CN213803067U - Single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation equipment - Google Patents
Single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation equipment Download PDFInfo
- Publication number
- CN213803067U CN213803067U CN202022252925.9U CN202022252925U CN213803067U CN 213803067 U CN213803067 U CN 213803067U CN 202022252925 U CN202022252925 U CN 202022252925U CN 213803067 U CN213803067 U CN 213803067U
- Authority
- CN
- China
- Prior art keywords
- fluidized bed
- stirring
- zone
- liquid separation
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000000926 separation method Methods 0.000 title claims abstract description 60
- 238000005469 granulation Methods 0.000 title claims abstract description 42
- 230000003179 granulation Effects 0.000 title claims abstract description 42
- 239000007788 liquid Substances 0.000 title claims abstract description 36
- 238000001914 filtration Methods 0.000 title claims abstract description 31
- 230000008878 coupling Effects 0.000 title claims abstract description 14
- 238000010168 coupling process Methods 0.000 title claims abstract description 14
- 238000005859 coupling reaction Methods 0.000 title claims abstract description 14
- 238000003756 stirring Methods 0.000 claims abstract description 107
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 99
- 239000000725 suspension Substances 0.000 claims abstract description 69
- 238000009826 distribution Methods 0.000 claims abstract description 18
- 230000003068 static effect Effects 0.000 claims abstract description 17
- 239000011324 bead Substances 0.000 claims abstract description 15
- 238000007667 floating Methods 0.000 claims abstract description 4
- 239000010802 sludge Substances 0.000 claims description 41
- 238000002156 mixing Methods 0.000 claims description 19
- 238000005243 fluidization Methods 0.000 claims description 10
- 238000002955 isolation Methods 0.000 claims description 7
- 239000004744 fabric Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 abstract description 31
- 239000007787 solid Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 description 12
- 239000008187 granular material Substances 0.000 description 9
- 239000004576 sand Substances 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 238000005189 flocculation Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000007790 scraping Methods 0.000 description 6
- 230000009471 action Effects 0.000 description 5
- 238000005352 clarification Methods 0.000 description 5
- 230000016615 flocculation Effects 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000013019 agitation Methods 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000011161 development Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000008602 contraction Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- 241001330002 Bambuseae Species 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 239000011146 organic particle Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
Landscapes
- Filtration Of Liquid (AREA)
Abstract
本实用新型公开了一种单电机循环造粒流化床耦合过滤固液分离设备，其中，内筒内的造粒流化区内的搅拌轴上安装有搅拌叶片；搅拌轴的底端穿过布水装置以及进水管的底部与刮泥板相连；分离区内设置有悬浮层过滤固液分离装置；悬浮层过滤固液分离装置分为上下两部分，上部为静止悬浮层，下部为搅动悬浮层，静止悬浮层内充满漂浮着的轻质悬浮珠，搅动悬浮层内设置有滤层搅拌叶片，滤层搅拌叶片通过搅拌轴连接套筒套装在搅拌轴上；单个搅拌驱动电机通过搅拌轴同时带动滤层搅拌叶片、搅拌叶片和刮泥板一起转动。本实用新型中的悬浮层过滤固液分离装置能够有效截留流化床底部无法去除的微小颗粒，使得分离区中的水浊度和悬浮物明显降低。
The utility model discloses a single-motor circulating granulation fluidized bed coupling filtration solid-liquid separation equipment, wherein a stirring blade is installed on a stirring shaft in a granulating fluidized zone in an inner cylinder; the bottom end of the stirring shaft passes through The bottom of the water distribution device and the water inlet pipe is connected with the scraper; the separation zone is provided with a suspended layer filtration solid-liquid separation device; the suspended layer filtration solid-liquid separation device is divided into upper and lower parts, the upper part is a static suspension layer, and the lower part is a stirring suspension layer The static suspension layer is filled with floating light suspension beads, and the stirring suspension layer is provided with a filter layer stirring blade, and the filter layer stirring blade is sleeved on the stirring shaft through the stirring shaft connecting sleeve; Drive the filter layer stirring blade, stirring blade and scraper to rotate together. The suspended layer filtration solid-liquid separation device in the utility model can effectively intercept the tiny particles that cannot be removed at the bottom of the fluidized bed, so that the water turbidity and suspended solids in the separation zone are significantly reduced.
Description
Technical Field
The utility model belongs to the water treatment field relates to the granulation fluidized bed, concretely relates to single motor circulating granulation fluidized bed coupling filters solid-liquid separation equipment.
Background
Along with the development of national economy, the task of water pollution treatment is heavier and heavier, the concentration of suspended matters in water is higher and heavier, and the task of removing the suspended matters in a water treatment process is heavier and heavier, so that the development and research of efficient solid-liquid separation devices are inevitable development trends. A great deal of water treatment technology and equipment based on the theory of suspension layer solid-liquid separation are developed and widely applied to practical engineering, and typical equipment comprises a France Wikiya Actifl o clarification tank, a France Degremont company Densa Deg high-density clarification tank, an efficient carrier flocculation device developed by Philip and the like. The equipment successfully realizes the integration and the equipment of the water treatment technology, has obvious water quality purification effect, and has certain technical defects. For example, the Actiflo clarification tank forms a high-density and large-particle floc suspension layer at the lower part of an inclined tube area, so that the flocculation time is greatly shortened, the surface load can reach more than 80 m/h, but the flocculation area is large, and the number of accessory equipment is large; the Densa Deg high-density clarification tank process organically combines the processes of coagulation, clarification, inclined tube sedimentation, sludge backflow and the like, the surface load can reach 20-50 m/h, but the occupied area of a flocculation area is larger; ballasted flocculation apparatus can also achieve higher surface loads, but the ancillary equipment is overly cumbersome. The domestic waterworks also adopt precipitation and concentration, supernatant is discharged or recycled, and sludge is discharged after dehydration. The method has the advantages of low efficiency, large investment, large occupied area, high operating cost, troublesome management and unsatisfactory effect.
The prior art discloses a high-efficiency solid-liquid separator and a high-efficiency integrated mud-water separation device, which are also provided with a reaction zone, a separation zone and a sludge concentration zone, and have the capacity of treating high-concentration suspended matters and common-concentration wastewater, but the separation zones of the reaction zone, the separation zone and the sludge concentration zone need to be filtered by a filter screen to achieve the effect of solid-liquid separation in the separation zones. The disadvantage of this approach is that the screen is prone to clogging, requiring the placement of a flushing system; meanwhile, due to the fact that the filter screen is intercepted, muddy water particles are gathered near the filter screen, and water outlet can be affected due to the fact that the muddy water particles are not washed timely.
In addition, the existing filter screen has small interception effect on tiny particles in a granulation area, so that the turbidity of effluent is higher, the effluent effect is not good, and the solid-liquid separation efficiency is not favorably improved.
Disclosure of Invention
Not enough to prior art exists, the utility model aims to provide a single motor circulating granulation fluidized bed coupling filters solid-liquid separation equipment, solve among the prior art tiny granule that the fluidized bed bottom can not further be got rid of in the disengagement zone, lead to going out the high and two complicated unsafe problems of stirring of water turbidity.
In order to solve the technical problem, the utility model discloses a following technical scheme realizes:
a single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation device comprises a fluidized bed main body device, wherein a stirring device is arranged in an inner cylinder of the fluidized bed main body device, the top end of a stirring shaft of the stirring device extends out of the top end of the inner cylinder, penetrates through a separation area and a water collection area of the fluidized bed main body device and extends out of the top end of a tank body of the fluidized bed main body device, and the stirring shaft is driven to rotate by a stirring driving motor arranged at the top end of the tank body;
a stirring shaft in a granulation fluidization area in the inner cylinder is provided with stirring blades;
the bottom of the middle cylinder of the fluidized bed main body device is fixedly provided with a water distribution device, and the water distribution device is used as a rotating supporting seat of the stirring shaft to rotatably install the stirring shaft in the water distribution device;
a sludge scraping plate arranged on the inner side of the bottom of the tank body is arranged in a sludge concentration area of the fluidized bed main body device, and the bottom end of the stirring shaft penetrates through the water distribution device and the bottom of a water inlet pipe of the fluidized bed main body device and is connected with the sludge scraping plate;
a separation area of the fluidized bed main body device is internally provided with a suspension layer filtering solid-liquid separation device;
the suspension layer filtering solid-liquid separation device is divided into an upper part and a lower part, wherein the upper part is a static suspension layer, the lower part is a stirring suspension layer, an isolation screen is arranged above the static suspension layer, and the edge of the isolation screen is fixedly arranged on the inner wall of the tank body of the separation zone;
the static suspension layer and the stirring suspension layer are filled with floating light suspension beads, a stirring shaft connecting sleeve fixedly sleeved on the stirring shaft is arranged in the stirring suspension layer, the bottom end of the stirring shaft connecting sleeve is fixedly provided with a cross-shaped support frame, and a plurality of filter layer stirring blades positioned in the stirring suspension layer are uniformly and fixedly distributed on the cross-shaped support frame along the axial direction;
and a single stirring driving motor simultaneously drives the filter layer stirring blade, the stirring blade and the mud scraper to rotate together through the stirring shaft.
The utility model discloses still have following technical characteristic:
a sliding seal sleeve is arranged between the bottom of the water inlet pipe and the stirring shaft.
The light suspension beads are foamed plastic beads with density smaller than water density.
The fluidized bed main body device comprises a base frame, wherein a tank body is fixedly arranged on the base frame, and the tank body sequentially comprises a sludge concentration area, a circulating granulation area, a separation area and a water collection area from the bottom to the top;
the circulating granulation area is internally provided with a middle cylinder and an inner cylinder, the tank body, the middle cylinder and the inner cylinder are coaxially arranged from outside to inside in sequence, the inner cylinder is internally provided with a granulation fluidization area, a reflux area is arranged between the inner cylinder and the middle cylinder, and a sludge settling area is arranged between the middle cylinder and the tank body;
the top ends of the middle cylinder and the inner cylinder are open, and the top end of the middle cylinder is higher than the top end of the inner cylinder to form a backflow water inlet;
the bottom end of the inner cylinder is open, and the bottom end of the middle cylinder is contracted inwards at a position close to the bottom end of the inner cylinder, so that a backflow water outlet slit is formed between the bottom end of the inner cylinder and the contracted inner wall of the middle cylinder and is used for forming local negative pressure and providing backflow power;
the bottom of the contracting inner wall of the middle cylinder is provided with a mixing area with an open top end and a closed bottom end, the backflow water outlet slit is communicated with the top end of the mixing area, the bottom end of the mixing area is communicated with the water inlet pipe, and the water inlet pipe penetrates through the side wall of the tank body and extends out of the tank body.
And a water distribution device is fixedly arranged in the mixing area.
The inner diameter of the mixing area is smaller than that of the inner cylinder, and the bottom of the tank body and the bottom of the mixing area are both set to be a conical hopper bottom.
The water inlet pipe is provided with a water inlet concentration meter.
The outer wall of the tank body is provided with a sludge discharge pipe communicated with a sludge concentration area in the tank body.
And a water outlet pipe is arranged on the tank body top cover at the top of the water collecting area.
Compared with the prior art, the utility model, following technological effect has:
the suspension layer filtering solid-liquid separation device in the utility model can effectively intercept the micro particles which can not be removed at the bottom of the fluidized bed, so that the water turbidity and suspended matters in the separation zone are obviously reduced; the utility model discloses utilize the suspension layer granule that has formed inside the fluidized bed inner tube to carry out cyclic utilization between inner tube and well section of thick bamboo, constantly have the suspended solid to supply in making the inner tube, guaranteed the growth and the update on suspension layer in the inner tube, solved the problem that low turbid water suspended solid supplied not enough, suspension layer granule can't grow.
(II) the utility model discloses a agitating unit is changed into single motor stirring by bi-motor stirring in the past, has removed the bottom and has scraped the mud motor, and the same top motor is used to mud scraper and agitating unit, has reduced the whole height of equipment, has reduced the equipment fixing height. Meanwhile, the problem of water leakage of a bottom motor is avoided, the workload of equipment installation and later maintenance is reduced, the operation is simpler and more convenient, and the manufacturing cost is reduced.
