CN113477421B

CN113477421B - Unpowered cyclone claw solid-liquid separator and separation method

Info

Publication number: CN113477421B
Application number: CN202110847338.0A
Authority: CN
Inventors: 贺诚; 大卫·阮
Original assignee: Individual
Current assignee: Individual
Priority date: 2021-07-27
Filing date: 2021-07-27
Publication date: 2023-04-18
Anticipated expiration: 2041-07-27
Also published as: CN113477421A

Abstract

The invention discloses an unpowered cyclone claw solid-liquid separator which comprises a shell with an upper barrel and a lower barrel, wherein a cyclone claw generator is arranged in the upper barrel, the lower barrel is a precipitate storage cavity, the cyclone claw generator comprises a plurality of cone parallel groove arrays stacked together, and a plurality of parallel groove walls arranged in parallel are arranged on the cone parallel groove arrays. In addition, the separation method based on the unpowered cyclone claw solid-liquid separator is also provided: firstly, the inflow main flow is divided, and then the suspended particles in the inflow are grabbed to a relatively quiet tank bottom from a rapid inflow by utilizing the rotational flow generated in parallel tanks when the divided flow flows through the notches above the cone parallel tank arrays, so that the interference of the main flow is reduced, the distance between the suspended particles and the tank bottom is shortened, the sedimentation of the suspended particles (particularly the light and small particles which are easy to interfere) in the sewage is promoted, and the capability of capturing the light and small particles under the condition of large inflow is obviously improved.

Description

Unpowered cyclone claw solid-liquid separator and separation method

Technical Field

The invention relates to a solid-liquid separator with unpowered cyclone claws and a separation method, belonging to the technical field of rain sewage treatment and environmental protection.

Background

The urban rain season rainwater runoff, in particular to the surface runoff formed in the early stage of heavy rain or heavy rain and the combined overflow sewage have the characteristics of large instantaneous water amount, high solid suspended matter content, large pollution load and the like. If the waste water is directly discharged into urban water without treatment, serious pollution is caused to the waste water. The method has the advantages of simple structure, small occupied area, long service life, convenient maintenance and management and the like, has better effect of removing larger suspended particles, and is being applied more and more. However, almost all unpowered cyclones currently in use have a common problem: the removal of small size particles is not ideal in the case of large inflows. The research and application in the aspect of China are few, and no mature technology and equipment belong to the China. With the gradual importance of initial rainwater runoff and combined overflow sewage pollution in China and the large-scale development and implementation of sponge cities at the present stage, the solid-liquid cyclone separation technology will become a focus area.

Meanwhile, in the field of urban and rural sewage treatment, sewage desanding is always a common problem, for example, the desanding effect is poor, which can cause the aggravation of the abrasion of a series of subsequent equipment on the one hand, and on the other hand, can also cause the deposition of a large amount of sand in the process units such as the primary sedimentation tank, the aeration tank, the sludge storage tank and the sludge digestion tank, even block pipelines, and seriously affect the production. Due to the influence of factors such as large-scale urban construction and imperfect pipe networks, the sand content of domestic sewage is generally higher, and the importance of sewage sand removal is more highlighted. The common sewage sand removal method is to use various different grit chambers, such as a gravity grit chamber, an explosion gas grit chamber, an inclined plate or inclined tube grit chamber, a rotational flow grit chamber and the like, and research results show that the grit chambers can only effectively remove sand grains with the size larger than 0.2mm, the occupied area is large, and a large amount of energy is consumed.

Therefore, how to effectively remove smaller and lighter particles from various rain water on a large scale has been a problem to be solved. The research finds that: 1. the removal of particles with a size of less than 0.25mm is the key to sewage treatment, because in runoff and other sewage, the heavy metal content of the small particles accounts for more than 80% of the total load; 2. more than half of the deposit size is greater than 0.3mm but only accounts for less than 15% of the total phosphorus and nitrogen; 3. half of the heavy metal adheres to particles between 0.06 and 0.20mm in size. Effective removal of fine particulate matter from water is important as smaller particles are found to cause more environmental pollution.

The main reason why various solid-liquid cyclone separators cannot effectively remove light and small suspended particles at present is that the suspended particles always run together with a main flow entering water in the separators. Based on the above, the invention provides an unpowered cyclone claw solid-liquid separator and a separation method, which utilize the cyclone generated in parallel grooves when main flow flows through the groove openings above the parallel groove array to grab suspended particles in inflow from rapid inflow to a relatively quiet groove bottom so as to reduce the interference of the main flow and shorten the distance between the suspended particles and the groove bottom, thereby promoting the sedimentation of the suspended particles (especially light and small particles which are easy to be interfered).

Disclosure of Invention

The purpose of the invention is as follows: aiming at the problems in the prior art, the invention provides the unpowered cyclone claw solid-liquid separator and the separation method, which can effectively remove suspended particles with various sizes in sewage, can obviously improve the capability of capturing light and small particles under the condition of large inflow, have no energy consumption, no secondary pollution risk, high efficiency, economy and easy maintenance.

The technical scheme is as follows: in order to achieve the purpose, the invention provides an unpowered cyclone claw solid-liquid separator which comprises a shell and a water inlet and outlet device on the shell, wherein the shell is of an upper barrel and lower cone structure, a cyclone claw generator is arranged in an upper barrel, a lower cone is a sediment storage cavity, the cyclone claw generator comprises a plurality of cone parallel groove arrays stacked together, each cone parallel groove array comprises a shell of the upper barrel and the lower barrel, the top of the shell is provided with an opening, the shell is provided with a plurality of parallel groove walls arranged in parallel, and the parallel groove walls extend along an upper cone surface of the shell.

Furthermore, the water inlet and outlet device comprises a water outlet pipe, a water inlet pipe, a right-angle bent pipe and a vertical water pipe which are sequentially communicated, wherein the pipe wall of the vertical water pipe is provided with round holes, and the round holes which are axially distributed are communicated with the treatment cavities among the cones and the groove arrays so as to realize the diversion effect of the water inlet main flow; the water outlet pipe is communicated with the upper cylinder of the shell, and the shell is provided with a partition plate for separating inlet water from outlet water.

Furthermore, aiming at the condition that large-size suspended substances in water need to be removed firstly, the water inlet and outlet device further comprises a water inlet pool, a water outlet pool and a filter screen, wherein the water inlet pool and the water outlet pool are arranged on the outer cylindrical surface of the shell in parallel, the water inlet pool is communicated with each treatment cavity through the filter screen, the right-angle bent pipe and the vertical water pipe are arranged in the water inlet pool, and the water outlet pipe is communicated with each treatment cavity through the water outlet pool.

Furthermore, the water inlet and outlet device also comprises a honeycomb plate, and the water inlet pool is communicated with each treatment cavity sequentially through the filter screen and the honeycomb plate. Inflow through the filter screen further flows into each treatment cavity through the honeycomb screen plate, the honeycomb screen plate is used for rectifying, water flow is forced to move along the horizontal direction more uniformly, and therefore rotational flow can be generated in the parallel grooves more effectively, generated rotational flow is more regular, and efficiency of capturing suspended particles is improved.

Further, the cone parallel groove array comprises an uppermost layer, a second layer and a third layer to a bottommost layer, wherein the top opening of the cone parallel groove array on the uppermost layer is larger than that of the second layer, the top opening of the cone parallel groove array on the second layer is larger than that of the third layer, the top opening of the cone parallel groove array on the third layer to the bottommost layer is consistent in size, inner cylinders are arranged at the top opening of the cone parallel groove array on the third layer to the bottommost layer, and adjacent inner cylinders are sequentially butted to form an inner channel communicated with a sediment storage cavity so as to ensure that the sediment storage cavity is basically isolated from main inflow water.

Furthermore, the tail end of the parallel groove wall is connected with a particle conveying channel, the particle conveying channel extends along the outer cylinder surface of the shell, and the particle conveying channels on the adjacent cone parallel groove arrays are butted up and down to form a settling channel communicated with the sediment storage cavity, so that the solid particles captured by each layer are conveyed into the sediment storage cavity under the condition of no water flow interference.

Furthermore, the parallel grooves between the particle conveying channel and the parallel groove walls are in one-to-one correspondence, the side walls of the particle conveying channel are provided with channel inlets, the tail parts of the parallel grooves are divided into two parts, the groove bottoms of half of the parallel grooves are communicated with the channel inlets, and the groove bottoms of the other half of the parallel grooves are provided with flanges used for guiding particles to the channel inlets.

Furthermore, the separator still includes self-cleaning device, self-cleaning device is including the spray pipe of intercommunication high pressure water source, the side limit is equipped with the pipeline that is used for pegging graft the spray pipe on the parallel cell wall, be equipped with the washing mouth of a plurality of intercommunication pipelines on the parallel cell wall, be equipped with the water jet that corresponds with the washing mouth on the spray pipe.

In addition, a separation method based on the unpowered cyclone claw solid-liquid separator comprises the following steps: firstly, the water inlet and outlet device is used for shunting the water inlet main flow, then the cyclone generated in the parallel grooves when the shunted water flows through the notches above the cone parallel groove array is used for catching suspended particles in the inflow from the rapid inflow to the relatively quiet groove bottom, and finally sediments falling on the parallel groove bottom or the parallel groove walls slide to a sediment storage cavity separated from the main flow along the steep groove bottom inclined surface.

Further, the separation method further comprises: finally, the sediment falling on the bottom or the walls of the parallel groove slides into the particle conveying channel along the steep slope of the bottom of the groove and falls into the sediment storage cavity along the particle conveying channel.

Has the advantages that: compared with the prior art, the unpowered cyclone claw solid-liquid separator and the separation method provided by the invention have the following advantages:

1. the cyclone claw solid-liquid separator can effectively remove suspended particles with various sizes in sewage, and can obviously improve the capability of capturing light and small particles under the condition of large inflow;

2. the water to be treated flows away from the water outlet pipe after surrounding the cone and making a groove array for one circle, and the liquid does not need to make a sharp turn at a large angle in the whole flowing process, so that the water resistance of the whole system is small, the head loss is low, and no special requirements are made on the heights of the water inlet and outlet pipe orifices and the relative heights between the water inlet and outlet pipe orifices;

3. the method has the advantages of no need of external power, no energy consumption, no moving parts, inflow and captured particle separation, no secondary pollution risk, reliable operation, convenient cleaning, easy maintenance and the like, can treat all inflow, is easy to increase the treatment capacity, and obtains higher treatment efficiency in more economic occupied area.

Drawings

FIG. 1 is a schematic overall structure diagram of a first embodiment of the present invention;

FIG. 2 is a schematic structural diagram of a housing according to a first embodiment of the invention;

FIG. 3 is a schematic overall structure diagram of a second embodiment of the present invention;

FIG. 4 is a schematic structural diagram of a housing according to a second embodiment of the present invention;

FIG. 5 is a schematic structural diagram of a swirling claw generator according to an embodiment of the present invention;

FIG. 6 is a schematic structural diagram of an uppermost cone parallel groove array according to an embodiment of the present invention;

FIG. 7 is a schematic structural diagram of a second-layer pyramid parallel groove array according to an embodiment of the present invention;

FIG. 8 is a schematic structural diagram of a third-to-bottommost cone parallel groove array according to an embodiment of the present invention;

FIG. 9 is a schematic structural diagram of a water inlet and outlet device according to a first embodiment of the present invention;

FIG. 10 is a schematic structural diagram of another parallel pyramidal groove array according to an embodiment of the present invention;

FIG. 11 is a schematic structural diagram of parallel slot walls of different shapes according to a first embodiment of the present invention;

FIG. 12 is a schematic view of a particle transport channel according to an embodiment of the present invention;

FIG. 13 is a schematic vertical cross-sectional view of a first embodiment of the present invention;

FIG. 14 is a schematic view of a structure of a parallel tank wall and an automatic cleaning device according to an embodiment of the present invention;

FIG. 15 is a numerical simulation of the swirling flow generated in the parallel channels when water flows through the parallel channels at 90 degrees in the present invention;

FIG. 16 is a schematic view of the overall structure of the third embodiment of the present invention;

the reference numerals in the figures include: 1. the device comprises a shell, 2, a support, 3, a swirling flow claw generator, 4, a streaming baffle, 5, a sampling tube, 6, a sampling port, 7, a right-angle bent tube, 8, a vertical water pipe, 9, a water inlet pipe, 10, a water outlet pipe, 11, a cone parallel groove array, 12, a honeycomb plate, 13, a filter screen, 14, a water inlet baffle, 15, parallel groove walls, 16, a particle conveying channel, 17, a circular baffle, 18, a precipitate storage cavity, 19, an inner channel, 20, a swirling flow, 21, a channel inlet, 22, a partition plate, 23, a circular opening, 24, a water inlet pool, 25, a water outlet pool, 26, a water spraying pipe, 27, a cleaning port, 28, a treatment cavity, 29, a water inlet opening, 30 and a flange.

Detailed Description

The following description of the preferred embodiments of the present invention with reference to the accompanying drawings will more clearly and completely illustrate the technical solutions of the present invention.

As shown in fig. 1-2, an unpowered cyclone claw solid-liquid separator comprises a housing 1 and a water inlet and outlet device on the housing, wherein the housing 1 is of an upper barrel and a lower barrel, a cyclone claw generator 3 is arranged in an upper barrel, a lower cone (the inclination should not be less than 45 degrees) is a precipitate storage cavity 18, the cyclone claw generator 3 comprises a plurality of cone parallel groove arrays 11 stacked together, the cone parallel groove arrays 11 comprise a housing of the upper barrel and the lower barrel, a circular opening 23 is arranged at the top of the housing, a plurality of parallel groove walls 15 arranged in parallel are arranged on a conical surface (the inclination should not be less than 45 degrees) of the housing, and the parallel groove walls 15 extend along the upper conical surface of the housing. The bottom of the housing 1 is provided with a plurality of supports 2 for supporting the swirling flow claw generator 3 to ensure that the caught suspended particles smoothly fall into the sediment storage chamber 18.

The rotational flow claw solid-liquid separator adopts the basic principle that the rotational flow generated in the parallel grooves when the main flow flows through the notches above the parallel groove arrays takes away suspended particles in the main flow, so that the interference of main flow disturbance force on the captured suspended particles is greatly reduced. As the inflow rate increases, although the residence time of the fluid in the separator is shortened, the probability of entrained particles is relatively increased since the strength of the swirl generated by the main flow will increase. The comparative experiment result shows that the particle removing efficiency of the cyclone claw solid-liquid separator is much less influenced by the inflow flow rate than that of other similar equipment, and the cyclone claw solid-liquid separator still has the advantage of obviously removing light and small suspended particles under the condition of large inflow rate.

In this embodiment, the water inlet and outlet device includes outlet pipe 10, inlet tube 9 that set up side by side, and inlet tube 9 passes through right angle return bend 7 and perpendicular water pipe 8 intercommunication, and perpendicular water pipe 8 is opened at the co-altitude not has the round hole, and the distribution and the aperture of round hole are decided by concrete application, and the round hole through the axial arrangement communicates each cone and moves the treatment chamber 28 between the groove matrix 11. The water outlet pipe 10 is communicated with the top of the upper cylinder body, and a partition plate 22 for separating inlet water from outlet water is arranged on the shell 1.

Furthermore, the side edge of the cone parallel groove array 11 is provided with a water inlet opening 29, so that the vertical water pipe 8 can extend to the bottom of the rotational flow claw generator 3 along the water inlet opening 29, and the bottom of the vertical water pipe 8 can be made into a cone shape, so that the opening at the bottom of the water pipe is smaller than the pipe diameter of the vertical water pipe. As shown in fig. 9, in order to prevent the inflow water from flowing into the sediment storage chamber, an inflow baffle 14 may be provided at the bottom of the vertical water pipe (i.e., below the water inlet openings of the bottom most cone parallel array).

After entering water from the water inlet pipe and entering the cyclone claw solid-liquid separator, the water flows into the vertical water pipe through the right-angle bent pipe, because the holes are distributed on the vertical water pipe at different heights, and the bottom opening of the vertical pipe can be connected with the tail pipe with the diameter gradually reduced according to the condition, the flow of the water is uniformly distributed in different water depths after the water flows out of the vertical water pipe, in other words, the water quantity flowing into the cones on different layers and the groove arrays is basically the same, and the inflow is efficiently divided.

As shown in fig. 3-4, for the application situation that large-sized suspended substances in the water need to be removed first, a water inlet tank 24 and a water outlet tank 25 need to be added to the housing 1, the water inlet tank 24 and the water outlet tank 25 are arranged in parallel on the outer cylindrical surface of the housing 1, the water inlet tank 24 is communicated with each treatment cavity 28 through the filter screen 13 and the honeycomb panel 12 in sequence, the right-angle elbow 7 and the vertical water pipe 8 are arranged in the water inlet tank 24, and the water outlet pipe 10 is communicated with each treatment cavity 28 through the water outlet tank 25.

The filter screen prevents large-size suspended matters in water from entering each treatment cavity 28, inflow of the filter screen is further rectified through the honeycomb screen plate, water flow is forced to uniformly move along the horizontal direction, accordingly, rotational flow can be generated in the parallel grooves more effectively, the generated rotational flow is more regular, and efficiency of capturing suspended particles is improved.

Furthermore, the height of the bottom of the water inlet pool is not higher than that of the bottom of the rotational flow claw generator, and the size of the water outlet pool is not larger than that of the water inlet pool; the width and length of the filter screen should cover the whole water inlet channel, and the mesh aperture of the filter screen should be determined by specific application and should not be smaller than 3mm generally; the total area of the openings of the honeycomb plate is at least 20% larger than the section of the water inlet pipe, the width and the length of the openings of the honeycomb plate can cover the whole water inlet channel, the thickness of the openings of the honeycomb plate is not less than 10cm, and the shape of the openings of the single honeycomb plate is not limited.

Because the cone parallel groove array is composed of a cone with a smooth surface and a plurality of parallel groove walls which are arranged in parallel, the structure of the cone parallel groove array is slightly different according to different installation positions, but the working principle of the cone parallel groove array is the same, and the sizes of the openings at the bottoms of the cones of all the cone parallel groove arrays are the same. As shown in fig. 6-8, the circular opening of the top cone parallel groove array is larger than that of the second layer, the circular opening of the second cone parallel groove array is larger than that of the third layer (the height of the circular opening is higher than that of the first layer but lower than that of the third cone parallel groove array), the circular openings of the third layer to the bottom cone parallel groove array are consistent in size, inner cylinders are arranged at the circular openings of the third layer to the bottom cone parallel groove array, and adjacent inner cylinders are sequentially butted to form an inner channel 19 communicated with the sediment storage cavity. That is, from the third layer, the structure of the parallel groove array of each layer of cones is basically the same.

As shown in fig. 13, the sediment storage chamber is substantially isolated from the main flow, and no other passage is available except for a small amount of water that can enter the sediment storage chamber along the particle transfer passage, so that the collected sediment will remain in the sediment storage chamber until it is removed, thereby preventing secondary pollution from occurring. In addition, a bypass baffle 4 may be installed at the bottom of the housing to prevent any possible bypass flow in the sediment storage chamber.

Furthermore, the parallel slot walls can have different arrangement modes according to different conditions: it may run along the cone radial line as shown in fig. 6-8, or at an angle to the cone radial line as shown in fig. 10; the parallel groove walls can be arranged perpendicular to the conical surface of the shell and can also be inclined to the conical surface of the shell at a small angle; the height of the parallel groove wall is not less than the net distance between two parallel groove walls, and the net distance between the parallel groove walls is different from top to bottom, so the height of the same parallel groove wall can be different from top to bottom. In some special applications, the parallel groove wall can be made to be zero height, i.e. the cone surface no longer has parallel grooves, which will evolve into a cone slope.

As shown in fig. 11, the parallel groove walls may have different shapes and the cross section may be: a-b, flat top and flat bottom, c, flat bottom and triangular top, d, flat top and bottom right lower corner are recessed, e, top is triangular and bottom right lower corner is recessed.

As shown in fig. 5, the tail end of the parallel groove wall 15 is connected with a particle conveying channel 16, the particle conveying channel 16 extends vertically along the outer cylindrical surface of the shell, and the particle conveying channels 16 on the adjacent parallel cone groove arrays 11 are butted up and down to form a settling channel communicated with a sediment storage cavity 18, so that solid particles captured in each layer are conveyed into the sediment storage cavity without any interference of water flow.

When the device is operated, firstly the main stream of the inlet water is shunted, then the suspended particles in the inlet flow are caught to the relatively quiet tank bottom from the rapid inlet flow by utilizing the rotational flow generated in the parallel tank when the shunted flow flows through the notches above the cone parallel tank array, finally the sediment falling on the parallel tank bottom or the parallel tank wall slides into the particle conveying channel along the steep tank bottom inclined plane and falls into the sediment storage cavity separated from the main stream along the particle conveying channel, and the inlet water flows away from the water outlet pipe after surrounding the cone parallel tank array for one circle.

As shown in fig. 12, the particle transport passage 16 and the parallel groove walls 15 are in a one-to-one correspondence, the side wall of the particle transport passage 16 is provided with a passage inlet 21, the tail of the parallel groove is divided into two parts, wherein one half of the groove bottom is communicated with the passage inlet 21, and the other half of the groove bottom is provided with a rib 30 for guiding the particles to the passage inlet 21.

That is, in order to reduce the probability of water flowing into the particle transport passage, the particle transport passage is only connected with the tail of the half groove of the parallel groove, the particles sliding down from the other half of the parallel groove are guided into the particle transport passage by the baffle plate, and the height of the inlet of the passage is lower than that of the wall of the parallel groove.

Furthermore, the top of the particle transport channel 16 of the uppermost cone parallel groove array is provided with a circular baffle 17, which aims to prevent water from flowing into the particle transport channel and force the inlet water to run around the uppermost cone parallel groove array.

Furthermore, the bottom of the sediment storage cavity 18 is provided with a sampling port 6 and a sampling pipe 5 which are used for sampling during the experiment and are not an underflow drain outlet. But also can be used for discharging the collected precipitate in practical application. Another method of cleaning the collected sediment is to suck the bottom sediment from the top opening of the cyclone claw solid-liquid separator through an internal channel 19. The equipment does not need special maintenance management in normal times.

When treating some viscous sewage with the cyclone claw solid-liquid separator, some deposits may be attached in the parallel grooves, and frequent cleaning is required in order to maintain the working efficiency of the cyclone claw solid-liquid separator, thereby providing an automatic cleaning apparatus. As shown in fig. 14, the automatic cleaning device includes a spray pipe 26 communicated with a high-pressure water source, a pipeline for inserting the spray pipe 26 is opened on the upper side of the parallel groove wall 15, a plurality of cleaning openings 27 communicated with the pipeline are opened on the parallel groove wall 15, and a spray opening corresponding to the cleaning opening 27 is opened on the spray pipe 26.

Further, the upper ends of all the spray pipes 26 inserted into the pipe are communicated with each other and connected with a high-pressure water source, and the lower ends of the spray pipes 26 are closed. When cleaning is required, the connected high pressure water is opened and the high pressure water is ejected from the cleaning ports 27 in the parallel tank walls 15 to remove the deposits in the tank.

As shown in fig. 15, when the incoming water is circulated between the parallel arrays of cones, due to the kinetic power and direction of travel of the water stream, a swirling flow 20 is created in the parallel channels as it passes through the slots above the parallel channels at 90 degrees (or nearly 90 degrees) to the direction of extension of the parallel channels. Based on this, the present invention promotes the precipitation of suspended particles from several aspects: firstly, the divided inflow is limited in a processing cavity between the cone parallel groove arrays, so that the probability of capturing suspended particles by rotational flow can be increased to a great extent; secondly, the suspended particles in the main stream can be brought to a relatively quiet tank bottom part from the rapid main stream to reduce the interference of the main stream, and the distance between the suspended particles and the tank bottom is shortened; finally, the contact area of the inclined plates which can promote the sedimentation of the particles is greatly increased, and the sediments falling on the bottom of the parallel groove or the parallel groove walls slide to the particle conveying channel at the tail end along the steep inclined surface of the bottom of the groove, because each layer of particle conveying channel is connected to form an almost closed long channel, and the entering sediments are always conveyed to the sediment storage cavity at the bottom.

The cyclone claw solid-liquid separation equipment provided by the invention can be used as a high-efficiency solid-liquid separator or a sedimentation tank for treating rainwater runoff, combined overflow sewage, urban and rural sewage, mining, oil extraction and other sewage, has no special requirements on a use area, and can be installed under the ground or on the ground.

When in use, the rainwater and sewage supply pipe is connected with the water inlet pipe, and the water outlet pipe is connected with the discharge pipe to run. When the cyclone claw solid-liquid separator is installed underground, a hole needs to be formed in the ground right above the central hole of the cyclone claw generator so as to suck and remove sediments. For the cyclone claw solid-liquid separator with the water inlet and outlet pool, the ground right above the water inlet pool is also provided with holes for absorbing large-size substances.

Under the condition that the diameter of the rotational flow claw generator is determined, the required stacking number of the cone parallel groove arrays can be determined according to the requirements of treatment flow and efficiency. Because the cyclone claw generator is formed by vertically stacking a plurality of cone parallel groove arrays, the processing capacity of the cyclone claw solid-liquid separator can be improved by increasing the stacking number of the cone parallel groove arrays without increasing the diameter of the separator, thereby obtaining higher processing efficiency in more economic floor area.

The above embodiments relate to a design framework based on a cylindrical device, which can be modified to a similar device of an elliptical (as shown in fig. 16) or other polygonal configuration, of course, under the same principles.

Therefore, the above detailed description merely describes preferred embodiments of the present invention and does not limit the scope of the present invention. Without departing from the spirit and scope of the present invention, it should be understood that various changes, substitutions and alterations can be made herein by those skilled in the art without departing from the spirit and scope of the invention as defined by the appended claims and their equivalents.

Claims

1. The unpowered cyclone claw solid-liquid separator is characterized by comprising a shell and a water inlet and outlet device on the shell, wherein the shell is of an upper barrel and lower cone structure, a cyclone claw generator is arranged in an upper barrel, the lower cone is a precipitate storage cavity, the cyclone claw generator comprises a plurality of cone parallel groove arrays stacked together, each cone parallel groove array comprises a shell of the upper cone and lower barrel structure, a plurality of parallel groove walls arranged in parallel are arranged on the shell, and the parallel groove walls extend along an upper cone surface of the shell;

the water inlet and the water outlet of the water inlet and outlet device are communicated with the treatment cavity among the cone parallel groove arrays, and the shell is provided with a partition plate for separating inlet water from outlet water;

the tail end of the parallel groove wall is connected with a particle conveying channel, the particle conveying channel extends along the outer cylinder surface of the shell, and the particle conveying channels on the adjacent cone parallel groove arrays are in up-and-down butt joint to form a precipitation channel communicated with the precipitate storage cavity;

the parallel grooves between the particle conveying channel and the parallel groove walls are in one-to-one correspondence, the side walls of the particle conveying channel are provided with channel inlets, the tail parts of the parallel grooves are divided into two parts, the groove bottoms of half of the parallel grooves are communicated with the channel inlets, and the groove bottoms of the other half of the parallel grooves are provided with flanges used for guiding particles to the channel inlets.

2. The unpowered cyclone claw solid-liquid separator according to claim 1, wherein the water inlet and outlet device comprises a water outlet pipe, a water inlet pipe, a right-angle elbow pipe and a vertical water pipe, the water inlet pipe, the right-angle elbow pipe and the vertical water pipe are sequentially communicated, a pipe wall of the vertical water pipe is provided with a circular hole, the circular hole is axially distributed to communicate with the treatment cavity between the cone parallel groove arrays, and the water outlet pipe is communicated with the upper cylinder of the shell.

3. The unpowered cyclone claw solid-liquid separator according to claim 2, wherein the water inlet and outlet device further comprises a water inlet tank, a water outlet tank and a filter screen, the water inlet tank and the water outlet tank are arranged on the outer cylindrical surface of the housing in parallel, the water inlet tank is communicated with the treatment chambers through the filter screen, the right-angle elbow pipe and the vertical water pipe are arranged in the water inlet tank, and the water outlet pipe is communicated with the treatment chambers through the water outlet tank.

4. The unpowered cyclone claw solid-liquid separator according to claim 3, wherein the water inlet and outlet device further comprises a honeycomb plate, and the water inlet tank is communicated with the treatment chambers sequentially through a filter screen and the honeycomb plate.

5. The unpowered cyclone claw solid-liquid separator according to claim 1, wherein the conical parallel groove array comprises an uppermost layer, a second layer, a third layer and a bottommost layer, the top of the housing is provided with an opening, wherein the top opening of the uppermost conical parallel groove array is larger than that of the second layer, the top opening of the second conical parallel groove array is larger than that of the third layer, the top openings of the third layer and the bottommost conical parallel groove array are uniform in size, the top openings of the third layer and the bottommost conical parallel groove array are provided with inner cylinders, and adjacent inner cylinders are sequentially butted to form an inner channel communicated with the sediment storage cavity.

6. The unpowered cyclone claw solid-liquid separator according to claim 1 further comprising an automatic cleaning device, wherein the automatic cleaning device comprises a spray pipe communicated with a high-pressure water source, a pipeline for inserting the spray pipe is arranged on the upper side edge of the parallel groove wall, a plurality of cleaning openings communicated with the pipeline are arranged on the parallel groove wall, and a spray opening corresponding to the cleaning opening is arranged on the spray pipe.

7. A method of separating solid-liquid separators based on the unpowered cyclone claw of claim 1, comprising: firstly, the water inlet main flow is divided by the water inlet and outlet device, then the suspended particles in the inflow flow are caught to the relatively quiet tank bottom from the rapid inflow by the rotational flow generated in the parallel tank when the divided flow flows through the notches above the cone parallel tank array, and finally the sediments falling on the parallel tank bottom or the parallel tank walls slide into the granule conveying channel along the inclined plane of the tank bottom and fall into the sediment storage cavity along the granule conveying channel.