CN217188038U - Gravity flow folded plate flocculation and precipitation device - Google Patents
Gravity flow folded plate flocculation and precipitation device Download PDFInfo
- Publication number
- CN217188038U CN217188038U CN202220078168.4U CN202220078168U CN217188038U CN 217188038 U CN217188038 U CN 217188038U CN 202220078168 U CN202220078168 U CN 202220078168U CN 217188038 U CN217188038 U CN 217188038U
- Authority
- CN
- China
- Prior art keywords
- flocculation
- tank
- folded plate
- discharge pipe
- gravity flow
- 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.)
- Expired - Fee Related
Links
- 238000005189 flocculation Methods 0.000 title claims abstract description 85
- 230000016615 flocculation Effects 0.000 title claims abstract description 84
- 230000005484 gravity Effects 0.000 title claims abstract description 21
- 238000001556 precipitation Methods 0.000 title claims abstract description 8
- 239000010802 sludge Substances 0.000 claims abstract description 16
- 238000004062 sedimentation Methods 0.000 claims abstract description 14
- 229920003023 plastic Polymers 0.000 claims abstract description 8
- 239000004033 plastic Substances 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 34
- 239000010865 sewage Substances 0.000 abstract description 8
- 238000011282 treatment Methods 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 3
- 239000002245 particle Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 8
- 230000009471 action Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 3
- 230000003311 flocculating effect Effects 0.000 description 3
- 230000005012 migration Effects 0.000 description 3
- 238000013508 migration Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000005653 Brownian motion process Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000005537 brownian motion Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000011221 initial treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a gravity flow folded plate flocculation and precipitation device belongs to sewage treatment technical field. A gravity flow folded plate flocculation sedimentation device comprises a flocculation tank and a sludge tank, wherein the flocculation tank is of a flat spiral structure and comprises a tank wall and a tank bottom, the tank wall and the tank bottom are of a concrete structure, the sludge tank is arranged at the bottom of the tank wall of the flocculation tank, and the sludge tank is connected with the flocculation tank through a discharge pipe; the discharge pipe is made of plastic, and a discharge port of the discharge pipe is vertically arranged with the bottom of the sludge tank; one end of the discharge pipe is connected with a sewage discharge port of the flocculation tank, and a valve is arranged between the discharge pipe and the sewage discharge port and is made of plastic materials; the utility model provides a folded plate flocculation basin treatment effeciency among the prior art low down and area big problem.
Description
Technical Field
The utility model relates to a sewage treatment technical field specifically is a folded plate flocculation and precipitation device is flowed to gravity.
Background
The folded plate flocculation sedimentation tank is also called as a folded plate flocculation tank, is an important link in an urban sewage treatment system, and urban sewage subjected to primary treatment becomes reclaimed water meeting the discharge standard; the reclaimed water is precipitated by a horizontal sedimentation tank, substances with heavier specific gravity are precipitated and removed, the materials are filtered by a V-shaped filter tank, large-particle impurities contained in the reclaimed water are filtered, the filtered reclaimed water enters a folded plate flocculation tank, the reclaimed water enters the folded plate flocculation tank, floccules contained in the reclaimed water are further precipitated and removed, and then the reclaimed water is disinfected and sterilized to form water which can be used in most industries; in order to increase the sedimentation of the floccules, a folded plate is often required to be placed in the folded plate flocculation tank, and the folded plate is kept to form a certain included angle with the water flow direction so as to enable the floccules to collide with the water flow direction for sedimentation.
The folded plates in the prior art usually rely on self water heads to carry out water treatment, so that the water treatment efficiency is low, the occupied area is large, the space utilization rate is low, and the folded plate sedimentation efficiency is low; therefore, the utility model provides a gravity flow folded plate flocculation and precipitation device to solve the above problems.
SUMMERY OF THE UTILITY MODEL
1. The to-be-solved technical problem of the utility model
An object of the utility model is to provide a folded plate flocculation and precipitation device is flowed to gravity to solve the problem that proposes in the above-mentioned background art:
(1) the folded plate flocculation tank in the prior art has low treatment efficiency and large occupied area.
2. Technical scheme
In order to achieve the above object, the utility model provides a following technical scheme:
the utility model provides a gravity flow folded plate flocculation and precipitation device, includes flocculation basin and sludge impoundment, the flocculation basin is flat heliciform structure, the flocculation basin includes pool wall and bottom of the pool, pool wall and bottom of the pool are concrete structure, the sludge impoundment sets up in the pool wall bottom in the flocculation basin, sludge impoundment and flocculation basin pass through discharge pipe connection.
Preferably, the discharge pipe is made of plastic, and a discharge port of the discharge pipe is perpendicular to the bottom of the sludge tank.
Preferably, discharge pipe one end is connected with the drain of flocculation basin, be provided with the valve between discharge pipe and the drain, the valve is the plastics material.
Preferably, the inside central authorities of flocculation basin are fixed and are provided with multiunit folded plate, the folded plate is parallel folded plate or buckled plate, and is adjacent end to end between the folded plate.
Preferably, both ends in the flocculation tank are provided with bearing columns, and the bearing columns are fixedly connected with the inner side threads of each layer of the flocculation tank.
Preferably, the upper end and the lower end of the flocculation tank are respectively provided with a water inlet and a water outlet, and the outer edge of the flocculation tank is fixedly connected with a baffle.
3. Advantageous effects
(1) The utility model discloses a continuous scaling of folded plate unit makes rivers form the vortex of a large amount of different yards, has promoted the relative motion between the inside flocculating constituent particle of rivers, has increased the collision chance, so for baffle flocculation basin, the flocculation effect improves greatly.
(2) The utility model discloses can flow through gravity and reach the effect of flocculation with higher speed, reduce the area in flocculation basin simultaneously.
(3) The utility model discloses rivers can be through the gravity flood peak of self collision with higher speed when using to better reach the flocculation effect.
Drawings
Fig. 1 is a schematic structural view of the present invention;
fig. 2 is a top view of the flocculation tank of the utility model.
The reference numbers in the figures illustrate:
1. a water inlet; 2. folding the plate; 3. a load-bearing column; 4. a baffle plate; 5. a water outlet; 6. a flocculation tank.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Example 1:
referring to fig. 1-2, a gravity flow folded plate flocculation and sedimentation device comprises a flocculation tank 6 and a sludge tank, wherein the flocculation tank 6 is of a flat spiral structure, the flocculation tank 6 comprises a tank wall and a tank bottom, the tank wall and the tank bottom are of a concrete structure, the sludge tank is arranged at the bottom of the tank wall of the flocculation tank 6, and the sludge tank is connected with the flocculation tank 6 through a discharge pipe;
the discharge pipe is made of plastic, and a discharge port of the discharge pipe is vertically arranged with the bottom of the sludge tank;
one end of the discharge pipe is connected with a sewage discharge port of the flocculation tank 6, and a valve is arranged between the discharge pipe and the sewage discharge port and is made of plastic;
a plurality of groups of folded plates 2 are fixedly arranged in the center of the flocculation tank 6, the folded plates 2 are parallel folded plates or corrugated plates, and adjacent folded plates 2 are connected end to end;
both ends in the flocculation tank 6 are provided with bearing columns 3, and the bearing columns 3 are fixedly connected with the inner side threads of each layer of flocculation tank 6;
the upper end and the lower end of the flocculation tank 6 are respectively provided with a water inlet 1 and a water outlet 5, and the outer edge of the flocculation tank 6 is fixedly connected with a baffle 4;
when the utility model is used, water flow enters the flocculation tank 6 from the water inlet 1 and then flows downwards along the spiral flocculation tank 6 under the action of gravity, the folded plate 2 arranged in the flocculation tank can make the water flow generate effective collision for many times, and finally the flocculation process is smoothly finished and the water is discharged from the water outlet 5, so that the quality of the discharged water is improved;
the spiral flat flocculation tank 6 not only improves the space utilization rate, but also can accelerate the impact of water flow and the folded plate 2 by the circulation tank body under the action of gravity flow and the action of gravity, so that floccules are quickly flocculated, and the formation of a flocculating body can be accelerated when the water flow passes through a bend;
the folded plate flocculation tank is constructed by placing a certain number of parallel folded plates or corrugated plates in the tank, mainly using the wall-attached turbulent energy consumption mode generated by boundary layer separation caused by the scaling or turning of the folded plates 2, and keeping the input of trace and enough energy in the flocculation tank 6 along the way, thereby effectively improving the utilization rate of input energy and the volume utilization rate of coagulation equipment, increasing the relative movement of liquid flow, shortening the flocculation time and improving the sedimentation performance of a flocculating constituent;
the mathematical description of flocculation is generally divided into two separate processes: migration and adhesion; the migration process produces particle collisions, and the migration is caused by the velocity difference of particles in water, which in a folded plate flocculation basin is believed to be caused by: (1) the method comprises the following steps of (1) carrying out Brownian motion of particles (playing a main role in anisotropic flocculation), (2) carrying out turbulent vortex (cocurrent flocculation), (3) carrying out differential flocculation on the sedimentation velocity difference among the particles, wherein the adhesion depends on instantaneous acting force related to the surface property of the particles, the impact of the hydraulic property of a folded plate unit on floc particle collision is mainly shown in that the vortex-making effect of the folded plate unit and the continuous and uniform unit arrangement improve the distribution of turbulent energy consumption, so that the numerical value of a flocculation mode is improved, the flocculation effect is improved, water flow passes through the folded plate unit and can form symmetrical vortex and unilateral vortex under the action of a gradually expanding section and a gradually reducing section, the separation of a water flow boundary layer at a wave crest is a kinetic factor generating vortex, the separation is further decomposed into small-scale vortex according to the diffusivity of the vortex until the Reynolds number related to water flow micro-groups is low so that smaller vortex can not be generated any more, the large-scale vortex absorbs kinetic energy from the main flow and transfers the kinetic energy to the smaller-scale vortex in the movement process, and the kinetic energy is transferred step by step until the large-scale vortex reaches the micro-scale vortex; in larger scale vortex motion, the fluid viscosity is almost ineffective and negligible, and thus there is almost no energy consumption in the kinetic energy transfer;
in the micro-scale vortex motion, fluid viscosity plays a main role, energy transmitted to the lowest-level vortices is converted into heat energy through viscosity, countless large and small vortices exist in water flow at the same time, a series of pulse frequencies are generated, and a continuous frequency spectrum is formed; because the actual change range of the floc particle size is 1-1000um, a large section of vortex plays a role, and the limit of the large vortex and the small vortex cannot be strictly divided; the diffusion effect of the turbulence mainly depends on the turbulence with large scale, and the scale of the large vortex can be considered to be the same as the scale magnitude of the folded plate unit; the continuous scaling of folded plate unit makes rivers form the vortex of a large amount of different yards, has promoted the relative motion between the inside floc granule of rivers, has increased the collision chance, so for baffle flocculation basin, the flocculation effect improves greatly.
The above description is only the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art can substitute or change the technical solution and the improvement concept of the present invention within the technical scope disclosed in the present invention.
Claims (6)
1. The utility model provides a gravity flow folded plate flocculation and precipitation device, includes flocculation basin (6) and sludge impoundment, its characterized in that: the flocculation tank (6) is of a flat spiral structure, the flocculation tank (6) comprises a tank wall and a tank bottom, the tank wall and the tank bottom are of a concrete structure, the sludge tank is arranged at the bottom of the tank wall of the flocculation tank (6), and the sludge tank is connected with the flocculation tank (6) through a discharge pipe.
2. The gravity flow folded plate flocculation and sedimentation device of claim 1, wherein: the discharge pipe is made of plastic, and a discharge port of the discharge pipe is perpendicular to the bottom of the sludge tank.
3. A gravity flow folded plate flocculation and sedimentation device according to claim 2, wherein: one end of the discharge pipe is connected with a drain outlet of the flocculation tank (6), a valve is arranged between the discharge pipe and the drain outlet, and the valve is made of plastic.
4. A gravity flow folded plate flocculation and sedimentation device according to claim 3, wherein: the inside central authorities of flocculation basin (6) are fixed and are provided with multiunit folded plate (2), folded plate (2) are parallel folded plate or buckled plate, and are adjacent end to end between folded plate (2).
5. The gravity flow folded plate flocculation and sedimentation device of claim 4, wherein: the inner two ends of the flocculation tank (6) are provided with bearing columns (3), and the bearing columns (3) are fixedly connected with the inner side threads of each layer of flocculation tank (6).
6. The gravity flow folded plate flocculation and sedimentation device of claim 5, wherein: the flocculation basin is characterized in that a water inlet (1) and a water outlet (5) are respectively formed in the upper end and the lower end of the flocculation basin (6), and a baffle (4) is fixedly connected to the outer edge of the flocculation basin (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220078168.4U CN217188038U (en) | 2022-01-12 | 2022-01-12 | Gravity flow folded plate flocculation and precipitation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220078168.4U CN217188038U (en) | 2022-01-12 | 2022-01-12 | Gravity flow folded plate flocculation and precipitation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217188038U true CN217188038U (en) | 2022-08-16 |
Family
ID=82789994
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220078168.4U Expired - Fee Related CN217188038U (en) | 2022-01-12 | 2022-01-12 | Gravity flow folded plate flocculation and precipitation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217188038U (en) |
-
2022
- 2022-01-12 CN CN202220078168.4U patent/CN217188038U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107720959B (en) | Gas-liquid-solid three-phase separator | |
| CN201719868U (en) | Retention pond for sewage treatment | |
| CN108328786B (en) | Water treatment device and water treatment method | |
| CN109851089B (en) | Oil-gas field operation waste liquid treatment method and device | |
| CN217188038U (en) | Gravity flow folded plate flocculation and precipitation device | |
| CN207361975U (en) | A kind of sanitary sewage multi-stage treatment units | |
| CN107244724A (en) | A kind of small-sized coagulative precipitation tank and method suitable for decentralized wastewater draining characteristics | |
| CN210340446U (en) | Coagulating sedimentation device | |
| CN209835714U (en) | Coarse granulating device for oily sewage treatment | |
| CN207227067U (en) | A kind of new oily-water seperating equipment | |
| CN213141508U (en) | Novel high-efficient sedimentation tank of little sand | |
| CN210505856U (en) | Treatment device for production wastewater of water works | |
| CN109607656B (en) | Air floatation reactor | |
| CN207031054U (en) | A kind of small-sized coagulative precipitation tank suitable for decentralized wastewater draining characteristics | |
| CN207227070U (en) | Device for water-oil separating | |
| CN209428279U (en) | A kind of compact-sized sewage disposal device | |
| CN212651397U (en) | Three-dimensional inclined plate purification device and sedimentation tank with same | |
| CN106892494B (en) | Variable-speed multi-flow clarifier | |
| CN108144330B (en) | Three-dimensional inclined plate purification device and sedimentation tank with same | |
| CN216303367U (en) | Grid folded plate combined pool | |
| CN219341819U (en) | Baffling multi-point step release air floatation separation device | |
| CN213077581U (en) | Sewage treatment deposits device | |
| CN220413006U (en) | Integrated filler flocculation reaction sedimentation tank | |
| CN213141781U (en) | Sludge treatment device | |
| CN216639102U (en) | Self-balancing suspension sludge high-speed sedimentation tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20220816 |