(III) the utility model discloses a suspension layer filters solid-liquid separation equipment can effectively hold back the unable small particle who gets rid of in fluidized bed bottom, makes the turbidity of going out water and suspended solid obviously reduce, and the treatment effect is showing more. The utility model discloses utilized the high density performance of the granule that rises to the disengagement zone ground by bottom granulation district well. The fine particles in the raw water gradually form a spherical body with larger effective density through the agglomeration and flocculation process in the granulation area. Bigger spheroid granule directly turns into the sludge concentration district behind the inner tube, and the tiny particle that the bottom can't get rid of then gets into suspension layer filtration separation district, through stirring suspension layer, tiny particle can be held back by intensive suspension layer. If particles which are not intercepted exist, the particles can be intercepted when the particles ascend and pass through the static suspension layer, and the static suspension layer ensures a certain safety height. Through holding back to little granule, static suspension layer density increases and can drop to the stirring part, because the stirring effect, the granule surface mud that drops can drop to the bottom, and suspended material can continue to rise to top suspension layer because density diminishes, guarantees that suspension layer can have certain suspension height always. The suspension layer can continuously realize the interception of small particles through the processes of continuous filtration, density increase, mud surface falling and density reduction.
(IV) the utility model has good treatment effect on various water qualities. When water with high organic particle content is treated and the suspended matter density is low, the device mainly operates by sand-adding circulating granulation, and micro sand is added to provide high-density nuclei for suspended layer particles so as to generate high-density particles; and the micro-sand is recycled by the reinforced stirring and separating action of the particle circulating slit and the side wall of the mud-water separator; when water with high content of soluble organic matters is treated, the device mainly operates by powder carbon circulation granulation, and the particle density of a suspension layer is improved by adding powder carbon with relatively high density; and the powder carbon is recycled by the reinforced stirring and separating action of the particle circulating slit and the side wall of the mud-water separator.
Drawings
FIG. 1 is a schematic structural diagram of a single-motor circulating granulation fluidized bed coupled filtration solid-liquid separation device.
Fig. 2 is a schematic view of a-a cross-sectional structure in fig. 1.
FIG. 3 is a top sectional view of the suspension layer filtration solid-liquid separation apparatus.
The meaning of the individual reference symbols in the figures is: 1-a base frame, 2-a tank body, 3-a sludge concentration zone, 4-a circulating granulation zone, 5-a separation zone, 6-a water collection zone, 7-a middle cylinder, 8-an inner cylinder, 9-a granulation fluidization zone, 10-a backflow zone, 11-a sludge settling zone, 12-a backflow water inlet, 13-a contraction inner wall, 14-a backflow water outlet slit, 15-a mixing zone, 16-a water inlet pipe, 17-a water outlet pipe, 18-a stirring device, 19-a stirring shaft, 20-a stirring driving motor, 21-a mud scraping plate and 22-a suspension layer filtration solid-liquid separation device; 23-stirring blades, 24-water distribution device, 25-sliding sealing sleeve, 26-water inlet concentration meter and 27-sludge discharge pipe;
2201-static suspension layer, 2202-stirring suspension layer, 2203-isolation screen, 2204-light suspension beads, 2205-stirring shaft connecting sleeve, 2206-cross supporting frame and 2207-filtering layer stirring blade.
The following examples are provided to explain the present invention in further detail.
Detailed Description
It should be noted that all the components and devices of the present invention, unless otherwise specified, are all the components known in the art.
The following embodiments of the present invention are given, and it should be noted that the present invention is not limited to the following embodiments, and all the equivalent transformations made on the basis of the technical solution of the present application all fall into the protection scope of the present invention.
Example 1:
the embodiment provides a single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation device, which comprises a fluidized bed main body device, wherein a stirring device 18 is arranged in an inner cylinder 8 of the fluidized bed main body device, the top end of a stirring shaft 19 of the stirring device 18 extends out of the top end of the inner cylinder 8, penetrates through a separation region 5 and a water collection region 6 of the fluidized bed main body device, extends out of the top end of a tank body 2 of the fluidized bed main body device, and the stirring shaft 19 is driven to rotate by a stirring driving motor 20 arranged at the top end of the tank body 2;
a stirring shaft 19 in a granulation fluidization area 9 in the inner cylinder 8 is provided with a stirring blade 23;
the bottom of the middle cylinder 7 of the fluidized bed main body device is fixedly provided with a water distribution device 24, and the water distribution device 24 is used as a rotary supporting seat of the stirring shaft 19 to rotatably install the stirring shaft 19 in the water distribution device 24;
a mud scraping plate 21 arranged on the inner side of the bottom of the tank body 2 is arranged in the sludge concentration area 3 of the fluidized bed main body device, and the bottom end of the stirring shaft 19 passes through the water distribution device 24 and the bottom of the water inlet pipe 16 of the fluidized bed main body device and is connected with the mud scraping plate 21;
a separation area 5 of the fluidized bed main body device is internally provided with a suspension layer filtering solid-liquid separation device 22;
the suspension layer filtering solid-liquid separation device 22 is divided into an upper part and a lower part, wherein the upper part is a static suspension layer 2201, the lower part is a stirring suspension layer 2202, an isolation screen 2203 is arranged above the static suspension layer 2201, and the edge of the isolation screen 2203 is fixedly arranged on the inner wall of the tank body 2 of the separation zone 5;
floating light suspension beads 2204 are filled in the static suspension layer 2201 and the stirring suspension layer 2202, a stirring shaft connecting sleeve 2205 fixedly sleeved on the stirring shaft 19 is arranged in the stirring suspension layer 2202, a cross support frame 2206 is fixedly arranged at the bottom end of the stirring shaft connecting sleeve 2205, and a plurality of filter layer stirring blades 2207 positioned in the stirring suspension layer 2202 are uniformly and fixedly distributed on the cross support frame 2206 along the axial direction;
the single stirring drive motor 20 simultaneously rotates the filter layer stirring vanes 2207, the stirring vanes 23 and the mud scraper 21 together via the stirring shaft 19.
In a preferred embodiment of the present invention, the height of the can body 2 is about 6m, and the diameter thereof is not more than 4 m.
In this embodiment, the stirring blades 23 are installed at a certain distance from each other, the uppermost stirring blade 23 does not exceed the top end of the inner cylinder 8, and the lowermost stirring blade 23 is just arranged at the position of the particle circulation slit 14, so as to enhance the side wall effect and the effect of separating mud from water.
In this embodiment, the water distribution device 24 may be a conventional water distribution device known in the art.
As a preferable scheme of this embodiment, a sliding sealing sleeve 25 is arranged between the bottom of the water inlet pipe 16 and the stirring shaft 19. Water leakage from the inlet pipe 16 is avoided.
As a preferable mode of this embodiment, the light suspension beads 2204 are foamed plastic beads having a density lower than the density of water.
Specifically, the fluidized bed main body device comprises a base frame 1, a tank body 2 is fixedly arranged on the base frame 1, and the tank body 2 sequentially comprises a sludge concentration zone 3, a circulating granulation zone 4, a separation zone 5 and a water collection zone 6 from bottom to top;
a middle cylinder 7 and an inner cylinder 8 are arranged in the circulating granulation area 4, the tank body 2, the middle cylinder 7 and the inner cylinder 8 are coaxially arranged from outside to inside in sequence, a granulation fluidization area 9 is arranged in the inner cylinder 8, a reflux area 10 is arranged between the inner cylinder 8 and the middle cylinder 7, and a sludge settling area 11 is arranged between the middle cylinder 7 and the tank body 2;
the top ends of the middle cylinder 7 and the inner cylinder 8 are open, and the top end of the middle cylinder 7 is higher than the top end of the inner cylinder 8 to form a backflow water inlet 12;
the bottom end of the inner cylinder 8 is opened, and the bottom end of the middle cylinder 7 is contracted inwards at a position close to the bottom end of the inner cylinder 8, so that a backflow water outlet slit 14 is formed between the bottom end of the inner cylinder 8 and a contracted inner wall 13 of the middle cylinder 7 and is used for forming local negative pressure and providing backflow power;
the bottom end of the contraction inner wall 13 of the middle cylinder 7 is provided with a mixing area 15 with an open top end and a closed bottom end, the backflow water outlet slit 14 is communicated with the top end of the mixing area 15, the bottom end of the mixing area 15 is communicated with a water inlet pipe 16, and the water inlet pipe 16 penetrates through the side wall of the tank body 2 and extends out of the tank body 2.
In this embodiment, the middle cylinder 7 and the inner cylinder 8 can be fixed on the inner wall of the tank body 2 through a connecting ring or a rib. The top end of the middle cylinder 7 is away from the top end of the inner cylinder 8 and has a certain adjustable height, and the middle cylinder 7 is away from the bottom end of the separation area 5 and has a certain adjustable height.
In this embodiment, the sludge particles in the granulation fluidization region 9 in the inner cylinder 8 reach dynamic balance under the action of the inflow water flow power and the self gravity, and part of the formed sludge particles rise to the top of the inner cylinder 8 along with the water flow and circularly flow back to the circulating granulation region 4 before reaching the top of the middle cylinder 7.
Preferably, a water distribution device 24 is fixedly arranged in the mixing area 15,
preferably, the inner diameter of the mixing area 15 is smaller than that of the inner cylinder 8, and the bottom of the tank body 2 and the bottom of the mixing area 15 are both provided with conical hopper bottoms.
Preferably, the inlet pipe 16 is provided with an inlet concentration meter 26.
Preferably, a sludge discharge pipe 27 communicated with the sludge concentration area 3 in the tank body 2 is arranged on the outer wall of the tank body 2. In this embodiment, after the sludge particles in the inner cylinder 8 and the middle cylinder 7 reach the dynamic balance, a part of the sludge particles fall into the sludge settling area 11, and when the sludge in the sludge settling area 11 is accumulated to a certain height, the sludge is discharged through the sludge discharge pipe 27.
Preferably, a water outlet pipe 17 is arranged on the top cover of the tank body 2 at the top of the water collecting area 6.
The utility model discloses an equipment is when using, and medicaments such as little sand and/or powder carbon can be added as required in the former aquatic, and the former water advances to jar body 2 through inlet tube 16 to in the granulation fluidization district 9 of circulation granulation district 4, constantly rising under stirring vane 23's stirring, the granule grow gradually, and the granule turns over when reacing inner tube 8 top, gets into in the intermediate layer backward flow district 10 between inner tube 8 and the middle tube 7.
When muddy water circularly flows back to the backflow water outlet slit 14, negative pressure is formed locally, and due to the side wall reinforced stirring effect, the micro sand and/or the powdered carbon are separated from the sludge core body, so that the micro sand and/or the powdered carbon can be recycled. The micro sand and the sludge particles flow back to the granulation fluidization area 9 in the inner cylinder 8 again, the circulation is carried out until the height of the suspension layer reaches the top end of the middle cylinder 7, the large particles fall down, and the micro sand and the sludge particles enter the sludge concentration area 3 from the sludge settling area 11 until the micro sand and the sludge particles settle to the bottom end of the tank body 2.
Small amounts of fine particles continue to rise with the water flow to the separation zone 5. The particles enter the suspension layer filtration solid-liquid separation device 22 of the separation zone 5, sequentially pass through the agitation suspension layer 2204 and the static suspension layer 2203 along with water, and are stirred by the filter layer stirring blades in the agitation suspension layer 2204, so that the small particles can be intercepted by the light suspension beads 2204 in the dense agitation suspension layer 2204. If there are particles that are not trapped, the particles will be trapped by the lightweight suspension beads 2204 in the static suspension layer 2203 when rising through the static suspension layer 2203, and the static suspension layer 2203 ensures a certain safety height. By trapping small particles, the density increase of the lightweight suspended beads 2204 in the static suspended layer 2203 drops to the agitation suspended layer 2204, and due to the stirring action, the mud on the surface of the dropped lightweight suspended beads 2204 drops to the bottom and automatically drops to the sludge concentration zone 3 due to the action of gravity.
The clean water is discharged from the water collecting area 6 through the water outlet pipe 17.
In the whole process, the single stirring driving motor 20 simultaneously drives the filter layer stirring vanes 2207, the stirring vanes 23 and the mud scraping plate 21 to rotate together through the stirring shaft 19.
Claims (9)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022252925.9U CN213803067U (en) | 2020-10-13 | 2020-10-13 | Single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022252925.9U CN213803067U (en) | 2020-10-13 | 2020-10-13 | Single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213803067U true CN213803067U (en) | 2021-07-27 |
Family
ID=76957717
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022252925.9U Active CN213803067U (en) | 2020-10-13 | 2020-10-13 | Single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213803067U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112239257A (en) * | 2020-10-13 | 2021-01-19 | 西安建筑科技大学 | Single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation equipment |
-
2020
- 2020-10-13 CN CN202022252925.9U patent/CN213803067U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112239257A (en) * | 2020-10-13 | 2021-01-19 | 西安建筑科技大学 | Single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation equipment |
| CN112239257B (en) * | 2020-10-13 | 2024-04-26 | 西安建筑科技大学 | A single motor circulating granulation fluidized bed coupled filtration solid-liquid separation equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN112239257A (en) | Single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation equipment | |
| CN208327492U (en) | A kind of circulation of high efficient solid and liquid separation is granulating fluidized bed | |
| CN108467096B (en) | A circulating granulation fluidized bed equipment for low-temperature, low-turbidity, high-turbidity or high-algae water treatment | |
| RU204652U1 (en) | DEVICE FOR SEPARATING DISPERSIONS | |
| CN101585570A (en) | Integrative water purification device for high and low muddy water | |
| CN116715329A (en) | Water treatment equipment of small-water-quantity multi-cylinder circulating agglomeration granulation fluidized bed | |
| CN112239256B (en) | High-speed solid-liquid separation equipment of high-flow circulating granulation fluidized bed | |
| CN112239258B (en) | Peripheral transmission type high-speed solid-liquid separation equipment of large-flow circulating granulation fluidized bed | |
| CN105858735B (en) | A kind of vertical vortex idetified separation device and separation of solid and liquid it is granulating fluidized bed | |
| EP1494525B1 (en) | Method for the purification of wastewater in fish farming | |
| CN213803067U (en) | Single-motor circulating granulation fluidized bed coupling filtering solid-liquid separation equipment | |
| CN213803070U (en) | High-speed solid-liquid separation equipment of large-flow circulating granulation fluidized bed | |
| CN205709927U (en) | A kind of vertical eddy current idetified separation device and high efficient solid and liquid separation granulating fluidized bed | |
| KR102421273B1 (en) | Sedimentation tank for increasing separation efficiency of suspended solids | |
| CN204550258U (en) | A kind of waste disposal plant | |
| CN213803069U (en) | Peripheral transmission type high-speed solid-liquid separation equipment for large-flow circulating granulation fluidized bed | |
| CN112794570B (en) | A kind of treatment method aiming at white peony traditional Chinese medicine production wastewater | |
| CN116803919A (en) | Small water amount closed integrated circulating agglomeration granulation fluid bed water treatment equipment | |
| CN218345192U (en) | Water treatment equipment for coupling light suspended filler filtration of circulating granulation fluidized bed | |
| CN105999776A (en) | Sludge layer filtering and settling pond and method thereof | |
| CN110204103B (en) | Suspension medium layer filtering system based on hydraulic fluidization layering | |
| CN107149798A (en) | Efficient hydrodynamic clarifies clarifier | |
| CN211004716U (en) | Sewage treatment system | |
| CN215712533U (en) | Fold spiral shell hydroextractor with swash plate deposits function | |
| CN116693014B (en) | A large-volume open integrated circulating agglomeration and granulation fluidized bed water treatment equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |