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JP2017070875A - Cyclone type separator - Google Patents

Cyclone type separator Download PDF

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JP2017070875A
JP2017070875A JP2015197563A JP2015197563A JP2017070875A JP 2017070875 A JP2017070875 A JP 2017070875A JP 2015197563 A JP2015197563 A JP 2015197563A JP 2015197563 A JP2015197563 A JP 2015197563A JP 2017070875 A JP2017070875 A JP 2017070875A
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inflow
outflow
separator
pipe
liquid
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荘一郎 大崎
Soichiro Osaki
荘一郎 大崎
雅樹 武石
Masaki Takeishi
雅樹 武石
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NIKUNI CORP
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Abstract

PROBLEM TO BE SOLVED: To provide a cyclone type separator capable of being easily installed.SOLUTION: A cyclone type separator includes a separator body 4 where solid matter is separated while swirling a solid matter mixed liquid 2 inside and a separated liquid 3 is flown out to one side in an axial direction. A connection body 5 is disposed at the upper part of the separator body 4. The connection body 5 has an introduction passage 12 guiding the solid matter mixed liquid 2 from an inflow pipe into the separator body 4. The connection body 5 has a lead-out passage 13 guiding the separated liquid 3 from the separator body 4 to an outflow pipe. The introduction passage 12 has an inflow part 14 approximately parallel to the inflow pipe and an inflow detour part 15 guiding the solid matter mixed liquid 2 from the inflow part 14 to the inner peripheral surface of the separator body 4 in a tangential direction. The lead-out passage 13 has an outflow part 21 connected to the separator body 4 in an axial direction and an outflow detour part 22 guiding the separated liquid 3 from the outflow part 21 to the outflow pipe approximately parallel to the outflow pipe.SELECTED DRAWING: Figure 1

Description

本発明は、液体から固形物を分離除去するためのサイクロン式分離器に関する。   The present invention relates to a cyclonic separator for separating and removing solids from a liquid.

例えば工作機械から排出されたクーラント液等の液体から、スラッジ等の固形物を分離除去するサイクロン式分離器では、逆円錐形状の分離器本体内にて液体を旋回させながら固形物を分離する。   For example, in a cyclone separator that separates and removes solids such as sludge from a liquid such as a coolant discharged from a machine tool, the solids are separated while swirling the liquid in an inverted conical separator body.

この種のサイクロン式分離器では、分離器本体内で液体を適切に旋回させるために、汚水へ作用する遠心力を損なわないよう分離器本体内へ液体を流入させるとともに、液体へ作用する遠心力を損なわないよう固形物除去後の液体を分離器本体から流出させることが重要である。   In this type of cyclonic separator, in order to properly swirl the liquid in the separator body, the liquid flows into the separator body so as not to impair the centrifugal force acting on the sewage, and the centrifugal force acting on the liquid. It is important that the liquid after removing the solid matter is allowed to flow out of the separator main body so as not to damage the surface.

そのため、特許文献1および特許文献2のように、通常は、サイクロン式分離器の上流側に位置する流入配管が分離器本体の接線方向に接続され、サイクロン式分離器の下流側に位置する流出配管が分離器本体の軸方向の一端部である上端部から鉛直(流入側配管に対して略垂直)に接続された構成において、液体を分離器本体内へ接線方向に流入させ、かつ、分離器本体の軸方向に液体を流出させる。   Therefore, as in Patent Document 1 and Patent Document 2, normally, the inflow pipe located upstream of the cyclone separator is connected in the tangential direction of the separator body, and the outflow located downstream of the cyclone separator. In a configuration in which the pipe is connected vertically (substantially perpendicular to the inflow side pipe) from the upper end, which is one end in the axial direction of the separator body, the liquid flows into the separator body in the tangential direction and is separated. The liquid flows out in the axial direction of the vessel body.

特開2014−87744号公報JP 2014-87744 A 特開2015−39660号公報JP2015-39660A

ここで、サイクロン式分離器以外の例えばフィルタ式等の分離器が設置された既存の設備では、上流側の流入配管と下流側の流出配管とが互い略平行に配置されたいわゆるインライン型が一般的である。   Here, in an existing facility in which a separator such as a filter type other than a cyclone separator is installed, a so-called in-line type in which an upstream inflow pipe and a downstream outflow pipe are arranged substantially parallel to each other is generally used. Is.

そのため、このような既存の設備における既存の分離器に代えてサイクロン式分離器を設置するには、既存の設備の流入配管や流出配管に対して、分離器本体への流入経路や分離器本体からの流出経路を調整する必要がある。   Therefore, in order to install a cyclonic separator in place of the existing separator in such existing equipment, the inflow path to the separator body and the separator body with respect to the inflow pipe and outflow pipe of the existing equipment It is necessary to adjust the outflow route from

すなわち、例えば、流入配管および流出配管の一方に継ぎ手等を介して接続させたり、特許文献2の図5のように分離器本体から液体を分離器本体の上部の上部室へ一旦排出させて、この上部室から流出側配管へ液体を流出させたり、流入配管および流出配管の一方を鉛直に施工し直したりして、設計し直す必要があり、容易に設置できない問題が考えられる。   That is, for example, it is connected to one of the inflow pipe and the outflow pipe via a joint or the like, or the liquid is once discharged from the separator body into the upper chamber of the upper part of the separator body as shown in FIG. There is a problem that it is necessary to re-design the liquid from the upper chamber to the outflow side piping or to reconstruct one of the inflow piping and the outflow piping vertically, which cannot be easily installed.

したがって、例えばインライン型の配管経路である既存の設備であっても、容易に設置できるサイクロン式分離器が求められていた。   Therefore, for example, there has been a demand for a cyclonic separator that can be easily installed even with existing equipment that is an inline piping route.

本発明はこのような点に鑑みなされたもので、容易に設置できるサイクロン式分離器を提供することを目的とする。   The present invention has been made in view of these points, and an object thereof is to provide a cyclonic separator that can be easily installed.

請求項1に記載されたサイクロン式分離器は、流入配管から流入する固形物が混入した固形物混入液体を内部で旋回させながら固形物を分離除去し、その固形物を分離除去後の分離液体を流出配管へ流出するサイクロン式分離器であって、前記固形物混入液体を内部で旋回させながら前記固形物を分離し、前記分離液体を軸方向の一方側へ流出させる分離器本体と、前記流入配管と前記流出配管と前記分離器本体とに接続され、前記流入配管からの前記固形物混入液体を前記分離器本体内へ流入させ、前記分離器本体からの前記分離液体を前記流出配管へ流出させる接続体とを具備し、前記接続体は、前記流入配管および前記分離器本体内に連通して前記流入配管からの固形物混入液体を前記分離器本体内へ案内する導入路と、前記流出配管および前記分離器本体内に連通して前記分離器本体からの前記分離液体を前記流出配管へ案内する導出路とを有し、前記導入路は、前記流入配管に接続される流入部と、前記流入部に交差するように接続されて、前記分離器本体の内周面に対し接線方向に前記固形物混入液体を案内する流入迂回部とを有し、前記導出路は、前記分離器本体の軸方向の一方側に接続された流出部と、前記流出部に交差するように接続されかつ前記流出配管に接続される流出迂回部とを有し、前記流入部と前記流出迂回部とが互いに略平行に配置されているものである。   The cyclone separator according to claim 1 separates and removes the solid matter while rotating the solid matter mixed liquid mixed with the solid matter flowing in from the inflow pipe, and the separated liquid is separated and removed. A separator main body that separates the solid matter while swirling the solid-containing liquid inside, and causes the separated liquid to flow to one side in the axial direction, Connected to the inflow pipe, the outflow pipe, and the separator main body, the solid mixed liquid from the inflow pipe flows into the separator main body, and the separation liquid from the separator main body flows into the outflow pipe A connecting body for flowing out, and the connecting body communicates with the inflow pipe and the separator main body to guide the solid mixed liquid from the inflow pipe into the separator main body; and Outflow piping And a lead-out path that communicates with the separator main body and guides the separated liquid from the separator main body to the outflow pipe, and the introduction path includes an inflow portion connected to the inflow pipe; An inflow detour portion that is connected so as to intersect the inflow portion and guides the solid-mixed liquid in a tangential direction with respect to the inner peripheral surface of the separator body, and the outlet path of the separator body An outflow portion connected to one side in the axial direction, and an outflow bypass portion connected to the outflow pipe so as to intersect the outflow portion, and the inflow portion and the outflow bypass portion are mutually connected They are arranged substantially in parallel.

請求項2に記載されたサイクロン式分離器は、請求項1記載のサイクロン式分離器において、接続体は、流入部と流出迂回部とが互いに延長線上に配置され、流入迂回部は、前記流出迂回部の下方を回り込むように配置されているものである。   The cyclonic separator according to claim 2 is the cyclonic separator according to claim 1, wherein the connecting body is configured such that the inflow portion and the outflow bypass portion are arranged on an extension line, and the inflow bypass portion is connected to the outflow portion. It is arrange | positioned so that it may wrap around under the detour part.

本発明によれば、流入部と流出迂回部とが互いに略平行に配置されているため、流入配管および流出配管に容易に接続でき、容易に設置できる。   According to the present invention, since the inflow portion and the outflow detour portion are arranged substantially parallel to each other, they can be easily connected to the inflow piping and the outflow piping and can be easily installed.

本発明の一実施の形態に係るサイクロン式分離器の構成を示す一部を破断した構成図である。It is the block diagram which fractured | ruptured a part which shows the structure of the cyclonic separator which concerns on one embodiment of this invention. 同上サイクロン式分離器における接続体を示す断面図である。It is sectional drawing which shows the connection body in a cyclone type separator same as the above. 同上サイクロン式分離器における接続体の導入路を示す断面図である。It is sectional drawing which shows the introduction path of the connection body in a cyclone type separator same as the above.

以下、一実施の形態の構成について図面を参照しながら詳細に説明する。   Hereinafter, the configuration of an embodiment will be described in detail with reference to the drawings.

図1において、1はサイクロン式分離器であり、このサイクロン式分離器1は、例えば工作機械のクーラント液等の汚水である液体を処理する液処理システムの配管経路に設置されて、スラッジ等の固形物が混入した固形物混入液体2から固形物を分離除去するものである。   In FIG. 1, reference numeral 1 denotes a cyclonic separator. The cyclonic separator 1 is installed in a piping path of a liquid processing system for processing a liquid which is sewage such as a coolant liquid of a machine tool, for example, sludge. The solid matter is separated and removed from the solid matter mixed liquid 2 mixed with the solid matter.

すなわち、サイクロン式分離器1は、配管経路において上流側に位置する図示しない流入配管と、配管経路において下流側に位置する図示しない流出配管との間に設置され、流入配管から流入する固形物混入液体2を内部で旋回させながら固形物を分離除去して、その固形物が分離除去された分離液体3を流出配管へ流出する。   That is, the cyclonic separator 1 is installed between an inflow pipe (not shown) located on the upstream side in the piping path and an outflow pipe (not shown) located on the downstream side in the pipe path, and contains solid matter flowing in from the inflow pipe. The solids are separated and removed while the liquid 2 is swirled inside, and the separated liquid 3 from which the solids have been separated and removed flows out to the outflow pipe.

サイクロン式分離器1は、内部で固形物混入液体2から固形物を分離除去する略逆円錐筒状の分離器本体4の上部に、液処理システムの配管経路に接続される接続体5が設けられている。   The cyclone separator 1 is provided with a connection body 5 connected to a pipe path of a liquid processing system on an upper portion of a substantially inverted conical cylindrical separator body 4 that separates and removes solid matter from a solid-containing liquid 2 inside. It has been.

分離器本体4は、固形物混入液体2が流入する略逆円錐筒状の円錐形部11を有する。この円錐形部11は、軸方向の一方側の端部である上端部に接続体5を介して固形物混入液体2が流入する図示しない流入口が設けられ、この流入口から軸方向の他方側である下方へ向かって小径となるテーパ状に形成されている。   The separator body 4 has a substantially inverted conical cylindrical portion 11 into which the solid-containing liquid 2 flows. The conical portion 11 is provided with an inflow port (not shown) through which the solid substance mixed liquid 2 flows through the connecting body 5 at an upper end portion which is an end portion on one side in the axial direction. It is formed in a tapered shape having a smaller diameter toward the lower side.

また、流入口内には、図示しない円筒状の内筒部が同心状に取り付けられている。この内筒部は、円錐形部11から流入する分離液体3が上端部の流出口から流出する。すなわち、分離器本体4は、円錐形部11で固形物を分離した分離液体3が流出口を通って軸方向の一方側へ流出する。   A cylindrical inner cylinder portion (not shown) is concentrically attached in the inflow port. In the inner tube portion, the separation liquid 3 flowing from the conical portion 11 flows out from the outlet at the upper end. That is, in the separator body 4, the separation liquid 3 from which the solid matter is separated by the conical portion 11 flows out to one side in the axial direction through the outlet.

分離器本体4の軸方向の他方側の端部である下端部には、固形物混入液体2から分離された固形物が貯留される図示しない貯留部であるスラッジポットが接続される。   A sludge pot, which is a storage part (not shown) in which the solid matter separated from the solid matter mixed liquid 2 is stored, is connected to the lower end part that is the other end part in the axial direction of the separator body 4.

そして、分離器本体4は、流入口を通って内部に流入した固形物混入液体2を、円錐形部11と内筒部との間で旋回させるとともに円錐形部11の内周面のテーパに沿って下方へ流動させながら、固形物混入液体2から固形物を遠心分離する。また、分離した固形物を円錐形部11内の下部に沈殿させるとともに、固形物が分離された分離液体3を流出口から軸方向の一方側である上方へ流出させる。なお、固形物混入液体2から分離された固形物は、円錐形部11からスラッジポットへ排出される。   The separator body 4 swirls the solid-mixed liquid 2 that has flowed into the interior through the inflow port between the conical portion 11 and the inner cylindrical portion, and has a taper on the inner peripheral surface of the conical portion 11. The solid is centrifuged from the solid-containing liquid 2 while flowing downward along the line. Further, the separated solid matter is precipitated at the lower part in the conical portion 11, and the separation liquid 3 from which the solid matter has been separated is caused to flow upward from the outflow port, which is one side in the axial direction. Note that the solid matter separated from the solid matter mixed liquid 2 is discharged from the conical portion 11 to the sludge pot.

図2に示すように、接続体5は、流入配管および分離器本体4内部に連通する導入路12と、流出配管および分離器本体4内部に連通する導出路13とを有している。そして、導入路12は、流入配管からの固形物混入液体2を分離器本体4内における円錐形部11と内筒部との間へ案内し、導出路13は、分離器本体4の流出口からの分離液体3を流出配管へ案内する。   As shown in FIG. 2, the connection body 5 has an introduction path 12 that communicates with the inside of the inflow pipe and the separator body 4, and a lead-out path 13 that communicates with the inside of the outflow pipe and the separator body 4. The introduction path 12 guides the solid-mixed liquid 2 from the inflow pipe between the conical part 11 and the inner cylinder part in the separator main body 4, and the outlet path 13 is an outlet of the separator main body 4. The separated liquid 3 is guided to the outflow pipe.

導入路12は、流入配管に接続される流入部14が、流入配管と略平行になるように設けられている。すなわち、流入部14は、流入配管から略水平に断面視で直線状に開口されている。   The introduction path 12 is provided so that the inflow portion 14 connected to the inflow pipe is substantially parallel to the inflow pipe. That is, the inflow portion 14 is opened from the inflow piping in a straight line shape in a cross-sectional view substantially horizontally.

流入部14の中間部分には、流入迂回部15が接続されている。この流入迂回部15は、流入部14から略垂直に下方へ直線状に開口された第1の迂回部16と、この第1の迂回部16の下端部から略垂直に水平方向に開口された第2の迂回部17とを有している。すなわち、流入迂回部15は、流入部14から下方へ断面視で略L字状に形成されている。   An inflow detour portion 15 is connected to an intermediate portion of the inflow portion 14. The inflow detour portion 15 has a first detour portion 16 that is linearly opened downward from the inflow portion 14 in a straight line and a lower end portion of the first detour portion 16 that is substantially vertically opened in the horizontal direction. And a second detour unit 17. That is, the inflow detour portion 15 is formed in an approximately L shape in a cross-sectional view from the inflow portion 14 downward.

第2の迂回部17における第1の迂回部16とは反対側である先端部には、円形状に開口され円錐形部11の流入口に連通した流入開口部18が接続されている。この流入開口部18は、円錐形部11の流入口と同心状に配置されている。   An inflow opening 18 that is opened in a circular shape and communicates with the inflow port of the conical portion 11 is connected to the tip of the second detouring portion 17 that is opposite to the first detouring portion 16. The inflow opening 18 is disposed concentrically with the inlet of the conical portion 11.

第2の迂回部17は、流入開口部18の内周面に対して接線方向に接続されている。すなわち、第2の迂回部17は、流入開口部18を介して円錐形部11の内周面に対し接線方向に固形物混入液体2を案内する。   The second bypass portion 17 is connected in a tangential direction to the inner peripheral surface of the inflow opening 18. That is, the second detour portion 17 guides the solid-mixed liquid 2 through the inflow opening 18 in the tangential direction with respect to the inner peripheral surface of the conical portion 11.

なお、導入路12では、流入迂回部15の開口面積が流入部14の開口面積より小さいと、固形物混入液体2が流入部14から流入迂回部15に流入する際に開口面積の違いにより加圧されて、流入迂回部15から流入開口部18に流入させる固形物混入液体2に旋回力が付与されやすいので好ましい。   In addition, in the introduction path 12, if the opening area of the inflow detour portion 15 is smaller than the opening area of the inflow portion 14, the solid mixed liquid 2 is added due to the difference in opening area when flowing into the inflow detour portion 15 from the inflow portion 14. This is preferable because a swirl force is easily applied to the solid-mixed liquid 2 that is pressed and flows into the inflow opening 18 from the inflow detour portion 15.

導出路13は、断面視で鉛直方向に直線状に開口された流出部21が、分離器本体4の内筒部の流出口の下端部に接続されている。すなわち、流出部21は、分離器本体4に対して軸方向に接続されて、内筒部の流出口と同心状に配置されている。   In the lead-out path 13, an outflow portion 21 that is opened linearly in a vertical direction in a cross-sectional view is connected to the lower end portion of the outlet of the inner cylinder portion of the separator body 4. That is, the outflow portion 21 is connected to the separator body 4 in the axial direction and is arranged concentrically with the outlet of the inner cylinder portion.

流出部21における内筒部とは反対側の上端部には、この流出部21とは略垂直な流出迂回部22が接続されている。   An outflow detour portion 22 that is substantially perpendicular to the outflow portion 21 is connected to the upper end portion of the outflow portion 21 opposite to the inner cylinder portion.

この流出迂回部22は、略水平に直線状に開口されて流出配管に接続される。また、流出迂回部22は、流出配管に略平行に配置され、かつ、流入迂回部15における第2の迂回部17の上方に位置するように配置されている。   The outflow detour portion 22 is opened substantially linearly in a straight line and connected to the outflow pipe. In addition, the outflow detour portion 22 is disposed substantially parallel to the outflow pipe and is disposed above the second detour portion 17 in the inflow detour portion 15.

すなわち、接続体5では、流入部14と流出迂回部22とが略水平に互いに延長線上に位置するように配置され、流入迂回部15が、流出迂回部22の下方を回り込むように配置されている。   That is, in the connecting body 5, the inflow portion 14 and the outflow detour portion 22 are disposed so as to be positioned on the extension line substantially horizontally, and the inflow detour portion 15 is disposed so as to wrap around under the outflow detour portion 22. Yes.

なお、接続体5を形成する際には、例えばまず金型を用いて図3に示す導入路12を有する成形体を射出成形した後、別の金型を用いて導入路12を有する成形体の上部に導出路13を有する成形体を射出成形して一体成形する。   When forming the connection body 5, for example, a molded body having the introduction path 12 shown in FIG. 3 is first injection-molded using a mold, and then a molded body having the introduction path 12 using another mold. A molded body having a lead-out path 13 in the upper part is injection-molded and integrally molded.

次に、上記一実施の形態の作用および効果を説明する。   Next, the operation and effect of the one embodiment will be described.

サイクロン式分離器1で、固形物混入液体2から固形物を分離除去する際には、まず、固形物混入液体2が流入配管から接続体5の導入路12へ流入する。   When the solid matter is separated and removed from the solid matter mixed liquid 2 by the cyclone separator 1, first, the solid matter mixed liquid 2 flows into the introduction path 12 of the connection body 5 from the inflow pipe.

導入路12では、固形物混入液体2が流入部14から第1の迂回部16を通って第2の迂回部17に流入し、その後、第2の迂回部17から流入開口部18に内周面に対して接線方向に流入する。   In the introduction path 12, the solid mixed liquid 2 flows from the inflow portion 14 through the first detour portion 16 to the second detour portion 17, and then from the second detour portion 17 to the inflow opening 18. Inflows tangential to the surface.

流入開口部18の内周面の接線方向に流入した固形物混入液体2は、流入開口部18の内周面を旋回しながら流入口から円錐形部11内へ流入する。   The solid-mixed liquid 2 that has flowed in the tangential direction of the inner peripheral surface of the inflow opening 18 flows into the conical portion 11 from the inlet while swirling on the inner peripheral surface of the inflow opening 18.

円錐形部11では、固形物混入液体2が、旋回流となって円錐形部11のテーパに沿って下方へ流動し、遠心力によって比重差に基づき固液分離される。   In the conical portion 11, the solid-containing liquid 2 becomes a swirling flow and flows downward along the taper of the conical portion 11, and is separated into solid and liquid by centrifugal force based on the specific gravity difference.

また、固形物混入液体2から分離された固形物は、円錐形部11の下部に沈殿されてスラッジポットに貯留され、固形物が分離された分離液体3は、内筒部を通って分離器本体4の軸方向(上方)へ流動する。   Further, the solid separated from the solid-containing liquid 2 is precipitated in the lower part of the conical part 11 and stored in the sludge pot, and the separated liquid 3 from which the solid is separated passes through the inner cylinder part and is separated into a separator. It flows in the axial direction (upward) of the main body 4.

また分離液体3は、そのまま内筒部から流出部21内へ流動し、流出部21から流出迂回部22を通って流出配管へ流出される。   Further, the separation liquid 3 flows from the inner cylinder portion into the outflow portion 21 as it is, and flows out from the outflow portion 21 through the outflow bypass portion 22 to the outflow pipe.

そして、上記サイクロン式分離器1では、例えば流入配管と流出配管とが平行に配置されたいわゆるインライン型の配管経路内に設置する場合であっても、流入部14と流出迂回部22とが互いに平行に配置されているため、配管経路等を設計し直す必要がない。すなわち、新たな設備であっても既存の設備であっても、流入部14を流入配管に容易に接続でき、流出迂回部22を流出配管に容易に接続できるため、サイクロン式分離器1を容易に設置できる。なお、例えばフィルタ型分離器に対してサイクロン式分離器は、フィルタが不要であるためメンテナンスが容易であるが、フィルタ式分離器はインライン型の配管経路に設置されていることが多く、フィルタ式分離器を従来のサイクロン式分離器に変更する際には、配管経路の設計変更や継ぎ手等を用いる必要があったが、上記サイクロン式分離器1は、インライン型の配管経路でも容易に適用できる。   In the cyclone separator 1, the inflow portion 14 and the outflow detour portion 22 are connected to each other even if the inflow piping and the outflow piping are installed in a so-called in-line piping path, for example. Since they are arranged in parallel, there is no need to redesign the piping route. That is, since the inflow section 14 can be easily connected to the inflow pipe and the outflow bypass section 22 can be easily connected to the outflow pipe, whether it is a new facility or an existing facility, the cyclone separator 1 can be easily used. Can be installed. For example, a cyclonic separator is easy to maintain because a filter is not required for a filter type separator, but the filter type separator is often installed in an in-line type piping path. When the separator is changed to a conventional cyclone separator, it is necessary to use a design change of a piping route, a joint, or the like. However, the cyclone separator 1 can be easily applied to an inline piping route. .

また、導入路12が流入部14および流入迂回部15を有するため、流入配管から流入部14へ流入した固形物混入液体2を、流入迂回部15を介して円錐形部11の接線方向にスムーズに案内できるため、固形物混入液体2を分離器本体4内へ流入させる際に、分離器本体4内での旋回のための遠心力を損ないにくい。   In addition, since the introduction path 12 has the inflow portion 14 and the inflow bypass portion 15, the solid mixed liquid 2 that has flowed into the inflow portion 14 from the inflow pipe is smoothly passed through the inflow bypass portion 15 in the tangential direction of the conical portion 11. Therefore, it is difficult to impair the centrifugal force for swirling in the separator body 4 when the solid-containing liquid 2 flows into the separator body 4.

さらに、導出路13が流出部21と流出迂回部22とを有するため、分離液体3を分離器本体4から流出部21へ軸方向にスムーズに流出でき、分離器本体4内における分離液体3の流動が阻害されにくい。   Further, since the outlet path 13 has the outflow portion 21 and the outflow bypass portion 22, the separation liquid 3 can smoothly flow out in the axial direction from the separator body 4 to the outflow portion 21, and the separation liquid 3 in the separator body 4 can be discharged. The flow is difficult to be disturbed.

接続体5は、流入部14と流出迂回部22とが互いに延長線上に配置されているため、インライン型の配管経路に適用しやすい。   Since the inflow part 14 and the outflow detour part 22 are mutually arranged on the extension line, the connection body 5 is easy to apply to the in-line type piping route.

また、接続体5は、流入迂回部15が流出迂回部22の下方を回り込むように配置されているため、流入迂回部15によって固形物混入液体2を正確に分離器本体4の接線方向に案内できるとともに、コンパクトに設計できる。   In addition, the connecting body 5 is arranged such that the inflow detour portion 15 wraps around the lower portion of the outflow detour portion 22, so that the solid substance mixed liquid 2 is accurately guided in the tangential direction of the separator body 4 by the inflow detour portion 15. It can be designed compactly.

導入路12は、流入迂回部15の開口面積が流入部14の開口面積より小さいことにより、導入路12を流動する固形物混入液体2が開口面積の違いにより加圧され、流入開口部18に流入する固形物混入液体2に旋回力が付与されやすい。   In the introduction path 12, since the opening area of the inflow detour portion 15 is smaller than the opening area of the inflow section 14, the solid mixed liquid 2 flowing through the introduction path 12 is pressurized due to the difference in the opening area, A turning force is easily applied to the inflowing solid-containing liquid 2.

なお、上記一実施の形態では、接続体5は、流入部14と流出迂回部22とが互いに延長線上に配置された構成としたが、流入部14と流出迂回部22とが互いに平行な構成であれば、適宜変更できる。   In the above-described embodiment, the connection body 5 is configured such that the inflow portion 14 and the outflow detour portion 22 are arranged on an extension line. However, the inflow portion 14 and the outflow detour portion 22 are parallel to each other. If so, it can be appropriately changed.

また、接続体5は、流入迂回部15が流出迂回部22の下方を回り込むように配置された構成としたが、流入迂回部15が固形物混入液体2を分離器本体4の接線方向に案内でき、かつ、流入部14と流出迂回部22とが互いに平行な構成であれば、適宜変更できる。   In addition, the connecting body 5 is configured such that the inflow detour portion 15 is arranged so as to wrap around the lower portion of the outflow detour portion 22, but the inflow detour portion 15 guides the solid-mixed liquid 2 in the tangential direction of the separator body 4. If the inflow portion 14 and the outflow bypass portion 22 are configured to be parallel to each other, they can be changed as appropriate.

分離器本体4の下部にスラッジポットが設けられた構成としたが、このような構成には限定されず、例えば分離器本体4の外部を覆うようにカバー体を設け、このカバー体と分離器本体4との間にスラッジ等の分離した固形物を貯留する貯留部が設けられた構成等にしてもよい。   Although the sludge pot is provided in the lower part of the separator body 4, the present invention is not limited to such a structure. For example, a cover body is provided so as to cover the outside of the separator body 4, and the cover body and the separator are provided. You may make it the structure etc. which were provided with the storage part which stores the solid substances isolate | separated, such as sludge, between the main bodies 4.

1 サイクロン式分離器
2 固形物混入液体
3 分離液体
4 分離器本体
5 接続体
12 導入路
13 導出路
14 流入部
15 流入迂回部
21 流出部
22 流出迂回部
DESCRIPTION OF SYMBOLS 1 Cyclone type separator 2 Solid substance mixing liquid 3 Separation liquid 4 Separator main body 5 Connection body
12 Introduction route
13 Derived path
14 Inflow part
15 Inflow bypass
21 Outflow area
22 Outflow detour

Claims (2)

流入配管から流入する固形物が混入した固形物混入液体を内部で旋回させながら固形物を分離除去し、その固形物を分離除去後の分離液体を流出配管へ流出するサイクロン式分離器であって、
前記固形物混入液体を内部で旋回させながら前記固形物を分離し、前記分離液体を軸方向の一方側へ流出させる分離器本体と、
前記流入配管と前記流出配管と前記分離器本体とに接続され、前記流入配管からの前記固形物混入液体を前記分離器本体内へ流入させ、前記分離器本体からの前記分離液体を前記流出配管へ流出させる接続体とを具備し、
前記接続体は、前記流入配管および前記分離器本体内に連通して前記流入配管からの固形物混入液体を前記分離器本体内へ案内する導入路と、前記流出配管および前記分離器本体内に連通して前記分離器本体からの前記分離液体を前記流出配管へ案内する導出路とを有し、
前記導入路は、前記流入配管に接続される流入部と、前記流入部に交差するように接続されて、前記分離器本体の内周面に対し接線方向に前記固形物混入液体を案内する流入迂回部とを有し、
前記導出路は、前記分離器本体の軸方向の一方側に接続された流出部と、前記流出部に交差するように接続されかつ前記流出配管に接続される流出迂回部とを有し、
前記流入部と前記流出迂回部とが互いに略平行に配置されている
ことを特徴とするサイクロン式分離器。
A cyclone separator that separates and removes solid matter while swirling the solid matter mixed liquid mixed with the solid matter that flows in from the inflow pipe, and flows the separated liquid to the outflow pipe after separating and removing the solid matter. ,
A separator main body that separates the solid matter while swirling the solid-containing liquid inside, and causes the separated liquid to flow out to one side in the axial direction;
Connected to the inflow pipe, the outflow pipe, and the separator body, the solid mixed liquid from the inflow pipe flows into the separator body, and the separation liquid from the separator body flows into the outflow pipe. And a connecting body for flowing out to
The connecting body communicates with the inflow pipe and the separator main body to introduce a solid mixed liquid from the inflow pipe into the separator main body, and into the outflow pipe and the separator main body. A lead-out path that communicates and guides the separated liquid from the separator body to the outflow pipe;
The introduction path is connected to the inflow portion connected to the inflow pipe, and the inflow portion is connected so as to intersect the inflow portion, and guides the solid mixed liquid in a tangential direction with respect to the inner peripheral surface of the separator body. With a detour part,
The outlet path has an outflow portion connected to one side in the axial direction of the separator main body, and an outflow detour portion connected to the outflow pipe so as to intersect the outflow portion,
The cyclonic separator, wherein the inflow portion and the outflow detour portion are arranged substantially parallel to each other.
接続体は、流入部と流出迂回部とが互いに延長線上に配置され、
流入迂回部は、前記流出迂回部の下方を回り込むように配置されている
ことを特徴とする請求項1記載のサイクロン式分離器。
In the connection body, the inflow portion and the outflow detour portion are arranged on an extension line with each other,
The cyclonic separator according to claim 1, wherein the inflow detour portion is disposed so as to wrap around under the outflow detour portion.
JP2015197563A 2015-10-05 2015-10-05 Cyclone type separator Pending JP2017070875A (en)

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Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4950871U (en) * 1972-08-09 1974-05-04
JPS54128982U (en) * 1978-02-28 1979-09-07
JPS61291055A (en) * 1985-06-17 1986-12-20 ベロイト コ−ポレ−ション Cyclone separator
JPS61291054A (en) * 1985-06-17 1986-12-20 ベロイト コ−ポレ−ション Cyclone separator
JPS6231910U (en) * 1985-08-13 1987-02-25
JPS63305954A (en) * 1987-06-05 1988-12-13 Nippon Spindle Mfg Co Ltd Liquid cyclone
JP2011016131A (en) * 1999-04-15 2011-01-27 Hydro Internatl Plc Hydrodynamic separator
US20120097589A1 (en) * 2010-10-26 2012-04-26 Zodiac Pool Systems, Inc. Debris filter
JP2015131265A (en) * 2014-01-10 2015-07-23 村松風送設備工業株式会社 Dust separator

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4950871U (en) * 1972-08-09 1974-05-04
JPS54128982U (en) * 1978-02-28 1979-09-07
JPS61291055A (en) * 1985-06-17 1986-12-20 ベロイト コ−ポレ−ション Cyclone separator
JPS61291054A (en) * 1985-06-17 1986-12-20 ベロイト コ−ポレ−ション Cyclone separator
JPS6231910U (en) * 1985-08-13 1987-02-25
JPS63305954A (en) * 1987-06-05 1988-12-13 Nippon Spindle Mfg Co Ltd Liquid cyclone
JP2011016131A (en) * 1999-04-15 2011-01-27 Hydro Internatl Plc Hydrodynamic separator
US20120097589A1 (en) * 2010-10-26 2012-04-26 Zodiac Pool Systems, Inc. Debris filter
JP2015131265A (en) * 2014-01-10 2015-07-23 村松風送設備工業株式会社 Dust separator

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