CN220385864U - Sludge accelerating sedimentation device - Google Patents
Sludge accelerating sedimentation device Download PDFInfo
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- CN220385864U CN220385864U CN202320691335.7U CN202320691335U CN220385864U CN 220385864 U CN220385864 U CN 220385864U CN 202320691335 U CN202320691335 U CN 202320691335U CN 220385864 U CN220385864 U CN 220385864U
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- 239000010802 sludge Substances 0.000 title claims abstract description 69
- 238000004062 sedimentation Methods 0.000 title claims abstract description 21
- 238000000926 separation method Methods 0.000 claims abstract description 74
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 66
- 239000007788 liquid Substances 0.000 claims abstract description 63
- 239000012535 impurity Substances 0.000 claims abstract description 48
- 238000001914 filtration Methods 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 9
- 239000011521 glass Substances 0.000 claims description 7
- 238000010030 laminating Methods 0.000 claims description 6
- 239000003507 refrigerant Substances 0.000 claims description 6
- 238000004804 winding Methods 0.000 claims description 6
- 239000004576 sand Substances 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 4
- 239000004575 stone Substances 0.000 claims description 4
- 230000001133 acceleration Effects 0.000 claims 9
- 239000012530 fluid Substances 0.000 abstract description 32
- 230000001360 synchronised effect Effects 0.000 abstract description 4
- 239000010865 sewage Substances 0.000 description 20
- 238000000034 method Methods 0.000 description 14
- 230000000694 effects Effects 0.000 description 9
- 230000006872 improvement Effects 0.000 description 9
- 230000008569 process Effects 0.000 description 7
- 241000883990 Flabellum Species 0.000 description 5
- 230000008014 freezing Effects 0.000 description 5
- 238000007710 freezing Methods 0.000 description 5
- 230000001105 regulatory effect Effects 0.000 description 5
- 239000011259 mixed solution Substances 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 239000011268 mixed slurry Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 230000003631 expected effect Effects 0.000 description 2
- 239000013505 freshwater Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000008235 industrial water Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a sludge accelerating sedimentation device which comprises a body, wherein the body comprises a support arranged at the bottom of the body, a separation shell is arranged on the support, an input pipe is arranged on the separation shell, a clear water output pipe is arranged at the upper part of the other side of the separation shell, a sludge output pipe is arranged at the lower part of the separation shell, a mixed turbid liquid output pipe is arranged in the middle of the separation shell, a condensing device is arranged on the outer wall of the middle of the separation shell, valves for controlling the opening and closing are arranged on the clear water output pipe, the mixed turbid liquid output pipe and the sludge output pipe, and an accelerating separation device is also arranged on the body. The separator is provided with an input pipeline and an output pipeline, the output pipeline is provided with an upper output pipeline, a middle output pipeline and a lower output pipeline, the output pipelines respectively correspond to the export of light clear water, mixed turbid liquid and fluid sludge impurities, the synchronous increase of the input quantity and the input speed of the input pipeline can be realized, and the working efficiency of the equipment is improved.
Description
Technical Field
The utility model relates to the technical field of environmental protection and purification, in particular to a sludge accelerating sedimentation device.
Background
In China, reasonable utilization of water resources is always an inexhaustible topic, and the population of China is numerous, even if the population is' big ground, the average occupation of the resources per person of each person is also faced with a plurality of shortages and shortages. Fresh water resources are one of the material resources on which people depend most, and in China, the occupation amount of fresh water resources per person is optimistic in future prospect; meanwhile, china is used as an industrial large country, and in industrial production, the water utilization amount is very large, and the recycling or regeneration of the sewage after the utilization is particularly important. Therefore, the treatment of industrial water and impurity water of a mixture with high utilization difficulty is paid more attention to in the national level and the social organization level, the existing sewage treatment modes comprise a physical precipitation method, a chemical precipitation method, a biological degradation method and the like, in various treatment methods, industrial water is often the same water with fixed and impurity mixing quantity, in the sewage treatment process, the separation of sewage and sludge, the repurification treatment of sewage and the treatment of middle residues are core problems, in the existing treatment methods, the sedimentation method is relatively low in cost but high in purification efficiency, the use is relatively wide, but the existing sedimentation flow is used, the water in the sewage treatment device is required to be drained, then sediment and sludge are treated, the treatment mode is long in time consumption, the normal operation of the sewage treatment is influenced, a large amount of manpower and material resources are required to be consumed, great workload is brought to actual operation, the sewage treatment cost is high, when the amount of the sedimented sludge is large in many times, the sludge cannot be discharged in time, the sewage can be discharged after the sedimentation of the upper mixed water is required to be completely sedimented, and then the sewage can be discharged, and the work amount of impurities in unit time is relatively small is required to treat the sludge.
Disclosure of Invention
The technical problem to be solved by the utility model is to provide the sludge accelerating sedimentation device, which can effectively solve the problem of high cost of time consumption and labor consumption in the existing market sewage treatment process, realize multistage flexible regulation and control treatment, correspondingly treat sedimentation water and sludge at any time according to the needs, and improve the operation efficiency.
The following technical scheme is provided for solving the problems: the utility model provides a mud subsides device with higher speed, includes the body, the body is including the support of locating the body bottom, be provided with the separation shell on the support, set up the input tube on the separation shell, separation shell opposite side upper portion is provided with clear water output tube, separation shell lower part is provided with the mud output tube, and separation shell middle part is provided with mixed turbid liquid output tube, be provided with condensing equipment on the separation shell middle part outer wall, all be provided with the valve that the control was opened and was closed on clear water output tube, mixed turbid liquid output tube, the mud output tube, connect output pump I on the valve outside pipeline of clear water output tube, be provided with output pump II on the outside pipeline of mixed turbid liquid output tube valve, still be provided with separation device with higher speed on the body. The separator is provided with an input pipeline and an output pipeline, the output pipeline is provided with an upper output pipeline, a middle output pipeline and a lower output pipeline which respectively correspond to the export of light clear water, mixed turbid liquid and fluid sludge impurities, and the pipelines of the clear water output pipe and the mixed turbid liquid output pipe are provided with a valve and pumps I and II, so that the retention amount of the water mixed liquid in the separation shell can be controlled in time and can be regulated in time and efficiently, the discharge speed can be improved during discharge, the synchronous increase of the input quantity and the input speed of the input pipe can be realized, and the working efficiency of equipment can be improved; the input pipe is arranged in a horn shape, so that the mixed liquid is conveniently introduced; the condensing device is arranged on the separation shell, so that the temperature of the mixed liquid in the separation shell can be controlled, more precisely, the average temperature of the mixed liquid can be reduced to the temperature below room temperature or other temperatures above the freezing point, the solubility of the sludge impurities in the aqueous solution is controlled, the precipitation and water separation of the sludge and the impurities are facilitated, the more efficient mud-water separation is realized, the separation speed and the efficiency of the fluid sludge impurities in water and the mixed turbid liquid are increased by the additional accelerating and separating device, the separation is more sufficient, the multi-stage functional equipment accessories can be independently adjusted and opened according to the requirements, and the operation is flexible and efficient.
As an improvement, the accelerating and separating device is a turbulent flow motor arranged at the bottom of the separating shell, and a turbulent flow fan blade is arranged on an output shaft of the turbulent flow motor. The method comprises the steps of (1) sealing a connecting part of a vortex motor and a body, adding sewage mixed liquid into a separator through an input pipe arranged at the middle part of one side of the body, starting the vortex motor, directly impacting the position nearby a vortex fan blade by the added new sewage mixed liquid, fully circulating the new sewage mixed liquid under the stirring force of the vortex fan blade, closing the vortex motor, automatically settling the sewage mixed liquid, rising clear water, descending fluid sludge impurities, leaving mixed turbid liquid in the middle part, respectively leading out the fluid sludge impurities and clear water to the position nearby a boundary of the middle mixed turbid liquid after settling is stable, stopping leading out, starting the vortex motor again, accelerating circulation, fully and naturally settling again, respectively leading out the fluid sludge impurities and clear water, and putting the mixed turbid liquid into operation again after internal cleaning if the fluid sludge impurities are larger in proportion; according to the requirements, the mixed turbid liquid is not completely led out each time, and only clear water and fluid sludge impurities are led out each time, so that the operation is flexibly regulated and controlled, and the optimal working state of the equipment is ensured.
As an improvement, the turbulent flow fan blade is of a vertical sheet structure with a flat upper part and a convex lower part, and the lower side of the turbulent flow fan blade is of a fan shape with an arc edge. The vortex fan blade rotation process of the upper flat lower convex structure, the vortex fan blade and the mixed liquid flow intensity in the space below the vortex fan blade are high, the mixed liquid flow speed of the part above the vortex fan blade is gentle, the flow power of the upper part is mainly lower conduction, the vortex process effectively realizes the upward floating release separation of clear water on the upper part, after the clear water is fully separated, the vortex stops, the separation boundary between the fluid sludge impurity on the lower part and water after sedimentation is better and clearer, and the separation effect and the separation efficiency are higher.
As an improvement, the lower end of the output shaft of the turbulent flow motor is provided with a mud flow pushing plate which is in a fan-shaped structure and is arranged at the inner port of the mud output pipe in the separation shell. The mud flow pushing plate is arranged at the lower end of the output shaft of the turbulence motor and at the inner port of the sludge output pipe, so that the settled high-concentration sludge is continuously disturbed to keep the state of uniform dissolved density, the sludge is conveniently and smoothly guided out through the sludge output pipe without blocking, meanwhile, the fan-shaped mud flow pushing plate is used for disturbing the mud and generating thrust by rotating and centrifuging to continuously push the mud out of the sludge output pipe, and the technical effect that the mud can not be blocked and can be rapidly pushed is achieved.
As an improvement, the sludge output pipe is obliquely arranged downwards. The sludge and water mixture can flow out smoothly under the self gravity.
As an improvement, the separation housing is provided with a glass window which is arranged at the lower part of the separation housing and is arranged at the outer side of the mud plug flow board. The fluid sludge dissolution state and the fluid density are observed and judged, and the operation is adjusted timely, so that the operation is more accurate.
As an improvement, condensing equipment laminating winding is on the middle part outer wall of separation shell, condensing equipment includes external compressor and refrigerant pipeline, condenser, volatilizer, and the pipeline laminating winding of volatilizer is at the middle part outer wall of separation shell. The refrigerant is refrigerated, the refrigeration effect is stable and efficient, and the temperature control is accurate.
As an improvement, the condensing device is provided with a temperature display panel. The temperature is read in real time, the operation is convenient, the real-time temperature of the whole mixed liquid is always kept below 20 ℃, the mixed liquid temperature keeping effect above the freezing point is realized at the lowest, the actual operation takes the slurry outflow state as a judging element, and the temperature parameters are adjusted up and down according to the requirement at any time.
As an improvement, the end pipe orifice of the mixed turbid liquid output pipe is provided with an impurity removing and filtering device. Can further clear away a small amount of impurities remained in the settled discharged water effectively, and ensures that the water finally discharged by the mixed turbid liquid output pipe is clean water without pollution and impurities.
As an improvement, the impurity removal filter device comprises a filter box and a filter material arranged in the filter box, wherein the filter material is sand particles. The sand-stone particle combination effectively filters impurities in the mixed turbid liquid, and the stability function exerted in the device is more beneficial to thoroughly removing the sludge impurities, so that the expected effect is better.
The beneficial effects of the utility model are that: the separator is provided with an input pipeline and an output pipeline, the output pipeline is provided with an upper output pipeline, a middle output pipeline and a lower output pipeline which respectively correspond to the export of light clear water, mixed turbid liquid and fluid sludge impurities, and the pipelines of the clear water output pipe and the mixed turbid liquid output pipe are provided with a valve and pumps I and II, so that the retention amount of the water mixed liquid in the separation shell can be controlled in time and can be regulated in time and efficiently, the discharge speed can be improved during discharge, the synchronous increase of the input quantity and the input speed of the input pipe can be realized, and the working efficiency of equipment can be improved; the input pipe is arranged in a horn shape, so that the mixed liquid is conveniently introduced; the condensing device is arranged on the separation shell, so that the temperature of the mixed liquid in the separation shell can be controlled, more precisely, the average temperature of the mixed liquid can be reduced to the temperature below room temperature or other temperatures above the freezing point, the solubility of the sludge impurities in the aqueous solution is controlled, the precipitation and water separation of the sludge and the impurities are facilitated, the more efficient mud-water separation is realized, the separation speed and the efficiency of the fluid sludge impurities in water and the mixed turbid liquid are increased by the additional accelerating and separating device, the separation is more sufficient, the multi-stage functional equipment accessories can be independently adjusted and opened according to the requirements, and the operation is flexible and efficient.
Drawings
The utility model is further described below with reference to the accompanying drawings:
FIG. 1 is a schematic view of a partial cross-sectional structure of an embodiment of the present utility model.
Detailed Description
As shown in figure 1, the sludge accelerating sedimentation device comprises a body, the body comprises a bracket 1 arranged at the bottom of the body, a separating shell 2 is arranged on the bracket, an input pipe 3 is arranged on the separating shell, a clear water output pipe 4 is arranged at the upper part of the other side of the separating shell, a sludge output pipe 5 is arranged at the lower part of the separating shell, a mixed turbid liquid output pipe 6 is arranged at the middle part of the separating shell, a condensing device 7 is arranged on the outer wall of the middle part of the separating shell, valves 11 for controlling the opening and closing are arranged on the clear water output pipe, the mixed turbid liquid output pipe and the sludge output pipe, an output pump I15 is connected on the pipeline outside the valve of the clear water output pipe, an output pump II 16 is arranged on the pipeline outside the valve of the mixed turbid liquid output pipe, an accelerating separation device is also arranged on the body, the accelerating separation device is a vortex motor 8 arranged at the bottom of the separating shell, the output shaft 9 of the turbulent flow motor is provided with a turbulent flow fan blade 10 which is of a vertical type sheet structure with a flat upper part and a convex lower part, the lower side of the turbulent flow fan blade is in a arc edge fan shape, the lower end of the output shaft of the turbulent flow motor is provided with a mud flow pushing plate 17 which is arranged at the inner port of a mud output pipe in a separation shell in a fan-shaped structure, the mud output pipe is obliquely arranged downwards, the separation shell is provided with a glass window which is arranged at the lower part of the separation shell and is arranged at the outer side of the mud flow pushing plate, a condensing device is attached and wound on the outer wall of the middle part of the separation shell and comprises an external compressor, a refrigerant pipeline, a condenser and a volatilizer, the pipeline of the volatilizer is attached and wound on the outer wall of the middle part of the separation shell, the condensing device is provided with a temperature display plate 12, the tail end pipe orifice of the mixed turbid liquid output pipe is provided with a impurity removing and filtering device, the impurity removal and filtration device comprises a filtration box 13 and a filtration material 14 arranged in the filtration box, wherein the filtration material is sand particles; when the device works, mixed sludge slurry is poured from the mouth of an input pipe, smoothly flows into a separation shell through an obliquely arranged input pipe, the mixed slurry flows into a turbulent flow fan blade position, the impact position of the mixed slurry is just at the turbulent flow fan blade position, the mixed slurry flows into the device for scattering and rapidly rotating, mud and water are partially separated, high-density sludge impurities sink to the position of a sludge output pipe orifice, the device is pushed and stirred by a mud plug board to keep a uniform fluid state, when enough sludge is separated out, a clear water output pipe is opened, a proper amount of clear water with better sedimentation is released, the visual texture of discharged water is judged, when turbidity water is discharged, a valve of the clear water output pipe is closed, then the mixed turbid liquid output pipe is opened, the mixed turbid liquid flows into a filter box, clear water filtered by sediment in the mixed turbid liquid is discharged outside through a filter material in the filter box, the fluid state of sludge in a glass window is observed, when the fluid state is large and smooth circulation is not performed, the discharge of the mixed turbid liquid is stopped, the process input pipe continuously inputs new sewage mixed liquid, when the fluid is diluted again and the fluid is smooth, the valve of the mud is opened, and the fluid is discharged from the outside through the inclined plug board through the mud plug board; the outflow is carried out, the temperature of the condensing device is kept at 5-15 ℃, the ground solubility of the mixed impurities is kept low, and the heat generated by the high-speed rotation of the turbulent fan blades is cooled.
The technical scheme of the product comprises the following specific functions and corresponding technical effects of each functional component:
the separator is provided with an input pipeline and an output pipeline, the output pipeline is provided with an upper output pipeline, a middle output pipeline and a lower output pipeline which respectively correspond to the export of light clear water, mixed turbid liquid and fluid sludge impurities, and the pipelines of the clear water output pipe and the mixed turbid liquid output pipe are provided with a valve and pumps I and II, so that the retention amount of the water mixed liquid in the separation shell can be controlled in time and can be regulated in time and efficiently, the discharge speed can be improved during discharge, the synchronous increase of the input quantity and the input speed of the input pipe can be realized, and the working efficiency of equipment can be improved; the input pipe is arranged in a horn shape, so that the mixed liquid is conveniently introduced; the condensing device is arranged on the separation shell, so that the temperature of the mixed liquid in the separation shell can be controlled, more precisely, the average temperature of the mixed liquid can be reduced to the temperature below room temperature or other temperatures above the freezing point, the solubility of the sludge impurities in the aqueous solution is controlled, the precipitation and water separation of the sludge and the impurities are facilitated, the more efficient mud-water separation is realized, the separation speed and the efficiency of the fluid sludge impurities in water and the mixed turbid liquid are increased by the additional accelerating and separating device, the separation is more sufficient, the multi-stage functional equipment accessories can be independently adjusted and opened according to the requirements, and the operation is flexible and efficient.
In this embodiment, the accelerating and separating device is a turbulent flow motor 8 arranged at the bottom of the separating shell, a turbulent flow fan blade 10 is arranged on an output shaft 9 of the turbulent flow motor, the turbulent flow motor is in sealing connection with a joint of the body, the same sealing structure is arranged at the top end of the body, after the sewage mixed solution is added into the separator through an input pipe arranged at the middle position of one side of the body, the turbulent flow motor is started, the added new sewage mixed solution directly impacts the vicinity of the position of the turbulent flow fan blade, the newly added sewage mixed solution is fully circulated under the stirring force of the turbulent flow fan blade, the turbulent flow motor is closed, the sewage mixed solution automatically settles, clear water rises, fluid sludge impurities descend, mixed turbid solution stays in the middle part, after settling is stable, fluid sludge impurities and clear water are respectively led out to the position close to the vicinity of the boundary of the middle mixed turbid solution, the turbulent flow motor is started again, after accelerating circulation, the fluid sludge impurities and clear water are respectively led out, the mixed turbid solution is led out according to the quantity of the fluid sludge impurities, if the fluid sludge impurities has a larger proportion, the fluid sludge impurities are all led out once, and then the fluid sludge is cleaned up again; according to the requirements, the mixed turbid liquid is not completely led out each time, and only clear water and fluid sludge impurities are led out each time, so that the operation is flexibly regulated and controlled, and the optimal working state of the equipment is ensured.
In this embodiment, the vortex flabellum is the sagging sheet structure of protruding from top to bottom, the vortex flabellum downside is the arc fan-shaped, go up the vortex flabellum rotation process of protruding structure from top to bottom, the mixed liquid circulation intensity in vortex flabellum and below space is high, the mixed liquid circulation speed of part above the vortex flabellum is mild, and the circulation power on upper portion is the lower part conduction, the vortex process effectively realizes the come-up release separation of upper portion clear water, after the clear water fully separates, the vortex stops, separation boundary after the fluid mud impurity of lower part and water subside just is better clear, separation effect and separation efficiency are higher.
In this embodiment, the lower extreme of vortex motor output shaft sets up mud and pushes away the flow board 17, the flow board is fan-shaped structure and locates the interior port department of mud output tube in the separation shell, the flow board is in the lower extreme of vortex motor output shaft to locate the interior port department of mud output tube, realize keeping the mud state that its solution density is even with the continuous vortex of the higher concentration mud that subsides, it is convenient for export smoothly through the mud output tube and not take place to block up, the while fan-shaped structure mud pushes away the flow board to mud vortex, rotatory centrifugation produces the thrust and continuously pushes away mud to the mud output tube, form the technological effect that neither can block up but also can be by the department of pushing away fast.
In the embodiment, the sludge output pipe is obliquely arranged downwards, so that the sludge and water mixture can smoothly flow out under the self gravity.
In this embodiment, the separation shell sets up the glass window, and the glass window is located separation shell lower part and is established in the outside of mud plug flow board, observes and judges fluid mud dissolution state and fluid density, timely adjustment operation for the operation is more accurate.
In this embodiment, condensing equipment laminating winding is on separation shell middle part outer wall, condensing equipment includes external compressor and refrigerant pipeline, condenser, volatilizer, and the pipeline laminating winding of volatilizer is at separation shell middle part outer wall. The refrigerant is refrigerated, the refrigeration effect is stable and efficient, and the temperature control is accurate.
In this embodiment, the condensing device is provided with a temperature display panel 12, so that the temperature is read in real time, the operation is convenient, the real-time temperature of the whole mixed liquid is always kept below 20 ℃, the temperature keeping effect of the mixed liquid above the freezing point is realized at the lowest, the actual operation uses the slurry outflow state as a judging element, and the temperature parameter is adjusted up and down as required at any time.
In the embodiment, the impurity removing and filtering device is arranged at the end pipe orifice of the mixed turbid liquid output pipe, so that a small amount of impurities remained in settled discharged water can be further removed, and the finally discharged water of the mixed turbid liquid output pipe is clean water without pollution and impurities.
In this embodiment, impurity removal filter equipment includes filter cassette 13 and sets up the filter media 14 in the filter cassette, the filter media is sand stone granule, and sand stone granule combination is effective to filter impurity in the mixed turbid liquid, and the stability function of performance is more favorable to the thoroughly of decontamination mud impurity in this device, and the expected effect is better.
In addition to the above preferred embodiments, the present utility model has other embodiments, and those skilled in the art can make various changes and modifications according to the present utility model, which should fall within the scope of the present utility model without departing from the spirit of the present utility model.
Claims (10)
1. The utility model provides a mud subsides device with higher speed, includes the body, the body is including locating support (1) of body bottom, its characterized in that: be provided with separation shell (2) on the support, set up input tube (3) on the separation shell, separation shell opposite side upper portion is provided with clear water output tube (4), and separation shell lower part is provided with mud output tube (5), and separation shell middle part is provided with mixed turbid liquid output tube (6), be provided with condensing equipment (7) on the separation shell middle part outer wall, all be provided with valve (11) that control was opened and was closed on clear water output tube, mixed turbid liquid output tube, the mud output tube, connect output pump I (15) on the valve outside pipeline of clear water output tube, be provided with output pump II (16) on the outside pipeline of mixed turbid liquid output tube valve, still be provided with separation device with higher speed on the body.
2. A sludge acceleration sedimentation apparatus as claimed in claim 1, wherein: the accelerating and separating device is a turbulent flow motor (8) arranged at the bottom of the separating shell, and a turbulent flow fan blade (10) is arranged on an output shaft (9) of the turbulent flow motor.
3. A sludge acceleration sedimentation apparatus as claimed in claim 2, wherein: the turbulent flow fan blade is of a vertical sheet structure with a flat upper part and a convex lower part, and the lower side of the turbulent flow fan blade is of a fan shape with an arc edge.
4. A sludge acceleration sedimentation apparatus as claimed in claim 2, wherein: the lower end of the output shaft of the turbulent flow motor is provided with a mud plug flow plate (17), and the mud plug flow plate is of a fan-shaped structure and is arranged at the inner port of the mud output pipe in the separation shell.
5. A sludge acceleration sedimentation apparatus as claimed in claim 1, wherein: the sludge output pipe is obliquely arranged downwards.
6. A sludge acceleration sedimentation apparatus as claimed in claim 1, wherein: the separation shell is provided with a glass window, and the glass window is arranged at the lower part of the separation shell and at the outer side of the mud plug flow plate.
7. A sludge acceleration sedimentation apparatus as claimed in claim 1, wherein: the condensing equipment laminating winding is on separation shell middle part outer wall, condensing equipment includes external compressor and refrigerant pipeline, condenser, volatilizer, and the pipeline laminating winding of volatilizer is at separation shell middle part outer wall.
8. A sludge acceleration sedimentation apparatus as claimed in claim 1 or 7, wherein: the condensing device is provided with a temperature display plate (12).
9. A sludge acceleration sedimentation apparatus as claimed in claim 1, wherein: the tail end pipe orifice of the mixed turbid liquid output pipe is provided with an impurity removing and filtering device.
10. The sludge acceleration sedimentation device of claim 9, wherein: the impurity removal and filtration device comprises a filtration box (13) and a filtration material (14) arranged in the filtration box, wherein the filtration material is sand and stone particles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320691335.7U CN220385864U (en) | 2023-03-30 | 2023-03-30 | Sludge accelerating sedimentation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320691335.7U CN220385864U (en) | 2023-03-30 | 2023-03-30 | Sludge accelerating sedimentation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220385864U true CN220385864U (en) | 2024-01-26 |
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ID=89599118
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320691335.7U Active CN220385864U (en) | 2023-03-30 | 2023-03-30 | Sludge accelerating sedimentation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220385864U (en) |
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2023
- 2023-03-30 CN CN202320691335.7U patent/CN220385864U/en active Active
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