JP2007021357A - Polymer powder dissolving apparatus and manufacturing method of polymer solution - Google Patents
Polymer powder dissolving apparatus and manufacturing method of polymer solution Download PDFInfo
- Publication number
- JP2007021357A JP2007021357A JP2005206664A JP2005206664A JP2007021357A JP 2007021357 A JP2007021357 A JP 2007021357A JP 2005206664 A JP2005206664 A JP 2005206664A JP 2005206664 A JP2005206664 A JP 2005206664A JP 2007021357 A JP2007021357 A JP 2007021357A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- dissolution tank
- polymer powder
- polymer
- dissolving
- 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
Links
Landscapes
- Processing Of Solid Wastes (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Description
本発明は、高分子粉末を液体（溶媒）に溶解させる高分子粉末溶解装置、及び高分子溶液の製造方法に関する。 The present invention relates to a polymer powder dissolving apparatus for dissolving polymer powder in a liquid (solvent) and a method for producing a polymer solution.
従来、高分子粉末を溶媒に溶解する際に発生するダマやままこ等の未溶解物を効率的に溶解させるべく、様々な装置や方法が提案されている。例えば、タンク内の上方に高分子粉体凝集剤の定量落下供給口を設け、給水を前記供給口下方のタンク内空間に水平乃至斜め下方に散水するためのスプレーノズルを設けた高分子凝集剤溶解装置（特許文献１参照。）や、上下が開口となりかつ外筒に多数のスリット開口を有する混合室内に設けられた高速回転翼に依って行なわれ、該混合室内への液流入が混合室の上下より、前記水溶性高分子粉末の投入が混合室の上より行なわれ、かつ溶解容器内全体の液溶解が、混合室外筒のスリットを通った分散体を含めた液の循環混合によって行われる高速攪拌機を用いた水溶性高分子粉末を水の中に溶解する方法において、前記水溶性高分子粉末を、高速攪拌機によって攪拌されている２５℃以下の前記水の中に、３００秒以下の短時間で投入し、投入終了後前記攪拌状態において直ちに昇温を行う水溶性高分子粉末の溶解方法（特許文献２参照。）や、タンク内の溶剤に粉体を溶解させる粉体溶解方法において、タンク上部の、溶剤面よりも上の位置に、上を向いた凸の曲面を有する分散板を設置しておき、タンク内の溶剤を攪拌しながら前記分散板上に粉体を投下することにより、該分散板で分散した粉体をタンク内の攪拌中の溶剤の中に投入する粉体溶解方法（特許文献３参照。）が提案されている。 Conventionally, various apparatuses and methods have been proposed in order to efficiently dissolve undissolved materials such as lumps and mamako that are generated when polymer powder is dissolved in a solvent. For example, a polymer flocculant provided with a fixed amount dropping supply port of the polymer powder flocculant above the tank and a spray nozzle for spraying water horizontally or obliquely downward in the tank space below the supply port It is performed by a melting device (see Patent Document 1) or a high-speed rotary blade provided in a mixing chamber having openings on the upper and lower sides and a large number of slit openings in the outer cylinder. From above and below, the water-soluble polymer powder is introduced from above the mixing chamber, and the entire solution in the dissolution vessel is dissolved by circulating and mixing the liquid including the dispersion passing through the slit of the outer cylinder of the mixing chamber. In the method of dissolving a water-soluble polymer powder in water using a high-speed stirrer, the water-soluble polymer powder is added to the water at 25 ° C. or lower that is being stirred by a high-speed stirrer for 300 seconds or less. Put in a short time In the dissolution method of water-soluble polymer powder (see Patent Document 2) in which the temperature is raised immediately in the stirring state after the completion of charging, or in the powder dissolution method in which powder is dissolved in the solvent in the tank, the solvent at the top of the tank A dispersion plate having a convex curved surface facing upward is installed at a position above the surface, and the powder is dropped on the dispersion plate while stirring the solvent in the tank. There has been proposed a powder dissolution method (see Patent Document 3) in which a dispersed powder is put into a stirring solvent in a tank.
しかしながら、上記従来の装置や方法では、溶解に長時間を要し、また、必ずしも十分な溶解効果を得ることができなかった。 However, the above-described conventional apparatuses and methods require a long time for dissolution, and a sufficient dissolution effect cannot always be obtained.
本発明の課題は、高分子粉末を液体（溶媒）に投入した際に生じるダマやままこ等の未溶解物を効率的に溶解させることができる高分子粉末溶解装置、及び高分子溶液の製造方法を提供することにある。 An object of the present invention is to provide a polymer powder dissolution apparatus capable of efficiently dissolving undissolved materials such as lumps and mamako produced when polymer powder is introduced into a liquid (solvent), and a method for producing a polymer solution Is to provide.
本発明者らは、上記課題を解決すべく鋭意研究した結果、溶解槽内の液体を攪拌すると共に循環させ、該循環液を溶解槽内の液面に向かってスプレーすることにより、かかる課題を解決できることを見い出し、本発明を完成するに至った。すなわち、液面に浮遊した（気泡を抱き込んだ）高分子粉末に向かってスプレーすることにより、高分子粉末が液体を吸収して沈澱しやすくなると共に、未溶解の高分子粉末を含有した液体を循環させることにより、高分子粉末の溶解が効率的に進行することを見い出し本発明を完成するに至った。 As a result of diligent research to solve the above problems, the present inventors stir and circulate the liquid in the dissolution tank, and spray the circulating liquid toward the liquid surface in the dissolution tank. The inventors have found that this can be solved, and have completed the present invention. That is, by spraying toward the polymer powder floating on the liquid surface (embedding bubbles), the polymer powder absorbs the liquid and precipitates easily, and the liquid containing undissolved polymer powder. It was found that by dissolving the polymer powder, the dissolution of the polymer powder proceeded efficiently and the present invention was completed.
すなわち、本発明は、（１）液体導出口を下部に有する溶解槽と、該溶解槽内の液体を攪拌するための攪拌手段と、前記溶解槽内の液面に向かって噴射可能なスプレーノズルと、その一端が前記溶解槽の液体導出口に接続されると共にその他端が前記スプレーノズルに接続された配管、及び循環ポンプを具備する液体循環手段とを備えたことを特徴とする高分子粉末溶解装置や、（２）攪拌手段が、溶解槽内の液体を下方に誘導する攪拌翼を備えたことを特徴とする上記（１）に記載の高分子粉末溶解装置や、（３）溶解槽が、下方に向かって縮径したテーパー部を備え、該テーパー部の中心に液体導出口が設けられていることを特徴とする上記（１）又は（２）に記載の高分子粉末溶解装置や、（４）高分子粉体及び該高分子粉体を溶解するための液体を溶解槽に投入し、溶解槽内の液体を攪拌すると共に、前記溶解槽の下部から液体の一部を導出し、該導出した液体を配管を介してスプレーノズルに案内し、該スプレーノズルから溶解槽内の液面に向かって液体を噴射することを特徴とする高分子溶液の製造方法に関する。 That is, the present invention includes (1) a dissolution tank having a liquid outlet at the bottom, a stirring means for stirring the liquid in the dissolution tank, and a spray nozzle capable of spraying toward the liquid level in the dissolution tank And a liquid circulating means having a circulation pump, one end of which is connected to the liquid outlet of the dissolution tank and the other end of which is connected to the spray nozzle. The polymer powder dissolving device according to (1) above, wherein the dissolving device, (2) the stirring means includes a stirring blade for guiding the liquid in the dissolving tank downward, and (3) the dissolving vessel The polymer powder dissolving apparatus according to (1) or (2) above, wherein the polymer powder dissolving apparatus according to (1) or (2) is provided with a tapered portion having a diameter reduced downward, and a liquid outlet is provided at the center of the tapered portion. (4) The polymer powder and the polymer powder are dissolved. Liquid in the dissolution tank, stirring the liquid in the dissolution tank, leading out a part of the liquid from the lower part of the dissolution tank, guiding the derived liquid to a spray nozzle through a pipe, The present invention relates to a method for producing a polymer solution, wherein a liquid is ejected from a spray nozzle toward a liquid surface in a dissolution tank.
また、本発明は、（５）高分子粉体を溶解するための液体を溶解槽に投入し、該液体中に高分子粉末を複数回に分けて投入することを特徴とする上記（４）に記載の高分子溶液の製造方法や、（６）高分子粉体を溶解するための液体を溶解槽に投入し、該溶解槽内の液体中に高分子粉末を徐々に投入することを特徴とする上記（４）又は（５）に記載の高分子溶液の製造方法や、（７）高分子粉体が、セルロース誘導体の粉体であることを特徴とする上記（４）〜（６）のいずれかに記載の高分子溶液の製造方法や、（８）溶解槽内に重金属固定剤を投入することを特徴とする上記（４）〜（７）のいずれかに記載の高分子溶液の製造方法や、（９）上記（１）〜（３）に記載の高分子粉末溶解装置を用いたことを特徴とする上記（４）〜（８）のいずれかに記載の高分子溶液の製造方法に関する。 The present invention is also characterized in that (5) the liquid for dissolving the polymer powder is put into a dissolving tank, and the polymer powder is put into the liquid in a plurality of times. (6) A liquid for dissolving the polymer powder is charged into the dissolution tank, and the polymer powder is gradually charged into the liquid in the dissolution tank. (4) to (6), wherein the method for producing a polymer solution according to (4) or (5) above, or (7) the polymer powder is a powder of a cellulose derivative. The method for producing a polymer solution according to any one of (4) to (7) above, or (8) a heavy metal fixing agent is introduced into a dissolution tank. (4) to (4) characterized by using a production method and (9) the polymer powder dissolving apparatus according to (1) to (3) above. The method for producing a polymer solution according to any one of).
本発明の高分子粉末溶解装置や高分子溶液の製造方法によれば、高分子粉末を液体に投入した際に生じるダマやままこ等の未溶解物を効率的に溶解させることができる。 According to the polymer powder dissolving apparatus and the polymer solution manufacturing method of the present invention, it is possible to efficiently dissolve undissolved materials such as lumps and mamako that are produced when polymer powder is put into a liquid.
本発明の高分子粉末溶解装置としては、液体導出口を下部に有する溶解槽と、該溶解槽内の液体を攪拌するための攪拌手段と、前記溶解槽内の液面に向かって噴射可能なスプレーノズルと、その一端が前記溶解槽の液体導出口に接続されると共にその他端が前記スプレーノズルに接続された配管、及び循環ポンプを具備する液体循環手段とを備えた高分子粉末溶解装置であれば特に制限されるものではなく、本発明の装置によれば、溶解槽内の液体を攪拌すると共に循環させ、該循環液を溶解槽内の液面に向かってスプレーするので、高分子粉末を溶媒に投入した際に生じるダマやままこ等の未溶解物を効率的に溶解させることができる。 The polymer powder dissolution apparatus of the present invention includes a dissolution tank having a liquid outlet at the bottom, a stirring means for stirring the liquid in the dissolution tank, and sprayable toward the liquid level in the dissolution tank A polymer powder dissolving apparatus comprising a spray nozzle, a pipe having one end connected to the liquid outlet of the dissolution tank and the other end connected to the spray nozzle, and a liquid circulating means having a circulation pump. If there is no particular limitation, the apparatus of the present invention stirs and circulates the liquid in the dissolution tank, and sprays the circulating liquid toward the liquid surface in the dissolution tank. It is possible to efficiently dissolve undissolved materials such as lumps and mamako that are produced when the is introduced into a solvent.
前記溶解槽としては、その下部に液体導出口を有するものであれば特に制限されるものではなく、例えば、平面視して円形、四角形のステンレス等からなる容器を挙げることができ、製造される高分子溶液の品質の改変を防止するために、密閉構造とできるものが好ましい。また、液体導出口が設けられる溶解槽の下部とは、溶解槽の中央より下方の部分をいい、好ましくは、溶解槽の下部１／３の部分をいい、液体導出口は、溶解槽の周部に設けられてもよいが、底部に設けられることがより好ましく、底部の中央に設けられることがさらに好ましい。また、溶解槽は、下方に向かって縮径したテーパー部を備えていることが好ましく、その場合、液体導出口は、テーパー部の中心に設けられていることが好ましく、これにより、液体をよりスムーズに導出することができる。 The dissolution tank is not particularly limited as long as it has a liquid outlet at the lower part thereof. For example, a container made of stainless steel having a circular shape or a square shape in a plan view can be mentioned and manufactured. In order to prevent modification of the quality of the polymer solution, those capable of having a sealed structure are preferred. The lower part of the dissolution tank in which the liquid outlet is provided refers to a part below the center of the dissolution tank, preferably the lower third part of the dissolution tank, and the liquid outlet is the periphery of the dissolution tank. Although it may be provided in the portion, it is more preferably provided in the bottom portion, and further preferably provided in the center of the bottom portion. In addition, the dissolution tank preferably includes a tapered portion that is reduced in diameter downward, and in that case, the liquid outlet is preferably provided at the center of the tapered portion, whereby the liquid can be more concentrated. It can be derived smoothly.
前記攪拌手段としては、棒状部材や攪拌翼を備えた部材等を挙げることができ、攪拌翼を備えた部材であることが好ましく、通常、液体を円周方向に攪拌する手段である。攪拌翼を備えた部材は、溶解槽の中心に縦方向（深さ方向）に回転軸を有すると共に、攪拌翼が軸方向に所定間隔をあけて複数設けられることが好ましい。かかる攪拌翼は、溶解槽内の液体を下方に誘導するよう構成されたものが好ましく、これにより、液体を液体導出口からよりスムーズに導出することができる。 Examples of the stirring means include a rod-like member and a member provided with a stirring blade, and a member provided with a stirring blade is preferable. Usually, the liquid is stirred in the circumferential direction. The member provided with the stirring blade preferably has a rotation axis in the longitudinal direction (depth direction) at the center of the dissolution tank, and a plurality of stirring blades are provided at predetermined intervals in the axial direction. Such a stirring blade is preferably configured to guide the liquid in the dissolution tank downward, whereby the liquid can be more smoothly led out from the liquid outlet.
前記スプレーノズルとしては、溶解槽内の液面に向かって噴射可能なものであれば特に制限されるものではなく、１流体ノズルであってもよいし、２流体ノズルであってもよく、例えば、溶解槽の周部や天板部に設置することができる。粉末投入口が外周部にある場合、浮遊したままの粉末は液体の回転にあわせ外周部を回転するため、かかるスプレーノズルは液面の中心から離れた外周部に噴射できるよう配置することが好ましい。 The spray nozzle is not particularly limited as long as it can be sprayed toward the liquid surface in the dissolution tank, and may be a one-fluid nozzle or a two-fluid nozzle. It can be installed on the periphery of the dissolution tank or on the top plate. When the powder inlet is on the outer periphery, the powder that remains floating rotates the outer periphery in accordance with the rotation of the liquid. Therefore, the spray nozzle is preferably arranged so that it can be sprayed to the outer periphery away from the center of the liquid level. .
前記液体循環手段としては、その一端が前記溶解槽の液体導出口に接続されると共にその他端が前記スプレーノズルに接続された配管と循環ポンプとを具備する手段であれば特に制限されるものではなく、かかる配管は、例えば、ステンレス等からなり、攪拌効率をより向上させるために、内部に邪魔板が設けられていてもよい。また、循環ポンプとしては、所望の量の液体を循環させることが可能なものであれば特に制限されるものではなく、例えば、１分間に溶解槽内の液体の５〜８０％を循環させることができるものを挙げることができる。 The liquid circulation means is not particularly limited as long as it is a means having one end connected to the liquid outlet of the dissolution tank and the other end connected to the spray nozzle and a circulation pump. Instead, the piping is made of, for example, stainless steel, and a baffle plate may be provided inside in order to further improve the stirring efficiency. The circulation pump is not particularly limited as long as a desired amount of liquid can be circulated. For example, 5 to 80% of the liquid in the dissolution tank is circulated in one minute. Can be mentioned.
また、本発明の高分子粉末溶解装置は、液体を加熱する加熱手段を備えていてもよく、加熱手段としては、溶解槽を直接加熱するヒーターや、溶解槽の周囲に設けられた通路に温水を通過させる温水加熱手段を挙げることができる。 Further, the polymer powder dissolving apparatus of the present invention may be provided with a heating means for heating a liquid. As the heating means, a heater for directly heating the dissolving tank, or a hot water in a passage provided around the dissolving tank. A hot water heating means for passing the water can be used.
また、本発明の高分子溶液の製造方法としては、高分子粉体及び該高分子粉体を溶解するための液体を溶解槽に投入し、溶解槽内の液体を攪拌すると共に、前記溶解槽の下部から液体の一部を導出し、該導出した液体を配管を介してスプレーノズルに案内し、該スプレーノズルから溶解槽内の液面に向かって液体を噴射する高分子溶液の製造方法であれば特に制限されるものではなく、本発明の製造方法は、上記本発明の高分子粉末溶解装置を用いて好適に実施することができる。 Further, as a method for producing a polymer solution of the present invention, polymer powder and a liquid for dissolving the polymer powder are put into a dissolution tank, the liquid in the dissolution tank is stirred, and the dissolution tank A method for producing a polymer solution in which a part of a liquid is led out from a lower part of the liquid, the led liquid is guided to a spray nozzle through a pipe, and the liquid is ejected from the spray nozzle toward a liquid surface in a dissolution tank. There is no particular limitation as long as it is present, and the production method of the present invention can be preferably carried out using the polymer powder dissolving apparatus of the present invention.
溶解槽への高分子粉体及び該高分子粉体を溶解する液体の投入方法としては、例えば、高分子粉体を溶解するための液体を溶解槽に投入し、該液体に対して、溶解しようとする所定量の高分子粉体を一度に投入してもよく、溶解しようとする所定量の高分子粉体を溶解槽に投入し、その後、高分子粉体を溶解するための液体を投入してもよいが、より短時間で効率よく溶解するために、溶解槽内に投入した液体に対して、所定量の高分子粉末を複数回に分けて投入したり、所定量の高分子粉末を徐々に投入することが好ましく、複数回に分け、さらにその各回において徐々に投入する方法がより好ましく、攪拌を行いつつ投入することが特に好ましい。 As a method of charging the polymer powder into the dissolution tank and the liquid for dissolving the polymer powder, for example, a liquid for dissolving the polymer powder is charged into the dissolution tank and dissolved in the liquid. A predetermined amount of polymer powder to be dissolved may be charged at once, a predetermined amount of polymer powder to be dissolved is charged into a dissolution tank, and then a liquid for dissolving the polymer powder is added. In order to dissolve efficiently in a shorter time, a predetermined amount of polymer powder can be added to the liquid charged in the dissolution tank in multiple times, or a predetermined amount of polymer can be added. It is preferable to gradually add the powder, more preferably a method in which the powder is divided into a plurality of times and gradually added at each time, and it is particularly preferable to add the powder while stirring.
本発明の方法における液体の１分間当りの循環割合としては、特に制限されるものではなく、高分子粉末の種類、割合等に応じて適宜決定することができ、例えば、５〜８０％程度を挙げることができ、５〜５０％であることが好ましく、１０〜３０％であることがより好ましい。 The circulation rate per minute of the liquid in the method of the present invention is not particularly limited, and can be appropriately determined according to the type and ratio of the polymer powder, for example, about 5 to 80%. 5 to 50% is preferable, and 10 to 30% is more preferable.
本発明に用いる高分子粉末としては、水溶性高分子の粉末、油溶性高分子の粉末を挙げることができ、水溶性高分子としては、デンプン、ゼラチン、セルロース、ポリビニルアルコールや、これらの誘導体を挙げることができる。また、高分子粉末を溶解するための液体（溶媒）としては、例えば、水、希酸水溶液、希アルカリ水溶液、有機溶媒等を挙げることができる。 Examples of the polymer powder used in the present invention include water-soluble polymer powder and oil-soluble polymer powder. Examples of the water-soluble polymer include starch, gelatin, cellulose, polyvinyl alcohol, and derivatives thereof. Can be mentioned. Examples of the liquid (solvent) for dissolving the polymer powder include water, dilute acid aqueous solution, dilute alkali aqueous solution, and organic solvent.
また、本発明の高分子溶液の製造方法においては、溶解槽内に重金属固定剤を投入してもよく、かかる重金属固定剤は、液体に予め溶解させておいてもよいし、溶解槽内の液体に対して投入してもよい。かかる重金属固定剤含有液中に、カルボキシメチルセルロース塩等のセルロース誘導体の粉末を投入して高分子溶液を製造することにより、かかる高分子溶液は、飛灰中の重金属固定液として使用することができる。重金属固定剤としては、従来公知のものを使用することができ、例えば、イミン系硫黄化合物、ピロリジン系硫黄化合物、ピペラジン系硫黄化合物、カルバミン酸系硫黄化合物、チオール系化合物等を挙げることができる。 Further, in the method for producing a polymer solution of the present invention, a heavy metal fixing agent may be charged into the dissolution tank, and the heavy metal fixing agent may be previously dissolved in a liquid, You may throw in with respect to a liquid. By introducing a powder of a cellulose derivative such as carboxymethyl cellulose salt into the heavy metal fixing agent-containing liquid to produce a polymer solution, the polymer solution can be used as a heavy metal fixing liquid in fly ash. . As the heavy metal fixing agent, conventionally known ones can be used, and examples thereof include imine sulfur compounds, pyrrolidine sulfur compounds, piperazine sulfur compounds, carbamic acid sulfur compounds, and thiol compounds.
以下、本発明の高分子粉末溶解装置を図面を用いて説明する。図１は、本発明の一実施形態に係る高分子粉末溶解装置の概略説明図である。 Hereinafter, the polymer powder dissolving apparatus of the present invention will be described with reference to the drawings. FIG. 1 is a schematic explanatory diagram of a polymer powder dissolving apparatus according to an embodiment of the present invention.
図１に示すように、本発明の一実施形態に係る高分子粉末溶解装置１は、高分子粉末及び該高分子粉末を溶解するための液体（両者をあわせて液体Ａとする。）を収容する溶解槽２と、溶解槽２内の液体Ａを攪拌する攪拌翼３を備えた攪拌手段４と、溶解槽２内の液面に向かって噴射可能なスプレーノズル５と、溶解槽２の底部に設けられた液体導出口６及びスプレーノズル５を連通する配管７と、配管７に設けられた循環ポンプ８とを備えている。配管７及び循環ポンプ８で液体循環手段９を構成する。 As shown in FIG. 1, a polymer powder dissolving apparatus 1 according to an embodiment of the present invention contains a polymer powder and a liquid for dissolving the polymer powder (both are referred to as a liquid A). A dissolving tank 2, a stirring means 4 having a stirring blade 3 for stirring the liquid A in the dissolving tank 2, a spray nozzle 5 capable of spraying toward the liquid surface in the dissolving tank 2, and the bottom of the dissolving tank 2 A pipe 7 that communicates with the liquid outlet 6 and the spray nozzle 5 provided in the pipe 7 and a circulation pump 8 provided in the pipe 7 are provided. The pipe 7 and the circulation pump 8 constitute a liquid circulation means 9.
溶解槽２は、平面視して、直径が１５００ｍｍ程度の円形であり、かつ深さが１３００ｍｍ程度のステンレス（ＳＵＳ３０４）からなる容器であって、その下部は、下方に向かって縮径するようにテーバー状に形成されると共にその中心に直径４０ｍｍ程度の液体導出口６が設けられている。 The dissolution tank 2 is a container made of stainless steel (SUS304) having a circular shape with a diameter of about 1500 mm and a depth of about 1300 mm in plan view, and a lower portion thereof is reduced in diameter downward. A liquid outlet 6 having a diameter of about 40 mm is provided at the center of the taber.
攪拌手段４は、溶解槽２の中心に縦方向に回転軸１０が軸受１１で軸支されており、モータ１２の駆動により回転する。かかる回転軸１０には、その中央部から下方に所定間隔をあけて３つの攪拌翼３が設けられており、上２つの攪拌翼は、その直径が溶解槽２の直径の１／２程度の長さであって、最下部の攪拌翼は、その直径が溶解槽２の直径の１／６程度の長さである。回転軸１０の回転により、溶解槽２内の液体Ａを攪拌すると共に溶解槽２の底部に設けられた液体導出口６に誘導する。 In the stirring means 4, a rotary shaft 10 is supported by a bearing 11 in the longitudinal direction at the center of the dissolution tank 2, and rotates by driving of a motor 12. The rotating shaft 10 is provided with three stirring blades 3 at a predetermined interval downward from the center thereof, and the upper two stirring blades have a diameter of about ½ of the diameter of the dissolution tank 2. The diameter of the lowermost stirring blade is about 1/6 of the diameter of the dissolution tank 2. The rotation of the rotary shaft 10 agitates the liquid A in the dissolution tank 2 and guides it to the liquid outlet 6 provided at the bottom of the dissolution tank 2.
溶解槽２の下部の液体導出口６には配管の一端が接続されると共に、かかる配管７の他端は、溶解槽２の天板１３に設置されたスプレーノズル５に接続されている。スプレーノズル５は、一流体ノズルであって、循環ポンプ８からの液圧によって噴射可能となっており、また、溶解槽２内の液面の中心から離れた外周部に噴射するように設置されている。 One end of a pipe is connected to the liquid outlet 6 at the lower part of the dissolution tank 2, and the other end of the pipe 7 is connected to a spray nozzle 5 installed on the top plate 13 of the dissolution tank 2. The spray nozzle 5 is a one-fluid nozzle and can be sprayed by the liquid pressure from the circulation pump 8 and is set so as to spray to the outer peripheral portion away from the center of the liquid level in the dissolution tank 2. ing.
かかる高分子粉末溶解装置１を用いて、高分子溶解液を製造した。高分子粉末溶解装置１に、重金属固定剤であるピペラジン−Ｎ，Ｎ’−ビスカルボジチオ酸カリウム塩の水溶液（固形分含有量３５％）１０００ｋｇを投入し、次いで、カルボキシメチルセルロースナトリウム（品名：ＣＭＣ〈１３５０〉ダイセル化学工業（株）社製）６ｋｇを数回に分けて投入した。このとき粉末の飛散防止のため攪拌を２５〜３０ｒ．ｐ．ｍとし溶解槽を密閉、窒素雰囲気下にした。その後、撹拌を開始（２５０〜３００ｒ．ｐ．ｍ）すると共に、循環ポンプ（２００Ｌ／分）を始動させ、未溶解物を含む液体の循環を行った。３時間後、未溶解物は完全に溶解し、均一な溶液が得られた。かかる均一な溶液は、飛灰中の重金属を固定化に使用することができる。 Using this polymer powder dissolution apparatus 1, a polymer solution was produced. 1000 kg of an aqueous solution (solid content 35%) of piperazine-N, N′-biscarbodithioic acid potassium salt, which is a heavy metal fixing agent, is charged into the polymer powder dissolving apparatus 1, and then sodium carboxymethylcellulose (product name: CMC) <1350> Daicel Chemical Industries, Ltd. 6 kg) was added in several portions. At this time, stirring is performed for 25 to 30 r. p. m, the dissolution tank was sealed and placed in a nitrogen atmosphere. Thereafter, stirring was started (250 to 300 rpm) and the circulation pump (200 L / min) was started to circulate the liquid containing undissolved substances. After 3 hours, the undissolved material was completely dissolved, and a uniform solution was obtained. Such a uniform solution can be used for immobilizing heavy metals in fly ash.
１ 高分子粉末溶解装置
２ 溶解槽
３ 攪拌翼
４ 攪拌手段
５ スプレーノズル
６ 液体導出口
７ 配管
８ 循環ポンプ
９ 液体循環手段
１０ 回転軸
１１ 軸受
１２ モータ
１３ 天板
DESCRIPTION OF SYMBOLS 1 Polymer powder dissolution apparatus 2 Dissolution tank 3 Stirring blade 4 Stirring means 5 Spray nozzle 6 Liquid outlet 7 Piping 8 Circulating pump 9 Liquid circulating means 10 Rotating shaft 11 Bearing 12 Motor 13 Top plate
Claims (9)
The method for producing a polymer solution according to any one of claims 4 to 8, wherein the polymer powder dissolving apparatus according to any one of claims 1 to 3 is used.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005206664A JP4917283B2 (en) | 2005-07-15 | 2005-07-15 | Polymer powder dissolution apparatus and method for producing polymer solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005206664A JP4917283B2 (en) | 2005-07-15 | 2005-07-15 | Polymer powder dissolution apparatus and method for producing polymer solution |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2007021357A true JP2007021357A (en) | 2007-02-01 |
| JP4917283B2 JP4917283B2 (en) | 2012-04-18 |
Family
ID=37782808
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2005206664A Active JP4917283B2 (en) | 2005-07-15 | 2005-07-15 | Polymer powder dissolution apparatus and method for producing polymer solution |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP4917283B2 (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009073111A3 (en) * | 2007-11-30 | 2010-02-25 | Celanese International Corporation | Methods for incorporating polyvinyl alcohol particles into products |
| JP2013086022A (en) * | 2011-10-18 | 2013-05-13 | Daiyanitorikkusu Kk | Method for dissolving powdery water-soluble polymer compound |
| CN103240019A (en) * | 2013-05-17 | 2013-08-14 | 成都中牧生物药业有限公司 | Circulating liquid medicine granule disperser |
| JP2013240767A (en) * | 2012-05-22 | 2013-12-05 | Mizuho Kogyo Kk | Circulation mechanism of stirring device |
| WO2014158885A1 (en) * | 2013-03-14 | 2014-10-02 | Ecolab Usa Inc. | Polymer dissolution system |
| CN104941486A (en) * | 2015-06-17 | 2015-09-30 | 重庆市瑞轩豪邦新型建材有限公司 | Circulating type stirring machine |
| JP2017527439A (en) * | 2014-07-14 | 2017-09-21 | エヌケー カンパニー リミテッド | Drug storage and dissolution equipment for ballast water sterilization treatment |
| CN107551886A (en) * | 2017-09-30 | 2018-01-09 | 江阴市南丰科技有限公司 | A kind of Chemical Manufacture agitator tank |
| KR101816268B1 (en) | 2016-10-06 | 2018-02-22 | (주) 아미켐씨에스 | An Easy Cleaning type Antifouling Ceramic Coating Material and Manufacturing Device thereof |
| JP2019147077A (en) * | 2018-02-26 | 2019-09-05 | プライミクス株式会社 | Agitator |
| CN113707398A (en) * | 2021-09-02 | 2021-11-26 | 江苏传艺科技股份有限公司 | Insulated polyimide film processing technology and production equipment thereof |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111841426B (en) * | 2020-07-09 | 2021-04-16 | 广州美晨科技实业有限公司 | Intelligent mixing control device and method for food additives |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58223428A (en) * | 1982-06-21 | 1983-12-26 | Fuji Bussan Kk | Method and device for dissolving thickener |
| JPS6250787A (en) * | 1985-08-30 | 1987-03-05 | 株式会社東芝 | Computer-aided learning system |
| JPH07308558A (en) * | 1994-05-17 | 1995-11-28 | Sekisui Chem Co Ltd | Stirring device and polymerization method for adhesive |
| JPH105616A (en) * | 1996-06-24 | 1998-01-13 | Kubota Corp | Cleaning of slag and slag cleaning device |
| JPH115025A (en) * | 1997-06-17 | 1999-01-12 | Fuji Photo Film Co Ltd | Preparation of solution |
| JP2000319402A (en) * | 1999-05-14 | 2000-11-21 | Sony Corp | Method for dissolving binder resin and its apparatus |
| JP2001087603A (en) * | 1999-09-27 | 2001-04-03 | Sekisui Environment Kk | Polymeric flocculant dissolving apparatus |
-
2005
- 2005-07-15 JP JP2005206664A patent/JP4917283B2/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58223428A (en) * | 1982-06-21 | 1983-12-26 | Fuji Bussan Kk | Method and device for dissolving thickener |
| JPS6250787A (en) * | 1985-08-30 | 1987-03-05 | 株式会社東芝 | Computer-aided learning system |
| JPH07308558A (en) * | 1994-05-17 | 1995-11-28 | Sekisui Chem Co Ltd | Stirring device and polymerization method for adhesive |
| JPH105616A (en) * | 1996-06-24 | 1998-01-13 | Kubota Corp | Cleaning of slag and slag cleaning device |
| JPH115025A (en) * | 1997-06-17 | 1999-01-12 | Fuji Photo Film Co Ltd | Preparation of solution |
| JP2000319402A (en) * | 1999-05-14 | 2000-11-21 | Sony Corp | Method for dissolving binder resin and its apparatus |
| JP2001087603A (en) * | 1999-09-27 | 2001-04-03 | Sekisui Environment Kk | Polymeric flocculant dissolving apparatus |
Cited By (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8946348B2 (en) | 2007-11-30 | 2015-02-03 | Sekisui Specialty Chemicals America, Llc | Method for dissolving polyvinyl alcohol particles into aqueous media using high shear |
| WO2009073111A3 (en) * | 2007-11-30 | 2010-02-25 | Celanese International Corporation | Methods for incorporating polyvinyl alcohol particles into products |
| JP2013086022A (en) * | 2011-10-18 | 2013-05-13 | Daiyanitorikkusu Kk | Method for dissolving powdery water-soluble polymer compound |
| JP2013240767A (en) * | 2012-05-22 | 2013-12-05 | Mizuho Kogyo Kk | Circulation mechanism of stirring device |
| CN105142767A (en) * | 2013-03-14 | 2015-12-09 | 艺康美国股份有限公司 | Polymer dissolution system |
| US20140319071A1 (en) * | 2013-03-14 | 2014-10-30 | Ecolab Usa Inc. | Polymer dissolution system |
| WO2014158885A1 (en) * | 2013-03-14 | 2014-10-02 | Ecolab Usa Inc. | Polymer dissolution system |
| AU2014241826B2 (en) * | 2013-03-14 | 2017-10-19 | Ecolab Usa Inc. | Polymer dissolution system |
| RU2613952C1 (en) * | 2013-03-14 | 2017-03-22 | ЭКОЛАБ ЮЭсЭй ИНК., | System for polymer dilution |
| US9682347B2 (en) * | 2013-03-14 | 2017-06-20 | Ecolab Usa Inc. | Polymer dissolution system |
| CN103240019A (en) * | 2013-05-17 | 2013-08-14 | 成都中牧生物药业有限公司 | Circulating liquid medicine granule disperser |
| JP2017527439A (en) * | 2014-07-14 | 2017-09-21 | エヌケー カンパニー リミテッド | Drug storage and dissolution equipment for ballast water sterilization treatment |
| CN104941486A (en) * | 2015-06-17 | 2015-09-30 | 重庆市瑞轩豪邦新型建材有限公司 | Circulating type stirring machine |
| KR101816268B1 (en) | 2016-10-06 | 2018-02-22 | (주) 아미켐씨에스 | An Easy Cleaning type Antifouling Ceramic Coating Material and Manufacturing Device thereof |
| CN107551886A (en) * | 2017-09-30 | 2018-01-09 | 江阴市南丰科技有限公司 | A kind of Chemical Manufacture agitator tank |
| JP2019147077A (en) * | 2018-02-26 | 2019-09-05 | プライミクス株式会社 | Agitator |
| JP7061476B2 (en) | 2018-02-26 | 2022-04-28 | プライミクス株式会社 | Stirrer |
| CN113707398A (en) * | 2021-09-02 | 2021-11-26 | 江苏传艺科技股份有限公司 | Insulated polyimide film processing technology and production equipment thereof |
| CN113707398B (en) * | 2021-09-02 | 2022-10-14 | 江苏传艺科技股份有限公司 | Insulated polyimide film processing technology and production equipment thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4917283B2 (en) | 2012-04-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4917283B2 (en) | Polymer powder dissolution apparatus and method for producing polymer solution | |
| Williams et al. | Mechanochemical organocatalysis: do high enantioselectivities contradict what we might expect? | |
| JP2009512477A5 (en) | ||
| JP2011041896A (en) | Stirring vessel | |
| KR100507428B1 (en) | Device for mixing and dissolving solid granules in a liquid, in particular for producing nitrophosphate fertilisers | |
| TW202027850A (en) | High-concentration mixer for the preparation of a homogeneous suspension of cellulose in an aqueous solution of a tertiary amine oxide and process for using the same | |
| CN205832984U (en) | A kind of corollary apparatus of ballast water treatment | |
| KR20090010851U (en) | Apparatus for removing wastewater bubble | |
| JP2006512084A (en) | Apparatus, system and method for producing hydrogel particles | |
| CN211419613U (en) | Add medicine aeration agitating unit | |
| US3642257A (en) | Agitating apparatus | |
| CN114835222B (en) | Mixing and stirring device and mixing method for sewage treatment | |
| CN206474057U (en) | A kind of mixing channel of dry powder fully dissolved rabbling mechanism | |
| JPH11128732A (en) | Production of solid by precipitation | |
| CN210252108U (en) | Device for uniformly dissolving sodium sulfate in bipolar membrane system | |
| EP0136394A2 (en) | Method and apparatus for solution of gas in liquid | |
| WO2020158131A1 (en) | Ice slurry production system | |
| JP2009022873A (en) | Sludge flocculating/mixing device | |
| JP2017192896A (en) | Agitation device | |
| CN211712661U (en) | Paddle type stirring equipment for treating leather processing wastewater | |
| JP3751952B2 (en) | Sludge crusher | |
| JP2010207692A (en) | Agitator | |
| US20060210459A1 (en) | Method and apparattus for crystallization | |
| CN112657368A (en) | Solid-liquid mixing device for substances easy to release heat | |
| RU163705U1 (en) | APPARATUS FOR CHEMICAL AND TECHNOLOGICAL PROCESSES |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20080714 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20100722 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20110512 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20110705 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20120124 |
|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20120126 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20150203 Year of fee payment: 3 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 4917283 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |