CN211255341U - Cocurrent flow flotation solid-liquid separation tank - Google Patents

Cocurrent flow flotation solid-liquid separation tank Download PDF

Info

Publication number
CN211255341U
CN211255341U CN201921591758.1U CN201921591758U CN211255341U CN 211255341 U CN211255341 U CN 211255341U CN 201921591758 U CN201921591758 U CN 201921591758U CN 211255341 U CN211255341 U CN 211255341U
Authority
CN
China
Prior art keywords
subassembly
chamber
mud
pipe
water distribution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201921591758.1U
Other languages
Chinese (zh)
Inventor
戴文强
赵洪启
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wuxi Hi Tech Environmental Protection Equipment Technology Co ltd
Original Assignee
Wuxi Hi Tech Environmental Protection Equipment Technology Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Wuxi Hi Tech Environmental Protection Equipment Technology Co ltd filed Critical Wuxi Hi Tech Environmental Protection Equipment Technology Co ltd
Priority to CN201921591758.1U priority Critical patent/CN211255341U/en
Application granted granted Critical
Publication of CN211255341U publication Critical patent/CN211255341U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Abstract

The utility model relates to a syntropy flow flotation solid-liquid separation pond, including the cell body, the flow direction along rivers is equipped with the contact chamber of mutual intercommunication in proper order in the cell body, room is collected to separation chamber and clear water, be provided with syntropy flow flotation separation subassembly in the separation chamber, syntropy flow flotation separation subassembly includes a plurality of sloping plate subassemblies, the sloping plate subassembly includes the straight board of vertical setting, the top is connected in the entrapment swash plate of straight board bottom, the top is connected in the smooth mud swash plate of entrapment swash plate bottom, the bottom of sloping plate subassembly is provided with the sludge baffle, the sludge baffle is located between the adjacent sloping plate subassembly, the space between sludge baffle and its front side swash plate subassembly is clear water transport chamber, the space between sludge baffle and its rear side swash plate subassembly is mud transport chamber, clear water transport chamber and clear water collection chamber intercommunication. The utility model discloses a syntropy flow flotation solid-liquid separation pond goes out water of high quality, treatment effeciency height.

Description

Cocurrent flow flotation solid-liquid separation tank
Technical Field
The utility model relates to a sewage treatment device especially relates to a cocurrent flow flotation solid-liquid separation pond.
Background
At present, river water treatment has a common characteristic that the minimum treatment amount is tens of thousands of tons every day, and the large treatment amount is millions of tons every day. Maximum processing capacity 2500m capable of being transported by conventional dissolved air floatation single machine in market3Every day, if according to the riverWater treatment capacity 20000m38 pieces are needed for a/day calculation. The number of air floaters ordered by the owner is too large, and the investment cost of the owner is increased. And the conventional pressure dissolved air flotation backflow water amount is designed according to 30%, the lift is designed according to 50 meters, and the converted power cannot be tolerated by owners. Treating river water by adopting a conventional air floatation process. The energy consumption is too high, and the investment cost is too high. The main technical reason for the above problems is that the conventional pressure dissolved air flotation has too low operation efficiency. The design point of the conventional pressure dissolved air floatation hydraulic load is 7-10m3/m2The reflux ratio design point is 30-50%. One of the important factors affecting the efficiency of air floatation sewage treatment is the inclined plate component in the separation chamber. At present, in a common air floatation tank with an inclined plate assembly, the inclined plate assembly is a single inclined plate, and sludge and clear water are not isolated to a certain extent, so that the sludge easily enters a clear water collecting chamber along with water flow, and the quality of the discharged water is reduced.
In view of the above-mentioned defects, the present designer is actively making research and innovation to create a novel structure of cocurrent flow flotation solid-liquid separation tank, so that the tank has more industrial utilization value.
SUMMERY OF THE UTILITY MODEL
In order to solve the technical problem, the utility model aims at providing a cocurrent flow flotation solid-liquid separation pond that goes out water of high quality, treatment effeciency is high.
The utility model discloses a syntropy flow flotation solid-liquid separation pond, including the cell body, the room is collected to contact chamber, separation chamber and the clear water that is equipped with mutual intercommunication in proper order along the flow direction of rivers in the cell body, be provided with syntropy flow flotation separation subassembly in the separation chamber, syntropy flow flotation separation subassembly includes a plurality of ramp assemblies, the ramp assembly includes that straight board, the top of vertical setting connect in the entrapment swash plate of straight board bottom, the smooth mud swash plate of top connection in entrapment swash plate bottom, the bottom of ramp assembly is provided with the sludge baffle, the sludge baffle is located between the adjacent ramp assembly, the space between sludge baffle and its front side swash plate subassembly is clear water transport chamber, the space between sludge baffle and its rear side swash plate subassembly is mud transport chamber, clear water transport chamber with clear water collection chamber intercommunication.
Further, the utility model discloses a cocurrent flow flotation solid-liquid separation pond, be provided with high-speed flocculation separation reactor in the contact chamber, high-speed flocculation separation reactor includes a plurality of folded plate subassemblies, and the folded plate subassembly includes that riser, the top of vertical setting connect in the flocculation of catching swash plate of riser bottom.
Further, the utility model discloses a cocurrent flow flotation solid-liquid separation pond still includes the water distribution subassembly, the water distribution subassembly is responsible for and is located the water distribution that both sides and one end and water distribution were responsible for intercommunication, the other end and contact chamber intercommunication including the water distribution that is located the bottom of the pool and divides the pipe, the water distribution is responsible for the cross section of hole and the cross section of water distribution branch pipe hole and is triangle-shaped.
Further, the utility model discloses a cocurrent flow flotation solid-liquid separation pond, the both sides that the water distribution was responsible for all are provided with the first baffle that bottom and cell body linked firmly, and the top that the water distribution was responsible for still sets up two bottoms and the second baffle that the water distribution was responsible for and is connected, the outside of first baffle does the contact chamber does between first baffle and the adjacent second baffle do the separation chamber does between two second baffles the room is collected to the clear water.
Further, the utility model discloses a cocurrent flow flotation solid-liquid separation pond, be provided with U type clear water collecting vat in the clear water collecting chamber.
Further, the utility model discloses a cocurrent flow flotation solid-liquid separation pond, the bottom of separation chamber is provided with scrapes the mud subassembly, it includes scraper blade installation pole to scrape the mud subassembly, is provided with polylith wedge scraper blade on the scraper blade installation pole, scrapes the mud subassembly still including the installation pole linear drive device who is used for driving scraper blade installation pole back-and-forth movement.
Further, the utility model discloses a cocurrent flow flotation solid-liquid separation pond, be provided with the negative pressure recess on the terminal surface of the great one end of wedge scraper blade size.
Further, the utility model discloses a cocurrent flow flotation solid-liquid separation pond still includes the mud collection subassembly, the mud collection subassembly include with vacuum pump connection's the pipe of taking out the dirt, locate take out set up on the pipe lateral wall of dirt and with a plurality of loudspeaker form soil pick-up mouths of taking out dirt pipe intercommunication, the pipe of taking out the dirt sets up in the bottom of contact chamber.
Further, the utility model discloses a cocurrent flow flotation solid-liquid separation pond, the mud collection subassembly still includes the aeration scouring pipe, the aeration scouring pipe pass through communicating pipe with take out dirty pipe intercommunication.
Further, the utility model discloses a cocurrent flow flotation solid-liquid separation pond still includes the outer subassembly of arranging of mud evacuation, and the outer subassembly of arranging of mud evacuation includes vacuum pump and storing jar, sets up blow vent, filth entry and filth export on the storing jar, and the blow vent passes through a port intercommunication of pipeline and cross valve, and the air inlet and the gas outlet intercommunication of pipeline and vacuum pump, last port and the atmosphere intercommunication of cross valve are passed through respectively to two other ports of cross valve.
Borrow by above-mentioned scheme, the utility model discloses at least, have following advantage: the utility model discloses a syntropy flow flotation solid-liquid separation pond, the high-efficient separation of the wadding body, clear water and mud has been realized to the setting of ramp assembly. The running load is 30-35m3/m2H is increased to 40-50m3/m2H is used as the reference value. The suspended matter in the effluent is increased to 5 mg/L from 15 mg/L, and the target effluent index is close to that of a sand filter. Wherein, the setting of entrapment swash plate has realized the capture to less wadding body, makes it can be along the back come-up of entrapment swash plate and with other wadding body gathering for the wadding body of great volume and finally along the space come-up to the liquid level between the straight board. The setting of smooth mud swash plate for in the mud bucket of separation chamber bottom can be deposited on the surface of smooth mud swash plate and fall into along the smooth mud swash plate to the mud granule of great volume, during the concrete implementation, the inclination of smooth mud swash plate and horizontal plane is greater than the inclination of entrapment swash plate, thereby more does benefit to the landing of mud. In addition, the arrangement of the sludge partition plate enables the sludge conveying cavity for sludge sliding to be isolated from the clear water conveying cavity for clear water circulation to a certain extent, and further achieves the effects of diversion and isolation of sludge and clear water. During specific work, sludge slides along the sludge sliding inclined plate under the action of gravity and falls into the sludge hopper, and because the clear water conveying holes for communicating the clear water conveying cavity with the clear water collecting chamber correspond to the middle position of the sludge baffle plate, sludge particles are not easy to enter the sludge hopper through the clear water conveying cavityThe clear water is collected indoor to separate mud and clear water each other, prevent that mud from entering into the clear water along with rivers and collect indoor, improved the quality of water of final play.
To sum up, the utility model discloses a syntropy flow flotation solid-liquid separation pond goes out water of high quality, treatment effeciency height.
The above description is only an overview of the technical solution of the present invention, and in order to make the technical means of the present invention clearer and can be implemented according to the content of the description, the following detailed description is made with reference to the preferred embodiments of the present invention and accompanying drawings.
Drawings
FIG. 1 is a process system diagram of a co-current flotation solid-liquid separation tank;
FIG. 2 is a schematic elevation view of a co-current flotation solid-liquid separation cell;
FIG. 3 is a schematic top view of the cell body;
FIG. 4 is a schematic right view of a co-current flotation solid-liquid separation cell;
FIG. 5 is a schematic structural diagram of components of the tank body and the water distribution main pipe;
FIG. 6 is a schematic view of the structure of a flocculation separation reactor;
FIG. 7 is a schematic right view of a co-current flotation separation module;
FIG. 8 is a schematic elevation view of a co-current flotation separation module;
FIG. 9 is a schematic structural view of a ramp assembly;
FIG. 10 is a schematic elevation view of the mud scraping assembly;
FIG. 11 is a schematic view of the construction of a wedge-shaped squeegee;
FIG. 12 is a schematic view of the structure of the sludge collection assembly;
FIG. 13 is a schematic view of the structure of the soil pick-up pipe;
FIG. 14 is a schematic end view of a sludge collection assembly;
FIG. 15 is a schematic elevational view of a water distribution assembly;
FIG. 16 is a schematic top view of a water distribution assembly;
FIG. 17 is a side schematic view of a sludge collection assembly;
FIG. 18 is a structural block diagram of a sludge evacuation discharge assembly.
In the figure, a tank body 1, a contact chamber 2, a separation chamber 3, a clear water collection chamber 4, an inclined plate assembly 5, a straight plate 6, a collecting inclined plate 7, a mud sliding inclined plate 8, a mud baffle plate 9, a clear water conveying chamber 10, a mud conveying chamber 11, a flocculent body 12, a clear water conveying hole 13, a laminar flow baffle plate 14, a folded plate assembly 15, a vertical plate 16, a flocculation collecting inclined plate 17, an online self-cleaning releaser 18, a hydraulic distribution plate 19, a water distribution main pipe 20, a water distribution branch pipe 21, a first baffle plate 22, a second baffle plate 23, a U-shaped clear water collecting tank 24, a chain plate rotating slag scraping device 25, a scraper mounting rod 26, a wedge-shaped scraper 27, an electric push-pull rod 28, a negative pressure groove 29, a sewage suction pipe 30, a horn-shaped mud suction port 31, an aeration flushing pipe 32, a communicating pipe 33, a vacuum pump 34, a storage tank 35, a blow-off port 36, an inlet 37, a.
Detailed Description
The following detailed description of the embodiments of the present invention is provided with reference to the accompanying drawings and examples. The following examples are intended to illustrate the invention, but are not intended to limit the scope of the invention.
Referring to fig. 1 to 18, a cocurrent flow flotation solid-liquid separation tank, including cell body 1, contact chamber 2 that communicates each other is equipped with in proper order along the flow direction of rivers in the cell body, separation chamber 3 and clear water collection chamber 4, be provided with cocurrent flow flotation separation subassembly 4 in the separation chamber, cocurrent flow flotation separation subassembly includes a plurality of ramp plate subassemblies 5, ramp plate subassembly includes vertical setting's straight board 6, the top is connected in the entrapment swash plate 7 of straight board bottom, the top is connected in the smooth mud swash plate 8 of entrapment swash plate bottom, ramp plate subassembly's bottom is provided with sludge baffle 9, sludge baffle is located between the adjacent ramp plate subassembly, sludge baffle and the space between its front side ramp plate subassembly carry chamber 10 for clear water, sludge baffle and the space between its rear side ramp plate subassembly are mud and carry chamber 11, clear water carries chamber and clear water collection chamber intercommunication.
Due to the arrangement of the inclined plate assembly, efficient separation of the floccule 12, clear water and sludge is realized. Wherein, the setting of entrapment swash plate has realized the capture to less wadding body, makes it can be along the back come-up of entrapment swash plate and with other wadding body gathering for the wadding body of great volume and finally along the space come-up to the liquid level between the straight board. The setting of smooth mud swash plate for in the mud bucket of separation chamber bottom can be deposited on the surface of smooth mud swash plate and fall into along the smooth mud swash plate to the mud granule of great volume, during the concrete implementation, the inclination of smooth mud swash plate and horizontal plane is greater than the inclination of entrapment swash plate, thereby more does benefit to the landing of mud. In addition, the arrangement of the sludge partition plate enables the sludge conveying cavity for sludge sliding to be isolated from the clear water conveying cavity for clear water circulation to a certain extent, and further achieves the effects of diversion and isolation of sludge and clear water. During specific work, mud slides along the smooth mud swash plate and falls into the sludge bucket under the action of gravity, because the middle part position that the clear water delivery hole 13 that communicates clear water delivery chamber and clear water collection room corresponds the sludge baffle, consequently the mud granule is difficult for carrying the chamber through the clear water and enters into in the clear water collection room to separate mud and clear water each other, prevent that mud from entering into the clear water along with rivers and collect indoorly, improved the quality of water of final play water.
Preferably, the included angle between the collecting inclined plate and the horizontal plane is 55-65 degrees, and the included angle between the mud sliding inclined plate and the horizontal plane is more than 60 degrees.
Preferably, the inclined collection plate forms an angle of 60 degrees with the horizontal plane.
The inclination of the trapping clapboard is set to be 60 degrees, which is more beneficial to trapping and floating of the floccule.
Preferably, a laminar flow partition plate 14 is further arranged between the inclined plate assemblies, and two ends of the laminar flow partition plate are respectively connected with the inclined plate assemblies.
The setting of laminar flow baffle makes its connecting piece as the ramp assembly on the one hand, and on the other hand has realized the laminar flow effect to rivers, makes it be difficult for producing the turbulent flow. The sludge baffle plate can be arranged at the bottom end of the laminar flow baffle plate and is basically vertical to the laminar flow baffle plate.
Preferably, a high-speed flocculation separation reactor is arranged in the contact chamber, the high-speed flocculation separation reactor comprises a plurality of folded plate assemblies 15, each folded plate assembly comprises a vertical plate 16 and a flocculation inclined plate 17, the vertical plate is vertically arranged, and the top end of each folded plate assembly is connected to the bottom end of the corresponding vertical plate.
In specific implementation, the high-speed flocculation separation reactor is arranged at the upper half part of the contact chamber, the height from the hydraulic distribution plate is controlled to be about 300 mm, high-pressure gas-dissolved water flowing out of the on-line self-cleaning releaser 18 forms a micro bubble group with the particle size of 1-10um after energy dissipation treatment, and in the contact chamber, "bubble floc" formed by contact reaction of the bubbles, the floc and the high-molecular medicament flows into the high-speed flocculation separation component after flowing through the distance of about 300 mm to buffer and dissipate energy. At the moment, the high-speed flocculation separation reactor cannot impact flocs in the sewage and cannot crash the floc particles formed in the sewage. After flowing into high-speed flocculation separation reactor inner space, the wadding body grows up along catching the wadding swash plate back and gathering, and the rising speed can be faster and faster, and self rising speed adds the promotion of rivers, makes its rising speed improve more than the twice to accomplish the quick separation of wadding body and clear water. When the flocs float to the liquid level, scum is formed, and clear water turns around in the separation chamber and enters the cocurrent flow flotation separation assembly downwards to continuously finish floating and precipitation of a small amount of flocs. The sewage can reach 99.9 percent of suspended matter removal rate after being treated by the high-speed flocculation separation reactor and the cocurrent flow flotation separation component.
Preferably, an online self-cleaning releaser 18 is arranged on the side wall of the tank body, and the output end of the online self-cleaning releaser is communicated with the contact chamber.
The on-line self-cleaning releaser is a micro-bubble releasing device with a self-cleaning function, and is used for releasing micro-bubbles into a contact chamber, so that the aims of combining flocs and medicaments and forming flocs are fulfilled. The specific structure refers to Chinese patent with publication number 209113526U, an on-line self-cleaning releaser.
Preferably, a hydraulic balance plate 19 with a plurality of water distribution holes on the surface is arranged in the contact chamber, and the high-speed flocculation separation reactor is positioned above the hydraulic balance plate at a distance of 250-350 mm.
Preferably, the device also comprises a water distribution assembly, wherein the water distribution assembly comprises a main water distribution pipe 20 positioned at the bottom of the tank and water distribution pipes 21 positioned at two sides of the main water distribution pipe, one end of each water distribution pipe is communicated with the main water distribution pipe, and the other end of each water distribution pipe is communicated with the contact chamber.
Preferably, the cross section of the inner hole of the water distribution main pipe and the cross section of the inner hole of the water distribution pipe are both triangular.
The arrangement of the water distribution main pipe realizes the input of sewage. During specific work, sewage input to the water distribution main pipe enters the contact chamber through the water distribution pipes on the two sides, and therefore the sewage is input. The water distribution main pipe and the water distribution branch pipe are arranged to be triangular pipe bodies with triangular cross sections, so that sinking flocs can slide into the sludge hopper at the bottom along the side wall of the triangular pipe bodies, sludge is effectively prevented from being deposited on the surfaces of the water distribution main pipe and the water distribution branch pipe, meanwhile, the sludge is conveniently subjected to centralized treatment, and preferably, the included angles between the side walls of the water distribution main pipe and the water distribution branch pipe and the horizontal plane are larger than 55 degrees, so that the sludge can slide down conveniently.
Preferably, the two sides of the main water distribution pipe are provided with first partition plates 22, the bottom ends of which are fixedly connected with the tank body, two second partition plates 23, the bottom ends of which are connected with the main water distribution pipe, are arranged above the main water distribution pipe, the outer side of each first partition plate is a contact chamber, a separation chamber is arranged between each first partition plate and the corresponding adjacent second partition plate, and a clean water collection chamber is arranged between each two second partition plates.
Preferably, the hydraulic distribution plate is respectively connected with the tank body and the first partition plate, and the end part of the water distribution pipe penetrates through the first partition plate and extends into the contact chamber.
Preferably, a U-shaped clear water collecting tank 24 is arranged in the clear water collecting chamber.
Preferably, the second clapboard is provided with a clean water conveying hole 13 which is communicated with the clean water conveying cavity and the clean water collecting chamber.
Preferably, the top of the tank body is provided with a chain plate rotating slag scraping device 25.
The chain plate rotating slag scraping device is used for treating scum on a liquid level, and the specific structural principle of the chain plate rotating slag scraping device can refer to a reverse chain plate type slag scraping mechanism in a rectification sedimentation air floatation water treatment device with the publication number of 202054680U.
Preferably, the bottom of the separation chamber is provided with a mud scraping assembly, the mud scraping assembly comprises a scraper mounting rod 26, a plurality of wedge-shaped scrapers 27 are arranged on the scraper mounting rod, and the mud scraping assembly further comprises a mounting rod linear driving device for driving the scraper mounting rod to move back and forth.
The arrangement of the wedge-shaped scraper and the linear driving device of the mounting rod realizes the scraping operation of the sludge. The scraper mounting rod is used for mounting a wedge-shaped scraper, the wedge-shaped scraper is used for scraping sludge at the bottom of the pool, and the mounting rod linear driving device is used for realizing linear displacement driving on the scraper mounting rod, and can be an electric push-pull rod 28, an air cylinder or an oil cylinder and the like, wherein the electric push-pull rod is preferred. When specifically implementing, the great one end of wedge scraper blade size is towards the exit end of mud, concrete during operation, installation pole linear driving device drives scraper blade installation pole and wedge scraper blade and removes to the mud exit end, thereby it removes to the mud exit end to drive mud, scraper blade installation pole and wedge scraper blade are after that to remove to the opposite direction under installation pole drive arrangement's drive, at its reverse removal's in-process, the mud that is located wedge scraper blade wedge top side just removes to the other end of wedge scraper blade along the inclined plane of wedge scraper blade, thereby make the scraper blade can drive this mud when removing to the mud delivery outlet once more and further remove to the exit end, finally make the mud of bottom of the pool scraped out completely. The mud scraping assembly is simple in structure and high in mud scraping efficiency.
Preferably, the end face of the larger dimension end of the wedge-shaped scraper is provided with a negative pressure groove 29.
The arrangement of the negative pressure groove enables sludge on the wedge top side of the wedge-shaped scraper to be rapidly moved to the negative pressure groove along the inclined plane under the negative pressure effect generated by the negative pressure groove when the wedge-shaped scraper moves reversely, and accordingly the efficiency of scraping sludge is improved. Specifically, wedge scraper blade propelling movement mud speed is half of the speed of returning the journey, and the quick return is convenient for form vacuum negative pressure in the negative pressure groove department of wedge scraper blade to with the quick suction of mud to the negative pressure groove end of wedge scraper blade, be convenient for like this the propelling movement to the sludge impoundment. The angle of the wedge-shaped scraper is set between 20 and 30 degrees.
Preferably, the device also comprises a sludge collection assembly, wherein the sludge collection assembly comprises a sewage pumping pipe 30 connected with a vacuum pump, and a plurality of horn-shaped sludge suction ports 31 arranged on the side wall of the sewage pumping pipe and communicated with the sewage pumping pipe, and the sewage pumping pipe is arranged at the bottom of the contact chamber.
Preferably, the sludge collection assembly further comprises an aeration flushing pipe 32, and the aeration flushing pipe is communicated with the sewage suction pipe through a communication pipe 33.
The function of the sludge collection assembly is to ensure that the sludge is discharged quickly and smoothly. Its sewage pumping pipe that adopts length 7 meters, the sewage pumping pipe need guarantee to be greater than the outer drainage pressure more than 4 meters, just so can guarantee that the degree of consistency that sewage pumping pipe arranged mud reaches more than 90%, and the 10 meters negative pressure suction that produce through the vacuum pump provides the energy, can guarantee that the bottom of the pool row mud process is stable orderly. The arrangement of the horn-shaped sludge suction port increases the sludge suction action space of the sewage suction pipe. In addition, the arrangement of the aeration flushing pipe facilitates the flushing of the sewage pumping pipe by operators, thereby preventing the blockage of the sewage pumping pipe.
Preferably, the sludge vacuumizing and discharging device further comprises a sludge vacuumizing and discharging assembly, the sludge vacuumizing and discharging assembly comprises a vacuum pump 34 and a storage tank 35, a vent hole 36, a dirt inlet 37 and a dirt outlet 38 are arranged on the storage tank, the vent hole is communicated with one port of a four-way valve 39 through a pipeline, the other two ports of the four-way valve are respectively communicated with an air inlet and an air outlet of the vacuum pump through pipelines, and the last port of the four-way valve is communicated with the atmosphere.
The sludge vacuumizing outward discharging assembly realizes efficient discharge of scum and sludge, the vacuum pump is utilized to generate 10-meter negative pressure, air inside the storage tank is sucked and exhausted to the atmosphere, scum in the tank body and sludge at the bottom of the tank body are sucked and stored inside the tank body through the negative pressure generated inside the storage tank, after the sludge is fully collected, outlet air of the vacuum pump is pumped into the storage tank body through switching of the four-way valve, and the sludge and the scum are extruded from a sewage outlet into a subsequent sludge treatment device through air pressure.
Preferably, the sludge vacuumizing outward discharging assembly further comprises a transfer tank 40, one inlet of the transfer tank is communicated with the sewage pumping pipe through a pipeline, the other inlet of the transfer tank is communicated with the scum storage chamber on the tank body through a pipeline, and an output port of the transfer tank is communicated with a sewage inlet of the storage tank through a pipeline.
The setting of transfer pond has realized the extraction to dross and mud, and it is closed cell body during the concrete implementation.
Preferably, the vent of the canister is provided with an overflow prevention valve 41.
It is obvious to a person skilled in the art that the invention is not restricted to details of the above-described exemplary embodiments, but that the invention can be implemented in other specific forms by a person skilled in the art without departing from the spirit or essential characteristics of the invention. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description.
Furthermore, the above is only a preferred embodiment of the present invention, and is not intended to limit the present invention, it should be noted that, for those skilled in the art, a plurality of modifications and variations can be made without departing from the technical principle of the present invention, and these modifications and variations should also be regarded as the protection scope of the present invention. Also, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.

Claims (10)

1. A cocurrent flow flotation solid-liquid separation pond, its characterized in that: including the cell body, the room is collected to contact chamber, separation chamber and the clear water that follows rivers in the cell body and be equipped with mutual intercommunication in proper order, be provided with cocurrent flow flotation separation subassembly in the separation chamber, cocurrent flow flotation separation subassembly includes a plurality of sloping plate subassemblies, and the sloping plate subassembly includes that straight board, the top of vertical setting connect in the entrapment swash plate of straight board bottom, the smooth mud swash plate that the top is connected in entrapment swash plate bottom, and the bottom of sloping plate subassembly is provided with the sludge baffle, and the sludge baffle is located between the adjacent sloping plate subassembly, and the space between sludge baffle and its front side sloping plate subassembly is clear water transport chamber, and the space between sludge baffle and its rear side sloping plate subassembly is mud transport chamber, clear water transport chamber with clear water collection chamber intercommunication.
2. The co-current flotation solid-liquid separation cell of claim 1, wherein: the indoor high-speed flocculation separation reactor that is provided with of contact, high-speed flocculation separation reactor includes a plurality of folded plate subassemblies, and the folded plate subassembly includes that riser, the top of vertical setting connect in the flocculation catching swash plate of riser bottom.
3. The co-current flotation solid-liquid separation cell of claim 1, wherein: the water distribution assembly comprises a water distribution main pipe positioned at the bottom of the pool, water distribution branch pipes positioned at two sides of the water distribution main pipe, one ends of the water distribution main pipe are communicated with the water distribution main pipe, the other ends of the water distribution branch pipes are communicated with the contact chamber, and the cross sections of the water distribution main pipe inner holes and the cross sections of the water distribution branch pipe inner holes are both triangular.
4. The co-current flotation solid-liquid separation cell of claim 3, wherein: the water distribution device is characterized in that first partition plates are arranged on two sides of the main water distribution pipe, the bottom ends of the first partition plates are fixedly connected with the tank body, two second partition plates are arranged above the main water distribution pipe, the bottom ends of the second partition plates are connected with the main water distribution pipe, the contact chamber is arranged on the outer side of each first partition plate, the separation chamber is arranged between each first partition plate and the corresponding adjacent second partition plate, and the clean water collection chamber is arranged between each two second partition plates.
5. The co-current flotation solid-liquid separation cell of claim 1, wherein: the clear water is collected indoor and is provided with U type clear water collecting vat.
6. The co-current flotation solid-liquid separation cell of claim 1, wherein: the bottom of separation chamber is provided with scrapes the mud subassembly, it includes scraper blade installation pole to scrape the mud subassembly, is provided with polylith wedge scraper blade on the scraper blade installation pole, scrapes the mud subassembly and still includes the installation pole linear drive device that is used for driving scraper blade installation pole back-and-forth movement.
7. The co-current flotation solid-liquid separation cell of claim 6, wherein: and a negative pressure groove is formed in the end face of the end with the larger size of the wedge-shaped scraper.
8. The co-current flotation solid-liquid separation cell of claim 1, wherein: still include the mud collection subassembly, the mud collection subassembly includes the sewage pumping pipe of being connected with vacuum pump, locate on the sewage pumping pipe lateral wall set up and with a plurality of loudspeaker form sludge suction mouth of sewage pumping pipe intercommunication, the sewage pumping pipe sets up in the bottom of contact chamber.
9. The co-current flotation solid-liquid separation cell of claim 8, wherein: the sludge collection assembly further comprises an aeration flushing pipe, and the aeration flushing pipe is communicated with the sewage pumping pipe through a communicating pipe.
10. The co-current flotation solid-liquid separation cell of claim 9, wherein: still including the outer subassembly of arranging of mud evacuation, the outer subassembly of arranging of mud evacuation includes vacuum pump and storing jar, sets up blow vent, filth entry and filth export on the storing jar, and the blow vent passes through a port intercommunication of pipeline and cross valve, and the other two ports of cross valve are respectively through the air inlet and the gas outlet intercommunication of pipeline and vacuum pump, and the last port and the atmosphere intercommunication of cross valve.
CN201921591758.1U 2019-09-23 2019-09-23 Cocurrent flow flotation solid-liquid separation tank Active CN211255341U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921591758.1U CN211255341U (en) 2019-09-23 2019-09-23 Cocurrent flow flotation solid-liquid separation tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921591758.1U CN211255341U (en) 2019-09-23 2019-09-23 Cocurrent flow flotation solid-liquid separation tank

Publications (1)

Publication Number Publication Date
CN211255341U true CN211255341U (en) 2020-08-14

Family

ID=71959285

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201921591758.1U Active CN211255341U (en) 2019-09-23 2019-09-23 Cocurrent flow flotation solid-liquid separation tank

Country Status (1)

Country Link
CN (1) CN211255341U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110589923A (en) * 2019-09-23 2019-12-20 无锡海拓环保装备科技有限公司 Cocurrent flow flotation solid-liquid separation tank

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110589923A (en) * 2019-09-23 2019-12-20 无锡海拓环保装备科技有限公司 Cocurrent flow flotation solid-liquid separation tank

Similar Documents

Publication Publication Date Title
CN101879383B (en) Turn-back flow high-efficiency rectangular double-layer settling pond
CN115872505A (en) Seawater desalination impurity pretreatment assembly, system and process
CN211255341U (en) Cocurrent flow flotation solid-liquid separation tank
CN211255343U (en) Cocurrent flow flotation separation assembly
CN113521808A (en) New process for treating tail water of tap water
CN209853876U (en) Integrated grease separation water purifier
CN211255344U (en) Sludge vacuumizing discharge system
CN203971476U (en) A kind of high efficient full automatic settler
CN211255345U (en) High-speed flocculation separation component
CN211255340U (en) Fishbone-shaped water distribution system with full pool surface
CN211255342U (en) Tank bottom sludge collecting system
CN211770400U (en) Pool bottom mud scraping device
CN110589923A (en) Cocurrent flow flotation solid-liquid separation tank
CN212504366U (en) High turbid water treatment device and sewage treatment system
CN211705996U (en) Rectangular high-load sedimentation system
CN215250022U (en) Recycling system for stone plate processing wastewater
CN110589924A (en) Cocurrent flow flotation separation assembly
CN211706002U (en) Chain tensioning device and sedimentation system for secondary sedimentation tank
CN206391652U (en) A kind of pipe chute precipitating equipment
CN210710975U (en) Sloping plate-air flotation mud-water separation tank
CN113522856A (en) Workshop waste water, waste recovery system are built to PC intelligence
CN209323490U (en) Multifunctional ceiling algae head
CN209554929U (en) Cyanobacterial bloom emergency treatment device and cyanobacterial bloom emergency processing ship
CN205893018U (en) Municipal sewage mud separation processing system
CN215876558U (en) High-efficient sedimentation tank

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant