CN214422318U - Vertical vortex purifier of high turbidity or high rigidity water - Google Patents
Vertical vortex purifier of high turbidity or high rigidity water Download PDFInfo
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- CN214422318U CN214422318U CN202022388669.6U CN202022388669U CN214422318U CN 214422318 U CN214422318 U CN 214422318U CN 202022388669 U CN202022388669 U CN 202022388669U CN 214422318 U CN214422318 U CN 214422318U
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Abstract
The utility model discloses a high turbidity or high hardness water vertical vortex purification device, which comprises a raw water intake pump, wherein the water inlet of the raw water intake pump is connected with one end of a water guide pipe through a pipe, the water outlet of the raw water intake pump is connected with the water inlet of a pipeline mixer through a pipe, the water inlet of the pipeline mixer is connected with the liquid outlet of a dosing pump through a pipe, the liquid inlet of the dosing pump is connected with the liquid outlet of a dosing tank through a pipe, the water outlet of the pipeline mixer is connected with one end of the water guide pipe, and the other end of the water guide pipe is provided with an integrated water purification device, compared with the prior art, the utility model has the advantages of more compact process design, less dosing amount, higher controllable degree of water outlet effect, low water outlet turbidity, shorter construction period, reduced civil engineering investment, shortened construction period, lower operation cost, favorable energy conservation and shorter construction period, the movable high-turbidity water purification station is beneficial to solving the problem of long construction period and high operating cost of the high-turbidity water purification station.
Description
Technical Field
The utility model belongs to the technical field of water treatment facilities, especially a high turbidity contains silt water treatment facilities, especially relates to integrate steel purifier.
Background
The existing high-turbidity water treatment is generally treated by sedimentation, clarification and filtration, particularly, a sedimentation tank and a clarification tank are generally of a concrete structure, so that the volume is large, the water purification efficiency is low, the process flow is long, the occupied area is large, the construction period is long, the construction cost is high, the construction period is long, the construction environment is limited by a plurality of factors, a large amount of medicament is added during water purification, the operation cost is not saved, the water hardness treatment is complicated, the high-hardness water is harmful to the body health and causes equipment operation faults, the life and the production are influenced, meanwhile, once a water purification plant is built, process devices (limited by the area of the site) cannot be added according to the actual water quality condition, the land is not saved, the integration level is not high, the automatic control is inconvenient, and therefore, a device which integrates a plurality of process devices with small occupied area, high efficiency is necessarily designed on the basis of the prior art, the land is saved, and the flocculation effect of the medicament is fully utilized to improve the water purification efficiency and effect.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a vertical vortex purifier of high turbidity or high rigidity water to solve the problem that provides among the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme:
the utility model provides a vertical vortex purifier of high turbidity or high rigidity water, includes the raw water intake pump, the water inlet of raw water intake pump and the one end pipe joint of aqueduct, the delivery port of raw water intake pump passes through the water inlet pipe joint of aqueduct and pipe mixer, the water inlet of pipe mixer passes through the liquid catheter and adds the liquid outlet pipe joint of medicine pump, the inlet that adds the medicine pump passes through the liquid catheter and adds the liquid outlet pipe joint of medicine jar, the delivery port of pipe mixer is connected with the one end of aqueduct, and the other end of aqueduct is provided with integrated purifier.
As a further aspect of the present invention: the integrated water purifying device comprises a conical resistance plate, a rotational flow stirring blade, a mixing stirring cone, a protective railing, a barrel top support plate, a water outlet pipe, a vertical leg, a sewage discharge outlet, an overhauling inlet, a barrel, a ladder, a stirring motor, a first stirring shaft, an anti-disturbance sleeve, a buffer type water collecting tank, an inclined pipe support, a water inlet pipe, a sludge collecting hopper, a connecting pipe, a welding connecting sheet, a connecting support body, a second stirring shaft and a circular water intercepting pipe, wherein the vertical leg is fixedly arranged at the bottom of the barrel, the ladder is fixedly arranged on the outer side of the barrel, the barrel top support plate is fixedly arranged at the top of the barrel top support plate, the protective railing is fixedly arranged at the top of the barrel top support plate, the stirring motor is fixedly arranged at the top of the barrel top support plate, an output shaft of the stirring motor vertically penetrates through the barrel top support plate and is fixedly connected with one end of the first stirring shaft, the stirring device is characterized in that an anti-disturbance sleeve is sleeved outside the first stirring shaft, the inclined pipe is fixedly connected to the top of an inclined pipe support, the inclined pipe support is fixedly installed on a connecting support lug on the inner wall of a cylinder body, the connecting support lug on the inner wall of the cylinder body is fixedly connected to the cylinder body, the bottom end of the anti-disturbance sleeve vertically penetrates through the inclined pipe and is fixedly connected with a conical resistance plate, the bottom end of the first stirring shaft is fixedly connected with one end of a second stirring shaft through a coupler, the second stirring shaft extends into a mixing stirring cone body, the mixing stirring cone body is positioned under the conical resistance plate, a conical water flow tangential outlet is formed in the outer side of the mixing stirring cone body, a plurality of connecting support bodies are connected to the outer side of the mixing stirring cone body at equal intervals along the circumferential direction, the mixing stirring cone body is fixedly installed on the connecting support lug on the inner wall of the cylinder body through the connecting support bodies, and a plurality of groups of rotational flow stirring blades are sequentially installed on the second stirring shaft from top to bottom, the utility model discloses a mixing stirring pipe, including the barrel, the barrel is provided with the inclined tube, the mixing stirring cone inner wall is provided with the connecting pipe through welded connection piece fixedly connected with, be provided with the sand setting clearance between mixing stirring cone inner wall and the connecting pipe, the one end of connecting pipe is connected with the one end of inlet tube, the other end of inlet tube stretches out the barrel, the maintenance entry has been seted up in the barrel outside, the position that the barrel outside is located the pipe chute top is seted up the delivery port of being connected with outlet pipe one end, the position that the barrel is inside to be located under the mixing stirring cone is provided with the mud collection fill, the drain has been seted up to the barrel bottom, the delivery port of pipeline mixer passes through the aqueduct and advances water piping connection, the outlet pipe passes through the aqueduct and is connected with the water inlet of filtering pond, the barrel inner wall is located and has the buffering type catch basin with the opposite side welding of pipe incline direction.
As a further aspect of the present invention: the length of the rotational flow stirring blade is matched with that of the mixing stirring cone, and the inclination directions of the two opposite rotational flow stirring blades are mutually vertical.
Compared with the prior art, the beneficial effects of the utility model are that:
1. the utility model discloses be particularly suitable for and solve Xinjiang ice and snow melt water, the sand content is big, and hardness is high and high turbidity sewage, the utility model discloses the technical problem that needs to solve is: the integrated purification device for high-turbidity water has the characteristics of high process integration level, high automation control degree, small occupied area, field assembly in the later period, civil engineering reduction, construction period shortening, high water purification efficiency and effective land resource saving, saves more than 60% of land compared with the traditional process under the same treatment condition, has the water inlet turbidity of between 1000 and 3000NTU, controls the water outlet turbidity below 20NTU, and can control the water outlet turbidity below 1NTU after the filter tank is added by the process; the PAC dosage of the medicament is controlled to be below 30mg/L, and meanwhile, the lime dosage and the addition of crystal nuclei can be controlled for water with high hardness, so that the high-hardness water is treated, the power consumption is low, the addition of the medicament is small, the structural design is reasonable, the water purification effect is good, and the operation cost is low;
2. the utility model discloses high turbidity water treatment station takes up an area of littleer, and land utilization is higher, is particularly suitable for the processing of Xinjiang silt water, compares process design compacter with current technology, and the dosing is few, and it is higher to go out the controllable degree of water effect, and it is low to go out the water turbidity, and construction cycle is shorter, reduces the civil engineering input, shortens construction cycle, and the running cost is lower, is favorable to energy-conservation, and the factory building cycle is shorter, and is portable, is favorable to solving the high difficult problem of high turbidity water purification station construction cycle length working costs.
Drawings
FIG. 1 is a schematic diagram of a system of a vertical vortex water purification device for high turbidity or high hardness water.
Fig. 2 is a schematic diagram of an exploded structure of an integrated water purification device in a high turbidity or high hardness water vertical vortex purification device.
FIG. 3 is a schematic view of the structure of an integrated water purification device in a vertical vortex purification device for high turbidity or high hardness water.
FIG. 4 is a cross-sectional view of an integrated water purification unit in a vertical vortex water purification unit for high turbidity or high hardness water.
Fig. 5 is a side view of an integrated water purification unit in a vertical vortex water purification unit for high turbidity or high hardness water.
FIG. 6 is a schematic view of the structure of the mixing and stirring cone in the vertical vortex purifier for high turbidity or high hardness water.
FIG. 7 is a top view of a mixing agitator cone in a vertical vortex purifier for high turbidity or high hardness water.
FIG. 8 is a schematic view of the structure of the swirling mixing blades in the vertical swirling purification device for high turbidity or high hardness water.
FIG. 9 is a schematic view of the structure of a buffer type water collection tank in a vertical vortex purifier for high turbidity or high hardness water.
Shown in the figure: raw water intake pump 1, add medicinal cupping 2, add medicinal cupping 3, pipeline mixer 4, integrated purifier 5, filtering pond 6, toper resistance plate 7, whirl stirring vane 8, mix stirring cone (awl section of thick bamboo) 9, guard rail 10, barrel top backup pad 11, outlet pipe 12, found leg 13, drain 14, maintenance entry 15, barrel 16, ladder 17, agitator motor 18, first (mixing) shaft 19, prevent disturbance sleeve pipe 20, buffer type water catch bowl 21, pipe chute 22, pipe chute support 23, inlet tube 24, mud collecting bucket 25, connecting pipe 26, welded connection piece 27, connection support body 28 and second (mixing) shaft 29 and circular cutting pipe 30.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1 to 9, in an embodiment of the present invention, a vertical vortex purification apparatus for high-turbidity or high-hardness water includes a raw water intake pump 1, a chemical feeding tank 2, a chemical feeding pump 3, a pipeline mixer 4, an integrated water purification apparatus 5, a filter 6, a tapered resistance plate 7, a vortex stirring blade 8, a mixing stirring cone 9, a guard rail 10, a cylinder top support plate 11, a water outlet pipe 12, a stand leg 13, a sewage outlet 14, an access port 15, a cylinder 16, a ladder 17, a stirring motor 18, a first stirring shaft 19, a disturbance prevention sleeve 20, a buffer type water collection tank 21, an inclined pipe 22, an inclined pipe support 23, a water inlet pipe 24, a sludge collection hopper 25, a connecting pipe 26, a welding connection sheet 27, a connection support 28, a second stirring shaft 29 and a circular cutoff pipe 30, wherein a water inlet of the raw water intake pump 1 is connected with one end of a water conduit, a water outlet of the raw water intake pump 1 is connected with a water inlet of the pipeline mixer 4 through a water conduit, the water inlet of the pipeline mixer 4 is connected with the liquid outlet of the dosing pump 3 through a liquid guide pipe, the pipeline mixer 4 is manufactured and sold in the market by Jiangsu Jixiang environmental protection science and technology Limited company and has the model of JX-521, the pipeline mixer 4 is a mixer without any mechanical moving part and is actually similar to a three-way connecting pipe, fluid and medicament can be uniformly mixed in the flowing process in the pipeline, the liquid inlet of the dosing pump 3 is connected with the liquid outlet of the dosing tank 2 through the liquid guide pipe, the water outlet of the pipeline mixer 4 is connected with one end of a water guide pipe, the other end of the water guide pipe is provided with an integrated water purifying device 5, the integrated water purifying device 5 comprises a conical resistance plate 7, a rotational flow stirring blade 8, a mixing stirring cone 9, a protective railing 10, a cylinder top supporting plate 11, a water outlet pipe 12, a vertical leg 13, a sewage discharge port 14 and an overhaul inlet 15, Barrel 16, ladder 17, agitator motor 18, first (mixing) shaft 19, prevent disturbance sleeve pipe 20, buffer type water catch bowl 21, pipe chute 22, pipe chute support 23, inlet tube 24, mud collection fill 25, connecting pipe 26, welded connection piece 27, joint support 28 and second (mixing) shaft 29 and circular cutting pipe 30, barrel 16 bottom fixed mounting has grudging post 13, barrel 16 outside fixed mounting has ladder 17, barrel 16 top fixed mounting has barrel top backup pad 11, barrel top backup pad 11 top fixed mounting has guard rail 10, barrel top backup pad 11 top fixed mounting has agitator motor 18, the vertical barrel top backup pad 11 that runs through of output shaft of agitator motor 18 and with the one end fixed connection of first (mixing) shaft 19, first (mixing) shaft 19 outside cover is equipped with prevents disturbance sleeve pipe 20, pipe 22 fixed connection is at pipe chute support 23 top, the inclined tube support 23 is fixedly arranged on a connecting support lug on the inner wall of the tube body, the connecting support lug on the inner wall of the tube body is fixedly connected with the tube body 16, the bottom end of the disturbance-preventing sleeve 20 vertically penetrates through the inclined tube 22 and is fixedly connected with the conical resistance plate 7, the bottom end of the first stirring shaft 19 is fixedly connected with one end of the second stirring shaft 29 through a shaft coupling, the second stirring shaft 29 extends into the hollow mixing and stirring cone (cone) 9, the mixing and stirring cone 9 is positioned under the conical resistance plate 7, a cone water flow tangential outlet is arranged on the outer side of the mixing and stirring cone 9, a plurality of connecting support bodies 28 are equidistantly connected on the outer side of the mixing and stirring cone 9 along the circumferential direction, the mixing and stirring cone 9 is fixedly arranged on the connecting support lug on the inner wall of the tube body through the connecting support bodies 28, and a plurality of groups of rotational flow stirring blades 8 are sequentially arranged on the second stirring shaft 29 from top to bottom, the length of the rotational flow stirring blade 8 is matched with that of the mixing stirring cone 9, the inclination directions of the two opposite rotational flow stirring blades 8 are mutually vertical, the inner wall of the mixing stirring cone 9 is fixedly connected with a connecting pipe 26 through a welding connecting sheet 27, a sand setting gap is arranged between the inner wall of the mixing stirring cone 9 and the connecting pipe 26, one end of the connecting pipe 26 is connected with one end of a water inlet pipe 24, the other end of the water inlet pipe 24 extends out of the cylinder 16, the outer side of the cylinder 16 is provided with an overhaul inlet 15, the outer side of the cylinder 16 is provided with a water outlet which is positioned above the inclined pipe 22 and is connected with one end of a water outlet pipe 12, a sludge collecting hopper 25 is arranged in the cylinder 16 and is positioned right below the mixing stirring cone 9, the bottom of the cylinder 16 is provided with a sewage discharge outlet 14, the water outlet of the pipeline mixer 4 is connected with the water inlet pipe 24 through a water guide pipe, the water outlet pipe 12 is connected with the water inlet of the filter 6 through the water guide pipe, the inner wall of the barrel 16 is located on one side opposite to the inclined direction of the inclined pipe 22, the buffer type water collecting tank 21 is welded with the U-shaped buffer structure, the buffer type water collecting tank 21 is provided with the circular water intercepting pipe 30, the circular water intercepting pipe 30 is arranged in the buffer type water collecting tank 21 through self balance weight, and the buffer type water collecting tank 21 is designed in a buffer structure.
The first specific application embodiment:
raw water enters a pipeline mixer 4 through a pipeline by a raw water inlet pump 1 to be mixed, a medicament in a medicament adding tank 2 enters the pipeline mixer 4 through a pipeline by a medicament adding pump 3 to be mixed, the raw water in the pipeline mixer 4 enters a mixing stirring cone 9 through a water inlet pipe 24, a stirring motor 18 drives a rotational flow stirring blade 8 to rotate through a first stirring shaft 19 and a second stirring shaft 29, sand particles in the raw water fall into a sludge collecting hopper 25 through a sand setting gap at the bottom of the mixing stirring cone 9, a flocculating constituent makes a water inlet spiral move upwards through the rotational flow stirring blade 8, a flocculating constituent formed in the mixing stirring cone 9 is continuously compacted under the dual action of centrifugal force and gravity to form regular spheroidal particles, the regular spheroidal particles flow flows out through a cone water flow tangential outlet of the mixing stirring cone 9 and is acted by a conical resistance plate to reduce the rising speed to flow out from the cone water flow tangential outlet, because of the resistance of the water body, the water flow tangential force can only be kept at one side of the cone water flow tangential outlet, the particles sink into the mud collecting hopper 25, because of the continuous entering of the raw water, the water body continuously rises, the main flow direction of the water body is diffused and rises from the semicircle at one side of the side opening through the flow guiding function of the device, when the water body rises to the inclined tube 22, the particles settled by the inclined tube 22 fall onto the conical resistance plate 7 and are accelerated to settle along the conical resistance plate 7, the rising water flow mainly rises along the inclined direction of the inclined tube 22, the water body passes through the inclined tube 22 and flows into the buffer type water collecting tank 21 along the opposite direction of the inclined tube 22, the buffer type water collecting tank 21 adopts the buffer structure design, the water body entering the water collecting tank is prevented from entering the water collecting tank due to the over-fast flow velocity and entering the filter tank 6 for further filtration and discharge after being decelerated in the state of the buffer function blocked by the circular water intercepting tube 30, the effluent turbidity is below 1 NTU.
The second specific application embodiment:
for the treatment of the water with calcium and magnesium ions exceeding the standard, the adding amount of crystal nuclei and lime water is controlled according to the water hardness, the water with high turbidity exceeding the standard is prepared according to the water quality detection report, the medicaments (the main components of the medicaments are PAC, crystal nuclei and lime water) are prepared, the high-turbidity raw water and the prepared medicaments are sent into a main pipeline through a medicament adding pump 3, the raw water enters a pipeline mixer 4 for preliminary mixing and then enters an integrated water purifying device 5, the stirring speed of a stirring motor 18 in the integrated water purifying device 5 is controlled at 5rap, the hydraulic retention time is controlled at about 15min, the calcium and magnesium ions are coagulated and formed on the cone body, the calcium and magnesium ions are flocculated and attached to the crystal nuclei to form a sphere which is approximately regular under the combined action of a rotational flow stirring blade 8 and a mixing stirring cone 9, the sphere flows out from a cone water flow tangential outlet of the mixing stirring cone 9 and sinks into a mud collecting hopper 25, and the water body with the calcium and magnesium ions and large-particle flocculants removed passes through the flow guiding action of the device, the main direction of flow is by the semicircle diffusion of side direction mouth one side and rises, when rising to pipe chute 22, the granule that pipe chute 22 subsides falls into on toper resistance plate 7, subside with higher speed along toper resistance plate 7, rising rivers mainly rise along pipe chute 22 incline direction, through the water of pipe chute 22, flow in buffer type water catch bowl 21 along pipe chute 22 incline direction opposite direction, buffer type water catch bowl 21 adopts the buffer structure design, avoid getting into the water in buffer type water catch bowl 21 to bring partial granule into buffer type water catch bowl 21 because of too fast velocity of flow in, water in the buffer type water catch bowl 21 gets into filtering pond 6 through outlet pipe 12 and further filters and discharges, the play water turbidity is below 1NTU, play water hardness satisfies the standard requirement, the calcium magnesium ion clearance is greater than 75%.
1. The integrated design is adopted, the three-dimensional space is fully utilized, and a plurality of process flows are reasonably and orderly integrated into one device.
2. Adopt the cone flocculation to mix, through 8 designs of whirl stirring vane with mixing stirring cone 9 matches, the raw water is through mixing stirring cone 9 and 8 combined action of whirl stirring vane, make the water follow spiral cone upward rotary motion, the flocculation granule of aquatic receives under the effect of centrifugal force, to the gathering of spiral cone section of thick bamboo wall, receive the shearing action of gravity again simultaneously, make the flocculating constituent of gathering, the density increase, the volume is approximate circular, the granule flows along the cone rivers tangential outlet of mixing stirring cone 9, because the density of flocculating constituent increases, approximate circular settling velocity is with fast, the handling capacity is just bigger, the closely knit degree of granule is good, the medicament make full use of, it is efficient to clarify, and is good in effect.
3. The conical resistance plate 7 has two functions of (1) preventing over-high local ascending flow speed caused by too large water inlet pressure from being unfavorable for flocculation and sedimentation; (2) the conical inclined plate can be effectively formed to accelerate clarification.
4. The disturbance prevention sleeve 20 mainly prevents the rotation of the first stirring shaft 19 from influencing the movement of the upper water body, and the stirring only influences the disturbance of the water body of the mixing and stirring cone 9.
5. Pipe chute 22 and buffering type water catch bowl 21 rational design overall arrangement, buffering type water catch bowl 21 is if the welding is around middle part or the inside ring of barrel 16, it is poor to go out water effect turbidity, this is mainly influenced by the inclined position of pipe chute 22 and the position of mixing stirring cone 9 tangential opening, buffering type water catch bowl 21 will be placed in the opposite direction of pipe chute 22 slope and tangential opening direction, buffering type water catch bowl 21 adopts the buffer structure design simultaneously, avoid getting into during the water in buffering type water catch bowl 21 brings partial granule into buffering type water catch bowl 21 because of too fast velocity of flow, flow out through outlet pipe 12, the position is arranged and is gone out water turbidity effectively to be reduced 2 to 4NTU under the same circumstances of this equipment self contrast test surface.
Experiment time: 2020.09.09 test temperature is 17-20 deg.C
The experimenter: tianwenjie
The experiments are described generally: the integrated water purifying device has a cylindrical structure, the diameter is 2.2m, the height is 5m, test parameters, the rotating speed of a motor is 5r/min, the inlet water turbidity is 1000 +/-50 NTU, and the flow rate of a pump is 30m3The delivery lift is 16m, and the mixing, stirring and retention time is 15 min.
PAC dosage mode: according to 5% -10% configuration of weight concentration, the medicament dosage is at 20mg/L, and progress turbidity control is about 1000 +/-50 NTU, shows the turbidity of intaking according to the turbidity appearance of intaking, according to the time behavior, adds the loess, guarantees that the turbidity of intaking is stable, and the data of once taking notes every half an hour experiment, two hours before the experiment do not record data, and the data is unstable, the blowdown before the experiment.
Water collecting tank middle welding
| Recording time | Inlet water turbidity NTU | Turbidity NTU of effluent | PAC dosage mg/L | PAM dosage mg/L |
| 13:00 | 1000±50 | 12.11 | 20 | // |
| 13:30 | 1000±50 | 13.62 | 20 | / |
| 14:00 | 1000±50 | 12.83 | 20 | / |
| 14:30 | 1000±50 | 13.52 | 20 | / |
| 15:00 | 1000±50 | 13.19 | 20 | / |
| 15:30 | 1000±50 | 14.25 | 20 | / |
| 16:00 | 1000±50 | 14.85 | 20 | / |
| 16:30 | 1000±50 | 13.28 | 20 | / |
| 17:00 | 1000±50 | 13.96 | 20 | / |
| 17:30 | 1000±50 | 12.86 | 20 | / |
| 18:00 | 1000±50 | 13.13 | 20 | / |
| 18:30 | 1000±50 | 13.56 | 20 | / |
Experiment time: 2020.09.12 test temperature is 17-20 deg.C
The experimenter: tianwenjie
The experiments are described generally: the integrated water purifying device has a cylindrical structure, the diameter is 2.2m, the height is 5m, test parameters, the rotating speed of a motor is 5r/min, the inlet water turbidity is 1000 +/-50 NTU, and the flow rate of a pump is 30m3The delivery lift is 16m, and the mixing, stirring and retention time is 15 min.
PAC dosage mode: according to 5% -10% configuration of weight concentration, the medicament dosage is at 20mg/L, and progress turbidity control is about 1000 +/-50 NTU, shows the turbidity of intaking according to the turbidity appearance of intaking, according to the time behavior, adds the loess, guarantees that the turbidity of intaking is stable, and the data of once taking notes every half an hour experiment, two hours before the experiment do not record data, and the data is unstable, the blowdown before the experiment.
Oblique-degree reverse welding of water collecting tank inclined pipe
| Recording time | Inlet water turbidity NTU | Turbidity NTU of effluent | PAC dosage mg/L | PAM dosage mg/L |
| 13:00 | 1000±50 | 11.23 | 20 | / |
| 13:30 | 1000±50 | 10.00 | 20 | / |
| 14:00 | 1000±50 | 8.577 | 20 | / |
| 14:30 | 1000±50 | 8.724 | 20 | / |
| 15:00 | 1000±50 | 8.980 | 20 | / |
| 15:30 | 1000±50 | 9.032 | 20 | / |
| 16:00 | 1000±50 | 9.124 | 20 | / |
| 16:30 | 1000±50 | 9.290 | 20 | / |
| 17:00 | 1000±50 | 8.870 | 20 | / |
| 17:30 | 1000±50 | 8.288 | 20 | / |
| 18:00 | 1000±50 | 9.218 | 20 | / |
| 18:30 | 1000±50 | 9.323 | 20 | / |
Experiment time: 2020.09.13 weather sunny test temperature is 13-20 deg.C
The experimenter: tianwenjie
The experiments are described generally:
the experiments are described generally: the integrated water purifying device has a cylindrical structure, the diameter is 2.2m, the height is 5m, test parameters, the rotating speed of a motor is 5r/min, the inlet water turbidity is 1500 +/-50 NTU, and the flow rate of a pump is 30m3The delivery lift is 16m, and the mixing, stirring and retention time is 15 min.
PAC dosage mode: the dosage is 5-10% of the weight concentration, the dosage is 20mg/L, and the PAM dosage mode is as follows: prepared according to the weight concentration of 0.05-0.2 percent, and the adding amount is 1 mg/L; progress turbidity control is about 1500 ± 50NTU, and according to the turbidity of intaking that the turbidity appearance shows into water, according to the time behavior of operation, add the loess, guarantee that the turbidity of intaking is stable, and the experimental data is once taken notes every half an hour, and two hours before the experiment are not the record data, and data is unstable, the blowdown before the experiment.
Oblique-degree reverse welding of water collecting tank inclined pipe
| Recording time | Inlet water turbidity NTU | Turbidity NTU of effluent | PAC dosage mg/L | PAM dosage mg/L |
| 12:00 | 1500±50 | 10.94 | 20 | 1 |
| 12:30 | 1500±50 | 11.22 | 20 | 1 |
| 13:00 | 1500±50 | 10.82 | 20 | 1 |
| 13:30 | 1500±50 | 11.22 | 20 | 1 |
| 14:00 | 1500±50 | 10.45 | 20 | 1 |
| 14:30 | 1500±50 | 10.50 | 20 | 1 |
| 15:00 | 1500±50 | 10.48 | 20 | 1 |
| 15:30 | 1500±50 | 11.28 | 20 | 1 |
| 16:00 | 1500±50 | 10.76 | 20 | 1 |
| 16:30 | 1500±50 | 10.88 | 20 | 1 |
| 17:00 | 1500±50 | 10.54 | 20 | 1 |
| 17:30 | 1500±50 | 11.37 | 20 | 1 |
| 18:00 | 1500±50 | 10.76 | 20 | 1 |
Experiment time: 2020.09.14 test temperature is 16-20 deg.C
The experimenter: tianwenjie
The experiments are described generally:
the experiments are described generally: the integrated water purifier is of a cylindrical structure, the diameter is 2.2m, the height is 5m, test parameters, the rotating speed of a motor is 5r/min, the inlet water turbidity is 2000 +/-50 NTU, and the flow rate of a pump is 30m3The delivery lift is 16m, and the mixing, stirring and retention time is 15 min.
PAC dosage mode: the dosage is 5-10% of the weight concentration, the dosage is 20mg/L, and the PAM dosage mode is as follows: prepared according to the weight concentration of 0.05-0.2 percent, and the adding amount is 1 mg/L; progress turbidity control is about 2000 +/-50 NTU, and according to the turbidity of intaking that the turbidity appearance shows into water, according to the time behavior of operation, add the loess, guarantee that the turbidity of intaking is stable, and the experimental data is once taken notes every half an hour, and two hours before the experiment are not the record data, and data are unstable, the blowdown before the experiment.
Oblique-degree reverse welding of water collecting tank inclined pipe
| Recording time | Inlet water turbidity NTU | Turbidity NTU of effluent | PAC dosage mg/L | PAM dosage mg/L |
| 11:00 | 2000±50 | 13.94 | 20 | 1 |
| 11:30 | 2000±50 | 11.22 | 20 | 1 |
| 12:00 | 2000±50 | 12.26 | 20 | 1 |
| 12:30 | 2000±50 | 13.16 | 20 | 1 |
| 13:00 | 2000±50 | 12.85 | 20 | 1 |
| 13:30 | 2000±50 | 13.61 | 20 | 1 |
| 14:00 | 2000±50 | 13.16 | 20 | 1 |
| 14:30 | 2000±50 | 11.82 | 20 | 1 |
| 15:00 | 2000±50 | 13.16 | 20 | 1 |
| 15:30 | 2000±50 | 13.24 | 20 | 1 |
| 16:00 | 2000±50 | 12.88 | 20 | 1 |
| 16:30 | 2000±50 | 12.05 | 20 | 1 |
| 17:00 | 2000±50 | 12.26 | 20 | 1 |
| 17:30 | 2000±50 | 12.54 | 20 | 1 |
To sum up, Xinjiang local feedwater raw water generally all is snow melt nature raw water, and aquatic silt content is big, and current depositing reservoir area is big simultaneously, and equipment integration is not high, and under the equal dwell time, the treatment effeciency is low, and it is big to go out the water turbidity, and some medicaments are not by make full use of, cause the medicament use amount increase, increase the water supply station operating cost etc.. Raw water is added with a medicament and mixed by a pipeline mixer, a device water inlet pipe is connected, inlet water enters a mixing and stirring cone through a water inlet pipeline, a stirring motor drives a rotational flow stirring blade to rotate through a shaft, sand particles in the raw water fall into a mud collecting hopper through a sand setting gap at the bottom of the mixing and stirring cone, flocculating constituents enable the inlet water to spirally move upwards through the rotational flow stirring blade with the cone (each group of blade length of the rotational flow stirring blade corresponds to the cone, the inclined directions of the blades at two sides are mutually vertical), the flocculating constituents formed in the cone are continuously compact under the dual action of centrifugal force and gravity to form regular spheroidal particles, the regular spheroidal particles flow out through a tangential port of the mixing and stirring cone (under the action of a conical resistance plate, the ascending speed is reduced, the flocculating constituents flow flows out from the tangential port, and the tangential force of water flow can only be kept at one side of the tangential port due to the resistance of a water body) and sink into a mud collecting tank, because the continuous entering of raw water, the continuous rising of water, the water passes through the water conservancy diversion effect of device, main flow direction is by the semicircle diffusion rise of side direction mouth one side, when rising to the pipe chute under control, the granule that the pipe chute subsided falls into on the toper resistance board, subside along the cone is accelerated, ascending rivers mainly rise along the pipe chute incline direction, one side of supernatant water catch bowl welding barrel (strictly forbid all around the annular arrange, and middle position welding, the test must weld in pipe chute incline direction opposite barrel one side), the water on layer that gets into the supernatant through the pipe chute subsides the district, flow in the water catch bowl along pipe chute incline direction opposite direction, the water catch bowl adopts buffer structure design, avoid the water that gets into in the water catch bowl to bring into in partial granule gets into the water catch bowl because of too fast velocity of flow.
Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments or portions thereof without departing from the spirit and scope of the invention.
Claims (3)
1. The utility model provides a vertical vortex purifier of high turbidity or high rigidity water, includes raw water intake pump (1), its characterized in that: the water inlet of former water intake pump (1) and the one end pipe connector of aqueduct, the delivery port of former water intake pump (1) passes through the water inlet pipe connector of aqueduct and pipe mixer (4), the water inlet of pipe mixer (4) passes through the liquid catheter and adds the liquid outlet pipe connector of medicine pump (3), the inlet that adds medicine pump (3) passes through the liquid catheter and adds the liquid outlet pipe connector of medicine jar (2), the delivery port of pipe mixer (4) is connected with the one end of aqueduct, and the other end of aqueduct is provided with integrated purifier (5).
2. The vertical vortex cleaning apparatus for high turbidity or high hardness water according to claim 1, wherein: the integrated water purifying device (5) comprises a conical resistance plate (7), a rotational flow stirring blade (8), a mixing stirring cone (9), a protective railing (10), a cylinder top support plate (11), a water outlet pipe (12), upright legs (13), a sewage outlet (14), an overhauling inlet (15), a cylinder (16), a ladder (17), a stirring motor (18), a first stirring shaft (19), an anti-disturbance sleeve (20), a buffer type water collecting tank (21), an inclined pipe (22), an inclined pipe support (23), a water inlet pipe (24), a sludge collecting hopper (25), a connecting pipe (26), a welding connecting sheet (27), a connecting support body (28), a second stirring shaft (29) and a circular water intercepting pipe (30), wherein the upright legs (13) are fixedly installed at the bottom of the cylinder (16), the ladder (17) is fixedly installed on the outer side of the cylinder (16), the cylinder top support plate (11) is fixedly installed at the top of the cylinder (16), the anti-disturbance mixing stirring device is characterized in that a protective barrier (10) is fixedly mounted at the top of the barrel top supporting plate (11), a stirring motor (18) is fixedly mounted at the top of the barrel top supporting plate (11), an output shaft of the stirring motor (18) vertically penetrates through the barrel top supporting plate (11) and is fixedly connected with one end of a first stirring shaft (19), an anti-disturbance sleeve (20) is sleeved outside the first stirring shaft (19), an inclined tube (22) is fixedly connected to the top of an inclined tube support (23), the inclined tube support (23) is fixedly mounted on a barrel inner wall connecting lug, the barrel inner wall connecting lug is fixedly connected to the barrel (16), the bottom end of the anti-disturbance sleeve (20) vertically penetrates through the inclined tube (22) and is fixedly connected with a conical resistance plate (7), and the bottom end of the first stirring shaft (19) is fixedly connected with one end of a second stirring shaft (29) through a coupler, the second stirring shaft (29) extends into the mixing and stirring cone (9), the mixing and stirring cone (9) is positioned under the conical resistance plate (7), the outer side of the mixing and stirring cone (9) is provided with a cone water flow tangential outlet, the outer side of the mixing and stirring cone (9) is connected with a plurality of connecting support bodies (28) at equal intervals along the circumferential direction, the mixing and stirring cone (9) is fixedly installed on a barrel inner wall connecting lug through the connecting support bodies (28), a plurality of groups of rotational flow stirring blades (8) are sequentially installed on the second stirring shaft (29) from top to bottom, the inner wall of the mixing and stirring cone (9) is fixedly connected with a connecting pipe (26) through a welding connecting sheet (27), a sand settling gap is arranged between the inner wall of the mixing and stirring cone (9) and the connecting pipe (26), one end of the connecting pipe (26) is connected with one end of the water inlet pipe (24), the other end of inlet tube (24) stretches out barrel (16), overhaul entry (15) have been seted up in the barrel (16) outside, the delivery port of being connected with outlet pipe (12) one end is seted up to the position that the barrel (16) outside is located pipe chute (22) top, the position that the barrel (16) inside is located under mixing stirring cone (9) is provided with sludge hopper (25), drain (14) have been seted up to barrel (16) bottom, the delivery port of pipeline mixer (4) passes through the aqueduct and is connected with inlet tube (24), outlet pipe (12) are connected through the water inlet of aqueduct and filtering pond (6), barrel (16) inner wall is located and has buffering type water catch bowl (21) with pipe chute (22) opposite side welding of slope direction.
3. The vertical vortex cleaning apparatus for high turbidity or high hardness water according to claim 2, wherein: the length of the rotational flow stirring blade (8) is matched with that of the mixing stirring cone (9), and the inclination directions of the two opposite rotational flow stirring blades (8) are mutually vertical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022388669.6U CN214422318U (en) | 2020-10-24 | 2020-10-24 | Vertical vortex purifier of high turbidity or high rigidity water |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022388669.6U CN214422318U (en) | 2020-10-24 | 2020-10-24 | Vertical vortex purifier of high turbidity or high rigidity water |
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| Publication Number | Publication Date |
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| CN214422318U true CN214422318U (en) | 2021-10-19 |
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| CN202022388669.6U Active CN214422318U (en) | 2020-10-24 | 2020-10-24 | Vertical vortex purifier of high turbidity or high rigidity water |
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| Country | Link |
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