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JP2006130034A - Centrifugal dust collector and vacuum cleaner using the same - Google Patents

Centrifugal dust collector and vacuum cleaner using the same Download PDF

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JP2006130034A
JP2006130034A JP2004321660A JP2004321660A JP2006130034A JP 2006130034 A JP2006130034 A JP 2006130034A JP 2004321660 A JP2004321660 A JP 2004321660A JP 2004321660 A JP2004321660 A JP 2004321660A JP 2006130034 A JP2006130034 A JP 2006130034A
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flow
separation chamber
dust
dust collector
centrifugal
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Makoto Murakami
誠 村上
Hiromi Hirota
弘美 広田
Hiroyuki Kayama
博之 香山
Hiroaki Kurihara
裕明 栗原
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Panasonic Holdings Corp
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Matsushita Electric Industrial Co Ltd
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Abstract

【課題】圧送又は吸引装置の力が強く、分室内に発生した旋回流の流速の軸方向成分が大きい場合でも、分離室内に設置した固定翼により旋回流の回転方向成分を増加させることが可能な遠心力集塵装置を提供する。
【解決手段】本発明の遠心力集塵装置は、略円筒形の内形構造を有し塵埃を含む空気流から塵埃を旋回流Cで遠心分離する分離室4と、分離室4に塵埃を含む空気流Aを接線方向に流入させる吸気口2と、分離室4に連通し分離された塵埃を集塵する集塵室5と、塵埃と分離された空気流Dを遠心力集塵装置1外へ排出する排気管7を有し、分離室4内に旋回流Bの流速gの回転方向成分fを増加させるための固定翼を設置した構成を有する。これにより分離室内の旋回流Bは、固定翼間を流れる際に旋回流の流路面積が小さくなるため、旋回流Bの流速が増速されると同時に、旋回流Bの軸方向成分を弱め、回転方向成分が大きくなるように変換される。
【選択図】図1
[PROBLEMS] To increase the rotational direction component of a swirling flow by a fixed blade installed in a separation chamber even when the force of a pumping or suction device is strong and the axial component of the flow velocity of the swirling flow generated in the branch chamber is large. A centrifugal dust collector is provided.
A centrifugal dust collecting apparatus according to the present invention has a substantially cylindrical inner shape structure, a separation chamber 4 that centrifuges dust from an air flow containing dust in a swirl flow C, and dust in the separation chamber 4. A suction port 2 through which an air flow A including the air flows A flows in a tangential direction, a dust collection chamber 5 that collects dust separated in communication with the separation chamber 4, and a centrifugal dust collector 1 that collects the air flow D separated from the dust. It has an exhaust pipe 7 that discharges to the outside, and has a configuration in which fixed blades are installed in the separation chamber 4 to increase the rotational direction component f of the flow velocity g of the swirling flow B. As a result, the swirling flow B in the separation chamber has a smaller flow area when swirling between the fixed blades, so that the flow velocity of the swirling flow B is increased and the axial component of the swirling flow B is weakened. The rotation direction component is converted to be large.
[Selection] Figure 1

Description

本発明は、塵埃を含む空気流から旋回流の遠心力により塵埃を分離し、塵埃のみを集塵する遠心力集塵装置に関するものである。   The present invention relates to a centrifugal dust collector that separates dust from an air flow containing dust by centrifugal force of a swirling flow and collects only dust.

従来、この種の遠心力集塵装置はエアサイクルシステムやサイクロン方式の電気掃除機に多く利用されている(例えば、特許文献1、2参照)。   Conventionally, this type of centrifugal dust collector is widely used in air cycle systems and cyclone type vacuum cleaners (see, for example, Patent Documents 1 and 2).

図21及び図22は、特許文献1に記載された従来の遠心力集塵装置を示すものである。図21及び22に示すように、遠心力集塵装置35は、塵埃を含む空気流Aを吸引する吸気口2と、吸気口2に沿って略円筒形の内形構造を有し空気流Aを旋回させて発生した旋回流Bで空気流から塵埃を遠心分離する分離室4と、分離された塵埃を集塵する集塵室5と、前記塵埃と分離された空気流Dを分離室4内から排気口6を通して遠心力集塵装置35外へ排出する排気管7から構成された遠心力集塵装置が開示されている。   21 and 22 show a conventional centrifugal dust collector described in Patent Document 1. FIG. As shown in FIGS. 21 and 22, the centrifugal dust collecting device 35 has an air inlet 2 that sucks an air flow A containing dust and an inner cylindrical structure along the air inlet 2. The separation chamber 4 that centrifuges dust from the air flow by the swirl flow B generated by swirling the dust, the dust collection chamber 5 that collects the separated dust, and the separation chamber 4 that collects the air flow D separated from the dust. There is disclosed a centrifugal dust collecting device constituted by an exhaust pipe 7 for discharging from the inside through the exhaust port 6 to the outside of the centrifugal dust collecting device 35.

特許文献2では、接続パイプ内部に配設した旋回流発生翼にて直進する気流を旋回流に変換し、この旋回流中で発生する遠心力作用によって細塵を開口部を通じて細塵用集塵室に送り込み、その細塵用集塵室内での旋回流でさらに細塵を空気と分離する構成の遠心力集塵装置が開示されている。
特開2000−317349号公報 特開平8−322768号公報
In Patent Document 2, an air flow that goes straight by a swirl flow generating blade disposed inside a connection pipe is converted into a swirl flow, and fine dust is collected through an opening by a centrifugal force action generated in the swirl flow. There is disclosed a centrifugal dust collector configured to be fed into a chamber and further separate fine dust from air by a swirling flow in the dust collecting chamber for fine dust.
JP 2000-317349 A JP-A-8-322768

しかしながら、前記従来の構成では、細塵を分離する分離室内の旋回流をさらに強い旋回流とする構成を遠心力集塵装置内に有しておらず、つまり発生させた旋回流の回転方向成分をさらに増加できないため、圧送又は吸引装置の力が強く、旋回流の軸方向成分が大きい場合に、十分な遠心分離効果が得られず、塵埃が排気管内を通り、排気口から流れ出てしまうという課題を有していた。   However, in the conventional configuration, the centrifugal dust collector does not have a configuration in which the swirl flow in the separation chamber for separating fine dust is made stronger, that is, the rotational direction component of the generated swirl flow. Therefore, when the force of the pumping or suction device is strong and the axial component of the swirling flow is large, sufficient centrifugal separation effect cannot be obtained, and dust flows out from the exhaust port through the exhaust pipe. Had problems.

本発明は、前記従来の課題を解決するもので、発生した旋回流の流速の軸方向成分が大きい場合でも、分離室内に設置した固定翼により旋回流の回転方向成分を増加させることが可能な遠心力集塵装置を提供することを目的とする。   The present invention solves the above-described conventional problem, and even when the axial component of the flow velocity of the generated swirling flow is large, the rotational direction component of the swirling flow can be increased by the fixed blade installed in the separation chamber. An object is to provide a centrifugal dust collector.

前記従来の課題を解決するために、本発明の遠心力集塵装置は、略円筒形の内形構造を有し塵埃を含む空気流から塵埃を旋回流で遠心分離する分離室と、前記分離室に塵埃を含む空気流を接線方向に流入させる吸気口と、前記分離室に連通し分離された前記塵埃を集塵する集塵室と、前記分離室の略中心部に配置され前記塵埃と分離された空気流を分離室内から遠心力集塵装置外へ排出する排気管を有し、前記分離室内に旋回流の流速の回転方向成分を増加させるための固定翼を設置した構成を有するものである。   In order to solve the above-described conventional problems, the centrifugal dust collector of the present invention includes a separation chamber that has a substantially cylindrical inner structure and centrifuges dust from an air flow containing dust in a swirling flow, and the separation An air inlet for allowing an air flow containing dust to flow into the chamber in a tangential direction, a dust collection chamber for collecting the dust communicated and separated to the separation chamber, and the dust disposed at a substantially central portion of the separation chamber; Having an exhaust pipe for discharging the separated air flow from the separation chamber to the outside of the centrifugal dust collector, and having a configuration in which fixed blades for increasing the rotational direction component of the flow velocity of the swirling flow are installed in the separation chamber It is.

これによって、分離室内に発生した旋回流は固定翼に沿って流れるようになり、固定翼間を流れる際に旋回流の流路面積が小さくなるため旋回流の流速が増速されると同時に、旋回流の軸方向成分を弱め、回転方向成分が大きくなるように変換されるものである。   As a result, the swirl flow generated in the separation chamber flows along the fixed wings, and when the flow between the fixed wings, the flow area of the swirl flow is reduced, and the flow velocity of the swirl flow is increased. It is converted so that the axial component of the swirl flow is weakened and the rotational component is increased.

本発明の遠心力集塵装置は、吸気口より吸引された塵埃を含む空気の旋回流の流速を増速させ、かつ旋回流の回転方向成分を増加させて、空気流から塵埃を遠心分離する性能を向上させることができる。   The centrifugal dust collecting device of the present invention centrifuges dust from the air flow by increasing the flow velocity of the swirling flow of the air containing the dust sucked from the air inlet and increasing the rotational direction component of the swirling flow. Performance can be improved.

第1の発明は、略円筒形の内形構造を有し塵埃を含む空気流から塵埃を旋回流で遠心分離する分離室と、前記分離室に塵埃を含む空気流を接線方向に流入させる吸気口と、前記分離室に連通し分離された前記塵埃を集塵する集塵室と、前記分離室の略中心部に配置され前記塵埃と分離された空気流を分離室内から遠心力集塵装置外へ排出する排気管を有する遠心力集塵装置において、前記分離室内に旋回流の流速の回転方向成分を増加させるための固定翼を設置した構成とすることにより、分離室内に発生した旋回流は固定翼間を流れる際に流路面積が小さくなるため流速が増速されると同時に、固定翼に沿って流れるようになり、旋回流の軸方向成分を弱め、回転方向成分が大きくなるように変換することができる。   According to a first aspect of the present invention, there is provided a separation chamber having a substantially cylindrical inner shape structure for centrifuging dust in a swirling flow from an air flow containing dust, and an intake air for causing the air flow containing the dust to flow into the separation chamber in a tangential direction A dust collecting chamber for collecting the dust separated and communicated with the separation chamber; and a centrifugal dust collecting device arranged in a substantially central portion of the separation chamber for separating an air flow separated from the dust from the separation chamber. In the centrifugal dust collector having an exhaust pipe that discharges to the outside, a swirl flow generated in the separation chamber is configured by installing a fixed blade for increasing the rotational direction component of the flow velocity of the swirl flow in the separation chamber. Since the flow area is reduced when flowing between fixed blades, the flow velocity is increased, and at the same time, it flows along the fixed blades, weakening the axial component of the swirling flow and increasing the rotational component. Can be converted to

第2の発明は、特に、第1の発明の固定翼を軸流翼の形状を有した遠心力集塵装置とすることにより、旋回流の軸方向成分を軸流翼の羽根の傾斜角に応じて回転方向成分に変換させることができる。   In the second invention, in particular, by using the fixed blade of the first invention as a centrifugal dust collector having the shape of an axial flow blade, the axial direction component of the swirl flow is set to the inclination angle of the blade of the axial flow blade. Accordingly, the rotation direction component can be converted.

第3の発明は、特に第1の発明の固定翼を多段に固定した軸流翼を有する構成の遠心力集塵装置とすることにより、旋回流の軸方向成分を多段に固定した軸流翼の羽根の傾斜角や羽根枚数の組合せに応じて段階ごとに回転方向成分に変換でき、しかも変換回数を増やすことで圧送又は吸引装置の圧力にも打ち勝つ旋回流の回転方向成分を得ることができる。   The third invention is an axial flow blade in which the axial component of the swirling flow is fixed in multiple stages by using a centrifugal dust collecting device having an axial flow blade in which the fixed blades of the first invention are fixed in multiple stages. The rotational direction component of the swirling flow that can overcome the pressure of the pressure feeding or suction device can be obtained by increasing the number of conversions according to the combination of the blade inclination angle and the number of blades. .

第4の発明は、特に第1の発明の固定翼を螺旋翼の形状を有した遠心力集塵装置とすることにより、翼に沿って流れる旋回流の流路が長くなり、それによって旋回流の流速を増速させ、かつ旋回流の軸方向成分を回転方向成分に変換する時間が長くなるため、圧送又は吸引装置の圧力にも打ち勝つ旋回流の回転方向成分を得ることができる。さらに旋回流の翼への衝突を低減させ、軸流翼では翼部入口付近で詰まりやすいセロハン等の塵埃についても詰まらせることなく集塵室に集塵させることができる。   In the fourth aspect of the invention, in particular, the fixed wing of the first aspect of the invention is a centrifugal dust collector having the shape of a spiral wing, so that the flow path of the swirling flow flowing along the wing becomes long, and thereby the swirling flow Since the time for converting the axial component of the swirl flow into the rotation direction component becomes longer, the rotation direction component of the swirl flow that overcomes the pressure of the pressure feeding or suction device can be obtained. Further, the collision of the swirling flow with the blades can be reduced, and the dust can be collected in the dust collecting chamber without clogging the dust such as cellophane which is easily clogged in the vicinity of the blade portion entrance with the axial flow blade.

第5の発明は、特に第2〜4の発明の固定翼を傾斜角可変の軸流翼もしくは螺旋翼とした遠心力集塵装置とすることにより、圧送や吸引装置の能力に応じて固定翼の傾斜角を調整して、翼間を流れる旋回流の流路面積を調整することも可能になるため、旋回流の流速を増速させる時間と、旋回流の軸方向成分を回転方向成分に変換する時間を制御することができ、集塵に必要な遠心力を安定して得ることができる。   According to a fifth aspect of the present invention, in particular, the fixed blade according to the second to fourth aspects of the present invention is a centrifugal dust collecting device using an axial flow blade or a spiral blade with a variable inclination angle. It is also possible to adjust the flow path area of the swirl flow flowing between the blades by adjusting the inclination angle of the swirl, so the time for increasing the flow velocity of the swirl flow and the axial component of the swirl flow as the rotation direction component The conversion time can be controlled, and the centrifugal force required for dust collection can be stably obtained.

第6の発明は、特に第1〜5のいずれか1つの発明の固定翼を吸気口と分離室内の排気管入口との間に固定した構成の遠心力集塵装置とすることにより、吸気口より吸引された塵埃を含む空気は旋回しながら全て固定翼間を経由して流れるため、前記第1〜5の発明で説明した固定翼の遠心力向上効果を最大限に発揮することができる。   According to a sixth aspect of the present invention, there is provided a centrifugal dust collecting device having a configuration in which the fixed blade of any one of the first to fifth aspects of the invention is fixed between the intake port and the exhaust pipe inlet in the separation chamber. Since all the air including dust that has been sucked in flows while passing through between the fixed blades, the effect of improving the centrifugal force of the fixed blades described in the first to fifth inventions can be maximized.

第7の発明は、特に第1〜5のいずれか1つの発明の固定翼を分離室内の排気管入口付近に固定した遠心力集塵装置とすることにより、分離室内で発生した旋回流の回転方向成分が低下する排気管入口付近において、旋回流が固定翼間を流れて前記第1〜5の発明で説明した固定翼の遠心力向上効果が得られ、圧送又は吸引装置の圧力にも打ち勝つ旋回流の回転方向成分を得ることができる。   According to a seventh aspect of the present invention, in particular, the rotation of the swirling flow generated in the separation chamber is achieved by using a centrifugal dust collector in which the fixed wing of any one of the first to fifth aspects of the invention is fixed near the exhaust pipe inlet in the separation chamber. In the vicinity of the exhaust pipe inlet where the directional component decreases, the swirling flow flows between the fixed blades, and the effect of improving the centrifugal force of the fixed blades described in the first to fifth inventions is obtained, and the pressure of the pumping or suction device is overcome. The rotational direction component of the swirling flow can be obtained.

第8の発明は、特に第1〜7のいずれか1つの発明の固定翼を分離室内壁側にのみ設置した構成の遠心力集塵装置とすることにより、流速が大きい分離室内壁付近の旋回流に対し、旋回流の軸方向成分を弱め、回転方向成分を大きくなるように変換することができる。   In an eighth aspect of the present invention, in particular, a centrifugal dust collecting device having a configuration in which the fixed wing according to any one of the first to seventh aspects of the present invention is installed only on the separation chamber wall side, thereby turning around the separation chamber wall having a high flow velocity. With respect to the flow, the axial component of the swirl flow can be weakened and converted so as to increase the rotational component.

第9の発明は、略円筒形の内形構造を有し塵埃を含む空気流から塵埃を旋回流で遠心分離する分離室と、前記分離室に塵埃を含む空気流を接線方向に流入させる吸気口と、前記分離室に連通し分離された前記塵埃を集塵する集塵室と、前記分離室の略中心部に配置され前記塵埃と分離された空気流を分離室内から遠心力集塵装置外へ排出する排気管を有する遠心力集塵装置において、前記分離室内壁に旋回流の流速の回転方向成分を増加させる凹凸形状を設けた遠心力集塵装置とすることにより、分離室内に発生した旋回流は凹凸形状の内壁面に沿って流れるようになり、固定翼を設置したときと同様に旋回流の軸方向成分を弱め、回転方向成分を大きくなるように変換することができる。   According to a ninth aspect of the present invention, there is provided a separation chamber that has a substantially cylindrical inner shape structure and centrifugally separates dust from an air flow including dust, and an intake air that causes the air flow including dust to flow into the separation chamber in a tangential direction. A dust collecting chamber for collecting the dust separated and communicated with the separation chamber; and a centrifugal dust collecting device arranged in a substantially central portion of the separation chamber for separating an air flow separated from the dust from the separation chamber. In a centrifugal dust collector having an exhaust pipe that discharges to the outside, it is generated in the separation chamber by forming a concave and convex shape that increases the rotational direction component of the flow velocity of the swirl flow on the separation chamber wall. The swirl flow thus flows along the concave and convex inner wall surface, and the axial component of the swirl flow can be weakened and converted so as to increase the rotation direction component in the same manner as when the fixed blades are installed.

第10の発明は、特に第1〜9のいずれか1つの発明の遠心力集塵装置を電気掃除機の本体内に有した構成とすることにより、掃除機の吸込力に関わらず、吸引力が強くかつ高い集塵性能を有するサイクロン方式の電気掃除機を開発することができる。   In the tenth aspect of the invention, in particular, the centrifugal dust collector according to any one of the first to ninth aspects is provided in the main body of the electric vacuum cleaner, so that the suction force is independent of the suction force of the vacuum cleaner. It is possible to develop a cyclone type vacuum cleaner that is strong and has high dust collection performance.

以下、本発明の実施の形態について、図面を参照しながら説明する。なお、この実施の形態によって本発明が限定されるものではない。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. Note that the present invention is not limited to the embodiments.

(実施の形態1)
図1は本発明の第1の実施の形態における遠心力集塵装置の縦断面図を、図2はその平面図を示すものである。
(Embodiment 1)
FIG. 1 is a longitudinal sectional view of a centrifugal dust collector according to a first embodiment of the present invention, and FIG. 2 is a plan view thereof.

図1及び図2において、遠心力集塵装置1は、遠心力集塵装置1の上端に配置し塵埃を含む空気流Aを遠心力集塵装置1内に接線方向に流入させ旋回流Bを発生させる吸気口2と、旋回流Bの流速を増速させ、かつ旋回流Bの回転方向成分を増加させる働きをする軸流翼3aと、軸流翼3aにより回転方向成分の増加した旋回流Cで塵埃を含む空気流から塵埃を遠心分離する略円筒形の分離室4と、分離された塵埃を集塵する集塵室5と、分離室4の略中心部に配置され前記塵埃と分離された空気流Dを分離室4内から排気口6を通して遠心力集塵装置1外へ排出する排気管7から構成されている。ここで、軸流翼3aは吸気口2と分離室4内の排気管入口8との間に設けられている。   1 and 2, the centrifugal dust collector 1 is disposed at the upper end of the centrifugal dust collector 1, and an air flow A including dust is caused to flow into the centrifugal dust collector 1 in a tangential direction so as to generate a swirl flow B. The generated inlet 2, the axial flow blade 3 a that increases the flow velocity of the swirl flow B and increases the rotation direction component of the swirl flow B, and the swirl flow whose rotation direction component is increased by the axial flow blade 3 a A substantially cylindrical separation chamber 4 for centrifuging dust from an air flow containing dust at C, a dust collection chamber 5 for collecting the separated dust, and a substantially central portion of the separation chamber 4 to separate the dust. The exhaust air flow D is formed from an exhaust pipe 7 for discharging the air flow D from the separation chamber 4 through the exhaust port 6 to the outside of the centrifugal dust collector 1. Here, the axial flow blade 3 a is provided between the intake port 2 and the exhaust pipe inlet 8 in the separation chamber 4.

図3は、旋回流の流速の軸方向成分と回転方向成分を表す概略図である。   FIG. 3 is a schematic diagram showing the axial direction component and the rotational direction component of the flow velocity of the swirling flow.

図3に示すように、旋回流Eの流速aは、軸方向成分bと回転方向成分cの2つに分けられる。   As shown in FIG. 3, the flow velocity a of the swirling flow E is divided into two components, an axial component b and a rotational component c.

特に、遠心分離性能に大きく影響するのは旋回流Eの回転方向成分cである。   In particular, the rotational direction component c of the swirling flow E greatly affects the centrifugal separation performance.

図4に分離室内の排気管に固定した軸流翼の要部斜視図を示す。   FIG. 4 is a perspective view of a main part of the axial flow blade fixed to the exhaust pipe in the separation chamber.

図5に軸流翼の羽根の傾斜角を表す概略図を示す。   FIG. 5 is a schematic view showing the inclination angle of the blades of the axial flow blade.

図5において、傾斜角dは旋回流の軸方向に対する軸流翼3aの角度を示している。   In FIG. 5, the inclination angle d indicates the angle of the axial flow blade 3a with respect to the axial direction of the swirling flow.

以上のように構成された遠心力集塵装置について、以下その動作、作用を説明する。   The operation and action of the centrifugal dust collector configured as described above will be described below.

まず、吸気口2に吸引された塵埃を含む空気流Aは、吸気口2に沿って略円筒形をした分離室4の内壁面に沿って流れることで旋回流Bを発生させる。   First, the air flow A containing dust sucked into the air inlet 2 flows along the inner wall surface of the substantially cylindrical separation chamber 4 along the air inlet 2 to generate a swirl flow B.

図6に軸流翼付近の旋回流を表す概略図を示す。   FIG. 6 is a schematic diagram showing a swirling flow near the axial flow blade.

図6において、発生した旋回流Bは分離室4内に設置された軸流翼3aに沿って流れ、軸流翼3aの羽根の傾斜角dに応じて旋回流Bの流速の軸方向成分eは弱められて回転方向成分fに変換される。また旋回流Bが軸流翼3aの羽根間を流れる際に流路面積が小さくなるため、旋回流Bの流速gは増速され、旋回流Cを発生させる。このようにして発生した旋回流Cで塵埃を含む空気流から塵埃を遠心分離し、集塵室5内に前記塵埃を集塵する。分離された清潔な空気流Dは、分離室4内の排気管入口8を通り排気口6を抜けて遠心力集塵装置1外へ排出される。   In FIG. 6, the generated swirling flow B flows along the axial flow blade 3a installed in the separation chamber 4, and the axial component e of the flow velocity of the swirling flow B according to the inclination angle d of the blade of the axial flow blade 3a. Is weakened and converted into a rotation direction component f. Further, when the swirling flow B flows between the blades of the axial flow blades 3a, the flow path area is reduced, so that the flow velocity g of the swirling flow B is increased and the swirling flow C is generated. The swirling flow C generated in this manner is used to centrifuge the dust from the air flow including the dust and collect the dust in the dust collecting chamber 5. The separated clean air flow D passes through the exhaust pipe inlet 8 in the separation chamber 4, passes through the exhaust outlet 6, and is discharged out of the centrifugal dust collector 1.

軸流翼3aは羽根の枚数と傾斜角dを旋回流Bの流速gに応じて適切に選定することが重要となる。羽根の傾斜角dを大きくすると、羽根の向きが軸方向に対して垂直に近づくため、分離室4に発生した旋回流Bの軸方向成分を回転方向成分に変換する割合が大きくなる。また羽根の枚数を増やすと羽根間を流れる旋回流Bの乱れを低減し、かつ流路面積が小さくなり旋回流Bの増速効果を大きくすることができる。   It is important for the axial flow blade 3a to appropriately select the number of blades and the inclination angle d according to the flow velocity g of the swirl flow B. When the blade inclination angle d is increased, the direction of the blade approaches perpendicular to the axial direction, so that the ratio of the axial component of the swirling flow B generated in the separation chamber 4 to the rotational direction component increases. Further, when the number of blades is increased, the turbulence of the swirl flow B flowing between the blades can be reduced, the flow path area can be reduced, and the effect of increasing the swirl flow B can be increased.

以上のように、本実施の形態においては分離室4内に軸流翼3aを固定することにより、分離室4内に発生した旋回流Bの流速gを増速し、かつ旋回流Bの回転方向成分を増加させて、発生させた旋回流Cにより塵埃を遠心分離することで、圧送又は吸引装置の力が強く、旋回流の軸方向成分が大きい場合においても、十分な遠心分離性能を得ることができる。   As described above, in the present embodiment, by fixing the axial flow blade 3a in the separation chamber 4, the flow velocity g of the swirling flow B generated in the separation chamber 4 is increased, and the rotation of the swirling flow B is increased. By increasing the directional component and centrifuging the dust by the generated swirling flow C, sufficient centrifugal separation performance can be obtained even when the force of the pressure feeding or suction device is strong and the axial component of the swirling flow is large. be able to.

なお、この実施の形態において、図7に示すように、軸流翼3aを排気管入口8付近に固定した遠心力集塵装置9とすることにより、旋回流4が軸流翼3a間を流れて旋回流Bの回転方向成分fが増加し、旋回流Bの回転方向成分が低下する排気管入口8付近での遠心分離性能を向上させることができる。   In this embodiment, as shown in FIG. 7, by using the centrifugal dust collector 9 in which the axial flow blade 3a is fixed near the exhaust pipe inlet 8, the swirling flow 4 flows between the axial flow blades 3a. Thus, the centrifugal separation performance near the exhaust pipe inlet 8 where the rotational direction component f of the swirl flow B increases and the rotational direction component of the swirl flow B decreases can be improved.

(実施の形態2)
本発明の第2の実施の形態における遠心力集塵装置は、図1及び図2に示した本発明の第1に実施の形態と、軸流翼3aを2段設置の軸流翼3bとした以外は同様の構成を有するものであり、同一の構成については、同一の符号を付して詳細な説明は省略する。
(Embodiment 2)
The centrifugal dust collector in the second embodiment of the present invention is the same as that of the first embodiment of the present invention shown in FIGS. 1 and 2, and the axial flow blade 3a is provided with two stages of axial flow blades 3b. Except for the above, the same configuration is provided, and the same configuration is denoted by the same reference numeral and detailed description thereof is omitted.

図8は、本発明の第2の実施の形態における遠心力集塵装置の分離室4内の排気管7に固定した2段設置の軸流翼3bの要部斜視図を示すものである。   FIG. 8 shows a perspective view of a main part of the two-stage axial flow blade 3b fixed to the exhaust pipe 7 in the separation chamber 4 of the centrifugal dust collector in the second embodiment of the present invention.

以上のような軸流翼3bを固定した遠心力集塵装置について、以下その動作、作用を説明する。   The operation and action of the centrifugal dust collector with the axial flow blade 3b fixed as described above will be described below.

まず、吸気口2に吸引された塵埃を含む空気流Aから形成された旋回流Bは、軸流翼3b間を連続的に2回流れることになるため、旋回流Bの増速と軸方向成分eを回転方向成分fに変換する回数が増え、軸流翼3bを流れる旋回流Bの回転方向成分の向上効果を大きくすることができる。また、固定する軸流翼3bの羽根の傾斜角や羽根枚数の組合せに応じて段階ごとに回転方向成分に変換でき、圧送又は吸引装置の圧力にも打ち勝つ旋回流の回転方向成分を得ることができる。   First, since the swirl flow B formed from the air flow A containing dust sucked into the air inlet 2 flows twice continuously between the axial flow blades 3b, the speed of the swirl flow B is increased and the axial direction is increased. The frequency | count of converting the component e into the rotation direction component f increases, and the improvement effect of the rotation direction component of the swirl | vortex flow B which flows through the axial flow blade 3b can be enlarged. Further, the rotational direction component of the swirling flow that can be converted into the rotational direction component at each stage according to the combination of the inclination angle and the number of blades of the axial flow blade 3b to be fixed, and can overcome the pressure of the pressure feeding or suction device can be obtained. it can.

なお、この実施の形態では軸流翼を2段設置する場合で説明したが、2段に限定されるものではなく、2段以上に設置した場合でも同様の効果が得られることは言うまでもない。   In this embodiment, the case where two stages of axial flow blades are installed has been described. However, the present invention is not limited to two stages, and it goes without saying that the same effect can be obtained when two or more stages are installed.

(実施の形態3)
本発明の第3の実施の形態における遠心力集塵装置は、図1に示した本発明の第1に実施の形態と、軸流翼3aを螺旋翼10a以外は同様の構成を有するものであり、同一の構成については、同一の符号を付して詳細な説明は省略する。
(Embodiment 3)
The centrifugal dust collector in the third embodiment of the present invention has the same configuration as that of the first embodiment of the present invention shown in FIG. 1 except that the axial flow blade 3a is a spiral blade 10a. The same components are denoted by the same reference numerals, and detailed description thereof is omitted.

図9は、本発明の第3の実施の形態における分離室内の排気管に固定した螺旋翼の要部斜視図を示すものである。   FIG. 9 is a perspective view showing a main part of a spiral blade fixed to the exhaust pipe in the separation chamber according to the third embodiment of the present invention.

図9において、10aは1周の螺旋翼を示している。   In FIG. 9, reference numeral 10a denotes a spiral wing of one round.

図10に螺旋翼の羽根の傾斜角を表す概略図を示す。図10において、傾斜角hは旋回流の軸方向に対する螺旋翼10aの角度を示している。   FIG. 10 is a schematic diagram showing the inclination angle of the blades of the spiral wing. In FIG. 10, the inclination angle h indicates the angle of the spiral blade 10a with respect to the axial direction of the swirling flow.

以上のような螺旋翼10aを固定した遠心力集塵装置について、以下その動作、作用を説明する。   The operation and action of the centrifugal dust collector with the helical blade 10a fixed as described above will be described below.

まず、吸気口2に吸引された塵埃を含む空気流Aから形成された旋回流Bは、螺旋翼10aに沿って流れるようになり、旋回流Bの軸方向成分eは螺旋翼10aの傾斜角hに応じて回転方向成分に変換される。軸流翼に比べ翼に沿って流れる旋回流の流路が長くなるため、旋回流Bの流速を増速し、かつ軸方向成分eを回転方向成分fに変換する時間が長くなるため、旋回流Bの回転方向成分fを大幅に増加させることができる。さらに螺旋翼10aでは旋回流Bが螺旋翼10a入口での衝突のみになり、衝突回数を減らし安定した流れを形成することができる。また軸流翼では翼部入口付近で詰まりやすいセロハン等の塵埃についても詰まらせることなく集塵室5に集塵させることができる。   First, the swirl flow B formed from the air flow A containing dust sucked into the air inlet 2 flows along the spiral blade 10a, and the axial component e of the swirl flow B is the inclination angle of the spiral blade 10a. It is converted into a rotation direction component according to h. Since the flow path of the swirl flow that flows along the blade is longer than that of the axial flow blade, the time required to increase the flow velocity of the swirl flow B and convert the axial component e into the rotational component f is increased. The rotational direction component f of the flow B can be greatly increased. Further, in the spiral blade 10a, the swirl flow B becomes only a collision at the inlet of the spiral blade 10a, and the number of collisions can be reduced and a stable flow can be formed. Further, in the axial flow blade, dust such as cellophane that is easily clogged in the vicinity of the blade inlet can be collected in the dust collection chamber 5 without clogging.

以上のように、本実施の形態においては分離室4内に旋回流Bの流速gの回転方向成分fを増加させるための螺旋翼10aを固定することにより、分離室4内に発生した旋回流Bの流速gを増速させ、かつ旋回流Bの回転方向成分fを増加させて発生させた旋回流Cにより塵埃を遠心分離することで、圧送又は吸引装置の力が強く、旋回流Bの軸方向成分eが大きい場合においても、十分な遠心分離性能を得ることができる。   As described above, in this embodiment, the swirl flow generated in the separation chamber 4 by fixing the spiral blade 10 a for increasing the rotational direction component f of the flow velocity g of the swirl flow B in the separation chamber 4. By centrifuging the dust by the swirling flow C generated by increasing the flow velocity g of B and increasing the rotational direction component f of the swirling flow B, the force of the pressure feeding or suction device is strong, Even when the axial component e is large, sufficient centrifugal separation performance can be obtained.

なお、この実施の形態では1周の螺旋翼を設置する場合で説明したが、図11に示すように分離室内の排気管に固定した2周の螺旋翼10bもしくは2周以上の螺旋翼の場合でも同様の効果が得られるものである。   In this embodiment, the case where one round spiral blade is installed has been described. However, as shown in FIG. 11, in the case of two round spiral blades 10b fixed to the exhaust pipe in the separation chamber or two or more round spiral blades. However, the same effect can be obtained.

(実施の形態4)
本発明の第4の実施の形態における遠心力集塵装置は、図1に示した本発明の第1に実施の形態と、軸流翼3aを傾斜角可変の軸流翼もしくは螺旋翼とした以外は同様の構成を有するものであり、同一の構成については、同一の符号を付して詳細な説明は省略する。
(Embodiment 4)
The centrifugal dust collector in the fourth embodiment of the present invention is the same as that of the first embodiment of the present invention shown in FIG. 1, and the axial flow blade 3a is an axial flow blade or spiral blade having a variable inclination angle. Other than the above, the components have the same configuration, and the same components are denoted by the same reference numerals and detailed description thereof is omitted.

以上のような傾斜角可変の軸流翼もしくは螺旋翼を固定した遠心力集塵装置について、以下その動作、作用を説明する。   The operation and action of the centrifugal dust collecting apparatus having the variable tilt angle axial flow blade or the spiral blade fixed as described above will be described below.

まず、吸気口2に吸引された塵埃を含む空気流Aから形成された旋回流Bは、傾斜角可変の軸流翼もしくは螺旋翼に沿って流れるようになり、旋回流Bの軸方向成分eは前記傾斜角可変の軸流翼もしくは螺旋翼の傾斜角に応じて回転方向成分fに変換される。   First, the swirl flow B formed from the air flow A containing dust sucked into the air inlet 2 flows along the axial flow blade or the spiral blade having a variable inclination angle, and the axial component e of the swirl flow B Is converted into a rotation direction component f according to the inclination angle of the axial flow blade or spiral blade with variable inclination angle.

傾斜角可変の軸流翼もしくは螺旋翼の傾斜角の調整は、手動で切り換える方法と自動で切り換える方法がある。手動で切り換える場合には、吸気口2より吸引された塵埃を含む空気流Aの流速を、吸気口2付近に取付けた熱流速センサを用いて測定し、測定された流速に応じて傾斜角を手動つまみにより切り換える。   There are two methods for adjusting the tilt angle of the axial flow blade or the spiral blade having a variable tilt angle and a method for switching automatically. When switching manually, the flow velocity of the air flow A including dust sucked from the intake port 2 is measured using a heat flow rate sensor attached near the intake port 2, and the inclination angle is set according to the measured flow velocity. Switch with the manual knob.

また遠心力集塵装置の排気口6に延長管を取付け、吸引装置を用いて遠心力集塵装置内に吸気口2から塵埃を含む空気流Aを吸引する場合には、吸引装置の運転モード(例えば強、中、弱の3段階)に合わせて作業者が手動つまみにより、軸流翼もしくは螺旋翼の傾斜角の調整が行え、吸引力の強さに応じて必要な遠心力を安定して得ることができ、空気流から塵埃を遠心分離する性能を向上させることができる。   In addition, when an extension pipe is attached to the exhaust port 6 of the centrifugal dust collector and the air flow A containing dust is sucked into the centrifugal dust collector from the intake port 2 using the suction device, the operation mode of the suction device is used. The operator can adjust the tilt angle of the axial flow blade or the spiral blade with a manual knob according to the three levels (for example, strong, medium and weak), and stabilize the necessary centrifugal force according to the strength of the suction force. The performance of centrifuging dust from an air flow can be improved.

さらに作業者が手元操作部の運転モードボタンを操作することで、軸流翼もしくは螺旋翼の傾斜角を自動調整できる制御システムにしておけば、遠心力集塵装置を遠隔操作することができ、上記効果に加え、使い勝手も良くなるものである。   In addition, if the control system can automatically adjust the tilt angle of the axial flow blade or spiral blade by operating the operation mode button of the hand control unit, the centrifugal dust collector can be remotely operated, In addition to the above effects, usability is also improved.

一方、完全自動制御の場合には、あらかじめ対象とする塵埃を空気流から遠心分離するために必要な旋回流の流速を熱流速センサ又はLDV等を用いて測定し、吸気口2より吸引された塵埃を含む空気流Aの流速に対する軸流翼もしくは螺旋翼の傾斜角と旋回流Cの流速の相関関係から、塵埃を含む空気流Aの流速に応じて傾斜角を自動制御するシステムにする。   On the other hand, in the case of fully automatic control, the flow velocity of the swirl flow necessary for centrifuging the target dust from the air flow in advance is measured using a thermal flow velocity sensor or LDV, and sucked from the intake port 2. Based on the correlation between the inclination angle of the axial flow blade or the spiral blade and the flow velocity of the swirl flow C with respect to the flow velocity of the air flow A containing dust, the inclination angle is automatically controlled according to the flow velocity of the air flow A containing dust.

以上のように、本実施の形態においては分離室4内に旋回流Bの流速の回転方向成分fを増加させるため傾斜角可変の軸流翼もしくは螺旋翼のいずれかを固定することにより、圧送や吸引装置の能力に応じて傾斜角を調整し、翼間を流れる旋回流の流路面積を調整することも可能になるため、旋回流Bの流速gを増速させ、かつ旋回流Bの軸方向成分eを回転方向成分fに変換する時間を制御することができ、塵埃を空気流Cから遠心分離するために必要な遠心力を安定して得ることができる。   As described above, in the present embodiment, in order to increase the rotational direction component f of the flow velocity of the swirling flow B in the separation chamber 4, either the axial flow blade or the spiral blade having a variable inclination angle is fixed, so In addition, the inclination angle is adjusted according to the capacity of the suction device and the flow passage area of the swirling flow flowing between the blades can be adjusted, so that the flow velocity g of the swirling flow B is increased and the swirling flow B The time for converting the axial component e to the rotational component f can be controlled, and the centrifugal force required to centrifuge the dust from the air flow C can be stably obtained.

なお、実施の形態1〜4では、固定翼を排気管7に固定した場合で説明したが、この固定方法に限らず分離室4内壁に固定されていても良く、要するに分離室4内に固定翼を固定できれば良く、また固定翼を少なくとも排気管7及び分離室4内壁のいずれか一方に一体構成に設けてあれば、上記と同様の効果は得られるものである。   In the first to fourth embodiments, the case where the fixed blade is fixed to the exhaust pipe 7 has been described. However, the fixing blade is not limited to this fixing method, and may be fixed to the inner wall of the separation chamber 4. As long as the blades can be fixed, and the fixed blade is provided in at least one of the exhaust pipe 7 and the inner wall of the separation chamber 4, the same effect as described above can be obtained.

(実施の形態5)
本発明の第5の実施の形態における遠心力集塵装置は、図1に示した本発明の第3に実施の形態と、螺旋翼10aが分離室内壁側にのみ固定された螺旋翼10cとした以外は同様の構成を有するものであり、同一の構成については、同一の符号を付して詳細な説明は省略する。
(Embodiment 5)
The centrifugal dust collector in the fifth embodiment of the present invention includes a third embodiment of the present invention shown in FIG. 1 and a spiral blade 10c in which the spiral blade 10a is fixed only on the separation chamber wall side. Except for the above, the same configuration is provided, and the same configuration is denoted by the same reference numeral and detailed description thereof is omitted.

図12は、本発明の第5の実施の形態における遠心力集塵装置の要部断面の斜視図を示すものである。なお、図12では螺旋翼10cと、排気管7と、分離室4と、集塵室5のみを図示している。   FIG. 12: shows the perspective view of the principal part cross section of the centrifugal dust collector in the 5th Embodiment of this invention. In FIG. 12, only the spiral blade 10c, the exhaust pipe 7, the separation chamber 4, and the dust collection chamber 5 are illustrated.

以上のような螺旋翼10cを固定した遠心力集塵装置について、以下その動作、作用を説明する。   The operation and action of the centrifugal dust collector having the spiral blade 10c as described above will be described below.

まず、吸気口2に吸引された塵埃を含む空気流Aから形成された旋回流Bの流速aは、分離室4内の中央より外周部つまり分離室4の内壁付近が最も速くなるため、螺旋翼10cを分離室4の内壁側にのみ固定することで流速が速い分離室4内壁付近の旋回流の軸方向成分を弱め、回転方向成分をさらに大きくなるように変換することができる。   First, the flow velocity a of the swirl flow B formed from the air flow A containing dust sucked into the intake port 2 is the highest in the outer peripheral portion, that is, in the vicinity of the inner wall of the separation chamber 4 from the center in the separation chamber 4. By fixing the blade 10c only on the inner wall side of the separation chamber 4, it is possible to weaken the axial component of the swirling flow near the inner wall of the separation chamber 4 where the flow velocity is high, and to convert the rotational component further.

(実施の形態6)
図13及び図14は、本発明の第6の実施の形態における遠心力集塵装置の縦断面図を示すものである。
(Embodiment 6)
13 and 14 are longitudinal sectional views of a centrifugal dust collecting apparatus according to the sixth embodiment of the present invention.

なお、本発明の第6の実施の形態における遠心力集塵装置は、図1に示した本発明の第1に実施の形態と、分離室内に段付き壁構造を設け、固定翼を除いた構成とした以外は同様の構成を有するものであり、同一の構成については、同一の符号を付して詳細な説明は省略する。   The centrifugal dust collector in the sixth embodiment of the present invention is the same as that of the first embodiment of the present invention shown in FIG. 1 except that a stepped wall structure is provided in the separation chamber, and the fixed wing is removed. Except for the configuration, the configuration is the same, and the same configuration is denoted by the same reference numeral and detailed description thereof is omitted.

図13及び図14において、遠心力集塵装置11は、遠心力集塵装置11の上端に配置し塵埃を含む空気流Aを遠心力集塵装置11内に接線方向に流入させ旋回流Bを発生させる吸気口2と、旋回流の下降軸成分の方向へ向かって径が段階的に小さくなる段付き内壁構造12を有し旋回流Bの回転方向成分fを段付き内壁構造12により増加させた旋回流Cで塵埃を含む空気流から塵埃を遠心分離する分離室13と、分離された塵埃を集塵する集塵室5と、分離室4の略中心部に配置され前記塵埃と分離された空気流Dを分離室13内から排気口6を通して遠心力集塵装置11外へ排出する排気管7から構成されている。   13 and 14, the centrifugal dust collector 11 is arranged at the upper end of the centrifugal dust collector 11, and an air flow A containing dust is caused to flow into the centrifugal dust collector 11 in a tangential direction so as to generate a swirl flow B. The stepped inner wall structure 12 having a stepwise decreasing diameter toward the direction of the descending axis component of the swirling flow is generated and the rotational direction component f of the swirling flow B is increased by the stepped inner wall structure 12. The separation chamber 13 that centrifuges the dust from the air flow including dust in the swirling flow C, the dust collection chamber 5 that collects the separated dust, and the separation chamber 4 that is disposed substantially at the center of the separation chamber 4 is separated from the dust. The exhaust pipe 7 discharges the air flow D from the separation chamber 13 to the outside of the centrifugal dust collector 11 through the exhaust port 6.

以上のような分離室13を有する遠心力集塵装置11について、以下その動作、作用を説明する。   The operation and action of the centrifugal dust collector 11 having the separation chamber 13 as described above will be described below.

まず、吸気口2に吸引された塵埃を含む空気流Aは、吸気口2に沿って略円筒形の分離室13の内壁面に沿って流れることで旋回流Bを発生させる。発生した旋回流Bは旋回流の下降軸成分の方向へ向かって径が段階的に小さくなる段付き内壁構造12に沿って流れ、旋回流Bの流速の軸方向成分eは弱められて回転方向成分fに変換されて旋回流Cを発生させる。このようにして発生した旋回流Cで塵埃を含む空気流から塵埃を遠心分離し、集塵室5内に分離された塵埃を集塵する。分離された清潔な空気流Dは、分離室13内の排気管入口8を通り排気口6を抜けて遠心力集塵装置11外へ排出される。   First, the air flow A containing dust sucked into the air inlet 2 flows along the inner wall surface of the substantially cylindrical separation chamber 13 along the air inlet 2 to generate a swirl flow B. The generated swirl flow B flows along the stepped inner wall structure 12 whose diameter decreases stepwise toward the direction of the descending axis component of the swirl flow, and the axial component e of the flow velocity of the swirl flow B is weakened and the rotation direction. The swirl flow C is generated by being converted into the component f. The swirling flow C generated in this manner is used to centrifuge the dust from the air flow including the dust and collect the separated dust in the dust collecting chamber 5. The separated clean air flow D passes through the exhaust pipe inlet 8 in the separation chamber 13, passes through the exhaust outlet 6, and is discharged out of the centrifugal dust collector 11.

以上のように、本実施の形態においては分離室13内に段付き内壁構造12を設けることにより、実施の形態5と同様に流速が速い分離室13内壁近くの旋回流のみ、軸方向成分gを弱め回転方向成分fに変換させて遠心力を向上させることができる。また固定翼を必要としないため、遠心力集塵装置の構造が簡易化されると同時に軽量化を図ることができる。   As described above, in the present embodiment, by providing the stepped inner wall structure 12 in the separation chamber 13, only the swirling flow near the inner wall of the separation chamber 13 having a high flow velocity as in the fifth embodiment can be obtained. The centrifugal force can be improved by weakening and converting to a rotational direction component f. Moreover, since no fixed wing is required, the structure of the centrifugal dust collector can be simplified and the weight can be reduced.

なお、この実施の形態では分離室内に階段状の段付き内壁構造を有する遠心力集塵装置を設置する場合で説明したが、階段状の段付き内壁構造を螺旋状の溝構造にした場合でも同様の効果が得られるものである。   In this embodiment, the centrifugal dust collector having a stepped stepped inner wall structure is installed in the separation chamber, but even when the stepped stepped inner wall structure has a spiral groove structure. Similar effects can be obtained.

さらに、前記実施の形態以外に、図15及び16に示すように分離室14内壁面にリング上の凸部15を設けた構成を有する遠心力集塵装置16や、図17に示すように排気管17を分離室18の胴部から出す構成を有する遠心力集塵装置19や、図18に示すように分離室20と集塵室21の径が等しい構成を有する遠心力集塵装置22などが挙げられる。   Further, in addition to the above embodiment, the centrifugal dust collector 16 having a configuration in which the convex portion 15 on the ring is provided on the inner wall surface of the separation chamber 14 as shown in FIGS. 15 and 16, and the exhaust as shown in FIG. A centrifugal dust collector 19 having a configuration in which the pipe 17 is extended from the body of the separation chamber 18, a centrifugal dust collector 22 having a configuration in which the diameters of the separation chamber 20 and the dust collection chamber 21 are equal as shown in FIG. Is mentioned.

(実施の形態7)
図19は、本発明の第7の実施の形態におけるアップライト型の電気掃除機23の構成を表す概略図を示すものである。
(Embodiment 7)
FIG. 19 is a schematic diagram showing the configuration of the upright type vacuum cleaner 23 according to the seventh embodiment of the present invention.

図19において、電気掃除機23は、掃除機本体24内に吸引ファンモータ25を内蔵し、掃除機本体24の吸引側にノズル26を装備したホース27を接続する本体吸気口28を形成し、本体吸気口28に請求項1〜9のいずれか1項に記載の遠心力集塵装置29の吸気口30を接続し、排気口31は吸引ファンモータ25を備えた送風室32に通気口を有する仕切壁33を介して接続されている。   In FIG. 19, the vacuum cleaner 23 has a suction fan motor 25 built in the vacuum cleaner body 24, and a main body inlet 28 for connecting a hose 27 equipped with a nozzle 26 on the suction side of the vacuum cleaner body 24 is formed. An air inlet 30 of the centrifugal dust collector 29 according to any one of claims 1 to 9 is connected to the main body air inlet 28, and an air outlet 31 is provided with a vent hole in the air blowing chamber 32 provided with the suction fan motor 25. It connects via the partition wall 33 which has.

以上のような構成を有する電気掃除機について、以下その動作、作用を説明する。   About the vacuum cleaner which has the above structures, the operation | movement and an effect | action are demonstrated below.

まず、吸引ファンモータ25が駆動することにより遠心力集塵装置29内を負圧状態にして、ノズル26が吸い込んだ塵埃を含む空気流Fはホース27を通して遠心力集塵装置29内に吸引される。分離室内で旋回流の遠心力により塵埃は空気流から分離され、塵埃のみが集塵室に集塵される。分離された空気流Gは仕切壁33を通して吸引ファンモータ25に吸引される。   First, the suction fan motor 25 is driven to bring the centrifugal dust collector 29 into a negative pressure state, and the air flow F including dust sucked by the nozzle 26 is sucked into the centrifugal dust collector 29 through the hose 27. The The dust is separated from the air flow by the centrifugal force of the swirling flow in the separation chamber, and only the dust is collected in the dust collection chamber. The separated air flow G is sucked into the suction fan motor 25 through the partition wall 33.

電気掃除機の吸引力は手動で連続的もしくは不連続的に切り換え可能なものが多く、作業者は手元操作で掃除機の吸込力を選択して掃除を行う。作業者が吸込力の強いモードを選択した場合、送風室32内に設置された吸引ファンモータ25の強い吸引力により分離室内に発生する旋回流の軸方向成分は大きくなるが、実施の形態1〜6で説明した分離室内に設置された固定翼もしくは分離室の凹凸形状をした内形構造により旋回流の回転方向成分は増加して高い集塵性能が得られる。   In many cases, the suction force of the vacuum cleaner can be switched manually or discontinuously, and the operator selects the suction force of the vacuum cleaner by hand operation to perform cleaning. When the operator selects a mode with a strong suction force, the axial component of the swirling flow generated in the separation chamber is increased by the strong suction force of the suction fan motor 25 installed in the blower chamber 32. The rotational direction component of the swirling flow is increased and high dust collection performance can be obtained by the fixed blades installed in the separation chamber described in ˜6 or the inner structure having the irregular shape of the separation chamber.

以上のように、本実施の形態においては本発明の遠心力集塵装置29を電気掃除機本体23内に設置することにより、掃除機の吸引力が強くかつ高い集塵性能を有するサイクロン方式の電気掃除機を開発することができる。   As described above, in the present embodiment, by installing the centrifugal dust collecting device 29 of the present invention in the electric vacuum cleaner main body 23, a cyclone type having a strong suction force and high dust collecting performance of the vacuum cleaner. A vacuum cleaner can be developed.

なお、この実施の形態ではアップライト型の電気掃除機に遠心力集塵装置を設置する場合で説明したが、図20に示すようにキャニスタ型の電気掃除機34に設置する場合でも同様の効果が得られるものである。   In this embodiment, the case where the centrifugal dust collecting device is installed in the upright type vacuum cleaner has been described. However, the same effect can be obtained when the centrifugal dust collecting device is installed in the canister type vacuum cleaner 34 as shown in FIG. Is obtained.

以上のように、本発明にかかる遠心力集塵装置は、旋回流の流速の軸方向成分が大きい場合にも旋回流の回転方向成分を増加させることが可能になるので、サイクロン方式の電気掃除機やリサイクル用遠心分離機やエアサイクルシステム等の用途に適用できる。   As described above, the centrifugal dust collector according to the present invention can increase the rotational direction component of the swirl flow even when the axial component of the flow velocity of the swirl flow is large. It can be applied to applications such as a centrifuge, a recycling centrifuge, and an air cycle system.

本発明の第1、第2、第3、第4、第5、第6の実施の形態における遠心力集塵装置の縦断面図The longitudinal cross-sectional view of the centrifugal dust collector in 1st, 2nd, 3rd, 4th, 5th, 6th embodiment of this invention 本発明の第1、第2の実施の形態における遠心力集塵装置の平面図The top view of the centrifugal dust collector in the 1st, 2nd embodiment of this invention 本発明の第1の実施の形態における遠心力集塵装置の旋回流の方向成分を表す概略図Schematic showing the directional component of the swirl | vortex flow of the centrifugal dust collector in the 1st Embodiment of this invention 同遠心力集塵装置の軸流翼の要部斜視図Perspective view of the main part of the axial flow blade of the centrifugal dust collector 同遠心力集塵装置の軸流翼の羽根の傾斜角を表す概略図Schematic showing the inclination angle of the blade of the axial flow blade of the centrifugal dust collector 同遠心力集塵装置の軸流翼付近の旋回流を表す概略図Schematic representing the swirl flow near the axial flow blade of the centrifugal dust collector 同遠心力集塵装置の縦断面図Vertical section of the centrifugal dust collector 本発明の第2の実施の形態における遠心力集塵装置の2段設置軸流翼の要部斜視図The perspective view of the principal part of the two-stage installation axial flow blade of the centrifugal dust collector in the second embodiment of the present invention 本発明の第3の実施の形態における遠心力集塵装置の螺旋翼の要部斜視図The principal part perspective view of the spiral blade of the centrifugal dust collector in the 3rd Embodiment of this invention 同遠心力集塵装置の螺旋翼の羽根の傾斜角を表す概略図Schematic representing the inclination angle of the spiral blade of the centrifugal dust collector 同遠心力集塵装置の分離室内の排気管に固定した2周の螺旋翼の要部斜視図Perspective view of the main part of the spiral wing of two rounds fixed to the exhaust pipe in the separation chamber of the centrifugal dust collector 本発明の第5の実施の形態における遠心力集塵装置の腰部断面を示した斜視図The perspective view which showed the waist | hip | lumbar part cross section of the centrifugal dust collector in the 5th Embodiment of this invention 本発明の第6の実施の形態における遠心力集塵装置の縦断面図The longitudinal cross-sectional view of the centrifugal dust collector in the 6th Embodiment of this invention 同遠心力集塵装置の断面図Cross-sectional view of the centrifugal dust collector 本発明のその他の実施の形態における遠心力集塵装置の縦断面図The longitudinal cross-sectional view of the centrifugal-force dust collector in other embodiment of this invention 同遠心力集塵装置の断面図Cross-sectional view of the centrifugal dust collector 同遠心力集塵装置の縦断面図Vertical section of the centrifugal dust collector 同遠心力集塵装置の縦断面図Vertical section of the centrifugal dust collector 本発明の第7の実施の形態における遠心力集塵装置を用いたアップライト型電気掃除機の横断面図The cross-sectional view of the upright type vacuum cleaner using the centrifugal dust collector in the seventh embodiment of the present invention 同遠心力集塵装置を用いたキャニスタ型の電気掃除機の横断面図Cross-sectional view of a canister-type vacuum cleaner using the centrifugal dust collector 従来の遠心力集塵装置の縦断面図Vertical section of a conventional centrifugal dust collector 同遠心力集塵装置の平面図Top view of the centrifugal dust collector

符号の説明Explanation of symbols

1 遠心力集塵装置
2 吸気口
3a 軸流翼
3b 軸流翼(2段)
4 分離室
5 集塵室
6 排気口
7 排気管
8 排気管入口
9 遠心力集塵装置
10a 螺旋翼(1周)
10b 螺旋翼(2周)
10c 螺旋翼
11 遠心力集塵装置
12 段付き内壁構造
13 分離室
14 分離室
15 リング状の凸部
16 遠心力集塵装置
17 排気管
18 分離室
19 遠心力集塵装置
20 分離室
21 集塵室
22 遠心力集塵装置
23 電気掃除機(アップライト型)
24 掃除機本体
25 吸引ファンモータ
26 ノズル
27 ホース
28 本体吸気口
29 遠心力集塵装置
30 吸気口
31 排気口
32 送風室
33 仕切壁
34 電気掃除機(キャニスタ型)
35 遠心力集塵装置
DESCRIPTION OF SYMBOLS 1 Centrifugal dust collector 2 Intake port 3a Axial flow blade 3b Axial flow blade (two stages)
4 Separation chamber 5 Dust collection chamber 6 Exhaust port 7 Exhaust pipe 8 Exhaust tube inlet 9 Centrifugal dust collector 10a Spiral blade (1 round)
10b Spiral wing (2 laps)
DESCRIPTION OF SYMBOLS 10c Spiral blade 11 Centrifugal dust collector 12 Stepped inner wall structure 13 Separation chamber 14 Separation chamber 15 Ring-shaped convex part 16 Centrifugal dust collector 17 Exhaust pipe 18 Separation chamber 19 Centrifugal dust collector 20 Separation chamber 21 Dust collection Chamber 22 Centrifugal dust collector 23 Vacuum cleaner (upright type)
24 Vacuum Cleaner Body 25 Suction Fan Motor 26 Nozzle 27 Hose 28 Main Body Inlet 29 Centrifugal Dust Collector 30 Inlet 31 Exhaust 32 Blower Chamber 33 Partition Wall 34 Electric Vacuum Cleaner (Canister Type)
35 Centrifugal force dust collector

Claims (10)

略円筒形の内形構造を有し塵埃を含む空気流から塵埃を旋回流で遠心分離する分離室と、前記分離室に塵埃を含む空気流を接線方向に流入させる吸気口と、前記分離室に連通し分離された前記塵埃を集塵する集塵室と、前記分離室の略中心部に配置され前記塵埃と分離された空気流を分離室内から遠心力集塵装置外へ排出する排気管を有する遠心力集塵装置において、前記分離室内に旋回流の流速の回転方向成分を増加させるための固定翼を設置した構成の遠心力集塵装置。 A separation chamber having a substantially cylindrical inner shape structure for centrifugally separating dust from an air flow containing dust, a suction port for causing the air flow containing dust to flow into the separation chamber in a tangential direction, and the separation chamber A dust collection chamber for collecting the dust separated and communicated with the exhaust, and an exhaust pipe disposed at a substantially central portion of the separation chamber for discharging an air flow separated from the dust from the separation chamber to the outside of the centrifugal dust collector A centrifugal dust collector having a configuration in which fixed blades for increasing the rotational direction component of the flow velocity of the swirling flow are installed in the separation chamber. 固定翼は、軸流翼の形状を有した請求項1に記載の遠心力集塵装置。 The centrifugal dust collector according to claim 1, wherein the fixed blade has an axial flow blade shape. 固定翼は、多段に固定された軸流翼とした請求項1に記載の遠心力集塵装置。 The centrifugal dust collector according to claim 1, wherein the fixed blade is an axial flow blade fixed in multiple stages. 固定翼は、螺旋翼の形状を有した請求項1に記載の遠心力集塵装置。 The centrifugal dust collector according to claim 1, wherein the fixed wing has a spiral wing shape. 固定翼は、傾斜角可変の軸流翼もしくは螺旋翼とした請求項2〜4のいずれか1項に記載の遠心力集塵装置。 The centrifugal dust collector according to any one of claims 2 to 4, wherein the fixed blade is an axial flow blade or a spiral blade having a variable inclination angle. 固定翼は、少なくとも吸気口と分離室内の排気管入口との間に固定された構成の請求項1〜5のいずれか1項に記載の遠心力集塵装置。 The centrifugal dust collector according to any one of claims 1 to 5, wherein the fixed blade is fixed at least between the air inlet and the exhaust pipe inlet in the separation chamber. 固定翼は、分離室内の排気管入口付近に固定された構成の請求項1〜5のいずれか1項に記載の遠心力集塵装置。 The centrifugal dust collector according to any one of claims 1 to 5, wherein the fixed wing is fixed in the vicinity of the exhaust pipe inlet in the separation chamber. 固定翼は、分離室内壁側にのみ固定された請求項1〜7のいずれか1項に記載の遠心力集塵装置。 The centrifugal force dust collector according to any one of claims 1 to 7, wherein the fixed blade is fixed only to the separation chamber wall side. 略円筒形の内形構造を有し塵埃を含む空気流から塵埃を旋回流で遠心分離する分離室と、前記分離室に塵埃を含む空気流を接線方向に流入させる吸気口と、前記分離室に連通し分離された前記塵埃を集塵する集塵室と、前記分離室の略中心部に配置され前記塵埃と分離された空気流を分離室内から遠心力集塵装置外へ排出する排気管を有する遠心力集塵装置において、前記分離室内壁に旋回流の流速の回転方向成分を増加させる凹凸形状を設けた遠心力集塵装置。 A separation chamber having a substantially cylindrical inner shape structure for centrifugally separating dust from an air flow containing dust, a suction port for causing the air flow containing dust to flow into the separation chamber in a tangential direction, and the separation chamber A dust collection chamber that collects the dust separated and communicated with the exhaust chamber, and an exhaust pipe that is disposed substantially at the center of the separation chamber and that discharges an air flow separated from the dust from the separation chamber to the outside of the centrifugal dust collector The centrifugal dust collector which has the uneven | corrugated shape which increases the rotation direction component of the flow velocity of a swirl | vortex flow in the said separation chamber wall in the centrifugal dust collector which has. 請求項1〜9のいずれか1項に記載の遠心力集塵装置を本体内に有した構成の電気掃除機。 The vacuum cleaner of the structure which has the centrifugal dust collector of any one of Claims 1-9 in the main body.
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