CN221588325U - Coagulating sedimentation filters all-in-one - Google Patents
Coagulating sedimentation filters all-in-one Download PDFInfo
- Publication number
- CN221588325U CN221588325U CN202420049558.8U CN202420049558U CN221588325U CN 221588325 U CN221588325 U CN 221588325U CN 202420049558 U CN202420049558 U CN 202420049558U CN 221588325 U CN221588325 U CN 221588325U
- Authority
- CN
- China
- Prior art keywords
- water
- pipeline
- pac
- speed sand
- pipe connection
- 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
- 238000004062 sedimentation Methods 0.000 title claims abstract description 21
- 230000001112 coagulating effect Effects 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 70
- 239000010865 sewage Substances 0.000 claims abstract description 28
- 239000004576 sand Substances 0.000 claims abstract description 25
- 238000005345 coagulation Methods 0.000 claims abstract description 19
- 230000015271 coagulation Effects 0.000 claims abstract description 19
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 18
- 238000001914 filtration Methods 0.000 claims abstract description 17
- 238000003756 stirring Methods 0.000 claims description 18
- 239000000701 coagulant Substances 0.000 claims description 11
- 239000012535 impurity Substances 0.000 abstract description 25
- 230000000694 effects Effects 0.000 abstract description 8
- 239000008399 tap water Substances 0.000 abstract description 3
- 235000020679 tap water Nutrition 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 10
- 239000002245 particle Substances 0.000 description 7
- 230000003311 flocculating effect Effects 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 238000001179 sorption measurement Methods 0.000 description 4
- 238000005189 flocculation Methods 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000053 physical method Methods 0.000 description 2
- 229920002401 polyacrylamide Polymers 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 229940037003 alum Drugs 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Physical Water Treatments (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a coagulating sedimentation filtration integrated machine, which belongs to the technical field of water treatment and comprises a circulating water tank, wherein the circulating water tank is connected with a sewage lifting pump through a pipeline, the sewage lifting pump is connected with a coagulator through a pipeline, the coagulator is connected with a high-speed sand cylinder filter through a pipeline, the high-speed sand cylinder filter is connected with an ultraviolet disinfection device through a pipeline, the ultraviolet disinfection device is connected with a recycling water tank through a pipeline, the high-speed sand cylinder filter is also connected with a PAC metering pump through a pipeline, the PAC metering pump is connected with a PAC solution tank through a pipeline, and the PAC solution tank is connected with tap water in a factory through a pipeline; can solve the problems that the impurity removing effect is poor and the water requirement cannot be met in the existing water treatment mode. The utility model can treat slightly complex water quality by integrating the coagulation sedimentation and the filtration, can improve the impurity removal effect and meets the requirement of water for the rear end.
Description
Technical Field
The utility model relates to the technical field of water treatment, in particular to a coagulating sedimentation and filtration integrated machine.
Background
The water treatment mode comprises physical treatment and chemical treatment, the physical method comprises the steps of utilizing various filter materials with different pore sizes, removing impurities in water by utilizing an adsorption or separation mode, wherein the important adsorption mode is adsorption by activated carbon, and the separation method is to pass water through the filter materials to ensure that the impurities with larger volume cannot pass through, so as to obtain cleaner water.
The physical method also comprises a precipitation method, namely, the impurities with smaller specific gravity float on the water surface to be fished out, or the impurities with larger specific gravity are precipitated below to obtain the water surface. The chemical method is to convert the impurities in the water into substances less harmful to human bodies by using various chemicals, or concentrate the impurities, and the chemical treatment method with the longest history can be calculated by adding alum into the water, and the impurities in the water are concentrated, and then the volume is enlarged, so that the impurities can be removed by using a filtering method.
The existing water treatment mode has poor impurity removal effect and can not meet the water consumption requirement.
Disclosure of utility model
The utility model aims to provide a coagulating sedimentation filtration integrated machine, which can treat slightly complex water quality, improve impurity removal effect, meet the requirement of water for the rear end and solve the problems in the prior art through coagulating sedimentation filtration integrated arrangement.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
the utility model provides a coagulating sedimentation filters all-in-one, includes the circulating water pond, the circulating water pond passes through the pipe connection sewage elevator pump, the sewage elevator pump passes through the pipe connection coagulating machine, the coagulating machine passes through the high-speed sand jar filter of pipe connection, the high-speed sand jar filter passes through the pipe connection ultraviolet disinfection device, ultraviolet disinfection device passes through the pipe connection retrieval and utilization pond, the high-speed sand jar filter still passes through the pipe connection PAC metering pump, the PAC metering pump passes through the pipe connection PAC solution case, the PAC solution case passes through the tap water of pipe connection factory.
Preferably, one side of the coagulator is provided with a dosing device for adding coagulant into the coagulator.
Preferably, the coagulation device is provided with a water inlet, and the water inlet is connected with a water outlet of the sewage lifting pump.
Preferably, a drain pipe is arranged on the high-speed sand cylinder filter, the drain pipe is communicated with the water inlet through a valve, and the high-speed sand cylinder filter and the dosing equipment are both arranged on the concrete foundation.
Preferably, the ultraviolet disinfection device is provided with a water outlet, and the water outlet is connected with a reuse water tank.
Preferably, the PAC solution tank is provided with a rotating motor, an output shaft of the rotating motor is connected with a stirring shaft, and stirring blades for stirring the PAC solution are arranged on the stirring shaft.
Compared with the prior art, the utility model has the following beneficial effects:
The sewage in the circulating water tank is lifted into the coagulator through the sewage lifting pump, the coagulant is added into the coagulator through the dosing equipment, the sewage and the coagulant can fully contact and react to generate large-particle flocculating impurities through the coagulator, the large-particle flocculating impurities enter the high-speed sand cylinder filter, the large-particle flocculating impurities contained in the sewage can be efficiently removed through the high-speed sand cylinder filter, and then the sewage is subjected to irradiation disinfection through the ultraviolet disinfection device, so that the water consumption requirement can be met, the water quality slightly complicated can be treated through the integrated setting of coagulation sedimentation and filtration, the impurity removal effect can be improved, and the water consumption requirement at the rear end is met.
Drawings
FIG. 1 is a schematic diagram of the workflow of the coagulation sedimentation filtration all-in-one machine of the present utility model;
FIG. 2 is an enlarged view of the utility model at A in FIG. 1;
FIG. 3 is a schematic diagram of the integrated coagulating sedimentation filtration process of the present utility model;
fig. 4 is a schematic plan view of the coagulation sedimentation filtration integrated treatment of the present utility model.
In the figure: 1. a circulating water tank; 2. a sewage lifting pump; 3. a high-speed sand cylinder filter; 31. a blow-down pipe; 4. an ultraviolet ray disinfection device; 41. a water outlet; 5. a recycling pool; 6. PAC metering pump; 7. PAC solution tank; 71. a rotating electric machine; 72. a stirring shaft; 73. stirring the leaves; 8. a concrete foundation; 9. a coagulation device; 91. a water inlet; 10. and a dosing device.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
In order to solve the technical problem that the existing water treatment method has poor impurity removal effect and cannot meet the water requirement, referring to fig. 1-4, the present embodiment provides the following technical scheme:
The utility model provides a coagulating sedimentation filters all-in-one, includes circulating water pond 1, and circulating water pond 1 passes through pipeline connection sewage elevator pump 2, and sewage elevator pump 2 passes through pipeline connection coagulating machine 9.
In the present embodiment, one side of the coagulator 9 is provided with a dosing device 10, the dosing device 10 being used to add coagulant into the coagulator 9.
The coagulant is added into the coagulation device 9 by the drug adding device 10, wherein the coagulant is pac+pam;
PAC is also called polyaluminium chloride, is also called polyaluminium chloride for short, is an inorganic high molecular water treatment agent and is easy to dissolve in water, and because the polyaluminium chloride has different numbers of hydroxyl groups in molecules, after the polyaluminium chloride is added into sewage, the polyaluminium chloride is continuously hydrolyzed under the PH condition of the sewage, and a series of physical and chemical processes such as condensation, adsorption, precipitation and the like are accompanied in the hydrolysis process, so that the purification purpose is achieved; PAM is also known as polyacrylamide, and can be classified into anionic, cationic and nonionic for use in the wastewater treatment industry.
In this embodiment, the coagulation device 9 is provided with a water inlet 91, and the water inlet 91 is connected with the water outlet of the sewage lifting pump 2.
The sewage in the circulating water tank 1 is lifted into the coagulation device 9 by the sewage lifting pump 2, the coagulant is added into the coagulation device 9 by the dosing device 10, and the sewage and the coagulant can fully contact and react to generate large-particle flocculation impurities by the coagulation device 9.
The coagulator 9 is connected with the high-speed sand cylinder filter 3 through a pipeline, the high-speed sand cylinder filter 3 is connected with the ultraviolet disinfection device 4 through a pipeline, and the ultraviolet disinfection device 4 is connected with the reuse water tank 5 through a pipeline.
In this embodiment, a drain pipe 31 is provided on the high-speed sand cylinder filter 3, the drain pipe 31 is communicated with the water inlet 91 through a valve, and the high-speed sand cylinder filter 3 and the dosing device 10 are both installed on the concrete foundation 8.
In the embodiment, the ultraviolet disinfection device 4 is provided with a water outlet 41, and the water outlet 41 is connected with the reuse water tank 5.
It should be noted that, in the large granule flocculation impurity got into high-speed sand jar filter 3, can be with the high-efficient removal of large granule flocculation impurity that contains in the sewage through high-speed sand jar filter 3, again through the irradiation disinfection of ultraviolet disinfection device 4, can reach the water requirement, through setting up of coagulating sedimentation filtration integration, can handle slightly complicated quality of water, can promote impurity removal effect, satisfies the rear end water requirement.
The high-speed sand cylinder filter 3 is also connected with a PAC metering pump 6 through a pipeline, the PAC metering pump 6 is connected with a PAC solution tank 7 through a pipeline, and the PAC solution tank 7 is connected with tap water in a factory through a pipeline.
In this embodiment, the PAC solution tank 7 is provided with a rotating motor 71, an output shaft of the rotating motor 71 is connected to a stirring shaft 72, and stirring blades 73 for stirring PAC solution are provided on the stirring shaft 72.
The rotating motor 71 is started, and the rotating motor 71 drives the stirring shaft 72 and the stirring blade 73 to rotate, so that the stirring blade 73 stirs the PAC solution.
Working principle: the sewage in the circulating water tank 1 is lifted into the coagulator 9 through the sewage lifting pump 2, coagulant is added into the coagulator 9 through the dosing equipment 10, sewage and coagulant can be fully contacted and reacted to generate large-particle flocculating impurities through the coagulator 9, the large-particle flocculating impurities enter the high-speed sand cylinder filter 3, the large-particle flocculating impurities contained in the sewage can be efficiently removed through the high-speed sand cylinder filter 3, then the sewage is subjected to irradiation disinfection through the ultraviolet disinfection device 4, the water consumption requirement can be met, the water quality slightly complicated can be treated through the coagulation sedimentation and filtration integrated setting, the impurity removal effect can be improved, and the water consumption requirement at the rear end is met.
It is noted that relational terms such as first and second, and the like are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Moreover, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. The utility model provides a coagulating sedimentation filters all-in-one, includes circulating water pond (1), its characterized in that: the utility model discloses a sewage treatment device, including circulating water pond (1), sewage lifting pump (2) pass through pipe connection coagulating ware (9), coagulating ware (9) pass through high-speed sand jar filter (3) of pipe connection, high-speed sand jar filter (3) pass through pipe connection ultraviolet disinfection device (4), ultraviolet disinfection device (4) pass through pipe connection retrieval and utilization pond (5), high-speed sand jar filter (3) still pass through pipe connection PAC metering pump (6), PAC metering pump (6) pass through pipe connection PAC solution tank (7), PAC solution tank (7) pass through pipe connection factory running water.
2. The coagulation sedimentation filtration all-in-one machine according to claim 1, wherein: one side of the coagulator (9) is provided with a dosing device (10), and the dosing device (10) is used for adding coagulant into the coagulator (9).
3. The coagulation sedimentation filtration all-in-one machine according to claim 2, wherein: the coagulation device is characterized in that a water inlet (91) is formed in the coagulation device (9), and the water inlet (91) is connected with a water outlet of the sewage lifting pump (2).
4. A coagulation sedimentation filtration all-in-one machine according to claim 3, wherein: the high-speed sand cylinder filter (3) is provided with a drain pipe (31), the drain pipe (31) is communicated with the water inlet (91) through a valve, and the high-speed sand cylinder filter (3) and the dosing equipment (10) are both arranged on the concrete foundation (8).
5. The coagulation sedimentation filtration all-in-one machine according to claim 1, wherein: the ultraviolet disinfection device (4) is provided with a water outlet (41), and the water outlet (41) is connected with the reuse water tank (5).
6. The coagulation sedimentation filtration all-in-one machine according to claim 1, wherein: the PAC solution tank (7) is provided with a rotating motor (71), an output shaft of the rotating motor (71) is connected with a stirring shaft (72), and stirring blades (73) for stirring the PAC solution are arranged on the stirring shaft (72).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202420049558.8U CN221588325U (en) | 2024-01-09 | 2024-01-09 | Coagulating sedimentation filters all-in-one |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202420049558.8U CN221588325U (en) | 2024-01-09 | 2024-01-09 | Coagulating sedimentation filters all-in-one |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221588325U true CN221588325U (en) | 2024-08-23 |
Family
ID=92413406
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202420049558.8U Active CN221588325U (en) | 2024-01-09 | 2024-01-09 | Coagulating sedimentation filters all-in-one |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221588325U (en) |
-
2024
- 2024-01-09 CN CN202420049558.8U patent/CN221588325U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103739124B (en) | A kind of efficient water treatment device and water treatment method | |
| CN202358976U (en) | Glass wastewater treatment equipment | |
| CN100375648C (en) | On-line chemical cleaning method for membrane-bioreactor | |
| CN105366893A (en) | A printing and dyeing wastewater treatment system and method | |
| CN105948425B (en) | Papermaking wastewater treatment system | |
| CN104098235A (en) | Sewage treatment method of casing plant | |
| CN201971688U (en) | A system for removing silicon and oil from oily sewage | |
| CN204211569U (en) | A kind of paper waste advanced treatment apparatus | |
| CN221588325U (en) | Coagulating sedimentation filters all-in-one | |
| CN216764612U (en) | Environment-friendly industrial wastewater treatment device | |
| CN215559636U (en) | a waste water treatment system | |
| CN103566762A (en) | Immersion type ultra-filtration system | |
| CN213623750U (en) | A textile sewage treatment system | |
| CN220827320U (en) | Sewage treatment machine for livestock and poultry cultivation | |
| CN205258241U (en) | Printing and dyeing wastewater treatment system | |
| CN211644998U (en) | A sewage treatment device with high treatment efficiency | |
| CN104973722B (en) | A kind of dyeing and printing sewage processing system | |
| CN101759309A (en) | Water treatment technology | |
| CN209940665U (en) | Ceramic ultrafiltration membrane advanced treatment system for running water horizontal plate | |
| CN112759116A (en) | Contain FEP waste water recovery processing system | |
| CN217679420U (en) | Tap water supply device with purification performance | |
| CN216273536U (en) | Device of landfill leachate's RO method concentrate evaporation crystallization retrieval and utilization zero release | |
| CN208378683U (en) | A kind of sewage disposal device that purification efficiency is high | |
| CN110845047A (en) | Reclaimed water softening and recycling treatment system and method suitable for waste incineration power plant | |
| CN206720909U (en) | A kind of heavy metal wastewater thereby purifier in daily use chemicals production |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |