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JP4743245B2 - Dust collector and vacuum cleaner provided with the dust collector - Google Patents

Dust collector and vacuum cleaner provided with the dust collector Download PDF

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JP4743245B2
JP4743245B2 JP2008244487A JP2008244487A JP4743245B2 JP 4743245 B2 JP4743245 B2 JP 4743245B2 JP 2008244487 A JP2008244487 A JP 2008244487A JP 2008244487 A JP2008244487 A JP 2008244487A JP 4743245 B2 JP4743245 B2 JP 4743245B2
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dust
air
outlet
outflow
port
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JP2010075793A (en
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崇 松本
剛志 前田
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Mitsubishi Electric Corp
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Description

本発明は、塵埃の回収効率を増加させることができる集塵装置と、この集塵装置を備えた電気掃除機に関する。   The present invention relates to a dust collector capable of increasing dust collection efficiency and a vacuum cleaner provided with the dust collector.

電気掃除機に用いられている集塵装置は、紙や繊維によって形成されたフィルタ体、或いはサイクロン分離機構などの気流力を利用して、空気と塵埃とを分離し、集塵するものである。   A dust collector used in an electric vacuum cleaner separates air and dust by using aerodynamic force such as a filter body formed of paper or fiber, or a cyclone separation mechanism, and collects the dust. .

このうち、遠心分離を用いた集塵装置を備えた電気掃除機として、塵埃を遠心分離する二重円筒状のサイクロン分離筒と、このサイクロン分離筒により空気から分離されたごみを捕捉する補助フィルタを内部に有する集塵ケースとを、独立させて掃除機本体の下ケースに着脱可能に装着し、サイクロン分離筒の排気の一部を集塵ケースを介して電動送風機に流入させるようにしたものが知られている(例えば、特許文献1参照)。   Among them, as a vacuum cleaner equipped with a dust collecting device using centrifugal separation, a double-cylindrical cyclone separation cylinder that centrifuges dust, and an auxiliary filter that captures dust separated from air by the cyclone separation cylinder A dust-collecting case that has an internal structure is detachably attached to the lower case of the vacuum cleaner body so that part of the exhaust from the cyclone separating cylinder flows into the electric blower through the dust-collecting case. Is known (see, for example, Patent Document 1).

また、遠心分離を用いた集塵構造を備えた電気掃除機の他の例として、空気から異物を遠心分離する二重円筒状の第1サイクロンチャンバーと、第1サイクロンチャンバーを経た空気から再度異物を分離する第2サイクロンチャンバーとからなる多重サイクロンユニットと、多重サイクロンユニットの下部に結合され、遠心分離された異物を回収するゴミ回収ユニットとを備えたものも知られている(例えば、特許文献2参照)。   As another example of a vacuum cleaner having a dust collecting structure using centrifugal separation, a double-cylindrical first cyclone chamber for centrifuging foreign matter from air, and foreign matter again from air passing through the first cyclone chamber. Also known is a multi-cyclone unit comprising a second cyclone chamber that separates the gas and a dust collecting unit that is coupled to the lower part of the multi-cyclone unit and collects the separated foreign substances (for example, patent document) 2).

特開2004−65698号公報(第7図)Japanese Patent Laying-Open No. 2004-65698 (FIG. 7) 特開2006−88139号公報(第3図)Japanese Patent Laying-Open No. 2006-88139 (FIG. 3)

しかしながら、従来の二重円筒状のサイクロン分離筒にあっては、内部流路が一様な流路断面積となるように形成されていたため、流れ経路中での粘性摩擦による圧力損失によって逆圧力勾配が生じ、境界層の剥離が生じ易く、損失が大きい。   However, in the conventional double-cylindrical cyclone separation cylinder, the internal flow path is formed so as to have a uniform flow path cross-sectional area, so that the reverse pressure is caused by pressure loss due to viscous friction in the flow path. A gradient occurs, the boundary layer is easily peeled off, and the loss is large.

また、大塵埃と小塵埃を旋回させた場合には、旋回に伴う塵埃間の衝突や壁面との摩擦によって静電気が発生し、旋回室内の壁面へ小塵埃が付着し、集塵ケースへ分離される塵埃が減少し、壁面への塵埃の堆積に従って流路が狭小となり、空気動力学的損失が増大してしまう問題があった。   In addition, when large dust and small dust are swirled, static electricity is generated due to collision between the dust and friction with the wall surface, and small dust adheres to the wall surface inside the swivel chamber and is separated into a dust collection case. As a result, the flow path becomes narrower as dust accumulates on the wall surface, and the aerodynamic loss increases.

また、円筒状の分離部では旋回中心部の圧力が低下し、外壁の円筒に垂直な循環流が生じ、気流から分離した塵埃が舞い上がって塵埃の分離性能が低下するとともに、循環流による空気動力学的損失が生じていた。   In addition, in the cylindrical separation part, the pressure at the center of the swivel is lowered, a circulation flow perpendicular to the cylinder on the outer wall is generated, the dust separated from the air flow rises and the separation performance of the dust is reduced, and the air power by the circulation flow Loss has occurred.

また、集塵ケースやゴミ回収ユニットにおいては、収納された塵埃の一部が、前記逆圧力勾配の影響により集塵ケース内で舞い上がって分離部へと逆流するため、その対策が必要で構成が複雑となっていた。   Moreover, in the dust collection case and the dust collection unit, a part of the stored dust rises in the dust collection case due to the influence of the reverse pressure gradient and flows back to the separation part. It was complicated.

本発明の技術的課題は、空気動力学的損失を抑制できて、塵埃の回収効率を高めることができるようにすることにある。   A technical problem of the present invention is to be able to suppress aerodynamic loss and increase dust collection efficiency.

本発明に係る集塵装置は、1組以上の流入口と流出口との間に形成された略環状の流路の外壁に塵埃排出口を持ち、前記流出口からの空気の流出方向が前記流入口と前記流出口との間の空気の移動方向と略直交方向となるように形成されるとともに、前記流入口から前記流出口にかけて前記流路の断面積がなだらかに減少するように形成された気塵分離部と、前記気塵分離部の外壁の外側に配置され、前記塵埃排出口を介して前記気塵分離部と連なった集塵ケースとを備え、前記塵埃排出口の開口面形状は、前記流出口からの空気の流出方向にある辺を前記流出口からの空気の流出方向とは反対方向にある辺よりも長くした台形状からなるものである。 The dust collector according to the present invention has a dust discharge port on an outer wall of a substantially annular channel formed between one or more sets of inlets and outlets, and the outflow direction of air from the outlets is It is formed so as to be substantially perpendicular to the direction of air movement between the inflow port and the outflow port, and is formed so that the cross-sectional area of the flow path gradually decreases from the inflow port to the outflow port. A dust collecting part, and a dust collecting case arranged outside the outer wall of the dust separating part and connected to the dust separating part through the dust outlet, and the opening shape of the dust outlet Is formed in a trapezoidal shape in which the side in the outflow direction of the air from the outflow port is longer than the side in the direction opposite to the outflow direction of the air from the outflow port .

本発明の集塵装置によれば、略環状の気塵分離部の流入口から流出口にかけて流路断面積をなだらかに減少させているので、流入口から流出口にかけて流速が速まるとともに、圧力も漸増し、気流の旋回に伴った粘性摩擦による圧力損失を回復させることができる。このため、塵埃の回収効率が増加し、空気動力学的損失が減少する。
また、塵埃排出口の開口面形状は、流出口からの空気の流出方向にある辺を流出口からの空気の流出方向とは反対方向にある辺よりも長くした台形状からなるので、塵埃排出口の開口面内における速度分布を平坦化し、塵埃排出口を基点とした集塵ケース内の気流循環を減少させることができる。このため、塵埃の回収効率が増加する。
According to the dust collector of the present invention, the flow passage cross-sectional area is gradually reduced from the inlet to the outlet of the substantially annular dust separation unit, so that the flow velocity increases from the inlet to the outlet and the pressure also increases. The pressure loss due to the viscous friction associated with the swirling of the airflow can be recovered. This increases dust collection efficiency and reduces aerodynamic losses.
The shape of the opening surface of the dust outlet has a trapezoidal shape in which the side in the outflow direction of the air from the outlet is longer than the side in the direction opposite to the direction of the outflow of air from the outlet. It is possible to flatten the velocity distribution in the opening surface of the outlet and reduce the air flow circulation in the dust collection case with the dust discharge port as a base point. For this reason, the collection efficiency of dust increases.

実施形態1.
以下、図示実施形態により本発明を説明する。
図1は本発明の実施形態1に係る集塵装置を備えた電気掃除機の全体構成を示す斜視図、図2はその掃除機本体の構成を示す斜視図、図3はその気塵分離部および集塵ケース部における空気の流れを示す斜視図、図4はその気塵分離部および集塵ケース部における空気の流れを示す横断面図、図5はその気塵分離部および集塵ケース部における空気の流れを示す縦断面図、図6はその集塵装置の空気動力学性能を従来と比較して示すグラフで、縦軸に圧力損失(Pa )を、横軸に体積流量(m3/min )をとっている。
Embodiment 1. FIG.
The present invention will be described below with reference to illustrated embodiments.
FIG. 1 is a perspective view showing the overall configuration of a vacuum cleaner provided with a dust collector according to Embodiment 1 of the present invention, FIG. 2 is a perspective view showing the configuration of the vacuum cleaner body, and FIG. 4 is a perspective view showing the air flow in the dust collecting case part, FIG. 4 is a transverse sectional view showing the air flow in the dust separating part and the dust collecting case part, and FIG. 5 is the dust separating part and the dust collecting case part. FIG. 6 is a graph showing the aerodynamic performance of the dust collector in comparison with the prior art, with the vertical axis representing pressure loss (Pa) and the horizontal axis representing volume flow (m3 / min)).

本実施形態の集塵装置を備えた電気掃除機1は、図1及び図2のようにケース体4及び台座5を有する掃除機本体2と吸込具3を備えている。掃除機本体2には、台座5の下面に、床面を走行可能とする走行車輪6が設けられ、走行車輪6の上方に、台座5を介して電動送風機7が設置され、電動送風機7の上方に、塵埃を気流から分離する気塵分離部8が設置され、気塵分離部8の側方に集塵ケース9が設置されていて、このうち電動送風機7と気塵分離部8はケース体4に内包されるように配置されている。また、掃除機本体2の前側略中央には、吸込具3側の蛇腹ホース3aが着脱自在に接続されるホース接続口10が開口され、吸込具3を介して外部から気流を吸引するようになっている。   The vacuum cleaner 1 provided with the dust collector of this embodiment is equipped with the cleaner main body 2 and the suction tool 3 which have the case body 4 and the base 5 like FIG.1 and FIG.2. The vacuum cleaner body 2 is provided with traveling wheels 6 that can travel on the floor surface on the lower surface of the pedestal 5, and an electric blower 7 is installed above the traveling wheels 6 via the pedestal 5. Above, an air separation unit 8 for separating the dust from the airflow is installed, and a dust collecting case 9 is installed on the side of the air separation unit 8, and the electric blower 7 and the air separation unit 8 are the case. It is arranged so as to be included in the body 4. Further, a hose connection port 10 to which the bellows hose 3a on the suction tool 3 side is detachably connected is opened at the front center of the cleaner body 2 so that airflow is sucked from the outside through the suction tool 3. It has become.

気塵分離部8は、図3乃至図5のようにホース接続口10に連なる流入口40と、流出口41と、集塵ケース9に連なる塵埃排出口54とを有し、外壁50と内壁51と上面52と底面53にて略環状に形成され、かつこの略環状である流路の断面積の流れ経路中の最小面積が流出口41の開口面積と同一か或いはそれ未満となるように設定されている。塵埃排出口54は、気流から分離した塵埃を集塵ケース9に収納するために外壁50に開けたものである。   As shown in FIGS. 3 to 5, the dust separation unit 8 includes an inlet 40 that is continuous with the hose connection port 10, an outlet 41, and a dust discharge port 54 that is continuous with the dust collecting case 9. 51, upper surface 52, and bottom surface 53 are formed in a substantially annular shape, and the minimum area in the flow path of the cross-sectional area of the substantially annular flow path is equal to or less than the opening area of outlet 41. Is set. The dust discharge port 54 is opened in the outer wall 50 in order to store the dust separated from the airflow in the dust collecting case 9.

外壁50の上面から見た外形曲線は、ここでは図4のように代数螺旋(例えば放物螺旋、双曲螺旋、リチュース曲線等)に従う曲線形状とし、内壁51の上面から見た外形曲線は、円形状としている。上面52は、図5のように外壁50と内壁51を接続する曲面に形成されている。底面53は、図5のように流入口40から流出口41に従ってなだらかに上面側に漸近する曲面に形成され、流路断面積が流入口40から流出口41にかけて減少するように構成されている。このため、外壁50の上面側から見た螺旋形を、代数螺旋のうちのアルキメデスの螺旋に従う曲線形状とすることも可能となっている。   The outer shape curve viewed from the upper surface of the outer wall 50 is a curved shape that follows an algebraic spiral (for example, a parabolic spiral, a hyperbolic spiral, a Lithus curve, etc.) as shown in FIG. It has a circular shape. The upper surface 52 is formed as a curved surface connecting the outer wall 50 and the inner wall 51 as shown in FIG. As shown in FIG. 5, the bottom surface 53 is formed in a curved surface that gradually approaches the upper surface side from the inlet 40 to the outlet 41, and the flow path cross-sectional area decreases from the inlet 40 to the outlet 41. . For this reason, it is also possible to make the spiral shape seen from the upper surface side of the outer wall 50 into a curved shape following the Archimedean spiral of the algebraic spiral.

このように構成された本実施形態の集塵装置を備えた電気掃除機を用いて清掃する際、電動送風機7によって生じた負圧により吸込具3からホース接続口10を通じて掃除機本体2へと気流が誘起され、流入口40から気塵分離部8へ塵埃を含んだ気流が流入する。気塵分離部8へ流入した気流は、流出口41へ向かう経路中において旋回流れとなり、塵埃と気流に対して遠心加速度に従った慣性力が働く。その結果、塵埃と気流の密度差に従って塵埃は、外壁50へ漸近する運動軌跡となり、塵埃排出口54を通じて集塵ケース9へ流入する。一方、塵埃が取り除かれた気流は、流出口41へと排出される。   When cleaning is performed using the electric vacuum cleaner provided with the dust collector of the present embodiment configured as described above, the negative pressure generated by the electric blower 7 causes the suction tool 3 to pass through the hose connection port 10 to the cleaner main body 2. Airflow is induced, and airflow including dust flows from the inlet 40 to the dust separation unit 8. The airflow that has flowed into the dust separation unit 8 becomes a swirling flow in the path toward the outlet 41, and an inertial force according to centrifugal acceleration acts on the dust and the airflow. As a result, according to the density difference between the dust and the airflow, the dust becomes a movement locus asymptotic to the outer wall 50 and flows into the dust collecting case 9 through the dust discharge port 54. On the other hand, the airflow from which the dust has been removed is discharged to the outlet 41.

気塵分離部8の外壁50と内壁51は上面から見た外形曲線が半径を異にした円形となる2重円筒分離構造となっている。この場合、既述したように内部流路が一様な流路断面積となっていれば、流入口40から流出口41へと旋回流を生じさせる過程で、乱流による粘性摩擦によって圧力損失が生じるため、逆圧力勾配が発生し、境界層のはく離など空気動力学的損失につながる。しかし、本実施形態のように外壁50の上面から見た外形曲線を代数螺旋に従う曲線とし、底面53を流入口40から流出口41に従ってなだらかに上面側へ漸近させ、流路断面積を縮小せしめる、つまり気塵分離部8の圧力損失量と反比例して流路断面積を減少させることで、流入口40から流出口41にかけて流速が速まり、圧力も漸増し、気流の旋回に伴った粘性摩擦による圧力損失を回復させることができ、正圧力勾配とすることができる。その結果、図6のグラフに示すように従来に比し空気動力学的損失を減少させることができ、塵埃の回収効率が増加する。   The outer wall 50 and the inner wall 51 of the dust separation unit 8 have a double cylindrical separation structure in which the outer shape curves viewed from the top surface are circular with different radii. In this case, as described above, if the internal channel has a uniform channel cross-sectional area, pressure loss due to viscous friction due to turbulent flow in the process of generating a swirling flow from the inlet 40 to the outlet 41. As a result, a reverse pressure gradient occurs, leading to aerodynamic losses such as boundary layer separation. However, as in the present embodiment, the outer shape curve viewed from the upper surface of the outer wall 50 is a curve that follows an algebraic helix, and the bottom surface 53 is gradually approached from the inlet 40 to the upper surface according to the outlet 41 to reduce the channel cross-sectional area. That is, by decreasing the flow path cross-sectional area in inverse proportion to the pressure loss amount of the dust separation unit 8, the flow velocity increases from the inlet 40 to the outlet 41, the pressure gradually increases, and the viscosity accompanying the swirling of the airflow Pressure loss due to friction can be recovered, and a positive pressure gradient can be obtained. As a result, as shown in the graph of FIG. 6, the aerodynamic loss can be reduced as compared with the conventional case, and the dust collection efficiency is increased.

ところで、従来は気塵分離部8では流出口41から電動送風機7へと流路を形成する際に、流出口41において流れの拡大が生じ、空気動力学的損失が発生していた。すなわち、流出口41の開口面積が流路断面積より大きいと流速が減少し、流出口41付近での塵埃の堆積が生じやすくなり、空気動力学的損失が生じ易くなっていた。本実施形態においては、気塵分離部8の外壁50と内壁51と上面52と底面53にて形成される略環状である流路の断面積の流れ経路中における最小面積に対して、流出口41の開口面積を同一か或いはそれ未満に設定している。このため、流出口41部における流れの急拡大を防ぐことができる。この結果、流速の減少を抑制することができ、空気動力学的損失を更に低減することが可能となって、塵埃の回収効率をより向上させることができる。   By the way, conventionally, when the flow path is formed from the outlet 41 to the electric blower 7 in the dust separation unit 8, the flow is enlarged at the outlet 41 and an aerodynamic loss occurs. That is, if the opening area of the outlet 41 is larger than the cross-sectional area of the flow path, the flow velocity is reduced, dust is likely to accumulate near the outlet 41, and aerodynamic loss is likely to occur. In the present embodiment, the outflow port is smaller than the minimum area in the flow path of the cross-sectional area of the substantially annular channel formed by the outer wall 50, the inner wall 51, the upper surface 52, and the bottom surface 53 of the dust separation unit 8. The opening area of 41 is set to be the same or smaller. For this reason, the sudden expansion of the flow in the outlet 41 can be prevented. As a result, a decrease in flow velocity can be suppressed, aerodynamic loss can be further reduced, and dust collection efficiency can be further improved.

実施形態2.
図7は本発明の実施形態2に係る集塵装置の集塵ケース部の構成を示す斜視図であり、図中、前述の実施形態1のものに相当する部分には同一符号を付してある。なお、外壁と内壁と上面と底面にて形成される略環状の構成は、前述の実施形態1のものと同一であるため、説明にあたっては前述の図1乃至図6を参照するものとする。
Embodiment 2. FIG.
FIG. 7 is a perspective view showing the configuration of the dust collecting case portion of the dust collecting apparatus according to Embodiment 2 of the present invention. In the figure, parts corresponding to those of Embodiment 1 described above are given the same reference numerals. is there. The substantially annular configuration formed by the outer wall, the inner wall, the upper surface, and the bottom surface is the same as that of the first embodiment, and therefore, the description will be made with reference to FIGS.

集塵ケース9に収納された塵埃の中には、集塵ケース9内で舞い上がって気塵分離部8へと逆流する塵埃がある。これは、図3における気塵分離部8と略直方体形状の集塵ケース9とを連通させる塵埃排出口54の開口面内において、気塵分離部8から流入する塵埃と気流の間で流入速度がばらつき、その結果、異なった速度分布となることで塵埃排出口54を基点とした集塵ケース9内での気流循環現象が生じることに起因することが本発明者等の実験の結果判明した。さらに、塵埃排出口54の開口面内における圧力分布は、当該塵埃排出口54の上部で低く、下部で高くなることが分かった。   Among the dust stored in the dust collection case 9, there is dust that rises in the dust collection case 9 and flows back to the air separation unit 8. This is because the inflow speed between the dust flowing in from the dust separating unit 8 and the air flow is within the opening surface of the dust outlet 54 that connects the dust separating unit 8 and the substantially rectangular parallelepiped dust collecting case 9 in FIG. As a result of experiments by the present inventors, it was found that the phenomenon of air flow circulation in the dust collection case 9 with the dust discharge port 54 as a base point occurs due to the different speed distribution as a result. . Furthermore, it was found that the pressure distribution in the opening surface of the dust outlet 54 is low at the upper part of the dust outlet 54 and high at the lower part.

そこで、本実施形態の集塵装置では、図7のように塵埃排出口54Aの開口面形状を台形状とし、かつその上辺を下辺の4分の3未満の長さとすることで、塵埃排出口54Aの開口面内における上部での圧力を高め、塵埃排出口54Aの開口面内における速度分布を平坦化した。これにより、塵埃排出口54Aを基点とした集塵ケース9内の気流循環が減少し、塵埃の回収効率を高めることができた。   Therefore, in the dust collector of the present embodiment, the opening shape of the dust discharge port 54A is trapezoidal as shown in FIG. 7, and the upper side is less than three-fourths of the lower side. The pressure at the upper part in the opening surface of 54A was increased, and the velocity distribution in the opening surface of the dust discharge port 54A was flattened. Thereby, the air flow circulation in the dust collecting case 9 with the dust outlet 54A as a base point is reduced, and the dust collection efficiency can be improved.

すなわち、本実施形態においては、掃除機本体2の略環状の気塵分離部8の上面から見た螺旋形を、代数螺旋にて形成し、塵埃分離部8の流出口41の開口面積を流路断面積の流れ経路中の最小面積と同一か或いはそれ未満とし、さらに集塵ケース9の塵埃排出口54Aの形状を台形状とし、かつその上辺を下辺の4分の3未満の長さとしたので、流体損失の少ない集塵装置を実現できた。   That is, in this embodiment, the spiral shape seen from the upper surface of the substantially annular dust separating part 8 of the cleaner body 2 is formed by an algebraic helix, and the opening area of the outlet 41 of the dust separating part 8 is made to flow. The cross-sectional area is equal to or less than the minimum area in the flow path, the shape of the dust outlet 54A of the dust collecting case 9 is trapezoidal, and its upper side is less than three quarters of the lower side. Therefore, it was possible to realize a dust collector with little fluid loss.

なお、前述の各本実施形態では外壁50の上面から見た外形曲線を代数螺旋に従う曲線形状とし、内壁51の上面から見た外形曲線を円形状としたものを例に挙げて説明したが、これらの関係は逆でもよく、このような場合でも前述の各本実施形態と同等の作用効果を奏する。   In each of the above-described embodiments, the outer shape curve viewed from the upper surface of the outer wall 50 is a curved shape that follows an algebraic helix, and the outer shape curve viewed from the upper surface of the inner wall 51 is described as an example. These relationships may be reversed, and even in such a case, the same effects as those of the above-described embodiments can be obtained.

また、前述の各本実施形態では本発明の集塵装置を電気掃除機に適用したものを例に挙げて説明したが、これに限るものでなく、集塵装置が使用される空気調和機や電動工具の塵埃回収機構など、空気を作動流体とする製品、洗濯機の塵埃回収機構といった水を作動流体とする製品への応用も可能であることは言うまでもない。   In each of the above-described embodiments, the dust collector of the present invention is applied to a vacuum cleaner as an example. However, the present invention is not limited to this, and an air conditioner in which the dust collector is used, Needless to say, the present invention can also be applied to products using air as a working fluid, such as a dust collecting mechanism of an electric tool, and products using water as a working fluid, such as a dust collecting mechanism of a washing machine.

本発明の実施形態1に係る集塵装置を備えた電気掃除機の全体構成を示す斜視図である。It is a perspective view which shows the whole structure of the vacuum cleaner provided with the dust collector which concerns on Embodiment 1 of this invention. 本発明の実施形態1に係る集塵装置を備えた電気掃除機の掃除機本体の構成を示す斜視図である。It is a perspective view which shows the structure of the vacuum cleaner main body of the vacuum cleaner provided with the dust collector which concerns on Embodiment 1 of this invention. 本発明の実施形態1に係る集塵装置の気塵分離部および集塵ケース部における空気の流れを示す斜視図である。It is a perspective view which shows the flow of the air in the dust separation part and dust collection case part of the dust collector which concern on Embodiment 1 of this invention. 本発明の実施形態1に係る集塵装置の気塵分離部および集塵ケース部における空気の流れを示す横断面図である。It is a cross-sectional view which shows the flow of the air in the dust separation part and dust collection case part of the dust collector which concern on Embodiment 1 of this invention. 本発明の実施形態1に係る集塵装置の気塵分離部および集塵ケース部における空気の流れを示す縦断面図である。It is a longitudinal cross-sectional view which shows the flow of the air in the dust separation part and dust collection case part of the dust collector which concern on Embodiment 1 of this invention. 本発明の実施形態1に係る集塵装置の空気動力学性能を従来と比較して示すグラフである。It is a graph which shows the aerodynamic performance of the dust collector which concerns on Embodiment 1 of this invention compared with the past. 本発明の実施形態2に係る集塵装置の集塵ケース部の構成を示す斜視図である。It is a perspective view which shows the structure of the dust collection case part of the dust collector which concerns on Embodiment 2 of this invention.

符号の説明Explanation of symbols

1 電気掃除機、8 気塵分離部、9 集塵ケース、40 流入口、41 流出口、54,54A 塵埃排出口。   DESCRIPTION OF SYMBOLS 1 Vacuum cleaner, 8 dust separation part, 9 dust collection case, 40 inflow port, 41 outflow port, 54,54A Dust discharge port.

Claims (7)

1組以上の流入口と流出口との間に形成された略環状の流路の外壁に塵埃排出口を持ち、前記流出口からの空気の流出方向が前記流入口と前記流出口との間の空気の移動方向と略直交方向となるように形成されるとともに、前記流入口から前記流出口にかけて前記流路の断面積がなだらかに減少するように形成された気塵分離部と
前記気塵分離部の外壁の外側に配置され、前記塵埃排出口を介して前記気塵分離部と連なった集塵ケースと
を備え、
前記塵埃排出口の開口面形状は、前記流出口からの空気の流出方向にある辺を前記流出口からの空気の流出方向とは反対方向にある辺よりも長くした台形状からなることを特徴とする集塵装置。
A dust discharge port is provided on the outer wall of the substantially annular flow path formed between the one or more inflow ports and the outflow port, and the outflow direction of air from the outflow port is between the inflow port and the outflow port. A dust separation part formed so as to be substantially perpendicular to the air moving direction, and formed so that the cross-sectional area of the flow path gradually decreases from the inlet to the outlet ,
A dust collection case disposed on the outside of the outer wall of the dust separator, and connected to the dust separator through the dust outlet ;
The shape of the opening surface of the dust discharge port is a trapezoid in which a side in the outflow direction of air from the outflow port is longer than a side in the direction opposite to the outflow direction of air from the outflow port. Dust collector.
前記なだらかに減少とは、前記気塵分離部の圧力損失量と反比例して前記流路断面積を減少させたものであることを特徴とする請求項1記載の集塵装置。 Wherein A gradually decreases, the dust collecting apparatus of claim 1, wherein the inversely with the pressure loss of the gas dust separation unit is obtained by reducing the cross-sectional area of the flow path. 前記気塵分離部の外形形状あるいは内形形状を、螺旋形にしたことを特徴とする請求項1又は請求項2記載の集塵装置。   The dust collector according to claim 1 or 2, wherein an outer shape or an inner shape of the dust separation portion is a spiral shape. 前記螺旋形を、代数螺旋にて形成したことを特徴とする請求項3記載の集塵装置。   4. The dust collecting apparatus according to claim 3, wherein the spiral shape is an algebraic spiral. 記流断面積の最小面積に対して、前記流出口の開口面積を同一か或いはそれ未満としたことを特徴とする請求項1乃至請求項4のいずれかに記載の集塵装置。 For the minimum area of the cross-sectional area of the pre SL channel, dust collecting apparatus according to any one of claims 1 to 4, characterized in that the opening area of the outlet were the same or less. 前記流出口からの空気の流出方向とは反対方向にある辺を前記流出口からの空気の流出方向にある辺の4分の3未満の長さとしたことを特徴とする請求項1乃至請求項5のいずれかに記載の集塵装置。 It claims 1 to, characterized in that a length of less than three-quarters of the the direction of flow of air from the outlet port is an edge in the opposite direction to the outflow direction of the air from the outlet side The dust collector according to any one of 5 . 請求項1乃至請求項のいずれかに記載の集塵装置を備えた電気掃除機。 The vacuum cleaner provided with the dust collector in any one of Claims 1 thru | or 6 .
JP2008244487A 2008-09-24 2008-09-24 Dust collector and vacuum cleaner provided with the dust collector Expired - Fee Related JP4743245B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10071328B2 (en) 2014-10-22 2018-09-11 Dyson Technology Limited Apparatus for separating particles from a fluid
US10143346B2 (en) 2014-10-22 2018-12-04 Dyson Technology Limited Separator for removing dirt particles from an airflow
US10555651B2 (en) 2014-10-22 2020-02-11 Dyson Technology Limited Apparatus for separating particles from an airflow

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* Cited by examiner, † Cited by third party
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GB201320305D0 (en) * 2013-11-18 2014-01-01 Nifco Uk Ltd Apparatus for coalescing particles of a first fluid entrained in a flow of a second fluid

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JPH1026385A (en) * 1996-05-10 1998-01-27 Toto Ltd Range hood equipped with cyclone type dust collector
JP2001121039A (en) * 1999-10-26 2001-05-08 Ishikawajima Harima Heavy Ind Co Ltd Solid separation apparatus
JP2004229712A (en) * 2003-01-28 2004-08-19 Matsushita Electric Ind Co Ltd Vacuum cleaner
JP2006204550A (en) * 2005-01-28 2006-08-10 Hitachi Home & Life Solutions Inc Vacuum cleaner

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1026385A (en) * 1996-05-10 1998-01-27 Toto Ltd Range hood equipped with cyclone type dust collector
JP2001121039A (en) * 1999-10-26 2001-05-08 Ishikawajima Harima Heavy Ind Co Ltd Solid separation apparatus
JP2004229712A (en) * 2003-01-28 2004-08-19 Matsushita Electric Ind Co Ltd Vacuum cleaner
JP2006204550A (en) * 2005-01-28 2006-08-10 Hitachi Home & Life Solutions Inc Vacuum cleaner

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10071328B2 (en) 2014-10-22 2018-09-11 Dyson Technology Limited Apparatus for separating particles from a fluid
US10143346B2 (en) 2014-10-22 2018-12-04 Dyson Technology Limited Separator for removing dirt particles from an airflow
US10555651B2 (en) 2014-10-22 2020-02-11 Dyson Technology Limited Apparatus for separating particles from an airflow

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