CN213085758U - Treatment system for recycling high-turbidity high-salt-content reclaimed water - Google Patents
Treatment system for recycling high-turbidity high-salt-content reclaimed water Download PDFInfo
- Publication number
- CN213085758U CN213085758U CN202020452894.9U CN202020452894U CN213085758U CN 213085758 U CN213085758 U CN 213085758U CN 202020452894 U CN202020452894 U CN 202020452894U CN 213085758 U CN213085758 U CN 213085758U
- Authority
- CN
- China
- Prior art keywords
- filter
- water
- reverse osmosis
- slow
- reclaimed 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
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to a treatment system for recycling high-turbidity high-salt content reclaimed water, which comprises a biological aerated filter, a slow decarburization clarification tank, an ultrahigh-speed fiber filter, an immersed ultrafiltration device and a reverse osmosis device; the aeration biological filter import and well water pipeline are connected, the aeration biological filter export with slow decarbonization depositing reservoir access connection, slow decarbonization depositing reservoir export with hypervelocity fiber filter access connection, hypervelocity fiber filter export with submergence formula ultrafiltration device access connection, submergence formula ultrafiltration device export with reverse osmosis unit access connection, reverse osmosis unit exit linkage power plant water system. The utility model discloses can carry out advanced treatment to high turbid high salinity normal water, satisfy the reuse of reclaimed water requirement of power plant.
Description
Technical Field
The utility model belongs to the technical field of the advanced treatment of reclaimed water in thermal power plant, especially, relate to a processing system that is used for high turbid high salt content reclaimed water retrieval and utilization.
Background
The reclaimed water is also called reclaimed water, and the water quality is generally used as a distinguishing mark. The quality of the reclaimed water is between that of the upper water (feed water) and the lower water (discharge water). In China, the water quality of municipal sewage treated by a series of processes reaches a certain use standard, and the municipal sewage can be reused in a certain range. In power plants, reclaimed water is often used as a source of industrial water throughout the plant. Aiming at the characteristics of a power plant, a treatment system for recycling high-turbidity high-salt-content reclaimed water is needed.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a processing system for high turbid high salt content reuse of reclaimed water carries out advanced treatment through the high turbid high salt content reclaimed water to satisfy the power plant's reuse of reclaimed water requirement.
The utility model provides a treatment system for recycling high-turbidity high-salt content reclaimed water, which comprises a biological aerated filter, a slow decarburization clarification tank, an ultra-high-speed fiber filter, an immersed ultrafiltration device and a reverse osmosis device;
the aeration biological filter import and well water pipeline are connected, the aeration biological filter export with slow decarbonization depositing reservoir access connection, slow decarbonization depositing reservoir export with hypervelocity fiber filter access connection, hypervelocity fiber filter export with submergence formula ultrafiltration device access connection, submergence formula ultrafiltration device export with reverse osmosis unit access connection, reverse osmosis unit exit linkage power plant water system.
Furthermore, the biological aerated filter adopts a round ceramic filter material as a microorganism carrier.
By means of the scheme, the treatment system for recycling the high-turbidity high-salt-content reclaimed water can be used for performing advanced treatment on the high-turbidity high-salt-content reclaimed water, and the requirement on recycling the reclaimed water in a power plant is met.
The above description is only an overview of the technical solution of the present invention, and in order to make the technical means of the present invention clearer and can be implemented according to the content of the description, the following detailed description is made with reference to the preferred embodiments of the present invention and accompanying drawings.
Drawings
Fig. 1 is a schematic structural diagram of the treatment system for recycling high-turbidity high-salinity reclaimed water of the present invention.
Reference numbers in the figures:
1-aeration biological filter; 2-slow decarburization clarifying pool; 3-ultra-high-speed fiber filter; 4-an immersion ultrafiltration device; 5, a reverse osmosis device; 6-power plant water system.
Detailed Description
The following detailed description of the embodiments of the present invention is provided with reference to the accompanying drawings and examples. The following examples are intended to illustrate the invention, but are not intended to limit the scope of the invention.
Referring to fig. 1, the present embodiment provides a treatment system for recycling high-turbidity high-salt content reclaimed water, which includes a biological aerated filter 1, a slow decarburization clarification tank 2, an ultra-high-speed fiber filter 3, an immersed ultrafiltration device 4 and a reverse osmosis device 5;
the inlet of the biological aerated filter 1 is connected with a reclaimed water conveying pipeline, the outlet of the biological aerated filter 1 is connected with the inlet of a slow decarburization clarification tank 2, the outlet of the slow decarburization clarification tank 2 is connected with the inlet of an ultra-high speed fiber filter 3, the outlet of the ultra-high speed fiber filter 3 is connected with the inlet of an immersion ultrafiltration device 4, the outlet of the immersion ultrafiltration device 4 is connected with the inlet of a reverse osmosis device 5, and the outlet of the reverse osmosis device 5 is connected with a water system 6 of a power plant.
Through the treatment system, the high-turbidity and high-salt-content reclaimed water is subjected to advanced treatment sequentially through the biological aerated filter 1, the slow-speed decarburization clarification tank 2, the ultrahigh-speed fiber filter 3, the immersed ultrafiltration device 4 and the reverse osmosis device 5, the reclaimed water reuse requirement of a power plant can be met, and the treated reclaimed water is sent to the power plant water system 6 for reuse.
The system will be described in detail below.
An aeration biological filter.
The aeration biological filter is used for degrading organic matters in sewage and nitrifying ammonia nitrogen, adopts a circular ceramic filter material as a microorganism carrier in the biological filter, domesticates dominant strains with different functions, shortens biological oxidation time, improves biochemical treatment efficiency so as to adapt to the change of water quality and stabilize the treated water quality. The adopted aeration biological filter has the functions of removing SS, COD, BOD, nitrification, denitrification and removing AOX (harmful substances), and is characterized by integrating biological oxidation and suspended solid interception into a whole and saving subsequent sedimentation (secondary sedimentation tank); the volume load and the hydraulic load are large, the hydraulic retention time is short, the required capital investment is low, and the effluent quality is good; the operation energy consumption is low, and the operation cost is saved. In the operation process, oxygen is supplied by aeration at the bottom of the filter. The filter chamber is backwashed after running for a certain time; the back flushing adopts the combination of gas and water for back flushing, the back flushing sewage is discharged to a recovery water tank, and the effluent of the filter tank enters a clarification tank by gravity flow for subsequent treatment. The biological filter is mainly used for removing organic matters and ammonia nitrogen in raw water and removing the turbidity of the raw water by biological filtration. After passing through the biological filter, the stability of the sewage is improved.
Slow decarbonization clarification tank
The slow decarbonization clarification tank is sequentially provided with a condensation zone, a flocculation zone, a thrust zone and a concentration separation zone from the water inlet direction, the controllable sludge backflow is realized, and the residual sludge is sent to a filter press. Has the following advantages: the floor area can be saved by 50% to the maximum extent; the adaptability to water quality, flow and temperature change is strong; accurate pH control; controllable sludge backflow greatly improves the effluent quality and saves the use amount of medicines; fully-automatically discharging the sludge; the self-service water can be recycled and treated, and no waste water is generated; and (4) unattended operation.
Ultrahigh-speed fiber filter tank
The fiber filter tank system adopts a reinforced concrete super-high-speed fiber filter tank, and the material in the filter tank is plastic or SS 304.
Immersed ultrafiltration device
The ultrafiltration pressure is usually 0.02 MPa-0.30 MPa, the membrane aperture is 0.02-0.10 μm, the cut-off molecular weight is about 1000-500000 Dalton, and the method is a membrane separation technology capable of purifying, separating and concentrating the solution. An ultrafiltration process is generally understood to be a sieving process which is dependent on the pore size of the membrane, with the pressure difference across the membrane being the driving force and the ultrafiltration membrane being the filter medium. The ultrafiltration membrane can effectively remove suspended matters, colloidal particles, bacteria, most viruses and the like in water, has the removal rate of 20-60 percent for organic matters, and hardly intercepts small molecular organic matters and inorganic ions. The ultrafiltration system has high operation automation degree, small operation and maintenance workload, integrated equipment and small occupied area. The turbidity of the ultrafiltration effluent is less than 0.2NTU, and the SDI is less than 3, thus meeting the requirement of reverse osmosis influent water quality.
Reverse osmosis device
Reverse osmosis systems are commonly used in reclaimed water recycling systems, and the principle of the reverse osmosis system is that raw water passes through a membrane under the action of high pressure, and a solvent in the water diffuses from high concentration to bottom concentration so as to achieve the purposes of separation, purification and concentration. In the treatment of waste water, a reclaimed water recycling technical system is often selected and an indispensable part of the system is an RO reverse osmosis membrane system. The ultra-static pressure pump is used for high-pressure permeation, so that water molecules and ionic mineral elements pass through a reverse osmosis membrane, most heavy metals, organic matters, bacteria, viruses and the like dissolved in water cannot be trapped through the reverse osmosis membrane. Based on the principle of reverse osmosis, impurities in water, such as toxic substances of heat sources, filterable viruses, bacteria, toxins, compounds and heavy metals (arsenic, cobalt, cadmium, mercury and the like), and substances harmful to human health, such as metals, salts, free ions and the like, are separated from pure water by the reverse osmosis membrane. The reclaimed water reuse technology is characterized in that various physical, chemical, biological and other means are used for treating wastewater discharged by industry at different depths to achieve the water quality required by the process, and then the wastewater is reused in the process to save water resources.
The processing system has the following technical effects:
1. the impurity removal efficiency is high, and the quality of the produced water is greatly better than that of the traditional method;
2. the use of chemical agents is thoroughly eliminated or greatly reduced, and secondary pollution is avoided;
3. the system is easy to automate and has high reliability. The operation is simple, and the facility is only opened and closed at two gears;
4. the floor space requirement is small;
5. the cost is equivalent to that of the conventional water treatment system.
The above description is only a preferred embodiment of the present invention, and is not intended to limit the present invention, and it should be noted that, for those skilled in the art, a plurality of modifications and variations can be made without departing from the technical principle of the present invention, and these modifications and variations should also be regarded as the protection scope of the present invention.
Claims (1)
1. A treatment system for recycling high-turbidity high-salt-content reclaimed water is characterized by comprising a biological aerated filter, a slow decarburization clarification tank, an ultrahigh-speed fiber filter, an immersed ultrafiltration device and a reverse osmosis device;
the inlet of the biological aerated filter is connected with a reclaimed water conveying pipeline, the outlet of the biological aerated filter is connected with the inlet of the slow decarburization clarification tank, the outlet of the slow decarburization clarification tank is connected with the inlet of the ultra-high speed fiber filter, the outlet of the ultra-high speed fiber filter is connected with the inlet of the immersed ultrafiltration device, the outlet of the immersed ultrafiltration device is connected with the inlet of the reverse osmosis device, and the outlet of the reverse osmosis device is connected with a water system of a power plant;
the aeration biological filter adopts a round ceramic filter material as a microorganism carrier;
the slow decarburization clarification tank is sequentially provided with a coagulation zone, a flocculation zone, a thrust zone and a concentration separation zone from the water inlet direction;
the ultrahigh-speed fiber filter chamber is made of reinforced concrete and is made of plastics or SS304 materials.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202020452894.9U CN213085758U (en) | 2020-03-31 | 2020-03-31 | Treatment system for recycling high-turbidity high-salt-content reclaimed water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202020452894.9U CN213085758U (en) | 2020-03-31 | 2020-03-31 | Treatment system for recycling high-turbidity high-salt-content reclaimed water |
Publications (1)
Publication Number | Publication Date |
---|---|
CN213085758U true CN213085758U (en) | 2021-04-30 |
Family
ID=75600290
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202020452894.9U Active CN213085758U (en) | 2020-03-31 | 2020-03-31 | Treatment system for recycling high-turbidity high-salt-content reclaimed water |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN213085758U (en) |
-
2020
- 2020-03-31 CN CN202020452894.9U patent/CN213085758U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101851046B (en) | Device for deep treatment and complete recovery of coking wastewater and application method thereof | |
CN201942597U (en) | Treatment and recovery device for wastewater of coal-derived natural gas | |
KR20100115412A (en) | Appliance for processing sewage having biological process, sludge separator and membrane separator | |
CN208234724U (en) | Advanced treatment and reuse of dyeing waste water and Zero emission device | |
CN103159381A (en) | Fine chemical wastewater treatment and reuse method | |
CN102139991A (en) | Method for treating and recycling coal-derived natural gas waste water and device thereof | |
CN112174441A (en) | System and method for treating and recycling machining wastewater by using air flotation pretreatment, biochemistry and double-membrane method | |
CN208917033U (en) | Pre-treatment waste water treatment system | |
CN104129887A (en) | Reclaimed water recycling system based on membrane bioreactor | |
CN108862834A (en) | A kind of dyeing waste water advanced treatment system and its processing method | |
CN104030517A (en) | Advanced treatment recovery technology of coking wastewater | |
CN111392984A (en) | Advanced treatment system and method for supplementing water by using urban reclaimed water as circulating water of power plant | |
CN100418906C (en) | Method and apparatus for advanced treatment and reclamation of industrial wastewater | |
CN209113686U (en) | A kind of combination unit handling hc effluent with high salt | |
CN111606502A (en) | Harmless wastewater treatment process and system for livestock and poultry died of diseases | |
CN213085758U (en) | Treatment system for recycling high-turbidity high-salt-content reclaimed water | |
CN201024129Y (en) | Waste water zero discharge quick highly-effective automatic-clarification treatment field, device | |
CN110642382A (en) | Anaerobic and aerobic composite biological treatment desalting method | |
CN114873857B (en) | System and method for recycling and standard-reaching discharge of carbon dodecyl alcohol ester wastewater | |
CN101028960B (en) | Method for pre-treating seawater by flow-raising aeration biological filtering pool | |
CN202829788U (en) | Treatment device for benzene-containing waste water | |
CN212504439U (en) | Treatment system for recycling high-hardness reclaimed water | |
CN101481193A (en) | Zero discharge process for amino acid wastewater | |
CN114804547A (en) | High-concentration organic wastewater treatment system and method | |
CN212102493U (en) | Advanced treatment system for supplementing water by using urban reclaimed water as circulating water of power plant |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |