチ入口
12と反対側の出口13に向かつて移動され、そ
の間にピツチは熱分解、重縮合がなされ、メソフ
エーズが生成され、配管4aを通して次工程にさ
れる。 First, a predetermined amount of pitch, which is a starting material, is supplied from the inlet 12 into the reactor main body 11 of the heat treatment reactor 1, and a heat medium at a predetermined temperature is supplied from the heat medium inlet 15 to raise the temperature inside the main body 11, for example, to 450. When the rotating shafts 17 and 18 are rotated at the same speed and in the same direction with the temperature set at Since the stirring plates 23..., 24... are eccentric to the axes of the rotating shafts 17, 18 so as to draw a spiral trajectory in the direction, the stirring plates 23..., 24... form an intermittent screw, and the main body A strong feeding action occurs on the pitches fed into 11. Due to this action, the pitches in the main body 11 are moved toward the outlet 13 on the opposite side from the pitch inlet 12 while being stirred by the stirring plates 23..., 24..., during which time the pitches undergo thermal decomposition and polycondensation, and mesophase is produced. It is produced and sent to the next process through the pipe 4a.
従つて、本考案のピツチ製造用熱処理反応器に
よれば以下に示す効果を有する。 Therefore, the heat treatment reactor for pitch production of the present invention has the following effects.
熱分解、重縮合を行なう熱処理反応器1におけ
る反応器本体11内の攪拌板23…,24…から
なる攪拌板群を回転させると、攪拌板23…,2
4…間及び攪拌板23…,24…と本体11の間
では互いに接触する構造になつているため、それ
ら部材がセルフクリーニングされ、攪拌板23
…,24…表面や本体11内面に前述したコーキ
ング物が生成されるのを防止できる。その結果、
熱処理反応器1でのピツチの熱分解、重縮合反応
を迅速化でき、かつ熱効率の向上化を達成でき
る。 When the stirring plate group consisting of stirring plates 23..., 24... in the reactor main body 11 of the heat treatment reactor 1 that performs thermal decomposition and polycondensation is rotated, the stirring plates 23..., 2...
4 and between the stirring plates 23..., 24... and the main body 11, these members are self-cleaned, and the stirring plates 23..., 24... are in contact with each other.
..., 24... It is possible to prevent the above-mentioned caulking from being generated on the surface or the inner surface of the main body 11. the result,
The thermal decomposition of pitch and the polycondensation reaction in the heat treatment reactor 1 can be accelerated, and the thermal efficiency can be improved.
なお、上記実施例では熱処理反応器を構成する
回転軸を2本容器内を貫通して設けたが、3本以
上配設してもよい。 In the above embodiment, two rotating shafts constituting the heat treatment reactor were provided passing through the inside of the container, but three or more may be provided.
上記実施例では、回転軸に夫々軸着された攪拌
板を互いに接触するように配置したが、僅かな間
隙を置いて配置してもよい。 In the above embodiment, the stirring plates, which are respectively attached to the rotating shafts, are arranged so as to be in contact with each other, but they may be arranged with a slight gap between them.
上記実施例では、容器を各回転軸に軸着された
攪拌板からなる攪拌板群の回転軌道と等しい形状
としたが、該回転軌道より僅かに大きい形状にし
てもよい。 In the above embodiment, the shape of the container is equal to the rotation orbit of the stirring plate group consisting of the stirring plates mounted on each rotating shaft, but the shape may be slightly larger than the rotation orbit.
以上詳述し如く、本考案によれば軟化点が比較
的低いメソフエーズを多量に含み、高性能のピツ
チ系炭素繊維を製造できるピツチが得られること
は勿論、重縮合時のコーキングを防止できると共
に出発原料に対して高収率で前記ピツチを得るこ
とが可能なピツチ製造用熱処理反応器を提供でき
る。
As detailed above, according to the present invention, it is possible to obtain a pitch that contains a large amount of mesophase with a relatively low softening point and can produce high-performance pitch carbon fiber, as well as prevent coking during polycondensation. It is possible to provide a heat treatment reactor for producing pitches that can obtain pitches at a high yield based on starting materials.
第1図は本考案の一実施例を示すピツチ製造用
熱処理反応器の概略図、第2図は第1図の反応器
を示す部分切欠側面図、第3図は第2図の−
矢視方向の部分切欠側面図、第4図は第2図の
−線に沿う断面図、第5図は第2図の−線
に沿う断面図である。
1……熱処理反応器、11……反応器本体、1
2……ピツチ入口、13……ピツチ出口、14…
…ジヤケツト、17,18……回転軸、23,2
4……攪拌板。
Fig. 1 is a schematic diagram of a heat treatment reactor for pitch production showing an embodiment of the present invention, Fig. 2 is a partially cutaway side view showing the reactor of Fig. 1, and Fig. 3 is a diagram of the -
4 is a sectional view taken along the - line in FIG. 2, and FIG. 5 is a sectional view taken along the - line in FIG. 2. 1... Heat treatment reactor, 11... Reactor main body, 1
2... Pituchi entrance, 13... Pituchi exit, 14...
... Jacket, 17, 18 ... Rotating shaft, 23, 2
4... Stirring plate.
Claims (1)
互いに平行して配設された同一速度で回転する複
数の回転軸と、これら回転軸に側面が互いに密接
するように軸着され、かつ各回転軸間において面
方向で互いに合致するように配置された複数の攪
拌板とから構成され、前記各回転軸に軸着される
複数の攪拌板はその中心が回転軸の軸心に対し回
転軸方向に螺旋状の軌跡を描くように偏心して配
置され、かつ面方向で互いに合致する攪拌板同志
はそれらの中心が回転軸の軸心に対し同一方向、
同一距離となるよう偏心されると共に周面が互い
に僅かな間隙をおくかもしくは接触して配置さ
れ、更に前記反応器本体はその内部に配置される
攪拌板群の回転により描かれる最外端軌道に等し
いかもしくは僅かに大きい断面形状を有すること
を特徴とするピツチ製造用熱処理反応器。 a horizontally placed reactor body; a plurality of rotating shafts arranged parallel to each other in the length direction of the main body and rotating at the same speed; and the rotating shafts are pivoted to the rotating shafts so that the side surfaces thereof are in close contact with each other, and a plurality of stirring plates arranged so as to coincide with each other in the plane direction between the respective rotating shafts, and the plurality of stirring plates pivotally attached to the respective rotating shafts have their centers relative to the axis of the rotating shafts. Stirring plates that are arranged eccentrically so as to draw a spiral trajectory in the direction of the rotation axis and coincide with each other in the plane direction have their centers oriented in the same direction with respect to the axis of the rotation axis.
The reactor body is eccentrically spaced at the same distance, and its peripheral surfaces are arranged with a slight gap or in contact with each other, and the reactor body has an outermost trajectory drawn by the rotation of a group of stirring plates disposed inside the reactor body. 1. A heat treatment reactor for pitch production, characterized in that it has a cross-sectional shape equal to or slightly larger than .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1986012614U JPH0420495Y2 (en) | 1986-01-31 | 1986-01-31 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1986012614U JPH0420495Y2 (en) | 1986-01-31 | 1986-01-31 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62126238U JPS62126238U (en) | 1987-08-11 |
| JPH0420495Y2 true JPH0420495Y2 (en) | 1992-05-11 |
Family
ID=30800907
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1986012614U Expired JPH0420495Y2 (en) | 1986-01-31 | 1986-01-31 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0420495Y2 (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60189323U (en) * | 1984-05-29 | 1985-12-14 | 三菱重工業株式会社 | Stirring mixer |
| JPS60189322U (en) * | 1984-05-29 | 1985-12-14 | 三菱重工業株式会社 | Stirring mixer |
-
1986
- 1986-01-31 JP JP1986012614U patent/JPH0420495Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62126238U (en) | 1987-08-11 |
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