CN205115196U - Circulative cooling discharge water recycle device - Google Patents
Circulative cooling discharge water recycle device Download PDFInfo
- Publication number
- CN205115196U CN205115196U CN201520915352.XU CN201520915352U CN205115196U CN 205115196 U CN205115196 U CN 205115196U CN 201520915352 U CN201520915352 U CN 201520915352U CN 205115196 U CN205115196 U CN 205115196U
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- China
- Prior art keywords
- water
- cooling discharge
- discharge water
- flow mixing
- recycle device
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 111
- 238000001816 cooling Methods 0.000 title claims abstract description 55
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 37
- 239000000126 substance Substances 0.000 claims abstract description 26
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 11
- 239000003814 drug Substances 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims description 31
- 238000005189 flocculation Methods 0.000 claims description 21
- 230000016615 flocculation Effects 0.000 claims description 21
- 238000004140 cleaning Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 10
- 239000003899 bactericide agent Substances 0.000 claims description 8
- 150000001875 compounds Chemical class 0.000 claims description 7
- 238000004062 sedimentation Methods 0.000 claims description 6
- 239000010802 sludge Substances 0.000 claims description 5
- 241001067407 Cometes Species 0.000 claims description 3
- 239000004744 fabric Substances 0.000 claims description 3
- 244000005700 microbiome Species 0.000 abstract description 7
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical compound [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 abstract description 3
- 238000001914 filtration Methods 0.000 abstract description 3
- 230000003311 flocculating Effects 0.000 abstract description 2
- 244000052616 bacterial pathogens Species 0.000 abstract 1
- 125000004122 cyclic group Chemical group 0.000 abstract 1
- 239000003344 environmental pollutant Substances 0.000 abstract 1
- 230000001717 pathogenic Effects 0.000 abstract 1
- 231100000719 pollutant Toxicity 0.000 abstract 1
- 238000005057 refrigeration Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 2
- 239000000877 Sex Attractant Substances 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000005273 aeration Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000001112 coagulant Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000004059 degradation Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000003628 erosive Effects 0.000 description 1
- 239000000413 hydrolysate Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000000813 microbial Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001737 promoting Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004148 unit process Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Abstract
The utility model provides a refrigeration cycle water recycle device, including the water inlet, connect in the mixed flow ware of water inlet to reach the chemical tank that communicates with the mixed flow ware, the medicament in it mixes with the interior cooling discharge water of mixed flow ware, the exit linkage of mixed flow ware has the water treatment system, through the water treatment system after the filter passes through the clear water inflow ultrafiltration system after the filter filters, the ultrafiltration system is connected with the safety filter ware through the second booster pump, and the safety filter ware passes through the high -pressure pump to be connected in reverse osmosis unit, and the demineralized water after reverse osmosis unit handles flows back and receives and utilize through the delivery port. Through place the medicament in the mixed flow ware, can condense into the alumen ustum with the pollutant that cools off in the discharge water to killing the most microorganisms including pathogenic microbes of aquatic, later again through flocculating, deposit and filtering, handling through ultrafiltration system and reverse osmosis unit more afterwards, the stable cyclic utilization that retrieves can be realized to final messenger's cooling discharge water.
Description
Technical field
The utility model relates to water treatment correlative technology field, particularly relates to a kind of circulating cooling discharge water recycle device.
Background technology
Cooling circulating water system utilizes cooling discharge water to carry out equipment cooling process, recirculated water is in the process of cooling apparatus or product, water temperature raises, although the change of its physical behavior is little, but after recycling for a long time, dissolved substance in water is concentrated or disappear, dust accumulates, microbial growth, to cause in e-quipment and pipe dirty thing deposition or to metal equipment corrosion, therefore need one can process circulating cooling discharge water, steady in a long-termly can use, prejudicial circulating cooling discharge water recycle device is not had to pipeline and equipment.
Summary of the invention
Problem to be solved in the utility model is to provide a kind of cooling discharge water recycle device, can process, steady in a long-termly can use, can not cause damage to pipeline and equipment circulating cooling discharge water.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is: a kind of circulating cooling discharge water recycle device, comprise water-in, be connected to the flow mixing device of described water-in, and the chemical tank to be communicated with flow mixing device, medicament in it mixes with the cooling discharge water in flow mixing device, the outlet of described flow mixing device is connected with water purifying processing system, described water purifying processing system is connected with strainer by the first topping-up pump, clear water after being filtered flows into ultrafiltration system, described ultrafiltration system is connected with cartridge filter by the second topping-up pump, described cartridge filter is connected to reverse osmosis unit by high-pressure pump, de-mineralized water after reverse osmosis unit process flows out through water outlet to be recycled.
Further, described water purifying processing system comprise set gradually flocculation basin, transition pond, settling tank and clean water basin, described clean water basin are connected to described first topping-up pump, the bottom of described flocculation basin, transition pond, settling tank and clean water basin is equipped with sedimentation port, and described sedimentation port is connected to sludge sump by electric butterfly valve.
Further, described flocculation basin is the folded plate flocculator be arranged side by side, and its number is four.
Further, described settling tank is the tube settler be arranged side by side, and its number is three.
Further, described chemical tank is three, comprises flocculation chemical tank, helps solidifying chemical tank and bactericidal agent case, described flocculation chemical tank, help solidifying chemical tank and bactericidal agent case to be all connected with compound pump, and by compound pump, medicament is delivered to flow mixing device.
Further, described ultrafiltration system comprises ultra-filtration equipment and is connected to the ultrafiltration water tank of ultra-filtration equipment, and described ultrafiltration water tank is connected to described second topping-up pump.
Further, cartridge filter is provided with between described strainer and ultra-filtration equipment.
Further, Hand-operated butterfly valve and electric butterfly valve is provided with between described water-in and flow mixing device.
Further, described flow mixing device is straight-line type flow mixing device.
Further, described strainer is comet fabric filter.
The advantage that the utility model has and positively effect are: by placing medicament in flow mixing device, pollutent in cooling discharge water can be condensed into alumen ustum, and the most microorganisms comprising sex pheromone killed in water, afterwards again through flocculation, precipitation, aeration and filtration, process through ultrafiltration system and reverse osmosis unit more subsequently, finally enable cooling discharge water long-term stability recycle, can not cause damage to pipeline and equipment.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model
In figure:
1, water-in; 2, chemical tank; 3, flow mixing device; 4, water purifying processing system; 5, the first topping-up pump; 6, strainer; 7, ultrafiltration system; 8, the second topping-up pump; 9, cartridge filter; 10, high-pressure pump; 11, reverse osmosis unit; 12, water outlet; 13, electric butterfly valve; 14, Hand-operated butterfly valve; 21, flocculate chemical tank; 22, solidifying chemical tank is helped; 23, bactericidal agent case; 24, compound pump; 41, flocculation basin; 42, transition pond; 43, heavyly pond is determined; 44, clean water basin; 45, sludge sump; 71, ultra-filtration equipment; 72, ultrafiltration water tank.
Embodiment
Below in conjunction with accompanying drawing, specific embodiment of the utility model is illustrated:
As shown in Figure 1, steady in a long-term the recycling of the cooling discharge water used to enable the cooling discharge water recycle system, the utility model provides a kind of circulating cooling discharge water recycle device, comprise water-in 1, for cooling the inflow of discharge water, be connected to the flow mixing device 3 of water-in 1, and the chemical tank 2 to be communicated with flow mixing device 3, the medicament wherein arranged in chemical tank 2 mixes with the cooling discharge water in flow mixing device 3, pollutent in cooling discharge water can be condensed into alumen ustum, and the most microorganisms comprising sex pheromone killed in water, the outlet of flow mixing device 3 is connected with water purifying processing system 4, and it processes for and the mixed cooling discharge water of medicament interior to flow mixing device 3, obtains relatively limpid cooling discharge water, water purifying processing system 4 is connected with strainer 6 by the first topping-up pump 5, relatively limpid cooling discharge water after water purifying processing system 4 processes filters through filter 6 again, flow into ultrafiltration system 7 subsequently again to filter, remove the particulate in water, colloid, bacterium, ultrafiltration system 7 is connected with cartridge filter 9 by the second topping-up pump 8, and cartridge filter 9 is for removing the large granular impurity in cooling discharge water, cartridge filter 9 is connected to reverse osmosis unit 11 by high-pressure pump 10, and the cooling discharge water after reverse osmosis unit 11 processes flows out through water outlet 12, again enters the cooling discharge water recycle system and carries out cooling use.
In the present embodiment, strainer 6 is for filtering the cooling discharge water flowed out from water purifying processing system 4 carried by the first topping-up pump 5 further, eliminate remaining silt and microorganism, water quality is purified further, then ultrafiltration system 7 is entered, the present embodiment middle filtrator 6 is comet type fabric filter, to reach good filter effect.
Preferably, flow mixing device 3 adopts straight-line type flow mixing device, and cardinal principle is when making current by tubulation, under the effect in frictional belt, produce serial vortex, and in spatial attenuation thereafter, produce high-frequency vortex, thus the hydrolysate of coagulating agent complexity is fully mixed with the colloidal solid in former water.Straight-line type flow mixing device has good erosion resistance, and intensity is high, aesthetic in appearance, easy for installation, mixing rapidly and efficiently, the feature such as less energy-consumption.
Water purifying processing system 4 comprise set gradually flocculation basin 41, transition pond 42, settling tank 43 and clean water basin 44, clean water basin 44 are connected to the first topping-up pump 5, wherein:
Flocculation basin 41 is for the particle flocculation in the cooling discharge water that promotes flow mixing device 3 and flow out, and be precipitated to bottom, the present embodiment adopts four folded plate flocculators be arranged side by side, namely in folded plate flocculator, place the flap of some amount, current are along the upper and lower flowing of flap, through repeatedly turning back, be conducive to the flocculation promoting particle in cooling discharge water.What in the present embodiment, folded plate flocculator adopted is vertical-flow, is certainly not limited to vertical-flow, also can using of flat flow;
Excessive effect is played in 42, transition pond, and its cooling discharge water that flocculation basin 41 can be flowed out pools together, and precipitates further;
Settling tank 43 is for removing the suspended solid being suspended in and can precipitating in cooling discharge water, in the present embodiment, settling tank 43 adopts three tube settlers be arranged side by side, and in the cooling discharge water after three tube settlers, most of silt and throw out are removed;
Clean water basin 44 for cooling discharge water that settling tank 43 is flowed out in the environment of aerobic, microorganism biological circle is formed with the microorganism in pond, utilize microorganism to the biological degradation cleaning action cooling discharge water in the body of pond, reach the object of cooling wastewater treatment, realize the improvement of purification of water quality and water quality;
In the present embodiment, the bottom of described flocculation basin 41, transition pond 42, settling tank 43 and clean water basin 44 is equipped with sedimentation port, and this sedimentation port is connected to sludge sump 45 by electric butterfly valve 13, and then the throw out in above-mentioned each pond can be expelled in sludge sump 45.The effect of electric butterfly valve 13 is opened once at certain time intervals, above-mentioned each pond can not be precipitated too much, cause treatment effect bad.
Chemical tank 2 is set to three, it comprises flocculation chemical tank 21, helps solidifying chemical tank 22 and bactericidal agent case 23, wherein flocculating, chemical tank 21 is interior places flocculation agent, help in solidifying chemical tank 22 and place coagulant aids, sterilant placed by bactericidal agent case 23, flocculation chemical tank 21, helps solidifying chemical tank 22 and bactericidal agent case 23 to be all connected with compound pump 24, and by compound pump 24, medicament delivered to flow mixing device 3, mix with the cooling discharge water entered in flow mixing device 3, concurrent life is reacted accordingly.
Ultrafiltration system 7 comprises ultra-filtration equipment 71 and is connected to the ultrafiltration water tank 72 of ultra-filtration equipment 71, wherein ultra-filtration equipment 71 carries out ultrafiltration operation for the cooling discharge water carried by strainer 6, to remove particulate in water, colloid, bacterium, thermal source and organism, cooling discharge water after ultra-filtration equipment 71 ultrafiltration enters ultrafiltration water tank 72, and is delivered in cartridge filter 9 by the cooling discharge water in ultrafiltration water tank 72 by the second topping-up pump 8.
Preferably, between strainer 6 and ultra-filtration equipment 7, be also provided with cartridge filter 9, further the large granular impurity in cooling discharge water removed.
Between water-in 1 and flow mixing device 3, Hand-operated butterfly valve 14 and electric butterfly valve 13 is also provided with, for controlling the keying of whole water inlet process in the present embodiment.
Above embodiment of the present utility model has been described in detail, but described content being only preferred embodiment of the present utility model, can not being considered to for limiting practical range of the present utility model.All equalizations done according to the utility model scope change and improve, and all should still belong within this patent covering scope.
Claims (10)
1. a circulating cooling discharge water recycle device, it is characterized in that: comprise water-in (1), be connected to the flow mixing device (3) of described water-in (1), and the chemical tank (2) to be communicated with flow mixing device (3), medicament in it mixes with the cooling discharge water in flow mixing device (3), the outlet of described flow mixing device (3) is connected with water purifying processing system (4), described water purifying processing system (4) is connected with strainer (6) by the first topping-up pump (5), clear water after filter (6) filters flows into ultrafiltration system (7), described ultrafiltration system (7) is connected with cartridge filter (9) by the second topping-up pump (8), described cartridge filter (9) is connected to reverse osmosis unit (11) by high-pressure pump (10), de-mineralized water after reverse osmosis unit (11) process flows out through water outlet (12) to be recycled.
2. circulating cooling discharge water recycle device according to claim 1, it is characterized in that: described water purifying processing system (4) comprises the flocculation basin (41) set gradually, transition pond (42), settling tank (43) and clean water basin (44), described clean water basin (44) are connected to described first topping-up pump (5), described flocculation basin (41), transition pond (42), the bottom of settling tank (43) and clean water basin (44) is equipped with sedimentation port, described sedimentation port is connected to sludge sump (45) by electric butterfly valve (13).
3. circulating cooling discharge water recycle device according to claim 2, it is characterized in that: described flocculation basin (41) folded plate flocculator for being arranged side by side, its number is four.
4. circulating cooling discharge water recycle device according to claim 3, it is characterized in that: described settling tank (43) tube settler for being arranged side by side, its number is three.
5. circulating cooling discharge water recycle device according to claim 1, it is characterized in that: described chemical tank (2) is three, comprise flocculation chemical tank (21), help solidifying chemical tank (22) and bactericidal agent case (23), described flocculation chemical tank (21), help solidifying chemical tank (22) and bactericidal agent case (23) to be all connected with compound pump (24), and by compound pump (24), medicament is delivered to flow mixing device (3).
6. circulating cooling discharge water recycle device according to claim 1, it is characterized in that: described ultrafiltration system (7) comprises ultra-filtration equipment (71) and is connected to the ultrafiltration water tank (72) of ultra-filtration equipment (71), and described ultrafiltration water tank (72) is connected to described second topping-up pump (8).
7. circulating cooling discharge water recycle device according to claim 6, is characterized in that: be provided with cartridge filter (9) between described strainer (6) and ultra-filtration equipment (71).
8. cooling discharge water recycle device according to claim 1, is characterized in that: be provided with Hand-operated butterfly valve (14) and electric butterfly valve (13) between described water-in (1) and flow mixing device (3).
9. circulating cooling discharge water recycle device according to claim 1, is characterized in that: described flow mixing device (3) is straight-line type flow mixing device.
10. circulating cooling discharge water recycle device according to claim 1, is characterized in that: described strainer (6) is comet fabric filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520915352.XU CN205115196U (en) | 2015-11-17 | 2015-11-17 | Circulative cooling discharge water recycle device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520915352.XU CN205115196U (en) | 2015-11-17 | 2015-11-17 | Circulative cooling discharge water recycle device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205115196U true CN205115196U (en) | 2016-03-30 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520915352.XU Active CN205115196U (en) | 2015-11-17 | 2015-11-17 | Circulative cooling discharge water recycle device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205115196U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105858961A (en) * | 2016-05-09 | 2016-08-17 | 深圳恒通源环保科技有限公司 | Micro-fluctuation filtering system and method |
| CN109231566A (en) * | 2018-10-24 | 2019-01-18 | 广东欧沃环境科技有限公司 | A kind of reverse osmosis membrane secondary utilization device |
-
2015
- 2015-11-17 CN CN201520915352.XU patent/CN205115196U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105858961A (en) * | 2016-05-09 | 2016-08-17 | 深圳恒通源环保科技有限公司 | Micro-fluctuation filtering system and method |
| CN109231566A (en) * | 2018-10-24 | 2019-01-18 | 广东欧沃环境科技有限公司 | A kind of reverse osmosis membrane secondary utilization device |
| CN109231566B (en) * | 2018-10-24 | 2021-06-18 | 广东欧沃环境科技有限公司 | Reverse osmosis membrane reutilization device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |