CN204848505U - Dilute water circulating system - Google Patents
Dilute water circulating system Download PDFInfo
- Publication number
- CN204848505U CN204848505U CN201520214847.XU CN201520214847U CN204848505U CN 204848505 U CN204848505 U CN 204848505U CN 201520214847 U CN201520214847 U CN 201520214847U CN 204848505 U CN204848505 U CN 204848505U
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- China
- Prior art keywords
- water
- pump
- reverse osmosis
- circulation system
- circulating system
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Abstract
The utility model provides a dilute water circulating system, includes former water circulating system, regeneration water circulating system, ultrafiltration water circulating system, reverse osmosis water circulating system and workshop water circulating system, former water circulating system the delivery port with regeneration water circulating system the water inlet be linked together through the raw water pump, regeneration water circulating system's delivery port and ultrafiltration water circulating system's water inlet be linked together, ultrafiltration water circulating system's delivery port and reverse osmosis water circulating system's water inlet be linked together, reverse osmosis water circulating system's delivery port and workshop water circulating system's water inlet and former water circulating system's water inlet be linked together. The utility model discloses it changing the circulation into and supplies water to supply water traditional one way, the supply each with incessantly flowing in 24 hours in the airtight pipeline of circulation all the time before the water spot, can keep the ozone content in the pipeline not reduce like this, keep the sterilization function, avoided water to produce the risk of bacterium totally under quiescent condition simultaneously.
Description
Technical field
The utility model relates to a kind of service water supply system, particularly relates to the AES product dilution water recycle system.
Background technology
In tradition process for sulfonation, the process water that uses is single-pipeline supply, everywhere pipeline and with the dead angle of water spot too much, to cause in actual moving process bacteria breed in process water, and bring products into, product sanitary grade does not reach standard-required.
Summary of the invention
The utility model, in order to solve the problems of the technologies described above, provides a kind of dilution water recycle system being applied in sulfonation workshop.
Technical solution adopted in the utility model is:
A kind of dilution water recycle system, comprises former water circulation system, the reuse water recycle system, ultrafiltration water circulation system, the reverse osmosis water recycle system and workshop water circulation system; The water outlet of described former water circulation system is connected by raw water pump with the water inlet of the reuse water recycle system, the water outlet of the described reuse water recycle system is connected with the water inlet of ultrafiltration water circulation system, the water outlet of described ultrafiltration water circulation system is connected with the water inlet of the reverse osmosis water recycle system, and the water outlet of the described reverse osmosis water recycle system is connected with the water inlet of former water circulation system with the water inlet of workshop water circulation system.
Described former water circulation system comprises former water pot and former water-circulating pump, and described former water circulation system also comprises sterilant adding set, and described sterilant adding set is separately positioned on the water inlet pipeline of former water pot and the pipeline of former water-circulating pump water outlet.
Described workshop water circulation system comprises pure water tank, workshop water spot and working shaft, and pure water tank comprises pure water tank A and pure water tank B, and the pure water in pure water tank is transported to workshop water spot by pipeline by described working shaft.
The described dilution water recycle system also comprises ozone generation circulation device, described ozone generation circulation device is arranged in described workshop water circulation system, described ozone generation circulation device comprises ozonizer and cycle of ozone pump, the output tube of ozonizer is connected on the water inlet of pure water tank, and the pure water being dissolved with ozone pumps in pure water tank by cycle of ozone pump again.
The described reuse water recycle system comprises sandfiltration pot, softening agent A, softening agent B, regenerative pump and salt box, the water inlet of described sandfiltration pot is connected with former water circulation system by raw water pump, the water outlet of sandfiltration pot connects the water inlet of softening agent A and softening agent B respectively, softening agent A is connected with salt box and ultrafiltration water circulation system with the water outlet of softening agent B, and the recirculated water in salt box is back to softening agent A and softening agent B by regenerative pump.
Described ultrafiltration water circulation system comprises essence and filters filter, ultra-filtration equipment, middle water pot, middle water pump and ultrafiltration recoil pump, essence filters the water inlet of filter and is connected with the water outlet of softening agent B with the softening agent A of the reuse water recycle system, the water outlet that essence filters filter is connected with the water inlet of ultra-filtration equipment with middle water pot, the water outlet of middle water pot is connected with ultrafiltration recoil pump and middle water pump, the water outlet of ultrafiltration recoil pump is connected with the water outlet of ultra-filtration equipment, and the water outlet of middle water pump is connected on the water inlet of the reverse osmosis water recycle system.
The described reverse osmosis water recycle system, comprise security strainer, first-stage reverse osmosis pump, first-stage reverse osmosis device, two-pass reverse osmosis pump and second level reverse osmosis apparatus, the water inlet of described security strainer is connected with the water outlet of the middle water pump in ultrafiltration water circulation system, the water outlet of security strainer is connected with the water inlet of first-stage reverse osmosis device by first-stage reverse osmosis pump, the water outlet of first-stage reverse osmosis device is connected with second level reverse osmosis apparatus by two-pass reverse osmosis pump, the water outlet of second level reverse osmosis apparatus is connected respectively to the water inlet of former water circulation system and the water inlet of workshop water circulation system.
The beneficial effects of the utility model: traditional single channel supplies water and changes periodical feeding into by the utility model, within before supplying each water spot 24 hours in circulation closed pipeline all the time, do not arrhea dynamic, the ozone content in pipeline can be kept like this not reduce, maintain sterilizing function, completely avoid water under static state diseaseful risk simultaneously.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model dilution water recycle system.
Embodiment
A kind of dilution water recycle system, comprises former water circulation system, the reuse water recycle system, ultrafiltration water circulation system, the reverse osmosis water recycle system and workshop water circulation system; The water outlet of described former water circulation system is connected by raw water pump with the water inlet of the reuse water recycle system, the water outlet of the described reuse water recycle system is connected with the water inlet of ultrafiltration water circulation system, the water outlet of described ultrafiltration water circulation system is connected with the water inlet of the reverse osmosis water recycle system, and the water outlet of the described reverse osmosis water recycle system is connected with the water inlet of former water circulation system with the water inlet of workshop water circulation system.
Tap water supply passes into the former water pot 2 in former water circulation system and adds former water germicide, the recirculated water adding sterilant is pumped in former water pot 2 by former water-circulating pump 3 by the water in former water pot 2, squeeze in sandfiltration pot 6 by raw water pump 5 after former water pot 2 flows out, softening agent A7 and softening agent B8 is entered into after flowing through sandfiltration pot 6, recirculated water enters salt box 10 after softening agent, get back in softening agent A and softening agent B by regenerative pump 9 reflux again, the circulating water flow flowed out from softening agent enters in ultra-filtration equipment 18 and middle water pot 12 through accurate filter 21, the recirculated water entering ultra-filtration equipment 18 also flows in middle water pot 12 after ultrafiltration, recirculated water part in middle water pot 12 is squeezed in ultra-filtration equipment 18 by ultrafiltration recoil pump 13, the recirculated water of another part squeezes into security strainer 14 by middle water pump 15, workshop water circulation system and former water circulation system is entered again through first-stage reverse osmosis device 17 and second level reverse osmosis apparatus 20, the recirculated water entering workshop water circulation system is stored in pure water tank A22 and pure water tank B23, by cycle of ozone pump 24, the recirculated water being dissolved with ozone is back in pure water tank A22 and pure water tank B23, by working shaft 26, recirculated water is transported to workshop water spot 11 from pure water tank.
Claims (7)
1. the dilution water recycle system, is characterized in that, comprises former water circulation system, the reuse water recycle system, ultrafiltration water circulation system, the reverse osmosis water recycle system and workshop water circulation system; The water outlet of described former water circulation system is connected by raw water pump with the water inlet of the reuse water recycle system, the water outlet of the described reuse water recycle system is connected with the water inlet of ultrafiltration water circulation system, the water outlet of described ultrafiltration water circulation system is connected with the water inlet of the reverse osmosis water recycle system, and the water outlet of the described reverse osmosis water recycle system is connected with the water inlet of former water circulation system with the water inlet of workshop water circulation system.
2. the dilution water recycle system according to claim 1, it is characterized in that, described former water circulation system comprises former water pot (2) and former water-circulating pump (3), described former water circulation system also comprises the first sterilant adding set (1) and the second sterilant adding set (4), the first described sterilant adding set is arranged on the water inlet pipeline of former water pot (2), and the second sterilant adding set (4) is arranged on the pipeline of former water-circulating pump (3) water outlet.
3. the dilution water recycle system according to claim 1, it is characterized in that, described workshop water circulation system comprises pure water tank, workshop water spot (11) and working shaft (26), pure water tank comprises pure water tank A (22) and pure water tank B (23), and the pure water in pure water tank is transported to workshop water spot (11) by pipeline by described working shaft (26).
4. the dilution water recycle system according to claim 3, it is characterized in that, the described dilution water recycle system also comprises ozone generation circulation device, described ozone generation circulation device is arranged in described workshop water circulation system, described ozone generation circulation device comprises ozonizer (25) and cycle of ozone pump (24), the output tube of ozonizer (25) is connected on the water inlet of pure water tank, and the pure water being dissolved with ozone pumps in pure water tank by cycle of ozone pump (24) again.
5. the dilution water recycle system according to claim 1, it is characterized in that, the described reuse water recycle system comprises sandfiltration pot (6), softening agent A (7), softening agent B (8), regenerative pump (9) and salt box (10), the water inlet of described sandfiltration pot (6) is connected with former water circulation system by raw water pump (5), the water outlet of sandfiltration pot (6) connects the water inlet of softening agent A (7) and softening agent B (8) respectively, softening agent A (7) is connected with salt box (10) and ultrafiltration water circulation system with the water outlet of softening agent B (8), recirculated water in salt box (10) is back to softening agent A (7) and softening agent B (8) by regenerative pump (9).
6. the dilution water recycle system according to claim 1, it is characterized in that, described ultrafiltration water circulation system comprises essence and filters filter (21), ultra-filtration equipment (18), middle water pot (12), middle water pump (15) and ultrafiltration recoil pump (13), the water inlet that essence filters filter (21) is connected with the water outlet of reuse water recycle system softening agent A (7) with softening agent B (8), the water outlet that essence filters filter (21) is connected with the water inlet of ultra-filtration equipment (18) with middle water pot (12), the water outlet of middle water pot (12) is connected with ultrafiltration recoil pump (13) and middle water pump (15), the water outlet of ultrafiltration recoil pump (13) is connected with the water outlet of ultra-filtration equipment (18), the water outlet of middle water pump (15) is connected on the water inlet of the reverse osmosis water recycle system.
7. the dilution water recycle system according to claim 1, it is characterized in that, the described reverse osmosis water recycle system, comprise cartridge filter (14), first-stage reverse osmosis pump (16), first-stage reverse osmosis device (17), two-pass reverse osmosis pump (19) and second level reverse osmosis apparatus (20), the water inlet of described security strainer (14) is connected with the water outlet of the middle water pump (15) in ultrafiltration water circulation system, the water outlet of security strainer (14) is connected with the water inlet of first-stage reverse osmosis device (17) by first-stage reverse osmosis pump (16), the water outlet of first-stage reverse osmosis device (17) is connected with second level reverse osmosis apparatus (20) by two-pass reverse osmosis pump (19), the water outlet of second level reverse osmosis apparatus (20) is connected respectively to the water inlet of former water circulation system and the water inlet of workshop water circulation system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520214847.XU CN204848505U (en) | 2015-04-09 | 2015-04-09 | Dilute water circulating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520214847.XU CN204848505U (en) | 2015-04-09 | 2015-04-09 | Dilute water circulating system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204848505U true CN204848505U (en) | 2015-12-09 |
Family
ID=54739077
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520214847.XU Expired - Fee Related CN204848505U (en) | 2015-04-09 | 2015-04-09 | Dilute water circulating system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204848505U (en) |
-
2015
- 2015-04-09 CN CN201520214847.XU patent/CN204848505U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151209 Termination date: 20180409 |