CN205099513U - Processing system is softened to circulating water makeup water embrane method at normal water water source - Google Patents
Processing system is softened to circulating water makeup water embrane method at normal water water source Download PDFInfo
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- CN205099513U CN205099513U CN201520838434.9U CN201520838434U CN205099513U CN 205099513 U CN205099513 U CN 205099513U CN 201520838434 U CN201520838434 U CN 201520838434U CN 205099513 U CN205099513 U CN 205099513U
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- water
- outlet
- circulating
- water inlet
- embrane method
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 257
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 45
- 238000001816 cooling Methods 0.000 claims abstract description 18
- 238000006477 desulfuration reaction Methods 0.000 claims abstract description 12
- 239000003814 drug Substances 0.000 claims abstract description 11
- 238000001728 nano-filtration Methods 0.000 claims description 50
- 238000004140 cleaning Methods 0.000 claims description 39
- 239000002351 wastewater Substances 0.000 claims description 27
- 239000010802 sludge Substances 0.000 claims description 18
- 239000000126 substance Substances 0.000 claims description 16
- 238000005406 washing Methods 0.000 claims description 16
- 238000011001 backwashing Methods 0.000 claims description 12
- 239000002455 scale inhibitor Substances 0.000 claims description 10
- 239000003795 chemical substances by application Substances 0.000 abstract description 4
- 238000010521 absorption reaction Methods 0.000 abstract 2
- 230000003009 desulfurizing Effects 0.000 abstract 2
- 238000000034 method Methods 0.000 description 9
- 241000276438 Gadus morhua Species 0.000 description 7
- OYPRJOBELJOOCE-UHFFFAOYSA-N calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 7
- 239000011575 calcium Substances 0.000 description 7
- 229910052791 calcium Inorganic materials 0.000 description 7
- 235000019516 cod Nutrition 0.000 description 7
- 239000011777 magnesium Substances 0.000 description 7
- FYYHWMGAXLPEAU-UHFFFAOYSA-N magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 6
- 229910052749 magnesium Inorganic materials 0.000 description 6
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- 101700023688 LIME1 Proteins 0.000 description 4
- 235000015450 Tilia cordata Nutrition 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- 230000037250 Clearance Effects 0.000 description 3
- 230000035512 clearance Effects 0.000 description 3
- 239000000701 coagulant Substances 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 238000005429 turbidity Methods 0.000 description 3
- 238000005352 clarification Methods 0.000 description 2
- 230000001112 coagulant Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- JLVVSXFLKOJNIY-UHFFFAOYSA-N magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 2
- 229910001425 magnesium ion Inorganic materials 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 235000012970 cakes Nutrition 0.000 description 1
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 235000019600 saltiness Nutrition 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Abstract
The utility model discloses a processing system is softened to circulating water makeup water embrane method at normal water water source, include former pond, ultrafiltration device, middle water tank, receive and strain device, solution tank, circulative cooling tower, desulfurization absorption tower and antisludging agent medicine system, the delivery port in former pond is linked together with ultrafiltration device's water inlet, ultrafiltration device's delivery port is connected with the water inlet of middle water tank, the delivery port of middle water tank and the export of antisludging agent medicine system are received the entry of straining the device through pipeline and guan houyu and are linked together, the product water export of straining the device and solution tank's the entry received is linked together, solution tank's delivery port is linked together with the water inlet of circulative cooling tower, the export of the sewer of circulative cooling tower and the dense water export of straining the device of receiving all are linked together with the water inlet on desulfurization absorption tower. The utility model discloses can be effectual the concentrated multiplying power of improvement circulating water, cost and area are less, it is better to go out water quality of water.
Description
Technical field
The utility model belongs to reutilization of the sewage technical field, relates to a kind of circulating water system embrane method sofening treatment system of water resource of reclaimed water.
Background technology
Fuel-burning power plant is process water rich and influential family, and open circulation cooling system accounts for 60% ~ 80% of full station-service water inventory.When water resources worsening shortages, most thermal power plant has forbidden to use underground water, and restriction uses surface water.For response national energy-saving environmental protection policy and various places environmental requirement, a lot of power plant brings into use municipal middle water, in particular as the circulating water system that water of productive use ratio is the highest.
The total dissolved solidss content of middle water is usually high than fresh water, hardness, Cl
-, SO
4 2-all higher, fouling and the corrosion tendency of water are larger; COD, microorganism equal size are all higher, easily form Stickydeposit at places such as heat exchangers, may reduce condensing heat transfer efficiency and underdeposit corrosion; Suspended substance is more, easily forms dirt; Therefore, centering water must be entered process before entering circulating water system, remove hardness, sulfate radical, COD, suspended substance etc.
Traditional mid-water process craft is limestone-concrete treatment technique, by chemical agents such as dosing coagulant, lime, coagulant aidss, makes calcium, magnesium ion etc. cause dirt ion and generates CaCO
3, Mg (OH)
2deng indissoluble thing Precipitation; Suspension content is reduced under coagulation clarification effect; Limestone-concrete treatment also has certain removal effect to COD, microorganism etc.But lime treatment is applicable to the high water of temporary hardness ratio, otherwise the residual harness of water outlet is still higher, the raising of restriction recirculated water concentration rate; Lime dosing and metering system easily break down, and affect effluent quality; The sludge quantity formed is more, and need arrange sludge treating system, the mud cake after press filtration becomes solid waste need be disposed separately; Add various chemical medicaments, increase working cost; Ensure lime-coagulation clarification effect, need arrange larger pond body to ensure enough residence time, floor space is large.
Utility model content
The purpose of this utility model is the shortcoming overcoming above-mentioned prior art, provide a kind of circulating water system embrane method sofening treatment system of water resource of reclaimed water, this system effectively can improve the concentration rate of recirculated water, cost and floor space less, effluent quality is better.
For achieving the above object, the circulating water system embrane method sofening treatment system of the utility model water resource of reclaimed water comprises former pond, ultra-filtration equipment, intermediate water tank, nanofiltration device, filtered water tank, circulating cooling tower, desulfuration absorbing tower and Scale inhibitors medicine system;
The water outlet in former pond is connected with the water inlet of ultra-filtration equipment, the water outlet of ultra-filtration equipment is connected with the water inlet of intermediate water tank, the water outlet of intermediate water tank and the outlet of Scale inhibitors medicine system by pipeline and the entrance of Guan Houyu nanofiltration device be connected, the product water out of nanofiltration device is connected with the entrance of filtered water tank, the water outlet of filtered water tank is connected with the water inlet of circulating cooling tower, and the sewer outlet of circulating cooling tower and the dense water out of nanofiltration device are all connected with the water inlet of desulfuration absorbing tower.
Also comprise nanofiltration Cleaning Wastewater gathering system, the washing waste water outlet of nanofiltration device is connected with the water inlet in former pond through nanofiltration Cleaning Wastewater gathering system.
Also comprise ultrafiltration Cleaning Wastewater gathering system, the washing waste water outlet of ultra-filtration equipment is connected with the water inlet in former pond by ultrafiltration Cleaning Wastewater gathering system.
Also comprise sludge sump, the sludge outlet in former pond is connected with the entrance of sludge sump, and the sludge outlet place in former pond is provided with mud valve.
Also comprise backwashing system and chemically-cleaning device, the water outlet of intermediate water tank is connected with the water inlet of the water inlet of backwashing system and chemically-cleaning device, and the water outlet of backwashing system and the water outlet of chemically-cleaning device are connected with the water inlet of ultra-filtration equipment.
Also comprise chemical cleaning system and low-pressure washing system, the water outlet of filtered water tank is connected with the water inlet of the water inlet of chemical cleaning system and low-pressure washing system, and water outlet and the water outlet of low-pressure washing system of chemical cleaning system are connected with the water inlet of nanofiltration device.
The dense water out place of described nanofiltration device is provided with concentrated water discharge flow control valve.
The water outlet in former pond is connected by ultrafiltration service pump with the water inlet of ultra-filtration equipment.
The water outlet of intermediate water tank is connected by nanofiltration service pump with the water inlet of nanofiltration device.
The utility model has following beneficial effect:
The circulating water system embrane method sofening treatment system of water resource of reclaimed water described in the utility model is in the process processed the circulating water system of water resource of reclaimed water, the macromole objects such as suspended substance, colloid and particle in water are removed by ultra-filtration equipment, calcium again in nanofiltration device trap water, magnesium and sulfate radical etc. cause dirt ion, thus complete the embrane method sofening treatment of the circulating water system of water resource of reclaimed water, wherein, the turbidity of the water of being discharged by ultra-filtration equipment is low to moderate below 1NTU, pollution index SDI
15≤ 3, substituted the equipment such as settling pond and strainer in traditional sewerage disposing system simultaneously by ultra-filtration equipment, thus effectively reduce cost and the floor space of water treatment.In addition, water only need add Scale inhibitors before nanofiltration device process, namely realize calcium, magnesium and sulfate radical etc. by nanofiltration device and cause efficiently retaining of dirt ion, avoid Xiang Shuizhong to add the chemical agents such as lime, coagulating agent, dispersion stabilizer, save running cost, avoid being formed in treating processes mud, and do not affect water quality, to the rejection of calcium ion and magnesium ion up to 60%-70%, can more than 50% be reached to the rejection of sulfate ion up to more than 90%, COD and TOC clearance.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Wherein, 1 be former pond, 2 be ultra-filtration equipment, 3 be intermediate water tank, 4 be nanofiltration device, 5 be filtered water tank, 6 be circulating cooling tower, 7 be desulfuration absorbing tower, 8 be backwashing system, 9 be chemically-cleaning device, 10 be Scale inhibitors medicine system, 11 be low-pressure washing system, 12 be chemical cleaning system, 13 be ultrafiltration Cleaning Wastewater gathering system, 14 be nanofiltration Cleaning Wastewater gathering system, 15 for sludge sump.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail:
With reference to figure 1, the circulating water system embrane method sofening treatment system of water resource of reclaimed water described in the utility model comprises former pond 1, ultra-filtration equipment 2, intermediate water tank 3, nanofiltration device 4, filtered water tank 5, circulating cooling tower 6, desulfuration absorbing tower 7 and Scale inhibitors medicine system 10; The water outlet in former pond 1 is connected with the water inlet of ultra-filtration equipment 2, the water outlet of ultra-filtration equipment 2 is connected with the water inlet of intermediate water tank 3, the water outlet of intermediate water tank 3 and the outlet of Scale inhibitors medicine system 10 by pipeline and the entrance of Guan Houyu nanofiltration device 4 be connected, the product water out of nanofiltration device 4 is connected with the entrance of filtered water tank 5, the water outlet of filtered water tank 5 is connected with the water inlet of circulating cooling tower 6, and the sewer outlet of circulating cooling tower 6 and the dense water out of nanofiltration device 4 are all connected with the water inlet of desulfuration absorbing tower 7.
It should be noted that, the utility model also comprises nanofiltration Cleaning Wastewater gathering system 14, ultrafiltration Cleaning Wastewater gathering system 13, sludge sump 15, backwashing system 8, chemically-cleaning device 9, chemical cleaning system 12 and low-pressure washing system 11, and the washing waste water outlet of nanofiltration device 4 is connected through the water inlet of nanofiltration Cleaning Wastewater gathering system 14 with former pond 1; The washing waste water outlet of ultra-filtration equipment 2 is connected by the water inlet of ultrafiltration Cleaning Wastewater gathering system 13 with former pond 1; The sludge outlet in former pond 1 is connected with the entrance of sludge sump 15, and the sludge outlet place in former pond 1 is provided with mud valve, regularly automatically drains in sludge sump 15 by the mud in former pond 1, is then transported by mud tank car; The water outlet of intermediate water tank 3 is connected with the water inlet of the water inlet of backwashing system 8 and chemically-cleaning device 9, the water outlet of backwashing system 8 and the water outlet of chemically-cleaning device 9 are connected with the water inlet of ultra-filtration equipment 2, when applying, need the backwash time of default backwashing system 8, when to preset backwash time point time automatic back-washing once; When exceeding pre-set threshold value when pressure reduction in the process that ultra-filtration equipment 2 runs, chemically-cleaning device 9 carries out matting automatically simultaneously; The water outlet of filtered water tank 5 is connected with the water inlet of the water inlet of chemical cleaning system 12 and low-pressure washing system 11, and the water outlet of chemical cleaning system 12 and the water outlet of low-pressure washing system 11 are connected with the water inlet of nanofiltration device 4.
In addition, the dense water out place of described nanofiltration device 4 is provided with concentrated water discharge flow control valve; The water outlet in former pond 1 is connected by ultrafiltration service pump with the water inlet of ultra-filtration equipment 2; The water outlet of intermediate water tank 3 is connected by nanofiltration service pump with the water inlet of nanofiltration device 4.
Specific operation process of the present utility model is:
The circulating water system of the water resource of reclaimed water in former pond 1 enters into intermediate water tank 3 after ultra-filtration equipment 2 carries out ultrafiltration, water in intermediate water tank 3 enters into nanofiltration device 4 after mixing with the Scale inhibitors in Scale inhibitors medicine system 10, and after nanofiltration device 4 nanofiltration, be divided into product water and dense water, wherein, produce water and enter into filtered water tank 5, dense water enters into desulfuration absorbing tower 7 as sulfur removal technology water, product water in filtered water tank 5 as a supplement water enters circulating cooling tower 6, and the sewer of circulating water cooling tower 6 also enters into desulfuration absorbing tower 7 as sulfur removal technology water.
Embodiment
Water sample is certain Water of Power Plants water source, and turbidity is 9.08NTU, and calcium hardness is 3.86mmol/L, and magnesium hardness is 2.98mmol/L, SO
4 2-content is 130mg/L, Cl
-content is 96mg/L, Na
+content is 95mg/L, and dissolved solid content is 715mg/L, COD be 13mg/L, TOC is 9.10mg/L; The middle water designing treatment water yield is 1000m
3/ h.
Middle water 1000m
3/ h, ultrafiltration Cleaning Wastewater gathering system 13 carry out waste water 100m
3/ h, nanofiltration Cleaning Wastewater gathering system 14 carry out waste water 50m
3/ h enters former pond 1 and carries out preliminary precipitation, and regular automatic mud removing bottom former pond 1, sludge volume is about 15m
3/ h, is first stored in sludge sump 15, is then transported outward by mud tank car and disposes; Former pond 1 water outlet 1135m
3/ h promotes through ultrafiltration service pump and enters ultra-filtration equipment 2, and ultra-filtration equipment 2 produces water 1035m
3/ h enters in intermediate water tank 3, and ultrafiltration Cleaning Wastewater gathering system 13 is by 100m
3the water of/h is back to former pond 1, and the ultrafiltration rate of recovery is about 91.19%; Intermediate water tank 3 water outlet 1035m
3/ h enters nanofiltration device 4 after nanofiltration service pump promotes, and water 800m is produced in nanofiltration
3/ h enters circulating cooling tower 6 as circulating water system through filtered water tank 5, the dense water 185m of nanofiltration
3/ h enters desulfuration absorbing tower 7 as sulfur removal technology water, and substitute service water, nanofiltration Cleaning Wastewater gathering system 14 is by waste water 50m
3/ h is back to former pond 1; The nanofiltration rate of recovery is about 81.22%; The Water Sproading rate of the embrane method sofening treatment system of a whole set of water resource of reclaimed water is 80%.
It is 0.36NTU, SDI that water turbidity is produced in ultrafiltration
15be 2.38; The calcium hardness that water is produced in nanofiltration is 1.50mmol/L, and magnesium hardness is 1.15mmol/L, SO
4 2-content is 6.10mg/L, Cl
-content is 56mg/L, Na
+content is 21mg/L, and dissolved solid content is 200mg/L, COD be 6mg/L, TOC is 4.30mg/L.Calcium hardness rejection is about 61.14%, and magnesium hardness rejection is about 61.41%, SO
4 2-rejection is about 95.31%; Cl
-transmitance is about 58.33%, Na
+transmitance is about 22.11%; Ratio of desalinization is about 72.03%; It is 52.75% that COD clearance is about 53.85%, TOC clearance.
Calcium, the magnesium hardness of water are produced in nanofiltration, SO
4 2-, Cl
-, saltiness is all lower, and as this power plant's circulating cooling tower 6 make up water, recirculated water concentration rate is increased to 5 times by original 3 times, can save a large amount of circulating water system.
Claims (9)
1. the circulating water system embrane method sofening treatment system of a water resource of reclaimed water, it is characterized in that, comprise former pond (1), ultra-filtration equipment (2), intermediate water tank (3), nanofiltration device (4), filtered water tank (5), circulating cooling tower (6), desulfuration absorbing tower (7) and Scale inhibitors medicine system (10);
The water outlet in former pond (1) is connected with the water inlet of ultra-filtration equipment (2), the water outlet of ultra-filtration equipment (2) is connected with the water inlet of intermediate water tank (3), the water outlet of intermediate water tank (3) and the outlet of Scale inhibitors medicine system (10) by pipeline and the entrance of Guan Houyu nanofiltration device (4) be connected, the product water out of nanofiltration device (4) is connected with the entrance of filtered water tank (5), the water outlet of filtered water tank (5) is connected with the water inlet of circulating cooling tower (6), the sewer outlet of circulating cooling tower (6) and the dense water out of nanofiltration device (4) are all connected with the water inlet of desulfuration absorbing tower (7).
2. the circulating water system embrane method sofening treatment system of water resource of reclaimed water according to claim 1, it is characterized in that, also comprise nanofiltration Cleaning Wastewater gathering system (14), the washing waste water outlet of nanofiltration device (4) is connected through the water inlet of nanofiltration Cleaning Wastewater gathering system (14) with former pond (1).
3. the circulating water system embrane method sofening treatment system of water resource of reclaimed water according to claim 1, it is characterized in that, also comprise ultrafiltration Cleaning Wastewater gathering system (13), the washing waste water outlet of ultra-filtration equipment (2) is connected by the water inlet of ultrafiltration Cleaning Wastewater gathering system (13) with former pond (1).
4. the circulating water system embrane method sofening treatment system of water resource of reclaimed water according to claim 1, it is characterized in that, also comprise sludge sump (15), the sludge outlet in former pond (1) is connected with the entrance of sludge sump (15), and the sludge outlet place of former pond (1) is provided with mud valve.
5. the circulating water system embrane method sofening treatment system of water resource of reclaimed water according to claim 1, it is characterized in that, also comprise backwashing system (8) and chemically-cleaning device (9), the water outlet of intermediate water tank (3) is connected with the water inlet of the water inlet of backwashing system (8) and chemically-cleaning device (9), and the water outlet of backwashing system (8) and the water outlet of chemically-cleaning device (9) are connected with the water inlet of ultra-filtration equipment (2).
6. the circulating water system embrane method sofening treatment system of water resource of reclaimed water according to claim 1, it is characterized in that, also comprise chemical cleaning system (12) and low-pressure washing system (11), the water outlet of filtered water tank (5) is connected with the water inlet of the water inlet of chemical cleaning system (12) and low-pressure washing system (11), and the water outlet of chemical cleaning system (12) and the water outlet of low-pressure washing system (11) are connected with the water inlet of nanofiltration device (4).
7. the circulating water system embrane method sofening treatment system of water resource of reclaimed water according to claim 1, is characterized in that, the dense water out place of described nanofiltration device (4) is provided with concentrated water discharge flow control valve.
8. the circulating water system embrane method sofening treatment system of water resource of reclaimed water according to claim 1, is characterized in that, the water outlet of former pond (1) is connected by ultrafiltration service pump with the water inlet of ultra-filtration equipment (2).
9. the circulating water system embrane method sofening treatment system of water resource of reclaimed water according to claim 1, is characterized in that, the water outlet of intermediate water tank (3) is connected by nanofiltration service pump with the water inlet of nanofiltration device (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520838434.9U CN205099513U (en) | 2015-10-27 | 2015-10-27 | Processing system is softened to circulating water makeup water embrane method at normal water water source |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520838434.9U CN205099513U (en) | 2015-10-27 | 2015-10-27 | Processing system is softened to circulating water makeup water embrane method at normal water water source |
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| Publication Number | Publication Date |
|---|---|
| CN205099513U true CN205099513U (en) | 2016-03-23 |
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ID=55515304
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520838434.9U Active CN205099513U (en) | 2015-10-27 | 2015-10-27 | Processing system is softened to circulating water makeup water embrane method at normal water water source |
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| Country | Link |
|---|---|
| CN (1) | CN205099513U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105198123A (en) * | 2015-10-27 | 2015-12-30 | 西安西热水务环保有限公司 | Membrane-softening treatment system and method used for supplement water for circulating water of reclaimed water source |
-
2015
- 2015-10-27 CN CN201520838434.9U patent/CN205099513U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105198123A (en) * | 2015-10-27 | 2015-12-30 | 西安西热水务环保有限公司 | Membrane-softening treatment system and method used for supplement water for circulating water of reclaimed water source |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |