JP5773683B2 - Vibration agitator - Google Patents

Vibration agitator Download PDF

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JP5773683B2
JP5773683B2 JP2011039989A JP2011039989A JP5773683B2 JP 5773683 B2 JP5773683 B2 JP 5773683B2 JP 2011039989 A JP2011039989 A JP 2011039989A JP 2011039989 A JP2011039989 A JP 2011039989A JP 5773683 B2 JP5773683 B2 JP 5773683B2
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conduit
spiral blade
stirring
vibration
spiral
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JP2012176349A (en
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谷口 徹
徹 谷口
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冷化工業株式会社
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Description

本発明は、振動撹拌装置に係り、特に、液体又は粉体を均一に撹拌混合する、或いは均一な重合反応を促進する振動撹拌装置に関する。   The present invention relates to a vibration stirrer, and more particularly to a vibration stirrer that uniformly stirs and mixes liquids or powders or promotes a uniform polymerization reaction.

粉体に液体を添加して混合する場合、液体に粉体を添加して混合する場合、又は粉体と液体とを同時に添加して混合する場合において、液体中に粉体の二次凝集粒を発生させないように液体中に粉体を分散させる技術が考案されている。また、液体の重合反応を促進させて均一な重合物を製造する技術が考案されている。   When adding and mixing liquid to powder, when adding and mixing powder to liquid, or when adding and mixing powder and liquid simultaneously, secondary agglomerates of powder in the liquid A technique has been devised in which powder is dispersed in a liquid so as to prevent generation of water. In addition, a technique for producing a uniform polymer by promoting a liquid polymerization reaction has been devised.

特許文献1には、撹拌混合装置及び撹拌混合方法が開示されている。ここでは、内部に流体が流通するケーシングの内部に設けられた流通路の仕切り板に1つ以上の孔が設けられることが記載されている(図7、図8参照)。この孔により仕切り板間に形成される撹拌室内の撹拌度合を他の撹拌室と異ならせることができる。さらに、撹拌羽根にも1つ以上の孔が設けられることが記載されている。この孔により、撹拌羽根において孔の形成された部分の振動可能範囲に位置する撹拌室内の撹拌度合を他の撹拌室と異ならせることができる。   Patent Document 1 discloses a stirring and mixing device and a stirring and mixing method. Here, it is described that one or more holes are provided in a partition plate of a flow passage provided inside a casing through which a fluid flows (see FIGS. 7 and 8). With this hole, the degree of stirring in the stirring chamber formed between the partition plates can be made different from that of other stirring chambers. Furthermore, it is described that the stirring blade is provided with one or more holes. By this hole, the stirring degree in the stirring chamber located in the vibration possible range of the portion where the hole is formed in the stirring blade can be made different from other stirring chambers.

特許文献2には、分子量分布の狭い、または低分子量の重合物を効率よく製造することが可能な撹拌重合装置及び重合方法が開示されている。ここでは、導管を多段に仕切る仕切り板に流体を流通させる流通孔が形成されている。そして、導管内に撹拌体を所定のモードで細動させ、撹拌羽根による流体の流れの分散合流の繰り返しと、撹拌羽根の細動による流体の振動により重合溶液を撹拌し、重合反応を促進させることが記載されている。   Patent Document 2 discloses a stirring polymerization apparatus and a polymerization method capable of efficiently producing a polymer having a narrow molecular weight distribution or a low molecular weight. Here, a flow hole through which a fluid flows is formed in a partition plate that partitions the conduit in multiple stages. Then, the stirring body is fibrillated in a predetermined mode in the conduit, and the polymerization solution is stirred by repeating the dispersion and merging of the fluid flow by the stirring blades and the vibration of the fluid by the fibrillation of the stirring blades, thereby promoting the polymerization reaction. It is described.

特許第4366124号公報Japanese Patent No. 4366124 特許第4278245号公報Japanese Patent No. 4278245

しかしながら、従来の振動撹拌装置及び撹拌混合方法では、液体又は粉体、或いは重合溶液を均一に撹拌混合する能力が十分ではなく、所望の撹拌混合効果が得られないか、或いは撹拌時間がかかり過ぎ不経済であるという問題があった。   However, the conventional vibration stirring device and the stirring and mixing method do not have sufficient ability to uniformly stir and mix the liquid, powder, or polymerization solution, and the desired stirring and mixing effect cannot be obtained or the stirring time is too long. There was a problem of being uneconomical.

また、上記撹拌混合能力の限界により、混合可能な粉体と液体との組み合わせ、或いは重合溶液の種類が限定されるという問題があった。また、上記撹拌混合能力を向上させ、撹拌混合或いは撹拌重合に要する時間を短縮するという要求があった。   Moreover, there existed a problem that the combination of the powder and liquid which can be mixed, or the kind of polymerization solution was limited by the limit of the said stirring and mixing ability. Further, there has been a demand for improving the stirring and mixing ability and shortening the time required for stirring and mixing or stirring polymerization.

本願の目的は、かかる課題を解決し、撹拌体の振動により内部の液体又は粉体、或いは重合溶液に渦流或いは乱流を発生させ、撹拌効率の高い撹拌混合或いは撹拌重合を可能とする振動撹拌装置を提供することである。   The purpose of the present application is to solve this problem and generate vortex or turbulence in the internal liquid or powder or polymerization solution by vibration of the stirrer, which enables stirring mixing or stirring polymerization with high stirring efficiency. Is to provide a device.

上記目的を達成するため、本発明に係る振動撹拌装置は、撹拌される液体又は粉体、或いは溶液の流入口と流出口とを有し、内部に液体又は粉体、或いは溶液を流通させる円筒状の壁部と、壁部に螺旋状に固定されて内部に向かって突出する第1の螺旋羽根と、からなる導管と、導管内に設けられ、導管の軸方向に振動可能に支持された軸部と、軸部に螺旋状に固定されて外部に向かって突出する第2の螺旋羽根と、からなる撹拌体と、撹拌体の一端に連結されて撹拌体を軸方向に振動させる撹拌体振動源と、を備え、第1の螺旋羽根及び第2の螺旋羽根は、一定の間隔を保ちながら同じ螺旋を描くように連続し、導管の径方向に沿って二重螺旋を形成し、第1の螺旋羽根の内端部には、液体又は粉体、或いは溶液が流通可能な開口部又は切込み部が設けられ、第2の螺旋羽根の外端部には、液体又は粉体、或いは溶液が流通可能な開口部又は切込み部が設けられ、第1の螺旋羽根の開口部又は切込み部と、第2の螺旋羽根の開口部又は切込み部とは重ね合わされて設置されないことを特徴とする。 In order to achieve the above object, a vibration stirring apparatus according to the present invention has a liquid or powder to be stirred or a solution inlet and outlet and a cylinder through which the liquid or powder or solution flows. And a first spiral blade that is fixed to the wall in a spiral shape and protrudes toward the inside, and is provided in the conduit and supported so as to vibrate in the axial direction of the conduit. A stirring body comprising a shaft portion, a second spiral blade fixed to the shaft portion in a spiral shape and protruding outward, and a stirring body coupled to one end of the stirring body to vibrate the stirring body in the axial direction The first spiral blade and the second spiral blade are continuous so as to draw the same spiral while maintaining a constant interval, and form a double spiral along the radial direction of the conduit. At the inner end of one spiral blade, there is an opening or a cutout through which liquid, powder, or solution can flow. An opening or notch through which the liquid or powder or solution can flow is provided at the outer end of the second spiral blade, and the opening or notch of the first spiral blade The second spiral blade has an opening portion or a cut portion that is not overlapped and installed.

上記構成により、振動撹拌装置は液体又は粉体、或いは溶液が流通する導管内部に第1の螺旋羽根と第2の螺旋羽根とが二重螺旋を形成する。すなわち、従来液体又は粉体、或いは溶液が流通する流通路を仕切っていた仕切り板を改良して螺旋状の羽根とし、撹拌羽根と二重螺旋を形成するように配置したものである。そして、第1の螺旋羽根の内端部、及び第2の螺旋羽根の外端部であって、相互に重ね合わされない位置に開口部又は切込み部が設けられる。この構成で撹拌体を振動させることで、導管内部を流通する液体又は粉体、或いは溶液は、静止した第1の螺旋羽根の開口部又は切込み部、及び振動する第2の螺旋羽根の開口部又は切込み部周辺に生じる複雑な渦流或いは乱流により撹拌効率の高い撹拌混合或いは撹拌重合が可能となる。以下、この撹拌混合或いは撹拌重合を「第1の振動モードによる撹拌方法」と称する。   With the above configuration, in the vibration agitation apparatus, the first spiral blade and the second spiral blade form a double spiral inside the conduit through which liquid, powder, or solution flows. That is, the partition plate which has conventionally partitioned the flow path through which the liquid, powder, or solution flows is improved to be a spiral blade, and arranged so as to form a stirring blade and a double spiral. And an opening part or a notch | incision part is provided in the inner edge part of a 1st spiral blade, and the outer edge part of a 2nd spiral blade, Comprising: The position which is not mutually overlaid. By vibrating the stirring body with this configuration, the liquid, powder, or solution flowing through the inside of the conduit can be the stationary first spiral blade opening or notch, and the vibrating second spiral blade opening. Alternatively, a complicated vortex or turbulent flow generated around the cut portion enables agitation mixing or agitation polymerization with high agitation efficiency. Hereinafter, this stirring mixing or stirring polymerization is referred to as “stirring method in the first vibration mode”.

また、振動撹拌装置は、軸部の一部を壁部に固定する連結部を備え、連結部により軸部の一部を壁部に固定することで、撹拌体と導管とを相互に同期して振動させることが好ましい。これにより、撹拌体と導管とが双方とも同時に振動し、導管内部を流通する液体又は粉体、或いは溶液が、共に振動する第1の螺旋羽根の開口部又は切込み部、及び第2の螺旋羽根の開口部又は切込み部周辺に生じる複雑な渦流或いは乱流により撹拌効率の高い撹拌混合或いは撹拌重合が可能となる。以下、この撹拌混合或いは撹拌重合を「第2の振動モードによる撹拌方法」と称する。   In addition, the vibration agitation device includes a connecting part that fixes a part of the shaft part to the wall part, and the stirring body and the conduit are synchronized with each other by fixing a part of the shaft part to the wall part by the connecting part. It is preferable to vibrate. Thereby, both the stirring body and the conduit vibrate at the same time, and the liquid or powder or solution flowing through the conduit vibrates together. Stirring mixing or stirring polymerization with high stirring efficiency becomes possible by the complicated vortex flow or turbulent flow generated around the opening or notch portion. Hereinafter, this stirring mixing or stirring polymerization is referred to as “stirring method in the second vibration mode”.

また、振動撹拌装置は、導管を軸方向に振動させる導管振動源をさらに備え、導管振動源を導管に連結させることで、撹拌体と導管とを相互に独立して振動させることが好ましい。これにより、撹拌体と導管とが独立して振動し、導管内部を流通する液体又は粉体、或いは溶液が、相互に異なる振動数又は振幅により振動する第1の螺旋羽根の開口部又は切込み部、及び第2の螺旋羽根の開口部又は切込み部周辺に生じる複雑な渦流或いは乱流により撹拌効率の高い撹拌混合或いは撹拌重合が可能となる。以下、この撹拌混合或いは撹拌重合を「第3の振動モードによる撹拌方法」と称する。   In addition, it is preferable that the vibration stirring device further includes a conduit vibration source that vibrates the conduit in the axial direction, and the stirrer and the conduit are vibrated independently of each other by connecting the conduit vibration source to the conduit. Thus, the opening or notch of the first spiral blade in which the stirring body and the conduit vibrate independently and the liquid, powder, or solution flowing through the conduit vibrates at different frequencies or amplitudes. , And a complicated vortex or turbulent flow generated around the opening or notch of the second spiral blade enables stirring and mixing or stirring polymerization with high stirring efficiency. Hereinafter, this stirring mixing or stirring polymerization is referred to as “stirring method in the third vibration mode”.

さらに、振動撹拌装置は、導管の壁部の外周にはジャケットが設けられ、液体又は粉体、或いは溶液を冷却又は加熱可能な流通路が形成されるか、又は第1の螺旋羽根の断面内には液体又は粉体、或いは溶液を冷却又は加熱可能な流通路が形成されることが好ましい。これにより、重合反応の重合条件に応じて適切な温度設定を行うことができる。   Further, the vibration agitator is provided with a jacket on the outer periphery of the wall of the conduit, and a flow passage capable of cooling or heating the liquid, powder, or solution is formed, or in the cross section of the first spiral blade. It is preferable that a flow path capable of cooling or heating the liquid or powder or the solution is formed. Thereby, appropriate temperature setting can be performed according to the polymerization conditions of the polymerization reaction.

以上のように、本発明に係る振動撹拌装置によれば、撹拌体の振動により内部の液体又は粉体、或いは重合溶液に渦流或いは乱流を発生させ、撹拌効率の高い撹拌混合或いは撹拌重合を可能とする振動撹拌装置を提供することができる。   As described above, according to the vibration stirring apparatus according to the present invention, vortex or turbulence is generated in the internal liquid or powder or polymerization solution by the vibration of the stirring body, and stirring mixing or stirring polymerization with high stirring efficiency is performed. It is possible to provide a vibration agitating device that enables this.

本発明に係る振動撹拌装置の1つの実施形態の概略構成を示す断面図である。It is sectional drawing which shows schematic structure of one Embodiment of the vibration stirring apparatus which concerns on this invention. 第1螺旋羽根及び第2螺旋羽根による二重螺旋の構成を示す図1のA−A断面図である。It is AA sectional drawing of FIG. 1 which shows the structure of the double helix by a 1st spiral blade and a 2nd spiral blade. 第1螺旋羽根及び第2螺旋羽根に設けられる開口部の実施例を示す詳細断面図である。It is detail sectional drawing which shows the Example of the opening part provided in a 1st spiral blade and a 2nd spiral blade. 第1螺旋羽根及び第2螺旋羽根に設けられる切込み部の実施例を示す詳細断面図である。It is detail sectional drawing which shows the Example of the notch part provided in a 1st spiral blade and a 2nd spiral blade. 導管の壁部の外周に設けられる、溶液の加熱冷却方法の一つの実施例を示す断面図である。It is sectional drawing which shows one Example of the heating-cooling method of the solution provided in the outer periphery of the wall part of a conduit | pipe. 第1螺旋羽根の断面内に設けられる、溶液の加熱冷却方法の一つの実施例を示す断面図である。It is sectional drawing which shows one Example of the heating-cooling method of the solution provided in the cross section of a 1st spiral blade.

(振動撹拌装置の構成)
以下に、図面を用いて本発明に係る振動撹拌装置の実施形態につき、詳細に説明する。図1に、本発明に係る振動撹拌装置1の1つの実施形態の概略構成を示す。振動撹拌装置1は、導管2、撹拌体3、及び撹拌体振動源4から構成される。導管2は、内部に液体又は粉体、或いは重合溶液を流通させる円筒状の壁部5、及び壁部5に螺旋状に固定されて内部に向かって突出する第1螺旋羽根6からなる。ここで、以下、導管2の内部を流通して撹拌される「液体又は粉体、或いは重合溶液」を総称して「溶液等」と称する。撹拌体3は、導管2内に設けられ、導管2の軸方向に振動可能に支持された軸部7、及び軸部5に螺旋状に固定されて外部に向かって突出する第2螺旋羽根8からなる。そして、導管2は撹拌される溶液等の流入口10と流出口11とを有する。撹拌体振動源4は、撹拌体3の一端に連結されて撹拌体3を軸方向に振動させる。ここで、軸方向とは、撹拌体3の軸部5の軸方向をいう。
(Configuration of vibration agitator)
Hereinafter, embodiments of the vibration agitator according to the present invention will be described in detail with reference to the drawings. In FIG. 1, schematic structure of one embodiment of the vibration stirring apparatus 1 which concerns on this invention is shown. The vibration stirring device 1 includes a conduit 2, a stirring body 3, and a stirring body vibration source 4. The conduit 2 includes a cylindrical wall portion 5 through which a liquid or powder or a polymerization solution flows, and a first spiral blade 6 that is fixed to the wall portion 5 in a spiral shape and protrudes toward the inside. Hereafter, “liquid or powder, or polymerization solution” that is stirred through the inside of the conduit 2 will be collectively referred to as “solution or the like”. The stirrer 3 is provided in the conduit 2, and is supported by a shaft 7 that can vibrate in the axial direction of the conduit 2, and a second spiral blade 8 that is fixed to the shaft 5 in a spiral shape and protrudes outward. Consists of. The conduit 2 has an inlet 10 and an outlet 11 for the solution to be stirred. The stirring body vibration source 4 is connected to one end of the stirring body 3 to vibrate the stirring body 3 in the axial direction. Here, the axial direction refers to the axial direction of the shaft portion 5 of the stirring body 3.

図2に、第1螺旋羽根6及び第2螺旋羽根8による二重螺旋の構成を示す。第1螺旋羽根6及び第2螺旋羽根8は、導管2の径方向に沿って二重螺旋を形成する。ここで、「導管2の径方向に沿った螺旋」とは、図1及び図4に示すように、一定の半径を有して導管2の外周上を螺旋状に連続する線と導管2の中心線とを結ぶように形成された螺旋羽根をいう。そして、第1螺旋羽根6と第2螺旋羽根8とは、一定の間隔を保ちながら、同じ螺旋を描くように連続する。すなわち、従来、溶液等が流通する流通路を仕切っていた仕切り板を改良して螺旋状の羽根とし、撹拌羽根と二重螺旋を形成するように配置したものである。   In FIG. 2, the structure of the double helix by the 1st spiral blade 6 and the 2nd spiral blade 8 is shown. The first spiral blade 6 and the second spiral blade 8 form a double helix along the radial direction of the conduit 2. Here, the “spiral along the radial direction of the conduit 2” means a line that has a constant radius and spirally continues on the outer periphery of the conduit 2 as shown in FIGS. 1 and 4. A spiral blade formed to connect the center line. And the 1st spiral blade 6 and the 2nd spiral blade 8 continue so that the same spiral may be drawn, maintaining a fixed space | interval. That is, a partition plate that has conventionally partitioned a flow passage through which a solution or the like circulates is improved to be a spiral blade, and is arranged so as to form a double spiral with a stirring blade.

図3に、第1螺旋羽根6及び第2螺旋羽根8に設けられる開口部の実施例を示す。また、図4に、第1螺旋羽根6及び第2螺旋羽根8に設けられる切込み部17,18の実施例を示す。第1螺旋羽根6の内端部には、溶液等が流通可能な第1開口部15又は切込み部17が設けられ、第2螺旋羽根8の外端部には、溶液等が流通可能な第2開口部16又は切込み部18が設けられ、第1螺旋羽根6の第1開口部15又は切込み部17と、第2螺旋羽根8の第2開口部16又は切込み部18とは重ね合わされて設置されない。   In FIG. 3, the Example of the opening part provided in the 1st spiral blade 6 and the 2nd spiral blade 8 is shown. FIG. 4 shows an embodiment of the cut portions 17 and 18 provided in the first spiral blade 6 and the second spiral blade 8. A first opening 15 or a notch 17 through which a solution or the like can flow is provided at the inner end of the first spiral blade 6, and a second or the like through which the solution or the like can flow is provided at the outer end of the second spiral blade 8. Two openings 16 or notches 18 are provided, and the first opening 15 or notches 17 of the first spiral blade 6 and the second openings 16 or notches 18 of the second spiral blade 8 are overlapped and installed. Not.

図3及び図4では、第1開口部15及び第2開口部16は、円形の穴としているが、これに限らず、例えば三角形、四角形など他の形状でも良い。また、第1開口部15及び第2開口部16はそれぞれ第1螺旋羽根6の内端部、及び第2螺旋羽根8の外端部に設けられているが、この位置に限らず、例えば、第1螺旋羽根6の外端部、及び第2螺旋羽根8の内端部に設けられても良く、第1螺旋羽根6の第1開口部15と、第2螺旋羽根8の第2開口部16とが重ね合わされて設置されないことが条件となる。   In FIGS. 3 and 4, the first opening 15 and the second opening 16 are circular holes, but are not limited thereto, and may be other shapes such as a triangle and a quadrangle. The first opening 15 and the second opening 16 are provided at the inner end of the first spiral blade 6 and the outer end of the second spiral blade 8, respectively. It may be provided at the outer end of the first spiral blade 6 and the inner end of the second spiral blade 8, and the first opening 15 of the first spiral blade 6 and the second opening of the second spiral blade 8. No. 16 is overlapped and not installed.

図3及び図4では、切込み部17及び18は、長円形の切込みとしているが、これに限らず、例えば三角形、四角形など他の切込みの形状でも良い。また、切込み部17,18はそれぞれ第1螺旋羽根6の内端部、及び第2螺旋羽根8の外端部に設けられているが、この位置に限らず、例えば、第1螺旋羽根6の外端部、及び第2螺旋羽根8の内端部に設けられても良く、第1螺旋羽根6の切込み部17と、第2螺旋羽根8の切込み部18とが重ね合わされて設置されないことが条件となる。   In FIGS. 3 and 4, the incisions 17 and 18 are oval incisions, but are not limited thereto, and may be other incisions such as a triangle and a quadrangle. In addition, the notches 17 and 18 are provided at the inner end of the first spiral blade 6 and the outer end of the second spiral blade 8, respectively. It may be provided at the outer end portion and the inner end portion of the second spiral blade 8, and the cut portion 17 of the first spiral blade 6 and the cut portion 18 of the second spiral blade 8 may not be overlapped and installed. It becomes a condition.

(撹拌混合或いは撹拌重合の振動モード)
図1及び図2を用いて撹拌混合或いは撹拌重合の3つの振動モードによる撹拌方法を説明する。第1振動モードによる撹拌方法は、導管2を固定させ、撹拌体3のみを撹拌体振動源4により振動させるモードである。これにより、図2に示す導管2の軸方向振動(Z1)が0となり、導管2が静止した状態で撹拌体3の軸方向振動(Z2)が発生する。この振動モードにより、導管2内部を流通する溶液は、静止した第1螺旋羽根6の第1開口部15又は第1切込み部17、及び振動する第2螺旋羽根8の第2開口部16又は第2切込み部18周辺に生じる複雑な渦流或いは乱流により撹拌効率の高い撹拌混合或いは撹拌重合が可能となる。すなわち、静止した第1螺旋羽根6と第2螺旋羽根8との間に挟まれた溶液は上下動する第2螺旋羽根8,8´により抑え込み又は引き伸ばしを受け、第1開口部15或いは第2開口部16を通過する。この第1開口部15と第2開口部16とは、重ね合わされた位置にない。従って、溶液は、上下動する第2螺旋羽根8,8´による抑え込み又は引き伸ばしの際に複雑な渦流或いは乱流となって撹拌混合或いは撹拌重合される。
(Vibration mode of stirring mixing or stirring polymerization)
A stirring method in three vibration modes of stirring and mixing or stirring polymerization will be described with reference to FIGS. The stirring method in the first vibration mode is a mode in which the conduit 2 is fixed and only the stirring body 3 is vibrated by the stirring body vibration source 4. Thereby, the axial vibration (Z1) of the conduit 2 shown in FIG. 2 becomes zero, and the axial vibration (Z2) of the stirring member 3 is generated in a state where the conduit 2 is stationary. In this vibration mode, the solution flowing through the inside of the conduit 2 causes the first opening 15 or the first notch 17 of the stationary first spiral blade 6 and the second opening 16 or the second notch 17 of the vibrating second spiral blade 8 to move. The complicated vortex flow or turbulent flow generated around the two cut portions 18 enables stirring mixing or stirring polymerization with high stirring efficiency. That is, the solution sandwiched between the stationary first spiral blade 6 and the second spiral blade 8 is restrained or stretched by the second spiral blades 8 and 8 'moving up and down, and the first opening 15 or the second It passes through the opening 16. The first opening 15 and the second opening 16 are not in a superimposed position. Accordingly, the solution is stirred and mixed or polymerized as a complicated vortex or turbulent flow when being restrained or stretched by the second spiral blades 8 and 8 'moving up and down.

第2振動モードによる撹拌方法は、導管2と撹拌体3とを相互に同期して振動させるモードである。すなわち、図1に示す連結部9の連結ボルト21を締結することで、軸部7が壁部5に固定され、導管2は撹拌体振動源4により振動する撹拌体3と同期して振動する。これにより、図2に示す導管2の軸方向振動(Z1)、及び軸方向振動(Z1)に同期した撹拌体3の軸方向振動(Z2)が発生する。この振動モードにより、第1螺旋羽根6の第1開口部15又は第1切込み部17、及び第2螺旋羽根8の第2開口部16又は第2切込み部18との間に挟まれた溶液は、複雑な渦流或いは乱流により撹拌効率の高い撹拌混合或いは撹拌重合が可能となる。すなわち、第1螺旋羽根6と第2螺旋羽根8との間に挟まれた溶液は上下動する第1螺旋羽根6及び第2螺旋羽根8により慣性力を受け、第1開口部15或いは第2開口部16を通過する。この第1開口部15と第2開口部16とは、重ね合わされた位置にない。従って、溶液は、上下動する第1螺旋羽根6及び第2螺旋羽根8により第1開口部15又は第2開口部16野通過の際に複雑な渦流或いは乱流となって撹拌混合或いは撹拌重合される。   The stirring method in the second vibration mode is a mode in which the conduit 2 and the stirring body 3 are vibrated in synchronization with each other. That is, by fastening the connecting bolt 21 of the connecting portion 9 shown in FIG. 1, the shaft portion 7 is fixed to the wall portion 5, and the conduit 2 vibrates in synchronism with the stirring body 3 that is vibrated by the stirring body vibration source 4. . Thereby, the axial vibration (Z1) of the conduit 2 shown in FIG. 2 and the axial vibration (Z2) of the stirring body 3 synchronized with the axial vibration (Z1) are generated. Due to this vibration mode, the solution sandwiched between the first opening 15 or the first cut portion 17 of the first spiral blade 6 and the second opening 16 or the second cut portion 18 of the second spiral blade 8 is In addition, a complicated vortex or turbulent flow enables stirring and mixing or stirring polymerization with high stirring efficiency. That is, the solution sandwiched between the first spiral blade 6 and the second spiral blade 8 is subjected to inertial force by the first spiral blade 6 and the second spiral blade 8 moving up and down, and the first opening 15 or the second spiral blade 8 is moved. It passes through the opening 16. The first opening 15 and the second opening 16 are not in a superimposed position. Therefore, the solution becomes a complicated vortex or turbulent flow when passing through the first opening 15 or the second opening 16 by the first spiral blade 6 and the second spiral blade 8 that move up and down, and stirring and mixing or stirring polymerization. Is done.

第3振動モードによる撹拌方法は、図1に示すように、導管2を軸方向に振動させる導管振動源12を導管2に連結させることで、撹拌体振動源4に接続された撹拌体3と、導管振動源12に接続された導管2とを相互に独立して振動させるモードである。これにより、図2に示す導管2の軸方向振動(Z1)、及び撹拌体3の軸方向振動(Z2)がそれぞれ独立して発生する。この振動モードにより、第1螺旋羽根6の第1開口部15又は第1切込み部17、及び第2螺旋羽根8の第2開口部16又は第2切込み部18との間に挟まれた溶液は、複雑な渦流或いは乱流により撹拌効率の高い撹拌混合或いは撹拌重合が可能となる。   As shown in FIG. 1, the stirring method in the third vibration mode includes a stirring body 3 connected to the stirring body vibration source 4 by connecting a conduit vibration source 12 that vibrates the conduit 2 in the axial direction to the conduit 2. In this mode, the conduit 2 connected to the conduit vibration source 12 is vibrated independently of each other. Thereby, the axial vibration (Z1) of the conduit 2 and the axial vibration (Z2) of the stirring body 3 shown in FIG. 2 are generated independently. Due to this vibration mode, the solution sandwiched between the first opening 15 or the first cut portion 17 of the first spiral blade 6 and the second opening 16 or the second cut portion 18 of the second spiral blade 8 is In addition, a complicated vortex or turbulent flow enables stirring and mixing or stirring polymerization with high stirring efficiency.

(撹拌混合或いは撹拌重合の加熱冷却)
図5に、導管2の壁部5の外周に設けられる加熱冷却方法の一つの実施例を示す。導管2の壁部5の外周にはジャケット13が設けられ、ジャケット13内には溶液を冷却又は加熱可能な流通路14aが形成される。そして、流通路14aを流通する流体の流体流出入口19が設けられるが、流体の流入口と流出口とをそれぞれ設けても良い。このように、ジャケット13及び溶液を冷却又は加熱可能な流通路14aを設けることで、重合反応の重合条件に応じて適切な温度設定を行うことができる。例えば、アニオン重合やカチオン重合は、連鎖反応を考慮して通常低温で行われる。一方、ラジカル重合、乳化重合などは、重合開始を促進する場合には温度を上げ、重合が進行して連鎖反応に移行した場合、及び連鎖反応を終結させる場合には、重合温度を下げる必要がある。
(Stirring mixing or heating / cooling of stirring polymerization)
FIG. 5 shows an embodiment of the heating and cooling method provided on the outer periphery of the wall portion 5 of the conduit 2. A jacket 13 is provided on the outer periphery of the wall portion 5 of the conduit 2, and a flow passage 14 a capable of cooling or heating the solution is formed in the jacket 13. And although the fluid inflow / outflow port 19 of the fluid which distribute | circulates the flow path 14a is provided, you may provide the inflow port and outflow port of a fluid, respectively. As described above, by providing the jacket 13 and the flow passage 14a capable of cooling or heating the solution, an appropriate temperature can be set according to the polymerization conditions of the polymerization reaction. For example, anionic polymerization and cationic polymerization are usually performed at a low temperature in consideration of a chain reaction. On the other hand, in the case of radical polymerization, emulsion polymerization, etc., it is necessary to increase the temperature when the initiation of polymerization is promoted, and to lower the polymerization temperature when the polymerization proceeds to the chain reaction and when the chain reaction is terminated. is there.

図6に、第1螺旋羽根6の断面内に設けられる加熱冷却方法の一つの実施例を示す。第1螺旋羽根6の断面内には液体又は粉体を冷却又は加熱可能な流通路14bが形成される。そして、流通路14bを流通する流体の流体流出入口20が設けられるが、流体の流入口と流出口とをそれぞれ設けても良い。この第1螺旋羽根6の断面内に設けられる流通路14bは、図5に示す流通路14aと比較して簡易なディテールであり、撹拌重合が行われる第1螺旋羽根6及び第2螺旋羽根8により近接している。   FIG. 6 shows one embodiment of the heating and cooling method provided in the cross section of the first spiral blade 6. In the cross section of the first spiral blade 6, a flow path 14b capable of cooling or heating the liquid or powder is formed. And although the fluid inflow / outflow port 20 of the fluid which distribute | circulates the flow path 14b is provided, you may provide the inflow port and outflow port of a fluid, respectively. The flow passage 14b provided in the cross section of the first spiral blade 6 has simple details as compared with the flow passage 14a shown in FIG. 5, and the first spiral blade 6 and the second spiral blade 8 in which agitation polymerization is performed. Is closer.

1 振動撹拌装置、2 導管、3 撹拌体、4 撹拌体振動源、5 壁部、6 第1螺旋羽根、7 軸部、8,8´ 第2螺旋羽根、9 連結部、10 流入口、11 流出口、12 導管振動源、13 ジャケット、14a,14b 流通路、15 第1開口部、16 第2開口部、17 第1切込み部、18 第2切込み部、19,20 流体流出入口、 21 連結ボルト。
DESCRIPTION OF SYMBOLS 1 Vibration stirring apparatus, 2 Conduit, 3 Stirring body, 4 Stirring body vibration source, 5 Wall part, 6 1st spiral blade, 7 Shaft part, 8,8 '2nd spiral blade, 9 Connection part, 10 Inflow port, 11 Outlet, 12 Conduit vibration source, 13 Jacket, 14a, 14b Flow path, 15 First opening, 16 Second opening, 17 First notch, 18 Second notch, 19, 20 Fluid outflow inlet, 21 Connection bolt.

Claims (4)

撹拌される液体又は粉体、或いは溶液の流入口と流出口とを有し、内部に液体又は粉体、或いは溶液を流通させる円筒状の壁部と、壁部に螺旋状に固定されて内部に向かって突出する第1の螺旋羽根と、からなる導管と、 導管内に設けられ、導管の軸方向に振動可能に支持された軸部と、軸部に螺旋状に固定されて外部に向かって突出する第2の螺旋羽根と、からなる撹拌体と、 撹拌体の一端に連結されて撹拌体を軸方向に振動させる撹拌体振動源と、を備え、 第1の螺旋羽根及び第2の螺旋羽根は、一定の間隔を保ちながら同じ螺旋を描くように連続し、導管の径方向に沿って二重螺旋を形成し、第1の螺旋羽根の内端部には、液体又は粉体、或いは溶液が流通可能な開口部又は切込み部が設けられ、第2の螺旋羽根の外端部には、液体又は粉体、或いは溶液が流通可能な開口部又は切込み部が設けられ、第1の螺旋羽根の開口部又は切込み部と、第2の螺旋羽根の開口部又は切込み部とは重ね合わされて設置されないことを特徴とする振動撹拌装置。 A cylindrical wall having a liquid or powder to be agitated and a solution inlet and outlet, and a liquid, powder, or solution flowing therethrough, and a spiral fixed to the wall. A first spiral blade projecting toward the tube, a shaft provided in the conduit and supported so as to vibrate in the axial direction of the conduit, and fixed to the shaft in a spiral manner toward the outside. A second spiral blade projecting from the first stirring blade, and a stirring body vibration source coupled to one end of the stirring body to vibrate the stirring body in the axial direction, the first spiral blade and the second spiral blade The spiral blades are continuous so as to draw the same spiral while maintaining a constant interval, forming a double spiral along the radial direction of the conduit, and at the inner end of the first spiral blade, a liquid or powder, Alternatively, an opening or a notch through which the solution can flow is provided, and a liquid is provided at the outer end of the second spiral blade. Is provided with an opening or notch through which the powder or solution can flow, and the opening or notch of the first spiral blade and the opening or notch of the second spiral blade are not overlapped and installed. A vibration agitation device characterized by that. 請求項1に記載の振動撹拌装置であって、軸部の一部を壁部に固定する連結部を備え、連結部により軸部の一部を壁部に固定することで、撹拌体と導管とを相互に同期して振動させることを特徴とする振動撹拌装置。 It is a vibration stirring apparatus of Claim 1, Comprising: It has a connection part which fixes a part of shaft part to a wall part, and a stirring body and a conduit | pipe are provided by fixing a part of shaft part to a wall part by a connection part. And a vibration agitation device characterized by being vibrated in synchronization with each other. 請求項1に記載の振動撹拌装置であって、導管を軸方向に振動させる導管振動源をさらに備え、導管振動源を導管に連結させることで、撹拌体と導管とを相互に独立して振動させることを特徴とする振動撹拌装置。 2. The vibration agitation apparatus according to claim 1, further comprising a conduit vibration source that vibrates the conduit in an axial direction, and the agitator and the conduit are vibrated independently of each other by connecting the conduit vibration source to the conduit. A vibration stirrer characterized in that 請求項1乃至3のいずれか1項に記載の振動撹拌装置であって、導管の壁部の外周にはジャケットが設けられ、液体又は粉体、或いは溶液を冷却又は加熱可能な流通路が形成されるか、又は第1の螺旋羽根の断面内には液体又は粉体、或いは溶液を冷却又は加熱可能な流通路が形成されることを特徴とする振動撹拌装置。
4. The vibration agitating device according to claim 1, wherein a jacket is provided on an outer periphery of a wall portion of the conduit to form a flow path capable of cooling or heating the liquid, the powder, or the solution. Or a flow passage capable of cooling or heating a liquid, powder, or solution in the cross section of the first spiral blade.
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