CN117886485A - Flat ceramic dry film water purifying equipment - Google Patents
Flat ceramic dry film water purifying equipment Download PDFInfo
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- CN117886485A CN117886485A CN202410288359.7A CN202410288359A CN117886485A CN 117886485 A CN117886485 A CN 117886485A CN 202410288359 A CN202410288359 A CN 202410288359A CN 117886485 A CN117886485 A CN 117886485A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 73
- 239000000919 ceramic Substances 0.000 title claims abstract description 37
- 238000004062 sedimentation Methods 0.000 claims abstract description 123
- 239000012528 membrane Substances 0.000 claims abstract description 36
- 239000010865 sewage Substances 0.000 claims abstract description 27
- 238000004659 sterilization and disinfection Methods 0.000 claims description 21
- 230000005540 biological transmission Effects 0.000 claims description 19
- 238000007599 discharging Methods 0.000 claims description 17
- 238000005189 flocculation Methods 0.000 claims description 13
- 230000016615 flocculation Effects 0.000 claims description 13
- 239000008394 flocculating agent Substances 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 11
- 238000000746 purification Methods 0.000 claims description 8
- 239000004744 fabric Substances 0.000 claims description 6
- 238000005192 partition Methods 0.000 claims description 5
- 239000002893 slag Substances 0.000 claims description 5
- 239000005708 Sodium hypochlorite Substances 0.000 claims description 4
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 2
- 239000013049 sediment Substances 0.000 abstract description 55
- 230000000694 effects Effects 0.000 abstract description 9
- 239000010802 sludge Substances 0.000 abstract 1
- 238000007789 sealing Methods 0.000 description 9
- 238000001556 precipitation Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000005452 bending Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a flat ceramic dry film water purifying device, and relates to the technical field of water purifying devices. The invention comprises a bottom frame, a water inlet pipe, a sedimentation pipe group and a fine treatment pipe, wherein a plurality of groups of sedimentation pipe groups are arranged, each sedimentation pipe group consists of two groups of sedimentation pipes, a flat ceramic dry membrane is arranged in each fine treatment pipe, a drain valve is arranged at the bottom of each sedimentation pipe group, and a filter pressing tank capable of extruding sludge is arranged at the top of the bottom frame. The invention ensures that sediment and suspended matters can be quickly settled on the inner wall of the sedimentation pipes by arranging the V-shaped sedimentation pipe groups, and the sedimentation pipe groups are arranged in a plurality of groups, so that the sewage can be subjected to multiple sedimentation, meanwhile, the flocculant is independently added through each group of sedimentation pipes, the sewage can be effectively and fully mixed with the flocculant, the sedimentation effect is good, the sedimentated sewage is disinfected and sterilized through the fine treatment pipe, and the disinfected and sterilized water is filtered and purified through the flat ceramic dry membrane, so that the water with high mud content and high suspended matters can be purified.
Description
Technical Field
The invention relates to the technical field of water purification equipment, in particular to flat ceramic dry film water purification equipment.
Background
With the increase of urban population, domestic water is also rapidly increased, and the requirements on water treatment are higher and higher. The filtration module of the water purifying device is usually a ceramic membrane, which is divided into a tubular ceramic membrane and a ceramic flat membrane. The ceramic flat membrane surface is densely provided with micropores, the permeability is different according to different molecular diameters of permeated substances within a certain membrane pore diameter range, the pressure difference at two sides of the membrane is used as a driving force, the membrane is used as a filter medium, and under the action of certain pressure, when feed liquid flows through the surface of the membrane, only water, inorganic salt and micromolecular substances are allowed to permeate the membrane, and the suspended matters, glue, microorganisms and other macromolecular substances in the water are prevented from passing through.
The utility model discloses a pressure-bearing type flat membrane water purifying device which comprises a box body with an opening, wherein the box body is made of a wave-shaped water tank plate, a water inlet is formed in the side face or the top of the box body, a water outlet is formed in the bottom of the box body, a water collecting cover is detachably arranged at the opening of the box body, a water outlet is formed in the water collecting cover, a water purifying membrane group is arranged in the box body and comprises an upper membrane sealing plate and a lower membrane sealing plate, two ends of the upper membrane sealing plate and the lower membrane sealing plate are respectively connected through frame plates, a plurality of ceramic flat membranes which are arranged in parallel are fixedly arranged between the upper membrane sealing plate and the lower membrane sealing plate, the surface geometric shape of the ceramic flat membranes is W-shaped or zigzag, one end membrane hole of the ceramic flat membrane contacting with the lower membrane sealing plate is in a blocking state, one end membrane hole of the upper membrane sealing plate contacting with the water collecting cover is in a circulating state, and a water collecting cavity is formed between the upper membrane sealing plate and the water collecting cover.
Compared with the prior art, the patent has the following technical problems in the actual use process:
This patent all directly utilizes dull and stereotyped ceramic dry state membrane to handle sewage with prior art, and when suspended solid and silt volume were great in sewage, a large amount of silt and suspended solid can lead to dull and stereotyped ceramic dry state membrane to block up, influence dull and stereotyped ceramic dry state membrane's filtration rate, and need often wash dull and stereotyped ceramic dry state membrane, reduce water treatment efficiency.
Disclosure of Invention
The invention aims at: in order to solve the problems, the invention provides a flat ceramic dry film water purifying device.
The invention adopts the following technical scheme for realizing the purposes:
The flat ceramic dry film water purifying device comprises a bottom frame, wherein a bracket is arranged at the top of the bottom frame, a water inlet pipe is fixedly connected to the top of the bracket, a plurality of groups of sedimentation pipe groups are arranged at the top of the bottom frame, each sedimentation pipe group consists of two groups of sedimentation pipes, the two groups of sedimentation pipes are distributed in a V shape, the two groups of sedimentation pipes can swing synchronously and reversely, a connecting hose is arranged between the two groups of sedimentation pipes, the adjacent sedimentation pipe groups are communicated, the leftmost sedimentation pipe group is communicated with the water inlet pipe, the rightmost sedimentation pipe group is communicated with the fine treatment pipe, the fine treatment pipe is of a V-shaped design, a flat ceramic dry film is arranged in the fine treatment pipe, flocculant adding pipes are arranged at the outer sides of sedimentation pipes at the water inlet ends of the fine treatment pipe, and disinfection pipes are arranged at the outer sides of the water inlet ends of the fine treatment pipe;
The bottom of sedimentation tube group is provided with the blowoff valve, the filter-pressing jar that can extrude silt is installed at the top of chassis, filter-pressing jar and sedimentation tube group correspond the distribution, and are located the below of sedimentation tube group, the filter-pressing jar is linked together with the blowoff valve, the outside of filter-pressing jar is provided with the drain pipe, the collecting pipe is installed in the outside of chassis, the collecting pipe is linked together with all drain pipes.
Further, a plurality of groups of inner partition plates are arranged in the sedimentation tube.
Further, a plurality of groups of flow around plates are arranged in the left end of the finishing pipe, and a plurality of groups of flow around plates are distributed in a staggered mode.
Further, a slag discharging valve is arranged at the bottom of the bending part of the fine treatment pipe.
Further, a driving motor is arranged on the outer side of the bracket, a driving shaft is arranged at the output end of the driving motor, a plurality of groups of transmission groove groups are arranged on the outer side of the driving shaft, the transmission groove groups are arranged corresponding to the sedimentation pipe groups, and each transmission groove group consists of two groups of spiral grooves with opposite rotation directions;
The outside rotation of sedimentation tube is installed and is removed the nut, remove nut and helicla flute threaded connection, the top of chassis is provided with the mounting bracket, the guide way has been seted up to the inside of mounting bracket, the outside of sedimentation tube is provided with the traveller, the traveller is pegged graft in the guide way.
Further, the adjacent sedimentation tube sets are communicated through the connecting telescopic tube, the leftmost sedimentation tube set is communicated with the water inlet tube through the connecting telescopic tube, and the rightmost sedimentation tube set is communicated with the fine treatment tube and is connected with the telescopic tube.
Further, the filter-pressing tank is arranged in the mounting rack, a mud inlet is formed in the top of the filter-pressing tank, the mud inlet is communicated with the blow-off valve through a dirt guiding telescopic pipe, a mud discharging port capable of being automatically opened and closed is formed in the bottom of the filter-pressing tank, two groups of filter-pressing plates are connected in a sliding mode inside the filter-pressing tank, a drainage cavity is formed between the filter-pressing plates and the inner wall of the filter-pressing tank, the drainage pipe is communicated with the drainage cavity, filter-pressing cloth is arranged inside the filter-pressing plates, a push rod is arranged on the outer side of the filter-pressing plates and penetrates through the filter-pressing tank, and a top spring is arranged between the push rod and the filter-pressing tank;
the bottom of the sliding column is provided with a transmission block, and one surface of the transmission block, which is close to the ejector rod, is obliquely designed.
Further, the bottom of the mud discharging port is hinged with a mud discharging valve, the outer side of the filter pressing tank is hinged with a telescopic cylinder, and the telescopic end of the telescopic cylinder is hinged with the mud discharging valve.
Further, flocculation tank and disinfection jar are installed respectively to the both sides of chassis, have deposited the flocculating agent in the flocculation tank, have deposited sodium hypochlorite in the disinfection jar, flocculation tank and disinfection jar's top all is provided with the liquid pump, the liquid pump at flocculation tank top is linked together with the flocculating agent interpolation pipe through the conveyer pipe, the liquid pump at disinfection tank top is linked together with the disinfection pipe.
The beneficial effects of the invention are as follows:
1. The invention ensures that sediment and suspended matters can be quickly settled on the inner wall of the sedimentation pipes by arranging the V-shaped sedimentation pipe groups, and the sedimentation pipe groups are arranged in a plurality of groups, so that the sewage can be subjected to multiple sedimentation, meanwhile, the flocculant is independently added through each group of sedimentation pipes, the sewage can be effectively ensured to be fully mixed with the flocculant, the sedimentation effect is good, the sedimentated sewage is disinfected and sterilized through the fine treatment pipe, the disinfected and sterilized water is filtered and purified through the flat ceramic dry film, the blockage of the flat ceramic dry film can be effectively prevented, and the water purification efficiency is high.
2. According to the invention, by arranging the V-shaped sedimentation tube group, sediment and suspended solids flow into the bottom and enter the filter pressing tank, the filter pressing tank extrudes excessive water in the sediment, the excessive water is recycled through the drain pipe and the collecting pipe and is treated again through the equipment, so that the waste of water resources is avoided, and the sediment and suspended solids can be discharged at an accelerated speed when the sedimentation tube is closed due to the fact that the sedimentation tube can swing, so that the sedimentation tube is prevented from being blocked by excessive sediment, and the treatment is stable.
3. The invention is arranged by the two groups of settling pipes which can synchronously and reversely swing, not only can accelerate the discharge of sediment, but also can change the deposition speed of the sediment and suspended matters, is suitable for sewage treatment with different concentrations, and has wide treatment range.
Drawings
FIG. 1 is a schematic diagram of the overall system of the present invention;
FIG. 2 is a second overall schematic of the present invention;
FIG. 3 is a schematic view of the angle adjusting structure of the settling tube set of the present invention;
FIG. 4 is a schematic diagram of a settling tube stack and pressure filtration tank of the present invention;
FIG. 5 is a schematic diagram of a settling tube set of the present invention;
FIG. 6 is a schematic cross-sectional view of a settling tube set of the present invention;
FIG. 7 is a schematic representation of a filter press tank of the present invention;
FIG. 8 is a schematic cross-sectional view of a filter press tank of the present invention;
FIG. 9 is a schematic cross-sectional view of a finishing tube of the present invention.
Reference numerals: 1. a chassis; 101. a bracket; 102. a mounting frame; 103. a driving motor; 104. a drive shaft; 2. a water inlet pipe; 3. a sedimentation tube set; 31. moving the nut; 32. a flocculant adding pipe; 33. a connecting hose; 34. a spool; 35. a transmission block; 36. a blow-down valve; 37. a dirt guiding telescopic pipe; 38. an inner partition; 4. a finishing tube; 41. a flat ceramic dry film; 42. a slag discharging valve; 43. a flow-around plate; 5. a flocculation tank; 6. a liquid pump; 7. a delivery tube; 8. a sterilization tank; 9. a sterilizing tube; 10. a filter pressing tank; 1001. a mud inlet; 1002. a mud discharging valve; 1003. a telescopic cylinder; 1004. a filter pressing plate; 1005. press filtration cloth; 1006. a push rod; 1007. a top spring; 1008. a drain pipe; 11. a collection pipe; 12. and is connected with the telescopic pipe.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention more clear, the technical solutions of the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention.
The flat ceramic dry film water purifying apparatus according to a preferred embodiment of the present invention will be described in detail below.
Example 1
As shown in fig. 1-9, the flat ceramic dry film water purifying device comprises a bottom frame 1, a bracket 101 is arranged at the top of the bottom frame 1, a water inlet pipe 2 is fixedly connected to the top of the bracket 101, a plurality of groups of sedimentation pipe groups 3 and fine treatment pipes 4 are arranged at the top of the bottom frame 1, at least three groups of sedimentation pipe groups 3 are arranged, each sedimentation pipe group 3 consists of two groups of sedimentation pipes, the two groups of sedimentation pipes are distributed in a V shape, the two groups of sedimentation pipes can swing reversely synchronously, a connecting hose 33 is arranged between the two groups of sedimentation pipes, the adjacent sedimentation pipe groups 3 are communicated, the leftmost sedimentation pipe group 3 is communicated with the water inlet pipe 2, the rightmost sedimentation pipe group 3 is communicated with the fine treatment pipes 4, the fine treatment pipes 4 are of V-shaped design, flat ceramic dry film 41 is arranged in the fine treatment pipes 4, flocculant adding pipes 32 are arranged at the outer sides of the sedimentation pipes at the water inlet ends of the fine treatment pipes 4, and disinfection pipes 9 are arranged at the outer sides of the water inlet ends of the fine treatment pipes 4;
The bottom of sedimentation tube group 3 is provided with blowoff valve 36, and filter-pressing jar 10 that can extrude silt is installed at the top of chassis 1, and filter-pressing jar 10 and sedimentation tube group 3 correspond the distribution, and lie in the below of sedimentation tube group 3, and filter-pressing jar 10 is linked together with blowoff valve 36, and the outside of filter-pressing jar 10 is provided with drain pipe 1008, and collecting pipe 11 is installed in the outside of chassis 1, and collecting pipe 11 is linked together with all drain pipes 1008.
The sewage or sewage containing a large amount of sediment and suspended matters enters the equipment from the water inlet pipe 2, meanwhile, the water inlet end of the leftmost sedimentation pipe is filled with flocculating agent, the sewage is mixed with the flocculating agent, because the sedimentation pipe group 3 and the fine treatment pipe 4 are of V-shaped design, the sewage flow rate can be effectively reduced, the sewage can flow in the sedimentation pipe group 3 and the fine treatment pipe 4 at a desired speed, the sewage cannot flow too fast, because the sedimentation pipe group 3 is of V-shaped design, compared with a completely vertical sedimentation tank, the inclined plane can effectively improve the sedimentation speed of the sediment and the suspended matters, and compared with a flat pipeline, the sediment and the suspended matters after sedimentation are not easily taken away, the treatment effect is remarkable, then the sewage is subjected to multiple times of sedimentation under the action of the plurality of sedimentation pipe groups 3, so that the sediment cannot be fully mixed with the flocculating agent in the sediment because of primary sedimentation, the water after being subjected to primary sedimentation is filled with the sedimentation pipe group 3, the sewage enters the sedimentation pipe group 3 of the second group, the sedimentation time is limited in the first group 3, and is difficult to be fully mixed with the flocculating agent, and the sediment can be carried with a certain amount of sediment and the sedimentation pipe group 3 again enters the fine sedimentation pipe group 4, the fine sedimentation pipe group is completely, the disinfection effect is guaranteed, and the water is completely disinfected and the sedimentation pipe is completely treated by the sedimentation pipe group 4, and the water is completely has high-sterilizing effect, and the sedimentation effect is well is carried out by the sedimentation pipe-treated by the sedimentation pipe, and the water is subjected to the disinfection;
In the sedimentation process, as the sedimentation tube group 3 is of a V-shaped design, sediment automatically flows into the connecting hose 33 at the bottom, the time that sewage passes through one group of sedimentation tube groups 3 is taken as an interval, two groups of sedimentation tubes are gathered and swung towards the middle, the inclination angles of the two groups of sedimentation tubes are increased, sediment and sediment sedimentation speed is accelerated, meanwhile, the blow-off valve 36 is opened, sediment and sediment enter the filter-pressing tank 10, the filter-pressing tank 10 extrudes the sediment and sediment, extruded water enters the collecting tube 11 through the drain pipe 1008 and is collected, the collected water is treated through equipment again, water resources can be greatly saved, the sedimentation tube group 3 is not blocked, and the treatment effect is better;
By controlling the swinging of the two groups of sedimentation pipes according to the sediment and suspended matter content in the sewage, the initial angle of the two groups of sedimentation pipes is changed, the inclination angle is changed, and then the sedimentation speed can be changed, so that the device is suitable for sewage with different concentrations.
Further, the adjacent sedimentation tube sets 3 are communicated through the connecting telescopic tube 12, the leftmost sedimentation tube set 3 is communicated with the water inlet pipe 2 through the connecting telescopic tube 12, the rightmost sedimentation tube set 3 is communicated with the finishing tube 4 and is connected with the telescopic tube 12, and when the sedimentation tubes are closed through the arrangement of the connecting telescopic tube 12, the connecting telescopic tube 12 stretches, so that stable connection among all components is ensured.
Still further, flocculation tank 5 and disinfection jar 8 are installed respectively to the both sides of chassis 1, have deposited the flocculating agent in the flocculation tank 5, have deposited sodium hypochlorite in the disinfection jar 8, and flocculation tank 5 all is provided with liquid pump 6 with the top of disinfection jar 8, and liquid pump 6 at flocculation tank 5 top is linked together with flocculating agent interpolation pipe 32 through conveyer pipe 7, and liquid pump 6 at disinfection jar 8 top is linked together with disinfection pipe 9.
Example two
As shown in FIG. 6, the sedimentation tube is internally provided with a plurality of groups of inner partition plates 38, at least three groups are arranged, sewage can be separated through the arrangement of the inner partition plates 38, sediment deposition speed is further increased, and flocculating agent and sewage can be mixed more fully.
Example III
As shown in fig. 9, a plurality of groups of flow-around plates 43 are arranged in the left end of the finishing tube 4, and the plurality of groups of flow-around plates 43 are distributed in a staggered manner, so that the flow speed can be reduced, and sodium hypochlorite and sewage can be fully mixed.
Further, the bottom of the bending part of the fine treatment pipe 4 is provided with a slag discharge valve 42, and part of impurities filtered by the flat ceramic dry film 41 can be accumulated at the bottom of the fine treatment pipe 4, so that the impurities can be rapidly discharged through the arrangement of the slag discharge valve 42.
A fourth embodiment provides a swinging structure of a sedimentation tube;
As shown in fig. 1-4, a driving motor 103 is installed on the outer side of a bracket 101, a driving shaft 104 is installed at the output end of the driving motor 103, a plurality of groups of transmission groove groups are arranged on the outer side of the driving shaft 104, the transmission groove groups are arranged corresponding to a sedimentation pipe group 3, and each transmission groove group consists of two groups of spiral grooves with opposite rotation directions;
The outside rotation of sedimentation tube is installed and is moved nut 31, moves nut 31 and helicla flute threaded connection, and the top of chassis 1 is provided with mounting bracket 102, and the guide way has been seted up to the inside of mounting bracket 102, and the outside of sedimentation tube is provided with slide column 34, and slide column 34 is pegged graft in the guide way.
In the process of precipitation, because the precipitation tube group 3 is V-shaped design, therefore the precipitate can flow into the connecting hose 33 of bottom automatically, with the time that sewage passed through a set of precipitation tube group 3 as the interval, control driving motor 103 circular telegram, driving motor 103 drives drive shaft 104 and rotates, drive shaft 104 passes through the transmission groove group and moves nut 31 and drive two sets of precipitation tubes and draw together the swing in the centre, two sets of precipitation tube inclination increases, accelerate silt and precipitate bottom speed, blowoff valve 36 opens simultaneously, silt and precipitate get into filter-pressing jar 10, filter-pressing jar 10 is with silt and precipitate extrusion, extruded water is received in collecting pipe 11 through drain pipe 1008 entering, the water after the collection is again through equipment aftertreatment, can very big water economy resource, and can not cause precipitation tube group 3 to block up, the treatment effect is better.
Fifth embodiment, based on the above embodiment, a filter pressing tank 10 structure is provided;
As shown in fig. 4-8, the filter-pressing tank 10 is installed in the installation frame 102, a mud inlet 1001 is formed in the top of the filter-pressing tank 10, the mud inlet 1001 is communicated with the blow-down valve 36 through a dirt guiding telescopic pipe 37, a mud discharge port capable of being automatically opened and closed is formed in the bottom of the filter-pressing tank 10, two groups of filter-pressing plates 1004 are slidably connected in the filter-pressing tank 10, a drainage cavity is formed between the filter-pressing plates 1004 and the inner wall of the filter-pressing tank 10, the drainage pipe 1008 is communicated with the drainage cavity, a filter-pressing cloth 1005 is arranged in the filter-pressing plates 1004, a push rod 1006 is arranged on the outer side of the filter-pressing plates 1004, the push rod 1006 penetrates through the filter-pressing tank 10, and a push spring 1007 is arranged between the push rod 1006 and the filter-pressing tank 10;
the bottom of the sliding column 34 is provided with a transmission block 35, and one surface of the transmission block 35 close to the ejector rod 1006 is obliquely designed.
In the process of precipitation, because sediment tube group 3 is V type design, consequently, sediment can flow into the coupling hose 33 of bottom voluntarily, with the time of sewage through a set of sediment tube group 3 is the interval, control driving motor 103 circular telegram, driving motor 103 drives drive shaft 104 and rotates, drive shaft 104 passes through the transmission groove group and moves nut 31 and drive two sets of sedimentation tubes and draw together the swing in the middle, two sets of sedimentation tube inclination increases, speed of sediment and sediment settling velocity, blowoff valve 36 opens simultaneously, sediment and sediment get into filter-pressing tank 10, because drive shaft 104 highly fixed, consequently, the height of mobile nut 31 is fixed, two sets of sedimentation tubes draw together, its bottom descends, the sedimentation tube drives slide post 34 and descends, slide post 34 drives transmission piece 35 and promotes the ejector pin 1006 to slide in filter-pressing tank 10, ejector pin 1006 drives filter pressing plate 1004 and filter cloth 1005 and sediment and extrudees, sediment through the filter cloth in the water in sediment, the sediment flows out, the sediment gets into the drainage cavity, sediment is extruded in the while entering, the sediment is collected by 1008 in collecting pipe 11 through collecting the sediment, sediment and sediment is collected through collecting device, the sediment can not need of more compact and the sediment is carried out through the sediment and sediment is carried out to the sediment has no more has the effect to be more compact, the sediment is discharged through the sediment and is more is discharged through the sediment tube group 3, the sediment has no need to be more compact to be more processed, the sediment is more compact, the sediment is more discharged and more sediment is more discharged.
Further, a mud discharging valve 1002 is hinged to the bottom of the mud discharging port, a telescopic cylinder 1003 is hinged to the outer side of the filter pressing tank 10, and a telescopic end of the telescopic cylinder 1003 is hinged to the mud discharging valve 1002.
By controlling the extension of the telescopic cylinder 1003, the telescopic cylinder 1003 drives the mud discharging valve 1002 to swing downwards, the mud discharging valve 1002 enables a mud discharging opening to be opened, and the extruded sediment and sediment are automatically discharged under the action of gravity.
The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (9)
1. The flat ceramic dry film water purifying device comprises a bottom frame (1), and is characterized in that a bracket (101) is arranged at the top of the bottom frame (1), a water inlet pipe (2) is fixedly connected to the top of the bracket (101), a sedimentation pipe group (3) and a fine treatment pipe (4) are arranged at the top of the bottom frame (1), a plurality of groups of sedimentation pipe groups (3) are arranged, each sedimentation pipe group (3) consists of two groups of sedimentation pipes, the two groups of sedimentation pipes are distributed in a V shape, the two groups of sedimentation pipes can synchronously and reversely swing, a connecting hose (33) is arranged between the two groups of sedimentation pipes, the sedimentation pipe groups (3) are adjacent to each other, the leftmost sedimentation pipe group (3) is communicated with the water inlet pipe (2), the rightmost sedimentation pipe group (3) is communicated with the fine treatment pipe (4), the fine treatment pipe (4) is in a V-shaped design, flat ceramic dry film (41) is arranged in the inner part of the fine treatment pipe (4), flocculant adding pipes (32) are arranged on the outer sides of sedimentation pipes at the water inlet ends, and disinfection pipes (9) are arranged on the outer sides of the water inlet ends of the fine treatment pipe (4);
The bottom of sedimentation tube group (3) is provided with blowoff valve (36), filter-pressing jar (10) that can extrude silt are installed at the top of chassis (1), filter-pressing jar (10) correspond with sedimentation tube group (3) and distribute, and are located the below of sedimentation tube group (3), filter-pressing jar (10) are linked together with blowoff valve (36), the outside of filter-pressing jar (10) is provided with drain pipe (1008), collecting pipe (11) are installed in the outside of chassis (1), collecting pipe (11) are linked together with all drain pipes (1008).
2. The flat ceramic dry membrane water purification apparatus as claimed in claim 1, wherein a plurality of groups of inner partition plates (38) are provided inside the sedimentation tube.
3. The flat ceramic dry film water purifying device according to claim 1, wherein a plurality of groups of flow-around plates (43) are arranged in the left end of the finishing tube (4), and the groups of flow-around plates (43) are distributed in a staggered manner.
4. A flat ceramic dry film water purifying apparatus as claimed in claim 3, wherein a slag discharging valve (42) is provided at the bottom of the bent part of the finishing tube (4).
5. The flat ceramic dry film water purifying device according to claim 1, wherein a driving motor (103) is installed on the outer side of the bracket (101), a driving shaft (104) is installed at the output end of the driving motor (103), a plurality of groups of transmission groove groups are formed on the outer side of the driving shaft (104), the transmission groove groups are correspondingly arranged with the sedimentation pipe groups (3), and each transmission groove group consists of two groups of spiral grooves with opposite rotation directions;
The sedimentation pipe is characterized in that a movable nut (31) is rotatably arranged on the outer side of the sedimentation pipe, the movable nut (31) is in threaded connection with the spiral groove, a mounting frame (102) is arranged at the top of the bottom frame (1), a guide groove is formed in the mounting frame (102), a sliding column (34) is arranged on the outer side of the sedimentation pipe, and the sliding column (34) is inserted into the guide groove.
6. The flat ceramic dry membrane water purification device according to claim 5, wherein adjacent sedimentation tube sets (3) are communicated through a connecting telescopic tube (12), the leftmost sedimentation tube set (3) is communicated with a water inlet tube (2) through the connecting telescopic tube (12), and the rightmost sedimentation tube set (3) is communicated with a finishing tube (4) and is connected with the telescopic tube (12).
7. The flat ceramic dry membrane water purification device according to claim 6, wherein the filter pressing tank (10) is installed in the installation frame (102), a mud inlet (1001) is formed in the top of the filter pressing tank (10), the mud inlet (1001) is communicated with a sewage discharge valve (36) through a sewage guide telescopic pipe (37), a mud discharge opening capable of being automatically opened and closed is formed in the bottom of the filter pressing tank (10), two groups of filter pressing plates (1004) are connected in a sliding manner in the filter pressing tank (10), a drainage cavity is formed between the filter pressing plates (1004) and the inner wall of the filter pressing tank (10), a drain pipe (1008) is communicated with the drainage cavity, filter pressing cloth (1005) is arranged in the filter pressing plates (1004), an ejector rod (1006) is arranged on the outer side of the filter pressing plates (1004), the ejector rod (1006) penetrates through the filter pressing tank (10), and a top spring (1007) is arranged between the ejector rod (1006) and the filter pressing tank (10);
The bottom of the sliding column (34) is provided with a transmission block (35), and one surface of the transmission block (35) close to the ejector rod (1006) is obliquely designed.
8. The flat ceramic dry membrane water purification device according to claim 7, wherein a mud discharging valve (1002) is hinged at the bottom of the mud discharging port, a telescopic cylinder (1003) is hinged at the outer side of the filter pressing tank (10), and a telescopic end of the telescopic cylinder (1003) is hinged with the mud discharging valve (1002).
9. The flat ceramic dry membrane water purification device according to any one of claims 1 to 8, wherein flocculation tanks (5) and disinfection tanks (8) are respectively installed on two sides of the bottom frame (1), flocculating agents are stored in the flocculation tanks (5), sodium hypochlorite is stored in the disinfection tanks (8), liquid pumps (6) are respectively arranged at the tops of the flocculation tanks (5) and the disinfection tanks (8), the liquid pumps (6) at the tops of the flocculation tanks (5) are communicated with a flocculating agent adding pipe (32) through conveying pipes (7), and the liquid pumps (6) at the tops of the disinfection tanks (8) are communicated with a disinfection pipe (9).
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