CN211035437U - Spiral-flow type fast settling device - Google Patents
Spiral-flow type fast settling device Download PDFInfo
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- CN211035437U CN211035437U CN201921560506.2U CN201921560506U CN211035437U CN 211035437 U CN211035437 U CN 211035437U CN 201921560506 U CN201921560506 U CN 201921560506U CN 211035437 U CN211035437 U CN 211035437U
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- cyclone
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Abstract
The utility model discloses a spiral-flow type rapid sedimentation device, which relates to the technical field of water source sedimentation and filtration and solves the technical problems that the existing filter cannot filter water sources thoroughly and only one filter screen is used to lead the filter screen to generate impurity accumulation and blockage in the process of discharging water sources so as to reduce the working efficiency of the filter, and comprises a tank body, wherein the lower wall surface of the tank body is provided with a sludge discharge port, and the side wall surface of the tank body is provided with a water inlet, the sludge discharge port is connected with a timing discharge device, and sludge at the bottom of the tank body is discharged at regular intervals.
Description
Technical Field
The utility model relates to a water source subsides and filters technical field, specifically is a spiral-flow type subsides device fast.
Background
Sewage treatment, in order to make sewage reach the water quality requirement of discharging into a certain water body or reuse and carry out the process of purifying it, sewage treatment is widely used in each field such as building, agriculture, traffic, energy, petrochemical industry, environmental protection, urban landscape, medical treatment, food and beverage, also increasingly goes into common people's daily life.
In the process of sewage treatment, the sewage to be treated can carry more silt and heavy particles, the sewage to be treated needs to be filtered, impurities in the sewage are cleaned, for example, in the utility model patent named as a cyclone filter with publication number CN2836896, the impurities in a fluid are designed to be separated and settled for three times in the filter, the filtering effect is improved, the blocking probability of a flowmeter is reduced, the service life of the flowmeter is prolonged, the metering error is reduced, meanwhile, the separated impurities are settled in a lower container of the filter, a sewage discharge device is periodically opened for sewage discharge and flushing, a filter gland does not need to be opened for cleaning, the labor intensity of field operation workers is reduced, but the existing filter has poor cyclone effect, and only the impurities are blocked by a filter screen, when the filter is used for a long time, impurities easily block the filter screen, the discharge of a filtered water source is influenced, and the working efficiency of the filter is reduced, so that the water source cannot be effectively cleaned.
SUMMERY OF THE UTILITY MODEL
Not enough to prior art, the utility model provides a spiral-flow type subsides device fast has solved current filter and has thoroughly and only make the filter screen take place impurity with a filter screen and pile up the technical problem who blocks up and reduce filter work efficiency to the filtration at water source inadequately and discharge the water source in-process.
In order to achieve the above purpose, the utility model discloses a following technical scheme realizes: the utility model provides a spiral-flow type quick settlement device, includes a jar body, the mud discharging port has been seted up to jar body lower wall, the water inlet has been seted up to jar body lateral wall face, the delivery port has been seted up on jar body another lateral wall face, the internal chamber of jar has the swirler with the water inlet through the pipe connection, the runner pipe is installed to the swirler lower extreme, install the swash plate filler between runner pipe and the internal face of jar, lie in the swash plate filler below on the runner pipe and install the radiant panel, the internal ceramic membrane ware of receiving that lies in the swirler top of jar installs, the ceramic membrane ware of receiving passes through the pipe connection with the delivery port, jar body.
Preferably, the swirler is circular structure, the outer wall of swirler is equipped with the end of intaking, the end of intaking passes through the pipe connection with the water inlet, be equipped with the honeycomb duct in the swirler, honeycomb duct one end is connected with the end of intaking, the honeycomb duct other end is connected with the stand pipe in the swirler, the stand pipe is quarter semicircle type structure.
Preferably, the diameter of the port of the guide pipe is smaller than that of the water inlet end.
Preferably, the radiant panel is three, three the radiant panel is inverted funnel type structure respectively, and is three the port diameter crescent from top to bottom of radiant panel, three the bottommost radiant panel port covers in circulation pipe lower extreme port in the radiant panel.
Preferably, the inclined plate packing is obliquely arranged between the flow guide pipe and the inner wall surface of the tank body, and a plurality of through holes with the same structure are formed in the inclined plate packing.
Preferably, the bottom of the tank body is of a funnel-shaped structure.
Preferably, the top of the tank body is of an arc-shaped structure.
Preferably, the lower wall surface of the tank body is provided with a support frame at one side of the sludge discharge port.
Advantageous effects
The utility model provides a spiral-flow type subsides device fast, solved current filter to the filtration at water source thoroughly inadequately and discharge the water source in-process and only make the filter screen take place impurity pile up the technical problem who blocks up and reduce filter work efficiency with a filter screen, the utility model discloses a cyclone produces the whirl with pending sewage drainage, and increase the whirl route of sewage through the runner pipe, make impurity such as mud subside downwards along with the action of gravity, improve the settlement efficiency of sewage, and through the radiant panel, swash plate filler and ceramic membrane water collector filter the water after subsiding once more, block partial mud and the impurity that the water after the whirl was taken, improve the filtration efficiency of subsider to sewage, arrange the mud mouth outer through connecting regularly discharging to jar body bottom mud.
Drawings
Fig. 1 is the utility model relates to a spiral-flow type subsides device fast's owner looks structural schematic.
Fig. 2 is the utility model relates to a swirler structure sketch map of spiral-flow type quick settlement device.
In the figure: 1-tank body; 2-a sludge discharge port; 3-a water inlet; 4-water outlet; 5-a pipeline; 6-a swirler; 7-a flow-through tube; 8-sloping plate packing; 9-a radiation plate; 10-ceramic membrane water collector; 11-a vent; 12-water inlet end; 13-a flow guide pipe; 14-a guide tube; 15-a through hole; 16-a support frame.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-2, the present invention provides a technical solution: a spiral-flow type rapid sedimentation device comprises a tank body 1, a sludge discharge port 2 is arranged on the lower wall surface of the tank body 1, a water inlet 3 is arranged on the side wall surface of the tank body 1, a water outlet 4 is arranged on the other side wall surface of the tank body 1, an inner cavity of the tank body 1 and the water inlet 3 are connected with a cyclone 6 through a pipeline 5, a runner pipe 7 is arranged at the lower end of the cyclone 6, an inclined plate filler 8 is arranged between the runner pipe 7 and the inner wall surface of the tank body 1, a radiation plate 9 is arranged on the runner pipe 7 and below the inclined plate filler 8, a ceramic membrane water collector 10 is arranged in the tank body 1 and above the cyclone 6, the ceramic membrane water collector 10 is connected with the water outlet 4 through the pipeline 5, a vent 11 is arranged at the top of the tank body 1, the cyclone 6 is of a circular structure, a water inlet end, a flow guide pipe 13 is arranged in the cyclone 6, one end of the flow guide pipe 13 is connected with the water inlet end 12, the other end of the guide pipe 13 in the cyclone 6 is connected with a guide pipe 14, the guide pipe 14 is in a quarter-semicircle structure, the diameter of the port of the guide pipe 14 is smaller than that of the water inlet end 12, the number of the radiation plates 9 is three, the three radiation plates 9 are respectively of an inverted funnel-shaped structure, the diameters of the ports of the three radiation plates 9 are gradually increased from top to bottom, the port of the radiation plate 9 at the bottommost end of the three radiation plates 9 covers the port at the lower end of the circulating pipe 7, the inclined plate packing 8 is obliquely arranged between the guide pipe 13 and the inner wall surface of the tank body 1, a plurality of through holes 15 with the same structure are arranged on the inclined plate packing 8, the bottom of the tank body 1 is of a funnel-shaped structure, the top of the tank body 1 is of an arc-shaped structure, and a support frame 16 is arranged on one side, located on the sludge discharge port 2, of the lower wall surface of the tank body 1.
The following working principles, detailed connecting means thereof, and the following main descriptions of the working principles and processes thereof are well known in the art, and will be referred to by those skilled in the art for the specific connection and operation sequence of the components in the present disclosure.
Example (b): as can be seen from the attached drawings 1-2 of the specification, when in use, sewage to be treated is discharged into the tank body 1 through the water inlet 3 and flows into the cyclone 6, the cyclone 6 is drained through the guide pipe 13, the guide pipe 14 is in a quarter-half-circle structure, so that the sewage to be treated generates a cyclone effect under the action of the guide pipe 14, the sewage which swirls flows downwards under the action of the flow pipe 7, the sludge and impurities settle downwards under the action of gravity and fall to the bottom of the tank body 1, the water after cyclone settlement flows back to the water outlet 4, part of the sludge is brought up and flows to the water outlet 4 in the process that the settled water flows out of the water outlet 4, at the moment, the three radiation plates 9 perform first interception, the intercepted sludge and impurities are in a reversed-leakage hole structure because the radiation plates 9, impurity can be along with the inner wall downward movement of radiant panel 9, and fall to jar body 1 bottom, swash plate filler 8 carries out the interception for the second time, the water source passes through-hole 15 flow direction delivery port, impurity and mud are intercepted, because swash plate filler 8 is installed at jar internal 1 slope, mud and impurity can slide downwards along with swash plate filler 8 wall from this, and subside the bottom of jar body 1, ceramic membrane water collector 10 carries out further filtration absorption with the water source after twice filtering, discharge through delivery port 4, the mud of jar body 1 bottom is through row mud mouth 2 regularly discharge regularly, prevent that the more influence of mud from subsiding the filtration of device to sewage.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation. The use of the phrase "comprising one of the elements does not exclude the presence of other like elements in the process, method, article, or apparatus that comprises the element.
Claims (8)
1. A spiral-flow type rapid sedimentation device comprises a tank body (1) and is characterized in that a sludge discharge port (2) is formed in the lower wall surface of the tank body (1), a water inlet (3) is formed in the side wall surface of the tank body (1), a water outlet (4) is formed in the other side wall surface of the tank body (1), an inner cavity of the tank body (1) and the water inlet (3) are connected with a cyclone (6) through a pipeline (5), a circulating pipe (7) is installed at the lower end of the cyclone (6), an inclined plate filler (8) is installed between the circulating pipe (7) and the inner wall surface of the tank body (1), a radiation plate (9) is installed below the inclined plate filler (8) on the circulating pipe (7), a ceramic membrane water collector (10) is installed above the cyclone (6) in the tank body (1), and the ceramic membrane water collector (10) is connected with the water outlet, the top of the tank body (1) is provided with an air vent (11).
2. The spiral-flow type rapid sedimentation device according to claim 1, wherein the cyclone (6) has a circular structure, the outer wall surface of the cyclone (6) is provided with a water inlet end (12), the water inlet end (12) is connected with the water inlet (3) through a pipeline (5), a guide pipe (13) is arranged in the cyclone (6), one end of the guide pipe (13) is connected with the water inlet end (12), the other end of the guide pipe (13) in the cyclone (6) is connected with a guide pipe (14), and the guide pipe (14) has a quarter-semicircular structure.
3. A cyclonic rapid sedimentation device as claimed in claim 2, wherein the diameter of the end of the guide tube (14) is smaller than the diameter of the inlet end (12).
4. The spiral-flow type rapid sedimentation device according to claim 1, wherein the number of the radiation plates (9) is three, the three radiation plates (9) are in an inverted funnel-shaped structure, the diameters of the three radiation plates (9) are gradually increased from top to bottom, and the port of the radiation plate (9) at the bottom of the three radiation plates (9) covers the lower end port of the circulation pipe (7).
5. The spiral-flow type rapid settling device as claimed in claim 1, wherein the inclined plate packing (8) is obliquely arranged between the flow guide pipe (13) and the inner wall surface of the tank body (1), and a plurality of through holes (15) with the same structure are formed in the inclined plate packing (8).
6. A cyclonic rapid settling device as claimed in claim 1, wherein the bottom of the tank (1) is of a funnel-shaped configuration.
7. A spiral-flow type rapid settling device as claimed in claim 1, wherein the top of the tank (1) is a circular arc structure.
8. A spiral-flow type rapid sedimentation device according to claim 1, wherein a support frame (16) is installed on the lower wall surface of the tank (1) on one side of the sludge discharge port (2).
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CN201921560506.2U CN211035437U (en) | 2019-09-19 | 2019-09-19 | Spiral-flow type fast settling device |
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CN201921560506.2U CN211035437U (en) | 2019-09-19 | 2019-09-19 | Spiral-flow type fast settling device |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN112107886A (en) * | 2020-08-07 | 2020-12-22 | 青岛科技大学 | Separation and purification device for oil phase in oil, water and solid three-phase mixture |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112107886A (en) * | 2020-08-07 | 2020-12-22 | 青岛科技大学 | Separation and purification device for oil phase in oil, water and solid three-phase mixture |
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