CN204174022U - A kind of water purification system - Google Patents
A kind of water purification system Download PDFInfo
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- CN204174022U CN204174022U CN201420503321.9U CN201420503321U CN204174022U CN 204174022 U CN204174022 U CN 204174022U CN 201420503321 U CN201420503321 U CN 201420503321U CN 204174022 U CN204174022 U CN 204174022U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 166
- 238000000746 purification Methods 0.000 title claims abstract description 19
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 27
- 238000001914 filtration Methods 0.000 claims abstract description 24
- 230000001954 sterilising effect Effects 0.000 claims abstract description 23
- 239000003610 charcoal Substances 0.000 claims abstract description 14
- 239000008213 purified water Substances 0.000 claims abstract description 10
- 230000008676 import Effects 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 150000003839 salts Chemical class 0.000 claims description 7
- 230000000630 rising effect Effects 0.000 claims description 6
- 239000002351 wastewater Substances 0.000 claims description 6
- 239000006004 Quartz sand Substances 0.000 claims description 4
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 3
- 239000000919 ceramic Substances 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000003245 coal Substances 0.000 claims description 3
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 3
- 229910052748 manganese Inorganic materials 0.000 claims description 3
- 239000011572 manganese Substances 0.000 claims description 3
- 239000004576 sand Substances 0.000 claims description 3
- 238000004659 sterilization and disinfection Methods 0.000 claims description 3
- 230000008901 benefit Effects 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000004743 Polypropylene Substances 0.000 description 12
- 239000012528 membrane Substances 0.000 description 12
- 238000005516 engineering process Methods 0.000 description 10
- 230000006872 improvement Effects 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical group [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 150000002500 ions Chemical class 0.000 description 6
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 5
- 239000003456 ion exchange resin Substances 0.000 description 5
- 229920003303 ion-exchange polymer Polymers 0.000 description 5
- 239000003014 ion exchange membrane Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000003204 osmotic effect Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000005349 anion exchange Methods 0.000 description 3
- 150000001450 anions Chemical class 0.000 description 3
- 238000005341 cation exchange Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000003011 anion exchange membrane Substances 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000010612 desalination reaction Methods 0.000 description 2
- 238000009296 electrodeionization Methods 0.000 description 2
- 239000013505 freshwater Substances 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000013327 media filtration Methods 0.000 description 2
- 230000005012 migration Effects 0.000 description 2
- 238000013508 migration Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- -1 polypropylene Polymers 0.000 description 2
- 230000002829 reductive effect Effects 0.000 description 2
- 238000007493 shaping process Methods 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000011118 depth filtration Methods 0.000 description 1
- 238000000909 electrodialysis Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000009967 tasteless effect Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
A kind of water purification system, comprises the raw water box (1) connected successively, raw water pump (11), more medium filter (2), first charcoal filter (21), softening water strainer (22), SUS304 strainer (23), one-level water pump (31), first-stage reverse osmosis system (3), second charcoal filter (24), PP strainer (25), secondary water pump (41), two-stage reverse osmosis system (4), secondary water tank (5), 3rd water pump (51), EDI filtration unit (6), purifying abacterial water tank (7), purified water water pump (71), sterilizing unit (8), sterilizing unit (8) is connected with water spot (81) with user, the pipeline that SUS304 strainer (23) is connected with one-level water pump (31) is provided with magnetic valve (26) and first flow controller, the pipeline that 3rd water pump (51) is connected with EDI filtration unit (6) is provided with second amount controller, purifying abacterial water tank (7) arranges water level monitor.Its advantage is: long service life, and water treatment efficiency is good, easy to operate, meets environmental requirement.
Description
Technical field
The utility model relates to a kind of water-treatment technology field, especially a kind of water purification system.
Background technology
Existing a kind of patent No. is that CN201320386277.3 name is called that the Chinese utility model patent of " a kind of in order to provide the water treatment device of use for laboratory high purity water " discloses a kind of water treatment device, comprise the medium filter be communicated with by the road successively, automatical softener, raw water box, raw water pump, first accurate filter, one-level high-pressure pump, one-level RO device, secondary high-pressure pump, secondary RO device, RO produces water tank, EDI working shaft, second accurate filter, ultraviolet sterilizer, EDI device, de-gassing vessel, pure water tank, working shaft, TOC ultraviolet sterilizer, polishing mixed bed, millipore filter, reductive agent chemicals dosing plant is provided with between described automatical softener and raw water box, PH chemicals dosing plant is provided with between described one-level RO device and secondary high-pressure pump, the pole water of described EDI device is communicated to seal water tank by the road.The water treatment device of this utility model, adopts cascade filtration by media filtration, osmosis filtration and EDI treatment technology perfect combination, is aided with the protection of interpolation raising to reverse osmosis membrane of reductive agent simultaneously.But filtration unit is arranged on system starting position by this device, lacks buffering, shorten the time of system stable operation, affect filter effect, therefore the structure of this device also needs further improvement.
Summary of the invention
Technical problem to be solved in the utility model provides a kind of use range wide, long service life, the water purification system that water treatment efficiency is good.
The utility model solves the problems of the technologies described above adopted technical scheme: this water purification system, it is characterized in that, comprise successively by raw water box that pipeline is connected, more medium filter, first charcoal filter, softening water strainer, SUS304 strainer, first-stage reverse osmosis system, second charcoal filter, PP strainer, two-stage reverse osmosis system, secondary water tank after cascade filtration, EDI filtration unit, purifying abacterial water tank, sterilizing unit, be connected with water spot from sterilizing unit purified water out with user, the pipeline that described raw water box is connected with more medium filter is provided with raw water pump, the pipeline that SUS304 strainer is connected with first-stage reverse osmosis system is provided with one-level water pump, the pipeline that PP strainer is connected with two-stage reverse osmosis system is provided with secondary water pump, the pipeline that secondary water tank is connected with sterilizing unit is provided with the 3rd water pump, described purifying abacterial water tank is connected with sterilizing unit on pipeline and arranges purified water water pump, the pipeline that described SUS304 strainer is connected with one-level water pump is provided with magnetic valve and first flow controller, the pipeline that 3rd water pump is connected with EDI filtration unit is provided with second amount controller, purifying abacterial water tank arranges water level monitor.
As improvement, described first-stage reverse osmosis system is made up of upper, middle and lower three counter-osmosis devices, in lower two counter-osmosis devices be connected in parallel with from one-level water pump filtered water water pipe out, the water-in of a superposed counter-osmosis device is connected with cleaning water pipe by ground pipeline, first outlet of the counter-osmosis device in top is connected with the second import of the counter-osmosis device in middle part, second outlet and the 3rd of the counter-osmosis device in middle part of the counter-osmosis device in described top are connected by the water inlet pipe of pipeline with the second charcoal filter after exporting and exporting parallel connection with the 4th of the counter-osmosis device in bottom the.
As further improvement, described more medium filter adopts quartz sand, hard coal, porous ceramics or manganese sand can make the filter material of below water outlet turbidity degree of reaching.
Improve again, described more medium filter, the first activated charcoal filter, the second charcoal filter, softening water strainer are respectively arranged with wastewater drainage pipe.
As improvement, described softening water strainer is connected with salt cellar by pipeline, described salt cellar is provided with intake valve and bleed valve.
As improvement, described magnetic valve, first flow controller, second amount controller, water level monitor, raw water pump, one-level water pump, secondary water pump, the 3rd water pump are connected with electrical apparatus control system respectively by circuit.
As further improvement, described PP strainer is connected with secondary water pump and is provided with specific conductivity table on pipeline, and described specific conductivity table is connected with electrical apparatus control system by wire.
As improvement, the rising pipe of described purified water water pump is connected with sterilizing unit with vacuum breaker by diaphragm valve.
As improvement, described sterilizing unit is ultraviolet sterilization apparatus.
As improvement, described two-stage reverse osmosis system is in series by upper and lower two counter-osmosis devices, the import of a rising pipe and top counter-osmosis device of described secondary water pump is connected, the outlet of the counter-osmosis device in bottom is connected by the import of pipeline with secondary water tank, and in bottom, a counter-osmosis device one end is also gone up and is also provided with wastewater drainage pipe.
Compared with prior art, the utility model has the advantage of: reasonable in design, effectively can remove throw out, reduce throw out to the water pump of follow-up use and the wearing and tearing processing film; Adopt cascade filtration by media filtration, osmosis filtration and EDI treatment technology perfect combination, treatment effect is good, and working cost is lower; And adopt electrical apparatus control system, effectively can avoid that flow velocity is too fast or pipeline pressure is excessive, discharge dangerous situation in time, make use safer; Easy to operate, steady in a long-termly can run, meet environmental requirement, be worthy to be popularized.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model embodiment.
Embodiment
Below in conjunction with accompanying drawing embodiment, the utility model is described in further detail.
As shown in Figure 1, the present embodiment water purification system, comprise the raw water box 1 be connected by pipeline successively, more medium filter 2, first charcoal filter 21, softening water strainer 22, SUS304 strainer 23, first-stage reverse osmosis system 3, second charcoal filter 24, PP strainer 25, two-stage reverse osmosis system 4, secondary water tank 5 after cascade filtration, EDI filtration unit 6, purifying abacterial water tank 7, sterilizing unit 8, be connected with water spot 81 from sterilizing unit 8 purified water out with user, the pipeline that described raw water box 1 is connected with more medium filter 2 is provided with raw water pump 11, the pipeline that SUS304 strainer 23 is connected with first-stage reverse osmosis system 3 is provided with one-level water pump 31, the pipeline that PP strainer 25 is connected with two-stage reverse osmosis system 4 is provided with secondary water pump 41, the pipeline that secondary water tank 5 is connected with sterilizing unit 8 is provided with the 3rd water pump 51, described purifying abacterial water tank 7 is connected with sterilizing unit 8 on pipeline and arranges purified water water pump 71, the pipeline that described SUS304 strainer 23 is connected with one-level water pump 31 is provided with magnetic valve 26 and first flow controller, the pipeline that 3rd water pump 51 is connected with EDI filtration unit 6 is provided with second amount controller, purifying abacterial water tank 7 arranges water level monitor.Described first-stage reverse osmosis system 3 is made up of upper, middle and lower three counter-osmosis devices 32, in lower two counter-osmosis devices 32 be connected in parallel with from one-level water pump 31 filtered water water pipe out, the water-in of a superposed counter-osmosis device 32 is connected with cleaning water pipe by ground pipeline, first outlet of the counter-osmosis device in top is connected with the second import of the counter-osmosis device 32 in middle part, second outlet and the 3rd of the counter-osmosis device 32 in middle part of the counter-osmosis device 32 in described top are connected by the water inlet pipe of pipeline with the second charcoal filter 24 after exporting and exporting parallel connection with the 4th of the counter-osmosis device in bottom the.Described more medium filter 2 adopts quartz sand, hard coal, porous ceramics or manganese sand that water outlet turbidity can be made to reach the filter material of less than 3 degree.Described more medium filter 2, first activated charcoal filter 21, second charcoal filter 24, softening water strainer 22 are respectively arranged with wastewater drainage pipe 27.Described softening water strainer 22 is connected with salt cellar 28 by pipeline, and described salt cellar 28 is provided with intake valve and bleed valve.Described magnetic valve 26, first flow controller, second amount controller, water level monitor, raw water pump 11, one-level water pump 31, secondary water pump 41, the 3rd water pump 51 are connected with electrical apparatus control system respectively by circuit.Described PP strainer 25 is connected with secondary water pump 41 and is provided with specific conductivity table 29 on pipeline, and described specific conductivity table 29 is connected with electrical apparatus control system by wire.The rising pipe of described purified water water pump 71 is connected with sterilizing unit 8 with vacuum breaker 73 by diaphragm valve 72.Described sterilizing unit 8 is ultraviolet sterilization apparatus.Described two-stage reverse osmosis system 4 is in series by upper and lower two counter-osmosis devices 32, the import of a rising pipe and top counter-osmosis device 32 of described secondary water pump 41 is connected, the outlet of the counter-osmosis device 32 in bottom is connected by the import of pipeline with secondary water tank 5, and counter-osmosis device 32 one end, one, bottom is also provided with wastewater drainage pipe 27.This water purification system adopts Controlling System centralized Control, coordinates the signal feedback of the equipment such as under meter, tensimeter, water level monitor, Controlling solenoid valve, each pump working, and keeping system is steady in a long-term.
Above-mentioned EDI (Electrodeionization, electrodeionization technology) is a kind of pure water manufacturing technology ion exchange technique, ion exchange membrane technology and ion-conductance migrating technology combined.It is combined at electrodialysis and ion exchange technique, utilizes two end electrodes high pressure that charged ion in water is moved, and coordinate ion exchange resin and selective resin film to move removal with speeding-up ion, thus reach the object of desalt.The ultimate principle of EDI equipment: the principle of work of ion-exchange membrane and ion exchange resin is close, can optionally through ion, and wherein anion-exchange membrane only allows anion-permeable, does not allow cation permeable; And cationic exchange membrane only allows cation permeable, do not allow anion-permeable.Between a pair anion and cation exchange membrane, filling mixture iron exchange resin just defines an EDI unit.The space occupied by mixture iron exchange resin between anion and cation exchange membrane is called as freshwater room.Enumerate together by the EDI unit of some amount, anion-exchange membrane and cationic exchange membrane are alternately arranged, add special ion exchange resin between ion-exchange membrane, its space formed is called as dense hydroecium.Under the promotion of given volts DS, in freshwater room, zwitterion in ion exchange resin moves respectively to positive and negative electrode, and enters dense hydroecium through anion and cation exchange membrane, and the ion simultaneously in feedwater is adsorbed by ion exchange resin and occupies the room stayed due to ion-conductance migration.In fact the migration of ion and absorption are simultaneously and recur.By such process, the ions across ion exchange membrane in feedwater enters into dense hydroecium and is removed and becomes de-mineralized water.
Above-mentioned counter-osmosis device utilizes impressed pressure, makes the water in strong solution overcome the osmotic pressure of organic cellulose semi-permeable membranes and penetrate into dilute side, reach the device making water desalination, desalination.Be called for short RO (Reverse Osmosis Unit).Reverse osmosis is the most accurate embrane method liquid separation technology, working pressure is applied to overcome naturally osmotic pressure in water inlet (strong solution) side, when the working pressure higher than naturally osmotic pressure will reverse from the flow direction of water molecules naturally osmotic when being added on strong solution side, water is produced in the purification that the water molecules part in water inlet (strong solution) becomes dilute solution side by reverse osmosis membrane; Reverse osmosis equipment can stop the organism that all solvability salt and molecular weight are greater than 100, but allow water molecules through, reverse osmosis composite membrane ratio of desalinization is generally greater than 98%.
Above-mentioned PP strainer refers to the strainer of built-in PP filter core, and described PP filter core refers to and a kind of adopts nonpoisonous and tasteless polypropylene to be raw material, through heating and melting, sprays, draws, receives shaping and filter material that is that make.PP filter core has uniform pore diameter, outer thin interior close Depth Filtration structure, and it is high to have filtration efficiency, the good characteristic of acid and alkali-resistance.Effectively can remove the impurity such as suspended substance, particulate, iron rust in liquid.
Above-mentioned SUS304 strainer refers to the cartridge filter using 304 stainless steels as shell.Cartridge filter, also known as accurate filter, stainless steel is mostly adopted to do shell, inner dress filter core (such as PP cotton, nylon, the unlike material such as melt-blown), after being mainly used in multimedium pre-treatment filtration, before the membrane filter plant such as reverse osmosis, ultrafiltration.Be used for the subtitle substance of filtering after multi-medium filtering (such as small quartz sand, activated carbon granule etc.), to guarantee water filtration precision and protective membrane filtering element by the damage of large particulate matter.In-built filter core class of precision can be divided into 0.5 μ s, 1 μ s, 5 μ s, and 10 μ s etc., select different filtering accuracies according to different use occasions, to ensure the safety of rear water outlet precision and guarantee rear class membrane element.Its principle of work is: adopt shaping filter material, and under the effect of the pressure, make stoste by filter material, filter residue is stayed on tube wall, and filtrate is flowed out through filter material, thus reaches the object of filtration.
Claims (10)
1. a water purification system, it is characterized in that, comprise the raw water box (1) be connected by pipeline successively, more medium filter (2), first charcoal filter (21), softening water strainer (22), SUS304 strainer (23), first-stage reverse osmosis system (3), second charcoal filter (24), PP strainer (25), two-stage reverse osmosis system (4), secondary water tank (5) after cascade filtration, EDI filtration unit (6), purifying abacterial water tank (7), sterilizing unit (8), be connected with water spot (81) from sterilizing unit (8) purified water out with user, the pipeline that described raw water box (1) is connected with more medium filter (2) is provided with raw water pump (11), the pipeline that SUS304 strainer (23) is connected with first-stage reverse osmosis system (3) is provided with one-level water pump (31), the pipeline that PP strainer (25) is connected with two-stage reverse osmosis system (4) is provided with secondary water pump (41), the pipeline that secondary water tank (5) is connected with sterilizing unit (8) is provided with the 3rd water pump (51), described purifying abacterial water tank (7) is connected with sterilizing unit (8) on pipeline and arranges purified water water pump (71), the pipeline that described SUS304 strainer (23) is connected with one-level water pump (31) is provided with magnetic valve (26) and first flow controller, the pipeline that 3rd water pump (51) is connected with EDI filtration unit (6) is provided with second amount controller, purifying abacterial water tank (7) arranges water level monitor.
2. water purification system according to claim 1, it is characterized in that: described first-stage reverse osmosis system (3) is made up of upper, middle and lower three counter-osmosis devices (32), in lower two counter-osmosis devices (32) be connected in parallel with from one-level water pump (31) filtered water water pipe out, the water-in of a superposed counter-osmosis device (32) is connected with cleaning water pipe by ground pipeline, first outlet of the counter-osmosis device in top is connected with the second import of the counter-osmosis device (32) in middle part, second outlet and the 3rd of the counter-osmosis device (32) in middle part of the counter-osmosis device (32) in described top are connected by the water inlet pipe of pipeline with the second charcoal filter (24) after exporting and exporting parallel connection with the 4th of the counter-osmosis device in bottom the.
3. water purification system according to claim 2, is characterized in that: described more medium filter (2) adopts quartz sand, hard coal, porous ceramics or manganese sand that water outlet turbidity can be made to reach the filter material of less than 3 degree.
4. water purification system according to claim 3, is characterized in that: described more medium filter (2), the first activated charcoal filter (21), the second charcoal filter (24), softening water strainer (22) are respectively arranged with wastewater drainage pipe (27).
5. according to described water purification system arbitrary in Claims 1-4, it is characterized in that: described softening water strainer (22) is connected with salt cellar (28) by pipeline, and (28) are provided with intake valve and bleed valve with described salt cellar.
6., according to described water purification system arbitrary in Claims 1-4, it is characterized in that: described magnetic valve (26), first flow controller, second amount controller, water level monitor, raw water pump (11), one-level water pump (31), secondary water pump (41), the 3rd water pump (51) are connected with electrical apparatus control system respectively by circuit.
7. water purification system according to claim 6, it is characterized in that: described PP strainer (25) is connected with secondary water pump (41) and is provided with specific conductivity table (29) on pipeline, and described specific conductivity table (29) is connected with electrical apparatus control system by wire.
8. according to described water purification system arbitrary in Claims 1-4, it is characterized in that: the rising pipe of described purified water water pump (71) is connected with sterilizing unit (8) with vacuum breaker (73) by diaphragm valve (72).
9., according to described water purification system arbitrary in Claims 1-4, it is characterized in that: described sterilizing unit (8) is ultraviolet sterilization apparatus.
10. according to described water purification system arbitrary in Claims 1-4, it is characterized in that: described two-stage reverse osmosis system (4) is in series by upper and lower two counter-osmosis devices (32), the import of a rising pipe and top counter-osmosis device (32) of described secondary water pump (41) is connected, the outlet of the counter-osmosis device (32) in bottom is connected by the import of pipeline with secondary water tank (5), and counter-osmosis device (32) one end, one, bottom is also provided with wastewater drainage pipe (27).
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| CN201420503321.9U CN204174022U (en) | 2014-08-28 | 2014-08-28 | A kind of water purification system |
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| CN201420503321.9U CN204174022U (en) | 2014-08-28 | 2014-08-28 | A kind of water purification system |
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| CN204174022U true CN204174022U (en) | 2015-02-25 |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104843919A (en) * | 2015-05-25 | 2015-08-19 | 上海市质子重离子医院有限公司 | Proton heavy ion accelerator high-purity water circulating consumable automatic analysis system |
| CN106495371A (en) * | 2016-12-09 | 2017-03-15 | 天津泰达环保有限公司 | A kind of Boiler water Feeding System system for removing ferrimanganic |
| WO2017079929A1 (en) * | 2015-11-12 | 2017-05-18 | 孙英 | Environment-friendly and energy-saving ultrapure water apparatus for manufacturing glass envelopes |
| CN106927612A (en) * | 2017-04-28 | 2017-07-07 | 桂林医学院 | A kind of reverse osmosis purified water system |
| CN108285220A (en) * | 2018-03-06 | 2018-07-17 | 上海康雷分析仪器有限公司 | A kind of pure water system and with water lines chlorination equipment and technique |
| CN109020025A (en) * | 2018-08-10 | 2018-12-18 | 尹小美 | A kind of filtering and purifying and its working method for water purification |
| CN110604310A (en) * | 2019-10-29 | 2019-12-24 | 朱瑞东 | System and method for extracting food-grade water-soluble silicon element from rice hulls |
| CN111115908A (en) * | 2020-01-20 | 2020-05-08 | 北京德馨康益生物科技有限公司 | Active liquid preparation system |
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2014
- 2014-08-28 CN CN201420503321.9U patent/CN204174022U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104843919A (en) * | 2015-05-25 | 2015-08-19 | 上海市质子重离子医院有限公司 | Proton heavy ion accelerator high-purity water circulating consumable automatic analysis system |
| WO2017079929A1 (en) * | 2015-11-12 | 2017-05-18 | 孙英 | Environment-friendly and energy-saving ultrapure water apparatus for manufacturing glass envelopes |
| CN106495371A (en) * | 2016-12-09 | 2017-03-15 | 天津泰达环保有限公司 | A kind of Boiler water Feeding System system for removing ferrimanganic |
| CN106927612A (en) * | 2017-04-28 | 2017-07-07 | 桂林医学院 | A kind of reverse osmosis purified water system |
| CN108285220A (en) * | 2018-03-06 | 2018-07-17 | 上海康雷分析仪器有限公司 | A kind of pure water system and with water lines chlorination equipment and technique |
| CN108285220B (en) * | 2018-03-06 | 2024-01-26 | 上海康雷分析仪器有限公司 | Water purification system and disinfection device and process for water pipeline |
| CN109020025A (en) * | 2018-08-10 | 2018-12-18 | 尹小美 | A kind of filtering and purifying and its working method for water purification |
| CN110604310A (en) * | 2019-10-29 | 2019-12-24 | 朱瑞东 | System and method for extracting food-grade water-soluble silicon element from rice hulls |
| CN111115908A (en) * | 2020-01-20 | 2020-05-08 | 北京德馨康益生物科技有限公司 | Active liquid preparation system |
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