SEPARATION STRUCTURE FOR DUST CUP OF VACUUM CLEANER
20220400919 · 2022-12-22
Inventors
Cpc classification
A47L9/1691
HUMAN NECESSITIES
International classification
Abstract
A separation structure for a dust cup of a vacuum cleaner is provided and includes a cyclone separator. The cyclone separator is provided with a connecting ring, a plurality of arc blades, a plurality of flat plates, a conical tube and a cylindrical tube. Each arc blade has a top fixedly connected with the connecting ring and a bottom fixedly connected with a respective flat plate. The flat plates are fixedly mounted at a large end of the conical tube. A plurality of air inlets are formed by gaps defined by the connecting ring, the arc blades and the flat plates. The cylindrical tube is fixedly connected with and communicated with the conical tube. A small end of the conical tube is received in the cylindrical tube. An included angle between each arc blade and the respective flat plate is an obtuse angle.
Claims
1. A separation structure for a dust cup of a vacuum cleaner comprising a cyclone separator, wherein the cyclone separator is provided with a connecting ring, a plurality of arc blades, a plurality of flat plates, a conical tube and a cylindrical tube, each of the plurality of arc blades has a top fixedly connected with the connecting ring and a bottom fixedly connected with a respective one of the plurality of flat plates, the plurality of flat plates are fixedly mounted at a large end of the conical tube, a plurality of air inlets are formed by gaps defined by the connecting ring, the plurality of arc blades and the a plurality of flat plates, the cylindrical tube is fixedly connected with and communicated with the conical tube, a small end of the conical tube is received in the cylindrical tube, and an included angle between each of the plurality of arc blades and the respective one of the plurality of flat plates is an obtuse angle.
2. The separation structure according to claim 1, wherein the cyclone separator is provided with four arc blades and four flat plates, the four arc blades and the four plates are uniformly arranged at the large end of the conical tube along a circumference of the large end to define four air inlets.
3. The separation structure according to claim 2, wherein the small end of the conical tube is provided with four dust discharging openings and one dust falling opening.
4. The separation structure according to claim 3, further comprising a dust cup, a dust-proof skirt, and a filter screen, wherein a bottom of the filter screen is fixedly connected to the dust-proof skirt, the dust-proof skirt and the filter screen are received in the dust cup, and a bottom of the cylindrical tube abuts on a bottom wall of the dust cup.
5. The separation structure according to claim 4, wherein a height from an upper surface of the connecting ring to a lower surface of the flat plate is H1, a height of the conical tube is H2, and a ratio of H2 to H1 is in a range of 2 to 3.
6. The separation structure according to claim 5, wherein a height of the filter screen is H3, and a ratio of H3 to H1 is in a range of 2 to 2.5.
7. The separation structure according to claim 6, wherein a maximum outer diameter of the air inlet along a central axis is D1, an outer diameter of the filter screen is D2, and a ratio of D1 to D2 is in a range of 0.8 to 0.9.
8. The separation structure according to claim 7, wherein a distance from an outermost side of the dust-proof skirt to an inner side surface of the dust cup is D3, which is in a range of 6 mm to 10 mm.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0016] In order to illustrate the technical solutions according to the embodiments of the present disclosure more clearly, the accompanying drawings for describing the embodiments are introduced briefly in the following. Apparently, the accompanying drawings in the following description are merely some embodiments of the present disclosure, and those skilled in the art may derive other drawings from the accompanying drawings without creative efforts.
[0017]
[0018]
[0019]
[0020]
DETAILED DESCRIPTION
[0021] For clearer and complete description to the technical schemes of the present disclosure, the present disclosure is described further with reference to the accompanying drawings.
[0022] Referring to
[0023] In this embodiment, the included angle a between the arc blade 12 and the flat plate 13 is 95.5°. A primary separation may occur between a side wall of the dust cup 18 and the filter screen 20, a secondary separation and a tertiary separation may occur in the cyclone separator 10. Herein, the secondary separation occurs in a region from the connecting ring 11 to the plate 13, with a height H1, and the tertiary separation occurs in the conical tube 14 below a bottom of the plate 13, with a height H2. After entering the cyclone separator 10 from the air inlets 21, the air flow rotates in a high speed and meanwhile is accelerated downward, resulting in a good separation effect in the secondary separation and thus ensuring that the air flow enters the tertiary separation with a higher-speed rotating. The flow section of the conical tube 14 along a central axis is gradually reduced to ensure continuous acceleration of the rotating air flow, resulting in a better separation effect. The conical tube 14 is provided at its bottom the dust discharging openings 16 and the dust falling opening 17, with the number of the dust discharging openings 16 corresponding to the number of the air inlet 21, so that it is ensured that the fine dust is removed from the air flow more uniformly at the bottom.
[0024] Further, a height from an upper surface of the connecting ring 11 to a lower surface of the flat plate 13 is H1, i.e., the height for the secondary separation, and the height of the conical tube 14 is H2, i.e., the height of the tertiary separation, and a ratio of H2 to H1 is in a range of 2 to 3. The height of the filter screen is H3, and a ratio of H3 to H1 is in a range of 2 to 2.5. A maximum outer diameter of the air inlet 21 along the central axis is D1, that is, an outer diameter of the connecting ring 11 is D1, and an outer diameter of the filter screen is D2, and a ratio of D1 to D2 is in a range of 0.8 to 0.9. A distance from an outermost side of the dust-proof skirt to an inner side surface of the dust cup is D3, which is in a range of 6 mm to 10 mm.
[0025] In the present embodiment, the mixture of air and waste is sucked into the dust cup 18 from an inlet of the dust cup 18. A rotating air flow is first formed in a flow space between the side wall of the dust cup 18 and the filter screen 20. The primary separation is completed by a combined action of the centrifugal force and the filter screen 20, and a part of the waste with large volume is gradually deposited to the bottom of the dust cup 18. The air flow carrying small particles of the waste through the filter screen 20 enters the cyclone separator 10. Due to the special structural design of the cyclone separator 10, rotation of the air flow is speeded up, so that the small particles are completely separated from the air flow. The air flow enters a filter cotton of the dust cup 18 from a return pipe of the dust cup 18, is sucked and discharged with a motor of the dust cup 18. The small particles of the waste is gradually deposited to the cylindrical tube 15 at the bottom. The ratio of D1 to D2 is greater than 0.8 to ensure air intake efficiency. D3 is in the range of 6 mm to 10 mm, so as to prevent the waste at the bottom from floating up with stirring by the air flow.
[0026] It should be appreciated that the present disclosure may have various embodiments, and other embodiments obtained by those skilled in the art based on the embodiment in the present description without any creative effort fall within the protection scope of the present disclosure.