JPH02115295A - Reactor - Google Patents
ReactorInfo
- Publication number
- JPH02115295A JPH02115295A JP63268786A JP26878688A JPH02115295A JP H02115295 A JPH02115295 A JP H02115295A JP 63268786 A JP63268786 A JP 63268786A JP 26878688 A JP26878688 A JP 26878688A JP H02115295 A JPH02115295 A JP H02115295A
- Authority
- JP
- Japan
- Prior art keywords
- shaft
- impeller
- fluid
- openings
- heavy oil
- 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
Links
- 239000012530 fluid Substances 0.000 claims abstract description 31
- 238000004891 communication Methods 0.000 claims abstract description 7
- 238000006243 chemical reaction Methods 0.000 claims description 29
- 239000002994 raw material Substances 0.000 claims description 28
- 239000000463 material Substances 0.000 abstract 4
- 239000000376 reactant Substances 0.000 abstract 3
- 239000000295 fuel oil Substances 0.000 description 24
- 238000007664 blowing Methods 0.000 description 10
- 238000003756 stirring Methods 0.000 description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- 229910001873 dinitrogen Inorganic materials 0.000 description 5
- 238000012856 packing Methods 0.000 description 5
- 238000004821 distillation Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000011295 pitch Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 210000004907 gland Anatomy 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- -1 polycyclic aromatic compound Chemical class 0.000 description 3
- 239000010426 asphalt Substances 0.000 description 2
- 238000006068 polycondensation reaction Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000006482 condensation reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/712—Feed mechanisms for feeding fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71805—Feed mechanisms characterised by the means for feeding the components to the mixer using valves, gates, orifices or openings
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00054—Controlling or regulating the heat exchange system
- B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
- B01J2219/00058—Temperature measurement
- B01J2219/00063—Temperature measurement of the reactants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/18—Details relating to the spatial orientation of the reactor
- B01J2219/185—Details relating to the spatial orientation of the reactor vertical
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Working-Up Tar And Pitch (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の目的〕
(産業上の利用分野)
本発明は重質油等の原料を攪拌して反応させる反応装置
に係り、とりわけ反応流体を吹込みながら攪拌する反応
装置に関する。[Detailed Description of the Invention] [Object of the Invention] (Industrial Field of Application) The present invention relates to a reaction device for stirring and reacting raw materials such as heavy oil, and particularly to a reaction device for stirring while blowing a reaction fluid. Regarding.
(従来の技術)
従来、原料を攪拌して反応させる反応装置として、内部
に原料を収納した密閉容器と、この密閉容器に取付けら
れた回転翼とを備えたものが知られている。(Prior Art) Conventionally, as a reaction apparatus for stirring and reacting raw materials, there has been known a reaction apparatus that includes a closed container in which the raw materials are stored and a rotary blade attached to the closed container.
また密閉容器には、流体吹込装置、例えば空気吹込装置
が設けられ、回転翼による原料の攪拌中吉閉容器内の原
料に空気を吹込むようになっている。Further, the closed container is provided with a fluid blowing device, for example, an air blowing device, which blows air into the raw material in the closed container while the raw material is being stirred by a rotary blade.
攪拌中、重質油等の原料に空気を吹込むことにより、重
質油等を酸化することができ、これによって低揮発分を
留出するとともに、熱重縮合に加えて脱水素縮合、酸素
付加縮合反応を促進して高分子化を達成することができ
る。By blowing air into raw materials such as heavy oil during stirring, it is possible to oxidize the heavy oil, thereby distilling low volatile components, and in addition to thermal polycondensation, dehydrogenation condensation and oxygen Polymerization can be achieved by promoting addition condensation reactions.
このように攪拌中の重油中に空気を吹込む反応装置は、
重質油からの舗装用アスファルトの製造、メソフェース
小球体を含む品質ピッチの等方性の調整、ピッチ類の性
状調整(軟化点、粘度等の向上)、等方性炭素原料に向
いたモザイクコークス製造の前処理等に用いることがで
き、工業的応用範囲も広くなっている。A reactor that blows air into heavy oil while stirring is
Manufacture of paving asphalt from heavy oil, adjustment of isotropy of quality pitch including mesoface small spheres, adjustment of properties of pitches (improvement of softening point, viscosity, etc.), mosaic coke suitable for isotropic carbon raw materials It can be used for pre-treatment during manufacturing, and the range of industrial applications is widening.
なお、密閉容器に窒素ガス吹込装置を設け、密閉容器内
の原料に窒素ガスを吹込む反応装置も知られている。こ
の場合、重質油等の原料に窒素ガスを吹込むことにより
、重質油をビスブレーキングすることができる。Note that there is also known a reaction apparatus in which a nitrogen gas blowing device is provided in a closed container and nitrogen gas is blown into the raw material in the closed container. In this case, heavy oil can be visbroken by blowing nitrogen gas into the raw material such as heavy oil.
また熱分解重縮合反応を進めて多環芳香族化合物へ濃縮
するようなピッチ化工程においては、不均一反応を抑制
するため密閉容器内を同時に攪拌する必要がある。この
ようなピッチ化工程にも、窒素ガス吹込装置を有する反
応装置を用いることができる。In addition, in the pitch formation process in which the pyrolysis polycondensation reaction is advanced and concentrated into a polycyclic aromatic compound, it is necessary to simultaneously stir the inside of the closed container in order to suppress heterogeneous reactions. A reaction apparatus having a nitrogen gas blowing device can also be used in such a pitch forming step.
(発明が解決しようとする課題)
上述のような反応装置において、一般に空気吹込装置等
の流体吹込装置は回転翼と別個独立に設けられている。(Problems to be Solved by the Invention) In the reaction apparatus as described above, a fluid blowing device such as an air blowing device is generally provided separately and independently from the rotary blade.
このため原料を回転翼によって十分攪拌しても、反応流
体(例えば空気)と原料(例えば重質油)との間で気液
が均一に接触できないという問題が生じている。For this reason, even if the raw material is sufficiently stirred by the rotary blade, a problem arises in that gas-liquid cannot come into uniform contact between the reaction fluid (for example, air) and the raw material (for example, heavy oil).
このような問題を解決するため、密閉容器内に大量の反
応流体を吹込むことも考えられるが、この場合は密閉容
器内において原料の反応温度が低下したり不均一な温度
分布が生じたりしてしまう。In order to solve this problem, it is possible to inject a large amount of reaction fluid into the closed container, but in this case, the reaction temperature of the raw materials may drop or uneven temperature distribution may occur within the closed container. It ends up.
本発明はこのような点を考慮してなされたものであり、
適切な吹込量の反応流体を原料に効率よく均一に接触さ
せることができる反応装置を提供することを目的とする
。The present invention has been made in consideration of these points,
It is an object of the present invention to provide a reaction device that can efficiently and uniformly contact raw materials with an appropriate amount of blown reaction fluid.
(課題を解決するための手段)
本発明は、内部に原料を収納した密閉容器と、この密閉
容器に取付けられた回転翼とを備え、前記回転翼は前記
密閉容器の内部から外部へ延びるシャフトと、このシャ
フトの外周に固着され前記原料を攪拌するインペラとか
らなり、前記シャフトの内部に軸方向に延びる流路を形
成するとともに、前記シャフトの前記密閉容器の外部に
位置する箇所に前記流路内に反応流体を導入する流体導
入ユニオンを設け、前記インペラの外面に複数の開口を
設けるとともに、この開口と前記流路とを連通路で連通
したことを特徴とする反応装置である。(Means for Solving the Problems) The present invention includes a sealed container that stores raw materials therein, and a rotary blade attached to the sealed container, and the rotary blade has a shaft extending from the inside of the sealed container to the outside. and an impeller fixed to the outer periphery of the shaft to agitate the raw material, forming a flow path extending in the axial direction inside the shaft, and directing the flow to a portion of the shaft located outside the airtight container. The reaction device is characterized in that a fluid introduction union for introducing a reaction fluid into the channel is provided, a plurality of openings are provided on the outer surface of the impeller, and the openings and the flow channel are communicated with each other through a communication channel.
(作 用)
回転翼による攪拌中、流入導入ユニオンから反応流体を
流路に流入させ、その後流路内の反応流体を、連通路お
よびインペラの開口を経て原料内に放出させ、原料と反
応流体とを反応させる。(Function) During stirring by the rotary blade, the reaction fluid flows into the flow path from the inflow introduction union, and then the reaction fluid in the flow path is discharged into the raw material through the communication path and the opening of the impeller, and the raw material and the reaction fluid are react with.
(実施例)
以下、図面を参照して本発明の実施例について説明する
。(Example) Hereinafter, an example of the present invention will be described with reference to the drawings.
第1図乃至第3図は本発明による反応装置の一実施例を
示す図である。1 to 3 are diagrams showing one embodiment of a reaction apparatus according to the present invention.
このうち第3図は全体の概略系統図である。第3図に示
すように反応装置10は内部に原料、例えば重質油19
を収納した密閉容器11と、密閉容器11に取付けられ
た回転翼12とを備えている。このうち、回転g12は
密閉容器11の内部から外部へ延びるシャフト13と、
シャフトの外周に固着され重質油19を攪拌する主イン
ペラ14および副インペラ15とからなっている。この
うち主インペラ14はシャフト13の下端部に配設され
、副インペラ15は主インペラ14の上方に配設されて
いる。Of these, FIG. 3 is a schematic diagram of the entire system. As shown in FIG. 3, the reactor 10 contains a raw material, for example, heavy oil 19.
It is equipped with an airtight container 11 containing the airtight container 11, and a rotor blade 12 attached to the airtight container 11. Of these, the rotation g12 is caused by the shaft 13 extending from the inside of the closed container 11 to the outside;
It consists of a main impeller 14 and a sub-impeller 15 which are fixed to the outer periphery of the shaft and stir heavy oil 19. Among these, the main impeller 14 is arranged at the lower end of the shaft 13, and the sub-impeller 15 is arranged above the main impeller 14.
またシャフト13は、密閉容器11の外方に設けられた
モータ25およびギアボックス26によって駆動される
ようになっており、シャフト13の上端部には流体導入
ユニオン28が設けられている。Further, the shaft 13 is driven by a motor 25 and a gear box 26 provided outside the closed container 11, and a fluid introduction union 28 is provided at the upper end of the shaft 13.
また密閉容器11の側方には、重質油19を加熱するた
めのヒータ17が配設され、また密閉容器11の内部に
は保護管18a内に収納された熱電対18が温度測定を
行なうため設けられている。Further, a heater 17 for heating heavy oil 19 is arranged on the side of the closed container 11, and a thermocouple 18 housed in a protective tube 18a inside the closed container 11 measures the temperature. It is provided for this purpose.
さらに密閉容器11の上方蓋11aには、原料が反応し
た場合の生成物を受容器36に導く留出管35が接続さ
れ、また受容器36にはガス放出管37が取付けられて
いる。Further, a distillation pipe 35 is connected to the upper lid 11a of the closed container 11, and a distillation pipe 35 is connected to guide a product produced when the raw materials react to a receiver 36, and a gas discharge pipe 37 is attached to the receiver 36.
この留出管35および受容器36は、必要に応じて保温
または冷却手段が適宜用いられるようになっている(図
示せず)。The distillation pipe 35 and the receiver 36 are provided with heat insulating or cooling means (not shown) as appropriate.
次に、第1図および第2図により反応装置10について
詳述する。Next, the reactor 10 will be described in detail with reference to FIGS. 1 and 2.
シャフト13内には軸方向に延びる流路29が形成され
、シャフト13の上端部には反応流体、例えば空気を流
路29内に導入する流体導入ユニオン28が設けられて
いる。A channel 29 extending in the axial direction is formed in the shaft 13, and a fluid introduction union 28 for introducing a reaction fluid, for example, air into the channel 29, is provided at the upper end of the shaft 13.
流体導入ユニオン28には、流入管28aが設けられ、
この流体導入ユニオン28は全体として回転することな
く固定されている。The fluid introduction union 28 is provided with an inflow pipe 28a,
The fluid introduction union 28 is fixed as a whole without rotating.
またシャフト13の上方部にはベアリング27が設けら
れ、このベアリング27を境として、ベアリング27よ
り上方のシャフト13は固定されベアリング27より下
方のシャフト13は回動自在となっている。さらにシャ
フト13は密閉容器11の上方蓋11aを貫通して内部
から外部へ延び、このシャフトの貫通部はグランドパツ
キン22によって密閉されている。すなわち、グランド
パツキン22は、シャフト13の外周と上方蓋11a上
面に固着されたパツキン台21との間に配設され、この
グランドパツキン22はパツキン押え23によって保持
されている。A bearing 27 is provided above the shaft 13, and the shaft 13 above the bearing 27 is fixed, and the shaft 13 below the bearing 27 is rotatable. Further, the shaft 13 passes through the upper lid 11a of the closed container 11 and extends from the inside to the outside, and the penetrating portion of this shaft is sealed by a gland packing 22. That is, the gland packing 22 is disposed between the outer periphery of the shaft 13 and a packing stand 21 fixed to the upper surface of the upper lid 11a, and the gland packing 22 is held by a packing presser 23.
また、モータ25の出力軸には傘歯車25aが固着され
、この傘歯車25aはギアボックス26内でシャフト1
3の外周に設けられた傘歯車26aと係合している。こ
のうち、傘歯車26aはシャフト13に対して軸方向に
摺動自在となっており、このため重質油19の液位に応
じてシャフト13を上下方向にスライドさせた場合でも
、モータ25からの駆動力を傘歯車25g、26aを介
してシャフト13に伝達できるようになっている。Further, a bevel gear 25a is fixed to the output shaft of the motor 25, and this bevel gear 25a is attached to the shaft 1 within the gear box 26.
It engages with a bevel gear 26a provided on the outer periphery of No.3. Of these, the bevel gear 26a is slidable in the axial direction with respect to the shaft 13, so even when the shaft 13 is slid in the vertical direction according to the liquid level of the heavy oil 19, the motor 25 is not moved. The driving force can be transmitted to the shaft 13 via the bevel gears 25g and 26a.
さらにシャフト13は、反応終了後主インペラ14が液
位より上になるように引き上げることができる。Further, the shaft 13 can be raised so that the main impeller 14 is above the liquid level after the reaction is completed.
また、第2図に示すように、シャフト13の下端部に配
設された主インペラ14の外面には、複数の開口30が
設けられ、この複数の開口30とシャフト13内の流路
29とは連通路31で連通されている。Further, as shown in FIG. 2, a plurality of openings 30 are provided on the outer surface of the main impeller 14 disposed at the lower end of the shaft 13, and the plurality of openings 30 and the flow path 29 in the shaft 13 are connected to each other. are communicated through a communication path 31.
次にこのような構成からなる本実施例の作用について説
明する。Next, the operation of this embodiment having such a configuration will be explained.
まず密閉容器11内に重質油19を収納しておき、モー
タ25を回転させる。この場合、モータ25の駆動力は
傘歯車25aおよび傘歯車26aを経てシャフト13に
伝送され、シャフト13が回動する。このようなシャフ
ト13の回動により、主インペラ14および副インペラ
15が重質油19を攪拌する。First, heavy oil 19 is stored in the closed container 11, and the motor 25 is rotated. In this case, the driving force of the motor 25 is transmitted to the shaft 13 via the bevel gear 25a and the bevel gear 26a, and the shaft 13 rotates. Due to such rotation of the shaft 13, the main impeller 14 and the sub-impeller 15 agitate the heavy oil 19.
重質油19の攪拌中、流入管28aから流体導入ユニオ
ン28に流入した空気は、その後シャフト13内の流路
29内に流入する。続いて流路29内に流入した空気は
流路29に沿って下方に流れ、連通路31を経て主イン
ペラ14の開口30から重質油19内に放出される。While the heavy oil 19 is being stirred, air that has flowed into the fluid introduction union 28 from the inflow pipe 28a then flows into the flow path 29 within the shaft 13. Subsequently, the air flowing into the flow path 29 flows downward along the flow path 29, passes through the communication path 31, and is discharged into the heavy oil 19 from the opening 30 of the main impeller 14.
このように重質油19内に空気を吹込むことによって、
重質油19を酸化することができる。このように酸化さ
れた重質油は、以後例えば舗装用アスファルトの製造等
に用いられる。その後密閉容器11内の反応生成物は留
出管35を経て受容器36に導かれ、受容器36内のガ
スはガス放出管37から外部へ放出される。By blowing air into the heavy oil 19 in this way,
Heavy oil 19 can be oxidized. The heavy oil oxidized in this way is subsequently used, for example, in the production of asphalt for paving. Thereafter, the reaction product in the closed container 11 is led to the receiver 36 through the distillation pipe 35, and the gas in the receiver 36 is released to the outside from the gas release pipe 37.
以上説明したように、本実施例によれば、重質油19を
攪拌する主インペラ14の開口30から重質油19中に
空気を放出することができるので、空気と重質油19と
の接触を均一かつ確実に行なうことができる。このため
、重質油19内に大ユの空気を吹込む必要はなく、効率
よく短時間で重質油19と空気とを反応させることがで
きる。As explained above, according to this embodiment, air can be released into the heavy oil 19 from the opening 30 of the main impeller 14 that stirs the heavy oil 19, so that the air and the heavy oil 19 can be mixed. Contact can be made evenly and reliably. Therefore, there is no need to blow a large amount of air into the heavy oil 19, and the heavy oil 19 and air can be reacted efficiently and in a short time.
なお、上記実施例において、主インペラ14に開口30
を設けた例を示したが、これに限らず副インペラ15に
流路29と連通する開口を設けてもよい。また流体導入
ユニオン28から流路29内に導入される反応流体は空
気に限らず窒素ガス等であってもよく、さらに気体に限
らず原料と反応する液体であってもよ゛い。In addition, in the above embodiment, the main impeller 14 has an opening 30.
Although an example in which the impeller 15 is provided is shown, the present invention is not limited to this, and the sub impeller 15 may be provided with an opening that communicates with the flow path 29. Further, the reaction fluid introduced into the channel 29 from the fluid introduction union 28 is not limited to air, but may be nitrogen gas or the like, and is not limited to gas, but may also be a liquid that reacts with the raw material.
以上説明したように、本発明によれば原料を攪拌するイ
ンペラの開口から原料中に反応流体を放出させることが
できるので、反応流体と原料との接触を均一かつ確実に
行なうことができる。このため、原料中に大量に反応流
体を吹込む必要はなく、効率よく短時間で反応流体と原
料とを反応させることができる。As explained above, according to the present invention, the reaction fluid can be discharged into the raw material from the opening of the impeller that stirs the raw material, so that the reaction fluid and the raw material can be uniformly and reliably contacted. Therefore, there is no need to blow a large amount of the reaction fluid into the raw material, and the reaction fluid and the raw material can be reacted efficiently and in a short time.
第1図は本発明による反応装置の一実施例を示す側断面
図であり、第2図は本発明による反応装置の主インペラ
部を示す詳細図、第3図は本発明による反応装置と受容
器を示す概略系統図である。
10・・・反応装置、11・・・密閉容器、12・・・
回転翼、13・・・シャフト、14・・・主インペラ、
15・・・副インペラ、1つ・・・原料、28・・・流
体導入ユニオン、29・・・流路、30・・・開口、3
1・・・連通路。
出願人代理人 佐 藤 −雄FIG. 1 is a side cross-sectional view showing one embodiment of the reactor according to the present invention, FIG. 2 is a detailed view showing the main impeller portion of the reactor according to the present invention, and FIG. It is a schematic system diagram showing a container. 10... Reactor, 11... Sealed container, 12...
Rotating blade, 13... shaft, 14... main impeller,
15... Sub-impeller, 1... Raw material, 28... Fluid introduction union, 29... Channel, 30... Opening, 3
1...Communication path. Applicant's agent Mr. Sato
Claims (1)
けられた回転翼とを備え、前記回転翼は前記密閉容器の
内部から外部へ延びるシャフトと、このシャフトの外周
に固着され前記原料を攪拌するインペラとからなり、前
記シャフトの内部に軸方向に延びる流路を形成するとと
もに、前記シャフトの前記密閉容器の外部に位置する箇
所に前記流路内に反応流体を導入する流体導入ユニオン
を設け、前記インペラの外面に複数の開口を設けるとと
もに、この開口と前記流路とを連通路で連通したことを
特徴とする反応装置。It includes a sealed container that stores raw materials therein, and a rotary blade attached to the sealed container, and the rotary blade has a shaft extending from the inside of the sealed container to the outside, and is fixed to the outer periphery of the shaft to agitate the raw material. an impeller that forms a flow path extending in the axial direction inside the shaft, and a fluid introduction union that introduces the reaction fluid into the flow path at a location of the shaft located outside the closed container. . A reaction device, characterized in that a plurality of openings are provided on the outer surface of the impeller, and the openings and the flow path are communicated with each other through a communication path.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63268786A JPH02115295A (en) | 1988-10-25 | 1988-10-25 | Reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63268786A JPH02115295A (en) | 1988-10-25 | 1988-10-25 | Reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02115295A true JPH02115295A (en) | 1990-04-27 |
Family
ID=17463259
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63268786A Pending JPH02115295A (en) | 1988-10-25 | 1988-10-25 | Reactor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02115295A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0633060A1 (en) * | 1993-07-08 | 1995-01-11 | Biazzi Sa | Apparatus for gas-liquid reactions |
JP2013516504A (en) * | 2009-12-31 | 2013-05-13 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | Multipurpose reactor and process for producing modified bitumen |
JP2014113564A (en) * | 2012-12-11 | 2014-06-26 | Sumitomo Metal Mining Co Ltd | Stirring reactor |
-
1988
- 1988-10-25 JP JP63268786A patent/JPH02115295A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0633060A1 (en) * | 1993-07-08 | 1995-01-11 | Biazzi Sa | Apparatus for gas-liquid reactions |
US5478535A (en) * | 1993-07-08 | 1995-12-26 | Biazzi Sa | Apparatus for gas - liquid reactions |
JP2013516504A (en) * | 2009-12-31 | 2013-05-13 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | Multipurpose reactor and process for producing modified bitumen |
US9200205B2 (en) | 2009-12-31 | 2015-12-01 | Shell Oil Company | Multi-purpose reactor and process for the preparation of modified bitumen |
US10260003B2 (en) | 2009-12-31 | 2019-04-16 | Shell Oil Company | Multi-purpose reactor and process for the preparation of modified bitumen |
JP2014113564A (en) * | 2012-12-11 | 2014-06-26 | Sumitomo Metal Mining Co Ltd | Stirring reactor |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4915509A (en) | Mixer for mixing at least two free-flowing substances, especially those which react during mixing | |
US4007016A (en) | Continuous-flow reactor for high viscosity materials | |
US3220804A (en) | Apparatus for the continuous manufacture of polycondensation products | |
US3499873A (en) | Preparation of polyethylene terephthalate by means of free falling films | |
JPH02115295A (en) | Reactor | |
US3528782A (en) | Polycondensation reactor | |
US3279892A (en) | Rotary chemical reaction furnace for flowable substances | |
US1947852A (en) | Method of conducting caustic alkali fusions | |
CN1030899C (en) | Process and apparatus for dissolving organic product with microwave | |
CN212328297U (en) | Catalytic reaction device for preparing polyurethane adhesive | |
CN208661087U (en) | A kind of microchannel plate should synthesize the device of GMA acrylic resin | |
JPS6257636A (en) | Reaction apparatus for high-viscosity liquid | |
CN113509857A (en) | Production device of multifunctional molecular composite terminator | |
CN105688788A (en) | Reaction kettle for chemical industry workshop | |
US3357798A (en) | Centrifugal apparatus for obtaining chemical reactions | |
KR101340712B1 (en) | Mix apparatus including draft tube | |
CN218167031U (en) | Controllable reation kettle of temperature | |
CN206285893U (en) | A kind of reactor | |
SU1627243A1 (en) | Apparatus for polymerization | |
KR100961767B1 (en) | Spinning disc reactor | |
US2353237A (en) | Method for carrying out fusion reactions | |
CN104370288B (en) | Reactor | |
CN217614411U (en) | Lubricating oil mediation is with stirring reation kettle | |
CN216856363U (en) | High-efficiency fixed hopper mixer | |
SU997777A1 (en) | Planetary mixer |