Disclosure of Invention
In order to overcome the defects in the prior art and solve the technical problems, the invention provides an irrigation water treatment system.
The technical scheme adopted by the invention for solving the technical problems is as follows: according to the invention, through the arrangement of the circulating component and the dynamic filtering component, on one hand, the filtering and backwashing of the filtering component are simultaneously carried out by utilizing the dynamic filtering, so that the probability of blockage of the filtering component is reduced, on the other hand, the filtering and circulating of the flocculating agent are realized by the cooperation of the circulating component and the dynamic filtering, so that the purifying effect of the flocculating agent can be fully exerted, and the technical problem is solved.
The invention relates to an irrigation water treatment system, which comprises
The water pump is provided with a water pumping pipe and a water delivery pipe, and the end part of the water pumping pipe is provided with a filter head;
the flocculation cylinder is fixedly connected with the water suction pump, the water delivery pipe extends into the flocculation cylinder, and one end of the flocculation cylinder, far away from the water suction pump, is fixedly connected with a water outlet pipe;
the material box is fixedly arranged at the top end of the flocculation barrel, a flocculating agent is contained in the material box, and a material leaking hole is formed in the bottom of the material box and used for communicating the material box with the flocculation barrel;
also comprises
The circulating assembly is arranged inside the flocculation cylinder and is used for driving the flocculating agent to circularly flow in the flocculation cylinder;
the dynamic filtering component is arranged on the circulating component, is matched with the circulating component and is used for filtering large-particle impurities, is always in a rotating state under the impact of water flow and is used for filtering and backwashing in a circulating and alternating mode in the rotating process.
Preferably, the circulation assembly comprises
The guide groove is formed in the inner wall of the flocculation cylinder, the guide groove is spirally arranged in the flocculation cylinder, and one end of the water delivery pipe, which is positioned in the flocculation cylinder, is communicated with the guide groove;
the rotating pipe is rotatably arranged inside the flocculation cylinder, and stirring blades which are uniformly distributed are fixedly arranged on the rotating pipe;
the guide pipe is fixedly connected in the flocculation cylinder, the guide pipe is positioned in the rotating pipe, a reflux groove is formed between the guide pipe and the rotating pipe, the rotating pipe is provided with uniformly distributed sedimentation holes, the sedimentation holes correspond to the stirring blades one by one, and the sedimentation holes are used for communicating the reflux groove with the inner cavity of the flocculation cylinder;
the flocculation cylinder is obliquely installed, and the height above the ground of the flocculation cylinder is smaller along with the closer distance to the water delivery pipe.
Preferably, the dynamic filter assembly comprises
The rotating shaft is rotatably connected inside the flocculation cylinder, extends into the guide pipe and is designed coaxially with the guide pipe;
the filter ring is fixedly arranged on the rotating shaft, two ends of the filter ring are respectively in rotary sealing connection with the inner wall of the flocculation cylinder and the rotating pipe, the guide pipe extends into the filter ring, and the guide pipe is positioned in the opening at the top of the filter ring;
the first filter plate is fixedly connected to the filter ring, the filter ring is provided with a collection hole, the first filter plate extends into the collection hole, one end of the first filter plate, far away from the filter ring, is in an L shape, and the first filter plate is attached to the inner wall of the flocculation cylinder;
the auger, auger fixed mounting is on the rotation axis, and the auger is located the stand pipe inside, the stand pipe is kept away from filter ring one end and is extended to the flocculation section of thick bamboo outside.
Preferably, the first filter is kept away from and is filtered ring one side fixedly connected with second filter, filter fixedly connected with baffle on the ring, the baffle is located first filter, second filter middle part, the baffle all contactless with first filter, second filter, first filter, second filter and baffle constitute and wash the runner.
Preferably, the filter ring is fixedly connected with an annular breast board, and the annular breast board is fixedly connected with the first filter plate, the second filter plate and the partition plate.
Preferably, one side, close to the filter ring, of the second filter plate is hinged to a swing plate, the filter ring is fixedly connected with a limiting plate, and the swing plate is matched with the limiting plate and used for sealing the flushing flow channel.
Preferably, the water supply pipe is located a flocculation section of thick bamboo and installs the dispersion head, the dispersion head is incomplete annular tube, dispersion head middle part and water supply pipe switch on, the dispersion head is close to a flocculation section of thick bamboo internal portion and has seted up evenly distributed's small opening.
Preferably, the arrangement of the leakage holes on the dispersion head gradually reduces the density along with the approach of the distance from the water supply pipe.
The invention has the following beneficial effects:
1. according to the irrigation water treatment system, the direction of the filtering surface is opposite to that of the impact surface through the rotation of the dynamic filtering component in the process of being impacted by water flow, so that the dynamic filtering component alternately performs filtering and backwashing according to different positions in the motion process of the dynamic filtering component, the probability of blockage of the dynamic filtering component can be effectively reduced by utilizing regular backwashing, and further, the probability of equipment failure, unsatisfactory water treatment effect and the like caused by blockage of a filtering structure and the like in the irrigation water treatment process can be effectively reduced.
2. According to the irrigation water treatment system, the circulating component is arranged, so that on one hand, in the dynamic circulating process, the flocculating agent can be effectively prevented from being discharged to the outside when the flocculating agent is insufficiently flocculated and agglomerated to form a floccule, and the flocculation effect of the flocculating agent cannot be sufficiently exerted, on the other hand, in the circulating reciprocating process, the collision and contact probability of the flocculating agent and impurity particles in water flow is increased, the flocculation and agglomeration effects of the flocculating agent on the impurities in the water flow are further enhanced, and the removing effect on the impurities in the water flow is further enhanced.
Detailed Description
In order to make the technical means, the creation characteristics, the achievement purposes and the effects of the invention easy to understand, the invention is further described with the specific embodiments.
As shown in fig. 1 to 6, the irrigation water treatment system of the present invention comprises a water pump 1, wherein a water pumping pipe 11 and a water delivery pipe 12 are installed on the water pump 1, and a filter head is installed at an end of the water pumping pipe 11;
the flocculation cylinder 2 is fixedly connected with the water suction pump 1, the water delivery pipe 12 extends into the flocculation cylinder 2, and one end, far away from the water suction pump 1, of the flocculation cylinder 2 is fixedly connected with a water outlet pipe 21;
the material box 22 is fixedly arranged at the top end of the flocculation barrel 2, a flocculating agent is contained in the material box 22, a material leaking hole 23 is formed in the bottom of the material box 22, and the material leaking hole 23 is used for communicating the material box 22 with the flocculation barrel 2;
the circulating assembly is arranged inside the flocculation cylinder 2 and is used for driving the flocculating agent to circularly flow in the flocculation cylinder 2;
the dynamic filtering component is arranged on the circulating component, is matched with the circulating component and is used for filtering large-particle impurities, is always in a rotating state under the impact of water flow and is used for filtering and backwashing in a circulating and alternating mode in the rotating process;
when irrigation water is pumped, the device is moved to the side of a river or a pond, a water pumping pipe 11 arranged on a water pumping pump 1 is thrown into the river or the pond, the water pumping pump 1 is manually started, the water pumping pump 1 works to continuously pump water flow in the river or the pond through the water pumping pipe 11, during the process that the water flow flows into the water pumping pipe 11, massive garbage, sundries, bricks and stones mixed in the water flow are filtered by a filter head at the end part of the water pumping pipe 11, then the water flow in the water pumping pump 1 is conveyed by the water pumping pump 1 and pumped into a flocculation cylinder 2 through a water conveying pipe 12, at the moment, a flocculating agent is manually thrown into a material box 22 arranged above the flocculation cylinder 2, the flocculating agent drops into the flocculation cylinder 2 through a material leaking hole 23 at the bottom of the material box 22 under the action of gravity, the material box 22 adopted in the application is of a funnel-shaped structure with an opening at the upper part, the thrown flocculating agent is a PAC-type flocculating agent, the PAC-type flocculating agent is thrown into the water flow, can quickly react within 3-5 minutes, small particles are thrown into the flocculation cylinder in the water flow in an adsorption and are gradually coagulated mode, impurities are gradually discharged into a flocculation cylinder, and gradually settled at the top of the PAC-type flocculating cylinder, and gradually settled water flow is discharged into a water flow outlet pipe, and gradually,
in the process that water flows into the flocculation cylinder 2 through the water supply pipe 12, the water impacts a circulating assembly inside the flocculation cylinder 2, so that the circulating assembly rotates in the flocculation cylinder 2, in the process of rotating the circulating assembly, the water in the flocculation cylinder 2 can be made to rotate and rotate, further, impurities in the water flow are made to collide with colloid particles formed by a flocculating agent through the rotation of the water flow, the flocs with larger size are formed to be deposited downwards under the adsorption and aggregation effects of the flocculating agent, and then the impurities in the water flow are effectively removed, meanwhile, after the flocs lose the adsorption effect, namely the size is larger, the flocs move towards the bottom of the flocculation cylinder 2 under the action of gravity and are finally caught by a dynamic filtering assembly, the dynamic filtering assembly also rotates under the impact of the water flow, the flocs in the water flow are caught through the rotation, and finally are discharged to the outside, the dynamic filtering assembly is impacted by the water flow, so that the directions of a filtering surface and an impact surface are opposite, therefore, in the process that the filtering assembly moves according to the dynamic filtering assembly, the filtering efficiency is reduced, the problem of clogging of the filtering efficiency caused by the filtering efficiency of the filtering assembly is reduced, and the clogging of the filtering efficiency is reduced.
Illustratively, the circulating assembly comprises a guide groove 3, the guide groove 3 is arranged on the inner wall of the flocculation cylinder 2, the guide groove 3 is spirally arranged in the flocculation cylinder 2, and one end of the water delivery pipe 12, which is positioned in the flocculation cylinder 2, is communicated with the guide groove 3;
the rotating pipe 31 is rotatably arranged inside the flocculation cylinder 2, and stirring blades 32 which are uniformly distributed are fixedly arranged on the rotating pipe 31;
the guide pipe 33 is fixedly connected in the flocculation cylinder 2, the guide pipe 33 is positioned inside the rotating pipe 31, a backflow tank 34 is formed between the guide pipe 33 and the rotating pipe 31, the rotating pipe 31 is provided with sedimentation holes 35 which are uniformly distributed, the sedimentation holes 35 correspond to the stirring blades 32 one by one, and the sedimentation holes 35 are used for communicating the backflow tank 34 with the inner cavity of the flocculation cylinder 2;
the flocculation cylinder 2 is obliquely installed, and the height above the ground of the flocculation cylinder 2 is smaller along with the closer distance to the water delivery pipe 12;
the flocculation cylinder 2 is obliquely installed, the circulating component is parallel to the inner cavity of the flocculation cylinder 2, namely, the rotating pipe 31 and the flocculation cylinder 2 are coaxially designed, the dynamic filtering component is installed at the bottom of the flocculation cylinder 2, when the water suction pump 1 works, water flow is continuously pumped into the flocculation cylinder 2 through the water feeding pipe 12, the water feeding pipe 12 impacts the water flow into the guide groove 3, the guide groove 3 is spirally arranged, so that the water flow is spirally arranged along the flow path of the inner wall of the flocculation cylinder 2 under the action of the guide groove 3, and due to the arrangement of the guide groove 3, after the water flow in the flocculation cylinder 2 is accumulated to a certain height, the flow rate of the water flow close to the inner wall of the flocculation cylinder 2 is obviously higher than the flow rate of the water flow at the center of the flocculation cylinder 2, so that under the impact of the water flow guided by the guide groove 3, the impact force on the end part of the stirring blade 32 fixedly connected to the rotating pipe 31 is larger, and then cause the stirring vane 32 to drive the rotating tube 31 to rotate inside the flocculation cylinder 2, the rotating stirring vane 32 conflicts with the flocculant which moves downwards under the action of gravity, and the movement path of the floc group, therefore, under the action of the stirring vane 32, the flocculant and the floc group are stirred in water, the flocculant and the floc group change more in the flow path of the water flow, and the movement path is longer, so that the flocculant effectively contacts and collides with the water flow, the adsorption effect on impurities and particles in the water flow is enhanced, meanwhile, in the rotating process of the stirring vane 32, the stirring vane 32 has the effect of stirring the lower floc group upwards, the floc group moving to the upper part has the trend of moving downwards under the action of gravity, and the more the water flow rotates and rises more, so under the impact of the water flow, the floc group is not easy to directly settle to the bottom of the flocculation cylinder 2, therefore, the flocs have the trend of moving into the settling holes 35 in the continuous rotating and settling process, enter the reflux tank 34 through the settling holes 35, and have the trend of moving towards the lower part of the flocculation cylinder 2 along the reflux tank 34 under the action of gravity, and because the reflux tank 34 is communicated with the inner cavity of the flocculation cylinder 2 only through the settling holes 35, the impact effect of the continuously rotating and spirally flowing water in the flocculation cylinder 2 on the water flow in the reflux tank 34 is lower, the upward impact force on the flocs is further reduced, the flocs are convenient to settle towards the bottom of the flocculation cylinder 2,
when water flows out of the water supply pipe 12 under the action of the guide groove 3, in the process of spiral rising, small particle impurities and flocculants which do not form flocs after being salvaged by the dynamic filtering component at the bottom of the flocculation cylinder 2 move upwards under the impact of the water flow, and larger flocs are gradually formed in the process of moving to the upper part of the flocculation cylinder 2, the flocs have the trend of moving downwards under the action of gravity, and are settled to the bottom of the flocculation cylinder 2 again through the backflow groove 34, and are salvaged and discharged by the dynamic filtering component in the settling process, the salvaged small particles rise again, so that the flocculants and the small particle impurities are circulated up and down in the flocculation cylinder 2 until being discharged by the dynamic filtering component in the circulating process, on one hand, the flocculating agent can be effectively prevented from being insufficiently flocculated and agglomerated to form flocs, namely being discharged to the outside, the flocculating effect of the flocculants cannot be sufficiently exerted, on the other hand, the flocculating effect of the flocculating agent is increased when the flocculants collide with the impurity particles in the water flow in the reciprocating process, and the effect of the flocculating agent is enhanced.
Illustratively, the dynamic filtering assembly comprises a rotating shaft 4, the rotating shaft 4 is rotatably connected inside the flocculation cylinder 2, the rotating shaft 4 extends into the guide pipe 33 and is designed coaxially with the guide pipe 33;
the filter ring 41 is fixedly arranged on the rotating shaft 4, two ends of the filter ring 41 are respectively connected with the inner wall of the flocculation cylinder 2 and the rotating pipe 31 in a rotating and sealing manner, the guide pipe 33 extends into the filter ring 41, and the guide pipe 33 is positioned in the filter ring 41 and is provided with an opening;
the first filter plate 42 is fixedly connected to the filter ring 41, the filter ring 41 is provided with a collection hole 43, the first filter plate 42 extends into the collection hole 43, one end of the first filter plate 42, which is far away from the filter ring 41, is in an L shape, and the first filter plate 42 is attached to the inner wall of the flocculation cylinder 2;
the packing auger 44 is fixedly arranged on the rotating shaft 4, the packing auger 44 is positioned inside the guide pipe 33, and one end of the guide pipe 33, which is far away from the filter ring 41, extends to the outside of the flocculation cylinder 2;
the circulating assembly and the dynamic filtering assembly are coaxially arranged in the flocculation cylinder 2, the dynamic filtering assembly is arranged below the circulating assembly, when the water conveying pipe 12 pumps water to the flocculation cylinder 2, the water conveying pipe 12 is positioned in the flocculation cylinder 2 and is Y-shaped, one end of the water conveying pipe extends into the guide groove 3 and is arranged along the tangential direction of the guide groove 3, one end of the water conveying pipe extends into the flocculation cylinder 2 and is opened towards the filtering ring 41, the water flows in the flocculation cylinder 2 along the guide groove 3, under the impact and pushing action of the water flow, the first filter plate 42, the filtering ring 41 and the rotating shaft 4 rotate, in the rotating process of the first filter plate 42, the water is in motion interference with flocs deposited from the upper part, therefore, under the influence of the upward pushing action of the first filter plate 42 and the gravity of the flocs, part of the flocs move towards the filtering ring 41 along the first filter plate 42, finally enter the collecting holes 43 on the filtering ring 41 and further enter the inner cavity of the filtering ring 41, and further enter the inner cavity of the filtering ring 41 because the rotating shaft 4 is provided with the auger 44, and the auger 44 extends to the inner cavity of the guide pipe 33, and part of the spiral filtering ring 33 enters the inner cavity of the guide pipe 33, and the inner cavity of the filter pipe 33, so that part of the flocs can continuously convey water to pass through the guide pipe 33, and the opening of the guide pipe 33, and the guide pipe 33,
specifically, because the water flow pumped by the water pump 1 has a certain kinetic energy, after the water flow enters the flocculation cylinder 2, along with the increase of the flow path, the kinetic energy of the water flow is gradually weakened, so that the water flow impact force at the bottom of the flocculation cylinder 2 is large, the water flow impact force at the top is small, so that the rotation speed of the first filter plate 42 is high, and the rotation speed of the stirring blade 32 at the top is relatively slow, on one hand, the first filter plate 42 at the bottom has a high rotation speed, so that the formed flocs can be collected, and the rotation speed of the stirring blade 32 at the top is mild, so that the stability of the flocs forming can be enhanced, on the other hand, the rotation speed of the first filter plate 42 is high, so that the rotation speeds of the rotating shaft 4 and the auger 44 are relatively high, and further, the conditions of conveying the collected flocs upwards and discharging outwards are met,
meanwhile, because the first filter plates 42 are uniformly arranged on the filter ring 41, only the first filter plate 42 corresponding to the water supply pipe 12 is impacted by water flow, and the impact direction of the water flow is opposite to the filtering direction of the first filter plate 42, so that the back washing effect of the first filter plate 42 is achieved, and other first filter plates 42 which are not directly opposite to the water supply pipe 12 are driven to rotate by the filter ring 41, so that the first filter plates 42 which are not directly impacted by the water flow of the water supply pipe 12 play roles of rotating, filtering and catching, and because the flow velocity of the water flow in the flocculation cylinder 2 is gradually reduced from the inner wall to the center, so that the first filter plates 42 can conveniently collect flocs, because the first filter plates 42 adopted in the application are made of stainless steel screen meshes or filter cloth, in the rotating process of the first filter plates 42, flocculants and the like smaller than the meshes of the first filter plates 42 can permeate through the first filter plates 42, move upwards under the wrapping of the water flow at the guide groove 3, and deposit downwards again after the flocs are formed.
Illustratively, the second filter plate 5 is fixedly connected to one side of the first filter plate 42, which is far away from the filter ring 41, a partition plate 51 is fixedly connected to the filter ring 41, the partition plate 51 is positioned in the middle of the first filter plate 42 and the second filter plate 5, the partition plate 51 is not in contact with the first filter plate 42 and the second filter plate 5, and the first filter plate 42, the second filter plate 5 and the partition plate 51 form a washing flow passage 52;
by arranging the second filter plate 5 and the partition plate 51, and the second filter plate 5 and the partition plate 51 are made of the same material as the first filter plate 42, in the rotating process of the first filter plate 42, the second filter plate 5 is firstly contacted with the floc in the water flow and is stirred and intercepted by the second filter plate 5, so that the floc is settled on one side of the second filter plate 5 close to the rotating direction, along with the continuous upward rotation of the second filter plate 5, so that the floc moves towards the filter ring 41 under the action of gravity, at the moment, under the blocking action of the partition plate 51, the floc can not directly move towards the collecting holes 43, along with the moving process that the second filter plate 5 moves to the top end and gradually moves downwards along with the rotation, the floc flows towards the interval between the second filter plate 5 and the partition plate 51, and when the second filter plate 5 and the partition plate 51 move to the lowest position, the floc is settled to the partition plate 51, the first filter plate 42 and the boundary of the second filter plate 5, along with the rising of the first filter plate 42 and the second filter plate 5, the settled and then is aligned with the collecting holes 43, and finally dropped in the collecting holes 43,
after the flocs are intercepted by the second filter plate 5 and then enter the washing flow channel 52 formed by the first filter plate 42, the second filter plate 5 and the partition plate 51, the flocs can enter the collecting hole 43 after undergoing a rotation period, in a whole rotation period, the first filter plate 42, the second filter plate 5 and the partition plate 51 inevitably complete one back washing with the water conveying pipe 12, and when the flocs are back washed, the flocs are located in the washing flow channel 52, at the moment, the size of the flocs is small and is not enough to be filtered out, and under the action of the back washing water flow, the flocs penetrate through the first filter plate 42, the second filter plate 5 and the partition plate 51 and then are separated from the washing flow channel 52, so that when the flocs are collected, the flocs are washed, on one hand, a large amount of converged flocs and flocculating agent colloid are in contact with the pumped water flow in the water conveying pipe 12, and then the impurities in the pumped water flow in the water conveying pipe 12 are intercepted by the flocs, so that the flocculating agent is completely screened, and the flocculating agent is completely agglomerated and removed, and the flocculating efficiency of the flocs is further enhanced, and the flocculating agent is completely removed, and the probability of the water is reduced.
Illustratively, the filter ring 41 is fixedly connected with an annular baffle 53, and the annular baffle 53 is fixedly connected with the first filter plate 42, the second filter plate 5 and the partition plate 51;
through fixed connection annular breast board 53 on filtering ring 41, and annular breast board 53 and first filter 42, second filter 5, the equal fixed connection of baffle 51, and the runner 52 that will wash of annular breast board 53 is whole to be covered, consequently at annular breast board 53 and first filter 42, second filter 5, the synchronous pivoted in-process of baffle 51, annular breast board 53 can cooperate flocculation section of thick bamboo 2 inner wall and first filter 42, second filter 5, baffle 51, seal washing runner 52, and then can reduce at the washing in-process, the probability that the wadding of collection directly flows out, annular breast board 53 can be at first filter 42 simultaneously, second filter 5 is rotatory, the in-process of collection wadding, form and shelter from the effect, reduce behind the rivers disturbed, the probability that the wadding flutters to flocculation section of thick bamboo 2 top under the effect of disturbing rivers.
Illustratively, a swing plate 54 is hinged to one side of the second filter plate 5, which is close to the filter ring 41, a limit plate 55 is fixedly connected to the filter ring 41, and the swing plate 54 is matched with the limit plate 55 to close the flushing flow channel 52; through articulated swing board 54 on second filter 5, fixed limiting plate 55 on filter ring 41, in the second filter 5 by the rotatory in-process in bottom to top, swing board 54 is under the effect of gravity, downwardly deflection, and then make swing board 54 separate with limiting plate 55, cause the wadding group etc. to drop in washing runner 52 under the effect of gravity, and when second filter 5 from top to bottom moved, swing board 54 contacts with limiting plate 55 under the effect of gravity, and then seal between second filter 5 and the filter ring 41, and then the effective wadding group that prevents in washing runner 52 outwards flows again, when further reducing in washing runner 52 the direct impact of wadding group in receiving water pipe 12 rivers, not through the filtration, directly to washing runner 52 outward outflow's probability.
Illustratively, the water supply pipe 12 is positioned in the flocculation cylinder 2 and is provided with a dispersion head 6, the dispersion head 6 is an incomplete annular pipe, the middle part of the dispersion head 6 is communicated with the water supply pipe 12, and the part of the dispersion head 6, which is close to the flocculation cylinder 2, is provided with uniformly distributed weep holes 61; one end fixed mounting has dispenser head 6 in flow pipe 12 is located flocculation section of thick bamboo 2, and rivers among the flow pipe 12 get into dispenser head 6 inside back, and under the buffering of dispenser head 6, the guide effect, discharge in to flocculation section of thick bamboo 2 through weeping hole 61, enlarge the impact area of rivers on the one hand, reduce local impact dynamics too big, lead to the wadding group structure to be destroyed, and on the other hand enlarges the impact area, and the reinforcing is to the back flush effect of first filter 42, second filter 5 and baffle 51.
For example, the arrangement of the weep holes 61 on the dispersion head 6 gradually decreases along with the approaching of the distance from the water feeding pipe 12, and because the water flow impact force at the position close to the opening of the water feeding pipe 12 is large, and the water flow impact force at the position far away from the water feeding pipe 12 is small, the arrangement density of the weep holes 61 on the dispersion head 6 is changed, so that the density of the weep holes 61 at the positions with large water flow impact force is low, and the density of the local weep holes 61 with small water flow impact force is large, thereby enhancing the uniformity of the water outlet intensity on the dispersion head 6, and further avoiding the overlarge local water flow impact force.
The foregoing illustrates and describes the principles, general features, and advantages of the present invention. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are given by way of illustration of the principles of the present invention, but that various changes and modifications may be made without departing from the spirit and scope of the invention, and such changes and modifications are within the scope of the invention as claimed. The scope of the invention is defined by the appended claims and equivalents thereof.