JP2010007843A - High pressure vessel and mixed material supplying method using the same - Google Patents

High pressure vessel and mixed material supplying method using the same Download PDF

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JP2010007843A
JP2010007843A JP2008171260A JP2008171260A JP2010007843A JP 2010007843 A JP2010007843 A JP 2010007843A JP 2008171260 A JP2008171260 A JP 2008171260A JP 2008171260 A JP2008171260 A JP 2008171260A JP 2010007843 A JP2010007843 A JP 2010007843A
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pressure vessel
mixture
mixed material
stirring
high pressure
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JP5192927B2 (en
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Takashi Yajima
尊 矢嶋
Hidetoshi Ota
英俊 太田
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Taiyo Nippon Sanso Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a high pressure vessel of simple structure capable of excellently stirring and mixing a mixed material and capable of evening the composition of the mixed material in a short time, and to provide a method capable of supplying the mixed material at a constant mixing ratio to an external user even in the case of a mixed material easy to be cohered and deposited such as a mixed material of fine particles and a fluid by using this high pressure vessel. <P>SOLUTION: This high pressure vessel includes a vessel body 1 for storing a mixed material including at least one kind of fluid and a valve 2 for sealing an opening of the vessel body, and a stirring element 5 for stirring the mixed material with rotation or turn of the high pressure vessel is fixed to the vessel body or the valve 2. The stirring element is desirably fixed to a mixed fluid lead-out pipe 4 fitted to the valve. After stirring the mixed material with rotation or turn of the high pressure vessel, the mixed material is led out of the high pressure vessel. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、少なくとも1種の流体を含む混合物を供給する供給方法及びこの供給方法に用いられる高圧容器に関する。   The present invention relates to a supply method for supplying a mixture containing at least one fluid and a high-pressure vessel used in the supply method.

例えば、ヘリウム又は二酸化炭素とアルゴンとの混合ガスのように互いに混合し難いガスを高圧容器内に充填する場合、高圧容器内部で組成が均一となるのに長時間を要する。このため、所定の重量比にて充填した後に内容物を撹拌する必要がある。
例えば、実開昭61−161500号公報や特公平1−60291号公報に開示のように、高圧容器を回転させている。しかし、この方法ではガス濃度のばらつき解消に30分以上を要することがある。
For example, when a gas that is difficult to mix with each other, such as a mixed gas of helium or carbon dioxide and argon, is filled in the high-pressure vessel, it takes a long time for the composition to be uniform inside the high-pressure vessel. For this reason, it is necessary to stir the contents after filling at a predetermined weight ratio.
For example, as disclosed in Japanese Utility Model Laid-Open No. 61-161500 and Japanese Patent Publication No. 1-60291, the high-pressure vessel is rotated. However, this method may require 30 minutes or more to eliminate the variation in gas concentration.

また、充填時の組成均一化を改善させるための手段として、長手方向に数点孔があいた注入管兼注出管を挿入した発明(特開平9−133295号公報)が公開されている。この技術は、充填時の均一化であり、流体の種類等によっては、充填から長時間経過後、或いは供給時の組成均一化の課題がある。   Further, an invention (Japanese Patent Laid-Open No. Hei 9-133295) in which an injection tube and an extraction tube having several holes in the longitudinal direction are inserted is disclosed as means for improving the uniform composition at the time of filling. This technique is homogenization at the time of filling, and depending on the type of fluid, there is a problem of homogenizing the composition after a long time has elapsed since filling or at the time of supply.

一方、微粒子と流体との混合物を高圧容器に充填すると、時間経過とともに微粒子が凝集又は沈降し、混合物を一定濃度で取り出すことができなくなることがある。この場合には、高圧容器内の混合物を撹拌して組成を一定にすればよいが、高圧容器内の混合物に対して撹拌を行うことは通常の容器内の混合物の撹拌に比べて難しい。   On the other hand, when a high pressure vessel is filled with a mixture of fine particles and fluid, the fine particles may aggregate or settle over time, and the mixture may not be taken out at a constant concentration. In this case, the composition in the high-pressure vessel may be made constant by stirring the mixture, but it is difficult to stir the mixture in the high-pressure vessel as compared to stirring the mixture in a normal vessel.

混合物を貯蔵した高圧容器内の供給時の組成均一化を図る方法として、(1)撹拌体を持った高圧容器(特開2007−14889号公報)や、(2)撹拌子を内蔵した高圧容器(特開2007−321934号公報)などがある。
しかしながら、(1)の高圧容器では、気密部分において構造が複雑で、撹拌体を動かす場合、それぞれに駆動源として配線や配管または駆動ベルトなどの取り付け作業が伴い、ボンベ搬送時には衝撃などの外力で故障する可能性が高く、高価なものとなる。
As a method for homogenizing the composition at the time of supply in the high-pressure vessel storing the mixture, (1) a high-pressure vessel having a stirring body (Japanese Patent Laid-Open No. 2007-14889), or (2) a high-pressure vessel having a built-in stirrer (Japanese Patent Laid-Open No. 2007-321934).
However, in the high-pressure vessel of (1), the structure is complicated in the airtight part, and when moving the stirring body, each requires a work of attaching wiring, piping, or a driving belt as a driving source, and external force such as impact is used when transporting the cylinder. There is a high possibility of failure and it will be expensive.

また、(2)の高圧容器内に撹拌子を内蔵し、これをマグネチックスターラー等で撹拌する方法では、高圧容器においては強力な撹拌力が得られにくい。また、非磁性材料をボンベ本体に使用するため非常に高価なボンベとなる。
当然、両者とも一般的な高圧容器を使用することはできない。
実開昭61−161500号公報 特公平1−60291号公報 特開平9−133295号公報 特開2007−14889号公報 特開2007−321934号公報
Further, in the method (2) in which a stirring bar is built in the high-pressure vessel and this is stirred with a magnetic stirrer or the like, it is difficult to obtain a strong stirring force in the high-pressure vessel. Further, since a nonmagnetic material is used for the cylinder body, the cylinder is very expensive.
Naturally, neither can use a general high-pressure vessel.
Japanese Utility Model Publication No. 61-161500 Japanese Patent Publication No. 1-60291 JP-A-9-133295 JP 2007-14889 A JP 2007-321934 A

よって、本発明における課題は、混合物の撹拌、混合は良好に行え、かつ混合物の組成の均一化に要する時間が短時間ですみ、構造が簡単である高圧容器を得るとともに、この高圧容器を用いて微粒子と流体との混合物などの凝集、沈殿しやすい混合物であっても、一定の混合割合でこれを外部の使用先に供給できる供給方法を得ることにある。   Therefore, the problem in the present invention is that the mixture can be stirred and mixed well and the time required for homogenizing the composition of the mixture is short, and a high-pressure vessel having a simple structure is obtained. Thus, there is a need for a supply method that can supply a mixture of fine particles and a fluid that easily aggregates and precipitates to an external use destination at a constant mixing ratio.

かかる課題を解決するため、
請求項1にかかる発明は、少なくとも1種の流体を含む混合物を貯蔵する容器本体と、前記容器本体の開口を塞ぐバルブを有する高圧容器であって、
前記容器本体又は前記バルブに、前記高圧容器の回転または回動により前記混合物を撹拌する撹拌体が固定されたことを特徴とする高圧容器である。
請求項2にかかる発明は、前記撹拌体は、前記バルブに取り付けられた混合流体導出管に固定されていることを特徴とする請求項1記載の高圧容器である。
To solve this problem,
The invention according to claim 1 is a high-pressure container having a container body for storing a mixture containing at least one fluid, and a valve for closing an opening of the container body,
The high-pressure vessel is characterized in that an agitator for agitating the mixture by rotation or rotation of the high-pressure vessel is fixed to the vessel main body or the valve.
The invention according to claim 2 is the high-pressure vessel according to claim 1, wherein the stirring body is fixed to a mixed fluid outlet pipe attached to the valve.

請求項3にかかる発明は、請求項1または2に記載された高圧容器を用い、この高圧容器に充填された少なくとも1種の流体を含む混合物を前記高圧容器から導出する供給方法であって、
前記高圧容器の回転または回動により前記混合物を撹拌した後に前記混合物を前記高圧容器から導出することを特徴とする混合物の供給方法である。
請求項4にかかる発明は、前記混合物が、微小固体を含むことを特徴とする請求項3記載の混合物の供給方法である。
The invention according to claim 3 is a supply method of using the high-pressure vessel according to claim 1 or 2 to derive a mixture containing at least one fluid filled in the high-pressure vessel from the high-pressure vessel.
The mixture supply method, wherein the mixture is led out from the high-pressure vessel after the mixture is stirred by rotation or rotation of the high-pressure vessel.
The invention according to claim 4 is the method for supplying the mixture according to claim 3, wherein the mixture contains a fine solid.

請求項5にかかる発明は、前記流体が、常温・加圧で液化する液化ガスであることを特徴とする請求項3記載の混合物の供給方法である。
請求項6にかかる発明は、前記液化ガスが、超臨界状態または亜臨界状態であることを特徴とする請求項5記載の混合物の供給方法である。
The invention according to claim 5 is the method for supplying the mixture according to claim 3, wherein the fluid is a liquefied gas that is liquefied at room temperature and under pressure.
The invention according to claim 6 is the method for supplying the mixture according to claim 5, wherein the liquefied gas is in a supercritical state or a subcritical state.

本発明の高圧容器によれば、その内部に撹拌体が存在するため、混合物を充填した状態でこの高圧容器を回転または回動させることで、内部の混合物の流れが乱され、混合物が撹拌されて均一に混合されて、短時間で一定組成の混合物が得られる。
また、複雑な装置構成をとるものではないので、安価に得ることができ、しかも故障を起こすことも少ない。
According to the high-pressure vessel of the present invention, since the agitator is present in the interior thereof, the flow of the internal mixture is disturbed by rotating or rotating the high-pressure vessel with the mixture filled, and the mixture is agitated. And a uniform composition can be obtained in a short time.
Further, since it does not take a complicated apparatus configuration, it can be obtained at a low cost, and it is less likely to cause a failure.

本発明の供給方法によれば、高圧容器を回転または回動させて、混合物の組成を均一化したのち、高圧容器から外部の使用先に供給することになるので、例えば微粒子と流体との混合物などを、微粒子が全体に均一に分散した状態で供給することができる。
勿論、混合物が流体のみからなる場合にも組成が均一となった混合物を供給することができる。
According to the supply method of the present invention, the high-pressure vessel is rotated or rotated to uniformize the composition of the mixture, and then supplied from the high-pressure vessel to an external user. For example, a mixture of fine particles and fluid Can be supplied in a state in which the fine particles are uniformly dispersed throughout.
Of course, even when the mixture is composed of only a fluid, a mixture having a uniform composition can be supplied.

図1は、本発明の高圧容器の一例を示すものである。
図1中、符号1は容器本体を示す。この容器本体1は、鋼製の耐圧容器であって、いわゆるボンベと呼ばれているものでもある。
容器本体1の上部の開口部には、高圧ガス容器用バルブ2がねじ込まれて取り付けられている。このバルブ2の下部にはステンレス鋼管などからなるサイホン管(混合流体導出管)4が容器本体1内部に向けて一体に固定されている。
FIG. 1 shows an example of a high-pressure vessel of the present invention.
In FIG. 1, the code | symbol 1 shows a container main body. The container body 1 is a pressure-resistant container made of steel and is also called a so-called cylinder.
A high pressure gas container valve 2 is screwed into an opening at the top of the container body 1. A siphon tube (mixed fluid outlet tube) 4 made of a stainless steel tube or the like is integrally fixed to the lower portion of the valve 2 toward the inside of the container body 1.

このサイホン管4の下端は容器本体1の底部近くまで延びている。これにより、バルブ2を開とすることで、内部に充填された混合物をサイホン管4を経由して外部の使用先に供給できるようになっている。   The lower end of the siphon tube 4 extends to near the bottom of the container body 1. Thus, by opening the valve 2, the mixture filled inside can be supplied to the outside user through the siphon tube 4.

前記サイホン管4の外周面には、その上部から下部にかけて多数の撹拌体5、5・・が取り付けられている。
図1では、撹拌体5、5・・の存在を単に示しており、その形状、取付形態等は、図2に詳しく示している。
図2に示すように、この撹拌体5は、ステンレス鋼板などからなる長方形の軽く湾曲した羽根状の板体であって、その面方向がサイホン管4の軸線方向に対して30〜45度の角度で傾斜して溶接等により取り付けられたものである。
A large number of stirring bodies 5, 5,... Are attached to the outer peripheral surface of the siphon tube 4 from the upper part to the lower part.
In FIG. 1, the presence of the stirring bodies 5, 5... Is simply shown, and the shape, mounting form, and the like are shown in detail in FIG. 2.
As shown in FIG. 2, the stirring body 5 is a rectangular lightly curved blade-like plate body made of a stainless steel plate or the like, the surface direction of which is 30 to 45 degrees with respect to the axial direction of the siphon tube 4. It is attached by welding or the like inclined at an angle.

撹拌体5、5・・の取り付け位置については、サイホン管4の外周面に放射状に均等に4枚の撹拌体5、5・・が配され、この4枚の撹拌体5、5・・を1組として、サイホン管4の長さ方向に複数組、間隔を空けて配置され、さらには、長さ方向に隣り合う2組の撹拌体5は、個々の取り付け位置がサイホン管4の外周面でおいて45度ずつ交互に配されてもよい。   As for the mounting positions of the stirring bodies 5, 5,..., Four stirring bodies 5, 5,... Are arranged radially and evenly on the outer peripheral surface of the siphon tube 4, and the four stirring bodies 5, 5,. As one set, a plurality of sets of the siphon tubes 4 are arranged in the length direction at intervals, and two sets of the stirring bodies 5 adjacent to each other in the length direction are attached to the outer peripheral surface of the siphon tube 4. However, they may be alternately arranged at 45 degrees.

図3は、サイホン管4に対する撹拌体5の他の取付形態を示すものである。この例では、長方形の板体からなる撹拌体5、5・・の面方向がサイホン管4の軸線方向に平行している点が先の形態と異なるところである。それ以外の取付位置などは同様である。   FIG. 3 shows another form of attachment of the stirring member 5 to the siphon tube 4. In this example, the point that the surface direction of the stirring bodies 5, 5... Made of a rectangular plate body is parallel to the axial direction of the siphon tube 4 is different from the previous embodiment. Other mounting positions are the same.

このような高圧容器にあっては、容器本体1内に混合物を充填した状態で高圧容器をその軸線を回転軸として回転もしくは回動させると、内部の混合物の流れが多数の撹拌体5、5・・に邪魔されて乱され、これによって混合物が撹拌されて均一な混合状態となる。   In such a high-pressure vessel, when the high-pressure vessel is rotated or rotated around the axis of the high-pressure vessel in a state where the mixture is filled in the vessel main body 1, the flow of the internal mixture is increased to a large number of stirring bodies 5, 5 .. disturbed and disturbed, whereby the mixture is agitated to a uniform mixing state.

このため、混合物が、液体状態、超臨界状態、亜臨界状態の流体あるいは、この流体と微粒子との混合物であっても、各成分が均一に混合あるいは分散した状態となる。
したがって、混合物が2種以上の流体からなる場合には、これを高圧容器に充填後、供給時までの期間内で、少なくとも一度、高圧容器を回転または回動させておけば、均一な混合組成の混合物が得られ、これを使用先に供給できる。
For this reason, even if the mixture is a fluid in a liquid state, a supercritical state, a subcritical state, or a mixture of the fluid and fine particles, each component is uniformly mixed or dispersed.
Therefore, when the mixture is composed of two or more kinds of fluids, a uniform mixed composition can be obtained by rotating or rotating the high-pressure vessel at least once within the period up to the supply after filling the high-pressure vessel. Is obtained and can be supplied to the user.

また、混合物が流体と微粒子とからなる場合には、供給時の直前に、高圧容器を回転または回動させるか、もしくは高圧容器を回転または回動させつつ、混合物を使用先に供給することで、均一な分散状態の混合物を供給することが可能になる。   When the mixture is composed of a fluid and fine particles, the high-pressure vessel is rotated or rotated immediately before supply, or the mixture is supplied to the user while rotating or rotating the high-pressure vessel. It becomes possible to supply a mixture in a uniformly dispersed state.

なお、撹拌体5、5・・をサイホン管4に取り付ける形態以外に、バルブ2から直接内部に、または容器本体1内に伸ばした別個の部材に取り付けられても良い。さらに撹拌体5は板状でなく、棒状や線状でもよい。
また、撹拌体5の剛性の有無を問わない。さらに、撹拌体5は容器本体1内部に接着や溶着、カシメなど機械的固定方法で固定されてもよい。
In addition to the form in which the stirring bodies 5, 5... Are attached to the siphon tube 4, they may be attached directly to the inside from the valve 2 or to a separate member extended into the container body 1. Furthermore, the stirrer 5 is not plate-shaped but may be rod-shaped or linear.
It does not matter whether the stirrer 5 has rigidity. Further, the stirring member 5 may be fixed inside the container body 1 by a mechanical fixing method such as adhesion, welding, or caulking.

また、混合物がガス状態である場合には、サイホン管4は不要となるので、このような場合には、バルブ2に棒状部材又は管状部材を取り付け、これに撹拌体5、5・・を固定すればよい。あるいは、高圧容器の回転または回動により内部を撹拌可能な撹拌体5、5・・をバルブ2に直接取り付けてもよい。
高圧容器がガス注入管を持つ場合には、ガス注入管に撹拌体5、5・・を設ければよい。
Further, when the mixture is in a gas state, the siphon tube 4 is not necessary. In such a case, a rod-like member or a tubular member is attached to the valve 2 and the stirring bodies 5, 5,. do it. Or you may attach directly to the valve | bulb 2 the stirring body 5 which can stir the inside by rotation or rotation of a high-pressure vessel.
In the case where the high-pressure vessel has a gas injection tube, the gas injection tube may be provided with the stirring members 5, 5,.

以下、流体と微小固体との混合物を高圧容器から供給する方法について説明する。
図4は、上述の供給方法の具体例を示すものである。
この例では、混合物が充填された高圧容器6が回転盤7の上に置かれる。回転盤7は内蔵された回転駆動機構により回転可能または回動可能となっており、その上面に置かれた高圧容器6を回転角90度以内で往復回動させるほか、途中での回動速度または回転速度の変更、途中での停止が可能となる構成となっている。
Hereinafter, a method for supplying a mixture of fluid and fine solid from a high-pressure vessel will be described.
FIG. 4 shows a specific example of the above-described supply method.
In this example, a high-pressure vessel 6 filled with the mixture is placed on a turntable 7. The turntable 7 can be rotated or rotated by a built-in rotation drive mechanism. The high-pressure vessel 6 placed on the upper surface of the turntable 7 reciprocates within a rotation angle of 90 degrees, and the rotation speed in the middle. Alternatively, the rotation speed can be changed or stopped halfway.

回転盤7上に置かれた高圧容器6は、その底部付近において、外周部が3個のローラー8、8、8に挟まれて直立状態を保ったまま回動または回転できるようになっている。
高圧容器6は、そのバルブ2がフレキシブル配管9を介して固定状態となっている供給配管(図示略)に接続されている。
混合ガス供給時に、上記の状態で高圧容器6を回転角θ1≦90°で交互に回動を繰り返すことによって、内部の混合ガスが撹拌される。回転角θ1が90°以内であるため、フレキシブル配管9の接続先は固定配管10でも問題は無い。
The high-pressure vessel 6 placed on the turntable 7 can be rotated or rotated in the vicinity of its bottom while the outer peripheral portion is sandwiched between three rollers 8, 8, 8 while maintaining an upright state. .
The high-pressure vessel 6 is connected to a supply pipe (not shown) in which the valve 2 is fixed via a flexible pipe 9.
When the mixed gas is supplied, the internal mixed gas is stirred by alternately rotating the high-pressure vessel 6 at the rotation angle θ1 ≦ 90 ° in the above state. Since the rotation angle θ1 is within 90 °, there is no problem even when the flexible pipe 9 is connected to the fixed pipe 10.

図5は、供給方法の他の具体例を示すものである。
この例では、フレキシブル配管9が回転可能な接続金具11に接続され、この接続金具11は、供給配管10に接続されている。接続金具11にはスイベルジョイント等が用いられる。
混合ガス供給時には、上記の状態で(1)高圧容器6を回転角θ2で交互に反転させる、あるいは(2)高圧容器6を回転→減速→または停止→回転または反転させる、のいずれかの動作を繰りかえすことによって、内部の混合ガスが撹拌される。
FIG. 5 shows another specific example of the supply method.
In this example, the flexible pipe 9 is connected to a rotatable connection fitting 11, and the connection fitting 11 is connected to a supply pipe 10. A swivel joint or the like is used for the connection fitting 11.
At the time of supplying the mixed gas, in the above state, either (1) the high pressure vessel 6 is alternately reversed at the rotation angle θ2, or (2) the high pressure vessel 6 is rotated → decelerated → or stopped → rotated or reversed. By repeating the above, the internal mixed gas is agitated.

フレキシブル配管9の接続先が回転可能な接続金具11に接続されるため、回転角θ2は自由に設定でき、その範囲で自由に回転することができる。
なお、高圧容器6は、図3、図4に示すように、直立状態で回転または回動させるだけではなく、高圧容器6を傾斜した状態で、あるいは寝かせた状態で回転または回動させることができる。
Since the connection destination of the flexible pipe 9 is connected to the rotatable connection fitting 11, the rotation angle θ2 can be freely set and can rotate freely within the range.
As shown in FIGS. 3 and 4, the high-pressure vessel 6 can be rotated or rotated not only in an upright state but also in a tilted state or in a laid state. it can.

本発明での供給対象物は、高圧容器(ボンベ)に充填された少なくとも1種の流体を含む混合物である。
流体としては気体状態、液体状態、超臨界状態、亜臨界状態のいかなる状態でもよい。流体の種類としては、二酸化炭素、フロン、ハイドロフルオロエーテル、ジメチルエーテル(DME)、液化石油ガス(LGP)等、常温・加圧で液体となる液化ガスが常温で取り扱いし易く好ましい。また、窒素、アルゴン、クリプトン等、低温・加圧で液体となる液化ガスも使用可能である。また、超臨界状態を示す流体であるメタン、エタン、アセトン等も使用可能である。
The supply object in the present invention is a mixture containing at least one fluid filled in a high-pressure vessel (cylinder).
The fluid may be any state of a gas state, a liquid state, a supercritical state, and a subcritical state. As the type of fluid, liquefied gas that becomes liquid at room temperature and pressure, such as carbon dioxide, chlorofluorocarbon, hydrofluoroether, dimethyl ether (DME), and liquefied petroleum gas (LGP), is preferable because it is easy to handle at room temperature. Further, a liquefied gas that becomes liquid at a low temperature and under pressure, such as nitrogen, argon, krypton, etc., can also be used. Also, methane, ethane, acetone, etc., which are fluids showing a supercritical state, can be used.

混合物としては、流体同士の混合物、流体と微小固体との混合物が例示される。流体同士の混合物としては、気体状態同士、液体状態同士、気体状態と液体状態など、いかなる組合せでもよい。具体的な組合せとしては、ヘリウム又は二酸化炭素とアルゴンとの混合ガス等が例示される。
微小固体の形状は、粒子状、繊維状、筒状、線状、棒状、コイル状等、形状は問わない。また、材料も限定されない。
Examples of the mixture include a mixture of fluids and a mixture of a fluid and a fine solid. As a mixture of fluids, any combination such as a gas state, a liquid state, a gas state and a liquid state may be used. Specific examples of the combination include helium or a mixed gas of carbon dioxide and argon.
The shape of the minute solid may be any shape such as a particle shape, a fiber shape, a cylindrical shape, a linear shape, a rod shape, or a coil shape. Also, the material is not limited.

例えば、ニッケル、金、銀、パラジウム、白金、イリジウム、銅、インジウム、コバルト、リチウムなどの金属微粒子、アルミナ、シリカ、チタニア、酸化亜鉛、酸化銅、酸化マグネシウム、インジュウム・スズ酸化物(ITO)などの金属酸化物微粒子、金属窒化物微粒子などの金属非酸化物微粒子、鉛錯体、コバルト錯体、ニッケル錯体、白金錯体などの金属錯体微粒子、フラーレン、カーボンブラック、カーボンファイバ、ケッチェンブラック、カーボンナノチューブ、カーボンナノコイル、カーボンナノホーンなどのカーボン系微粒子、ポリテトラフルオロエチレン、ポリプロピレン、ポリカーボネイト、ウレタン樹脂、シリコーン樹脂、シリコーンゴム、フェノール樹脂、ポリエチレン、ナイロン樹脂、ポリスチレンなどのポリマー微粒子が挙げられる。   For example, metal particles such as nickel, gold, silver, palladium, platinum, iridium, copper, indium, cobalt, lithium, alumina, silica, titania, zinc oxide, copper oxide, magnesium oxide, indium tin oxide (ITO), etc. Metal oxide fine particles, metal non-oxide fine particles such as metal nitride fine particles, metal complex fine particles such as lead complex, cobalt complex, nickel complex, platinum complex, fullerene, carbon black, carbon fiber, ketjen black, carbon nanotube, Carbon-based fine particles such as carbon nanocoils and carbon nanohorns, polymers such as polytetrafluoroethylene, polypropylene, polycarbonate, urethane resin, silicone resin, silicone rubber, phenol resin, polyethylene, nylon resin, polystyrene Fine particles.

また、超臨界状態または亜臨界状態の流体を用いた場合には、以下の利点がある。
(1)高圧容器内ではポリマー微粒子、金属錯体を溶解することができる。
(2)高圧容器中では通常の液体よりも粘性抵抗が低いため、撹拌動力が低くて済む。
(3)高圧容器中の微粒子をポリマー射出成型に利用する場合、ポリマーの流動性を上げられる(粘度を下げる)。
(4)高圧容器中の微粒子を吹き付ける対象物がポリマー基材である場合、表面膨潤効果がある。
Further, when a supercritical or subcritical fluid is used, there are the following advantages.
(1) Polymer fine particles and metal complexes can be dissolved in a high-pressure vessel.
(2) Since the viscous resistance is lower than that of a normal liquid in a high-pressure vessel, the stirring power is low.
(3) When the fine particles in the high-pressure vessel are used for polymer injection molding, the fluidity of the polymer can be increased (the viscosity is decreased).
(4) When the object to which fine particles in the high-pressure vessel are sprayed is a polymer substrate, there is a surface swelling effect.

カーボンナノチューブ、カーボンナノコイル、金属微粒子などのような凝集性の高い微小固体の場合、高圧容器中で凝集するので一定濃度での供給が難しいことから、本発明が特に有効である。
混合物は、微小固体の分散性を向上させる分散剤のような各種添加剤を含んでもよい。分散剤としては、例えば界面活性剤が用いられる。微小固体と流体との混合物は、クロロホルム、エタノール等の有機溶媒や水等の溶媒をさらに含んでもよい。
In the case of minute solids with high cohesive properties such as carbon nanotubes, carbon nanocoils, and metal fine particles, the present invention is particularly effective because it aggregates in a high-pressure vessel and is difficult to supply at a constant concentration.
The mixture may contain various additives such as a dispersant that improves the dispersibility of the fine solid. As the dispersant, for example, a surfactant is used. The mixture of the fine solid and the fluid may further contain an organic solvent such as chloroform and ethanol, and a solvent such as water.

本発明の高圧容器の例を示す概略断面図である。It is a schematic sectional drawing which shows the example of the high pressure container of this invention. 本発明の高圧容器の例における要部を示す概略斜視図である。It is a schematic perspective view which shows the principal part in the example of the high pressure container of this invention. 本発明の高圧容器の他の例における要部を示す概略斜視図である。It is a schematic perspective view which shows the principal part in the other example of the high pressure container of this invention. 本発明の供給方法の例を示す概略斜視図である。It is a schematic perspective view which shows the example of the supply method of this invention. 本発明の供給方法の他の例を示す概略斜視図である。It is a schematic perspective view which shows the other example of the supply method of this invention.

符号の説明Explanation of symbols

1・・容器本体、2・・バルブ、4・・サイホン管、5・・撹拌体、6・・高圧容器、7・・回転盤、8・・ローラ、9・・フレキシブル配管、10・・固定配管、11・・接続金具 1 .. Container body, 2 .. Valve, 4 .. Siphon tube, 5 .. Stirring body, 6. Piping, 11. ・ Connecting bracket

Claims (6)

少なくとも1種の流体を含む混合物を貯蔵する容器本体と、前記容器本体の開口を塞ぐバルブを有する高圧容器であって、
前記容器本体又は前記バルブに、前記高圧容器の回転または回動により前記混合物を撹拌する撹拌体が固定されたことを特徴とする高圧容器。
A high-pressure container having a container body for storing a mixture containing at least one fluid, and a valve for closing an opening of the container body,
A high-pressure container, wherein a stirring body for stirring the mixture by rotation or rotation of the high-pressure container is fixed to the container main body or the valve.
前記撹拌体は、前記バルブに取り付けられた混合流体導出管に固定されていることを特徴とする請求項1記載の高圧容器。   The high-pressure vessel according to claim 1, wherein the agitator is fixed to a mixed fluid outlet pipe attached to the valve. 請求項1または2に記載された高圧容器を用い、この高圧容器に充填された少なくとも1種の流体を含む混合物を前記高圧容器から導出する供給方法であって、
前記高圧容器の回転または回動により前記混合物を撹拌した後に前記混合物を前記高圧容器から導出することを特徴とする混合物の供給方法。
A method for supplying a mixture containing at least one fluid filled in the high-pressure vessel from the high-pressure vessel using the high-pressure vessel according to claim 1 or 2,
A method for supplying a mixture, comprising: stirring the mixture by rotation or rotation of the high-pressure vessel and then extracting the mixture from the high-pressure vessel.
前記混合物が、微小固体を含むことを特徴とする請求項3記載の混合物の供給方法。   The method of supplying a mixture according to claim 3, wherein the mixture contains a fine solid. 前記流体が、常温・加圧で液化する液化ガスであることを特徴とする請求項3記載の混合物の供給方法。   The method for supplying a mixture according to claim 3, wherein the fluid is a liquefied gas that liquefies at room temperature and pressure. 前記液化ガスが、超臨界状態または亜臨界状態であることを特徴とする請求項5記載の混合物の供給方法。   The method for supplying a mixture according to claim 5, wherein the liquefied gas is in a supercritical state or a subcritical state.
JP2008171260A 2008-06-30 2008-06-30 High-pressure vessel and method of supplying a mixture using the same Expired - Fee Related JP5192927B2 (en)

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Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57148428U (en) * 1981-03-12 1982-09-17
JPS6187298U (en) * 1984-11-13 1986-06-07
JPH0160291B2 (en) * 1983-03-07 1989-12-21 Matsushita Electric Works Ltd
JPH0681711U (en) * 1993-05-07 1994-11-22 稔 大橋 Sludge production equipment
JP2000061282A (en) * 1998-08-24 2000-02-29 Toda Kogyo Corp Granule mixer
JP2001219047A (en) * 2000-02-07 2001-08-14 Yoshiko Ikeda Agitating method using agitation container having polygonal cylindrical filling volume
JP2007014889A (en) * 2005-07-08 2007-01-25 Shikoku Instrumentation Co Ltd Array-coating method and apparatus for microparticle by supercritical fluid
JP2007321934A (en) * 2006-06-02 2007-12-13 Hitachi Maxell Ltd Storage container, resin forming method, and plating film forming method

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57148428U (en) * 1981-03-12 1982-09-17
JPH0160291B2 (en) * 1983-03-07 1989-12-21 Matsushita Electric Works Ltd
JPS6187298U (en) * 1984-11-13 1986-06-07
JPH0681711U (en) * 1993-05-07 1994-11-22 稔 大橋 Sludge production equipment
JP2000061282A (en) * 1998-08-24 2000-02-29 Toda Kogyo Corp Granule mixer
JP2001219047A (en) * 2000-02-07 2001-08-14 Yoshiko Ikeda Agitating method using agitation container having polygonal cylindrical filling volume
JP2007014889A (en) * 2005-07-08 2007-01-25 Shikoku Instrumentation Co Ltd Array-coating method and apparatus for microparticle by supercritical fluid
JP2007321934A (en) * 2006-06-02 2007-12-13 Hitachi Maxell Ltd Storage container, resin forming method, and plating film forming method

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