CN205170610U - Circulation of adopting ozone biological activity charcoal deep purification system of directly drinking water - Google Patents
Circulation of adopting ozone biological activity charcoal deep purification system of directly drinking water Download PDFInfo
- Publication number
- CN205170610U CN205170610U CN201520834095.7U CN201520834095U CN205170610U CN 205170610 U CN205170610 U CN 205170610U CN 201520834095 U CN201520834095 U CN 201520834095U CN 205170610 U CN205170610 U CN 205170610U
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- water
- tank
- multiway valve
- programmable controller
- controller plc
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- Withdrawn - After Issue
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- 239000003610 charcoal Substances 0.000 title claims abstract description 36
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 238000000746 purification Methods 0.000 title claims abstract description 18
- 239000003651 drinking water Substances 0.000 title claims abstract description 12
- 235000020188 drinking water Nutrition 0.000 title abstract description 3
- 230000004071 biological effect Effects 0.000 title abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 203
- 238000006243 chemical reaction Methods 0.000 claims abstract description 33
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 31
- 238000005115 demineralization Methods 0.000 claims abstract description 26
- 230000002328 demineralizing effect Effects 0.000 claims abstract description 26
- 239000004575 stone Substances 0.000 claims abstract description 23
- 238000011010 flushing procedure Methods 0.000 claims description 33
- 238000001914 filtration Methods 0.000 claims description 24
- 230000003020 moisturizing effect Effects 0.000 claims description 15
- 238000004140 cleaning Methods 0.000 claims description 12
- 230000008929 regeneration Effects 0.000 claims description 12
- 238000011069 regeneration method Methods 0.000 claims description 12
- 150000003839 salts Chemical class 0.000 claims description 7
- 239000008399 tap water Substances 0.000 claims description 7
- 235000020679 tap water Nutrition 0.000 claims description 7
- 239000000706 filtrate Substances 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 4
- 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 claims description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims description 3
- 241000894006 Bacteria Species 0.000 claims description 3
- 235000013162 Cocos nucifera Nutrition 0.000 claims description 3
- 244000060011 Cocos nucifera Species 0.000 claims description 3
- 241000700605 Viruses Species 0.000 claims description 3
- 125000001309 chloro group Chemical group Cl* 0.000 claims description 3
- 238000006073 displacement reaction Methods 0.000 claims description 3
- 239000011630 iodine Substances 0.000 claims description 3
- 229910052740 iodine Inorganic materials 0.000 claims description 3
- 239000003456 ion exchange resin Substances 0.000 claims description 3
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 3
- 239000000693 micelle Substances 0.000 claims description 3
- 238000005554 pickling Methods 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 3
- 229920005989 resin Polymers 0.000 claims description 3
- 239000010865 sewage Substances 0.000 claims description 3
- 238000004659 sterilization and disinfection Methods 0.000 claims description 3
- 238000006276 transfer reaction Methods 0.000 claims description 3
- 238000003809 water extraction Methods 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 235000010755 mineral Nutrition 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000003245 working effect Effects 0.000 description 2
- 208000003251 Pruritus Diseases 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007803 itching Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 210000003296 saliva Anatomy 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses a circulation of adopting ozone biological activity charcoal deep purification system of directly drinking water solves the pure water and is not conform to healthy demand, and water purification unit's work efficiency is low, problem that filter core life is short. The running water filters jar (2) through physics and filters laggard incomes a water demineralization jar (3), has solenoid valve (4) and venturi (5) on the connecting pipe of water demineralization jar and reaction water tank (6), and the export of reaction water tank is connected with activated carbon canister (8) through booster pump (7) and first check valve, activated carbon canister export and active carbon, very stone jar (9) be connected, the active carbon, very the stone jar be connected with inclosed no tower water supply jar (11) through precision filter (10), second check valve.
Description
technical field:
The utility model is relevant with water purifying plant.
background technology:
Current water purifying plant is on the market nearly all manufacture pure water, and the waste of water is surprising, and pure water is not containing mineral substance, and pH is slightly acidic, does not meet health demand, the inefficiency of water purifying plant, and filter core is short for work-ing life.
utility model content:
It is high that the purpose of this utility model is to provide a kind of former water use efficiency, and make water containing mineral substance, weakly alkaline, working efficiency is high, the circulation direct-drinking water advanced purification system of the employing ozone biological activated carbon of filter core long service life.
The utility model is achieved in that
Adopt the circulation direct-drinking water advanced purification system of ozone biological activated carbon, tap water enters water demineralization tank 3 after physical filtering tank 2 filters, water demineralization tank and the pipe connecting of reaction water tank 6 there are magnetic valve 4 and Venturi tube 5, reaction water tank 6 exports and is connected with charcoal canister 8 with the second vacuum breaker through topping-up pump 7, charcoal canister outlet and gac, strange stone tank 9 connects, gac, strange stone tank is through accurate filter 10, second vacuum breaker is connected with airtight non-tower water supply tank 11, physical filtering tank 2 is made up of the filtrate of uniform diameter or the filter screen of uniform pore diameter, larger impurity in interception tap water, water after first step physical filtering tank filters enters second stage water demineralization tank, water demineralization tank is made up of ion exchange resin, reduce water hardness, the ozone gas produced by ozonizer by Venturi tube is sucked and mixes with water, mixed water enters third stage reaction water tank, reaction water tank is the container of band thrust-augmenting nozzle, ozone and the abundant mass transfer reaction of water in reaction water tank, kill bacteria virus, decompose larger molecular organics, remove chlorine residue, form ozone water, adopt topping-up pump by the water suction fourth stage charcoal canister in reaction water tank, the ozone water that the gac of fourth stage charcoal canister and the third stage react water tank forms ozone biological activated carbon, deep purifying is carried out to water quality, level V gac, strange stone tank adopts the pickling cocoanut active charcoal of high iodine number again to purify water quality, and improve the mouthfeel of water, strange stone filtrate is adopted to discharge far ir ray, macromolecular mass water is become small-micelle water, 6th grade of accurate filter adopts precision to be that the foldable filter element of 0.22-0.5 micron carries out secondary filter, control the opacity of water outlet, after the process of the first six grade, water purification enters in an airtight non-tower water supply tank, for user's water extraction is for certain pressure, the water outlet of non-tower water supply tank adopts overflow-type ultraviolet ray sterilizer to carry out sterilization and disinfection again to water purification, by direct-drinking water pipeline, water purification is delivered to the use water spot of user, with the sewage of water spot again from the water-in entering Venturi tube with the circulating line of water spot through motorized valve, the time switch of motorized valve 13 is controlled by programmable controller PLC, realize the water timing automatic circulation in pipeline, keep the freshness of the water in pipeline.
Running water pipe there is the second pressure transmitter 1, non-tower water supply tank outlet has the second pressure transmitter 12, reaction water tank has the 3rd pressure transmitter and overflow alarm sensor, adopts the programmable controller PLC multiway valve controlled on tank body to realize the auto-flushing of physical filtering tank, water demineralization tank, charcoal canister, gac, strange stone tank; The gap periods of rinsing and the time of flushing have pre-set in programmable controller PLC, after having arrived flushing cycle time point, programmable controller PLC sends flushes instructions to the second multiway valve on physical filtering tank, second multiway valve automatically switches to flushing state, carry out the flushing of physical filtering tank, after arriving flush time, programmable controller PLC sends and rinses END instruction to the second multiway valve on physical filtering tank, second multiway valve automatically switches to normally water state processed, terminate cleaning
After physical filtering tank has rinsed, programmable controller PLC sends flushes instructions to the second multiway valve on water demineralization tank, second multiway valve automatically switches and enters flushing state, after flush time arrives, programmable controller PLC sends softening regeneration instructions to the second multiway valve, second multiway valve automatically switches to softening reproduced state, when this state, salts solution in regeneration salt cellar sucks in water demineralization tank by the second multiway valve, regeneration displacement is carried out to soften resin, after regeneration time swap arrives, programmable controller PLC sends flushes instructions again to the second multiway valve, second multiway valve automatically switches to flushing state, again rinse, after flush time arrives again, programmable controller PLC sends and rinses END instruction to the second multiway valve, second multiway valve enters normally water state processed automatically, terminate cleaning,
After water demineralization tank has rinsed, programmable controller PLC sends flushes instructions to the 3rd multiway valve on charcoal canister, 3rd multiway valve automatically switches to flushing state, programmable controller PLC sends instruction simultaneously, Controlling solenoid valve 4 is opened to the moisturizing of reaction water tank, topping-up pump starts to charcoal canister moisturizing, realize the flushing of charcoal canister, after arriving when rinsing, programmable controller PLC sends and rinses stop instruction to multiway valve, multiway valve automatically switches to normally water state processed, programmable controller PLC sends instruction shut electromagnetic valve 4 and water pump simultaneously, terminate cleaning.
After charcoal canister has rinsed, programmable controller PLC sends flushes instructions to gac, the 4th multiway valve on strange stone tank, 4th multiway valve automatically switches to flushing state, programmable controller PLC sends instruction simultaneously, Controlling solenoid valve 4 is opened to the moisturizing of reaction water tank, topping-up pump starts through the moisturizing of rear class charcoal canister, realize gac, the flushing of strange stone tank, after arriving when rinsing, programmable controller PLC sends and rinses stop instruction to the 4th multiway valve, 4th multiway valve automatically switches to normally water state processed, programmable controller PLC sends instruction shut electromagnetic valve 4 and topping-up pump 7 simultaneously, terminate cleaning.
The utility model has following advantage:
One, water saving: the utility model adopts and automatically controls to rinse, and washing water quantity consumption is few, is about 3%, and general reverse osmosis water treatment system is because film precision is high, needs to rinse at any time, rinses and consumes water up to 50%-70%.
Two, production water is alkalescent mineral substance water, by the process of the utility model system, can not remove the mineral substance in water and trace element, ensures that water outlet is alkalescent water by ozone biological activated carbon and level V acid-washed active carbon.
Three, running cost is low, product after ozone decomposed is oxygen, greatly can increase the oxygen level in water, impel the 4th, microbial growth of itching well in level V charcoal canister, one deck microbial film is formed at activated carbon surface, microbial film can objectionable impurities in degradation water, reduce the load of gac, make extend one times the work-ing life of gac, the filter material replacement cycle reaches more than 12 months, and general water treating equipment after 3-6 months, just need more renew cartridge in use, thereby facilitating operation and maintenance, also reduce running cost.
State, applied range, adopt the terminal drinking water system of ozonation and biological activated carbon system, and being applicable to any take tap water as the terminal water conditioning of former water.
accompanying drawing illustrates:
Fig. 1 is system flowchart of the present utility model.
Fig. 2 is system front view of the present utility model.
Fig. 3 is the vertical view of Fig. 2.
Fig. 4 is the rear view of Fig. 2.
Fig. 5 is the shaft side figure of Fig. 2.
Fig. 6 is the shaft side figure of Fig. 4.
Fig. 7 is schematic circuit diagram of the present utility model.
embodiment:
Adopt the circulation direct-drinking water advanced purification system of ozone biological activated carbon, tap water enters water demineralization tank 3 after physical filtering tank 2 filters, water demineralization tank and the pipe connecting of reaction water tank 6 there are magnetic valve 4 and Venturi tube 5, reaction water tank 6 exports and is connected with charcoal canister 8 with the second vacuum breaker through topping-up pump 7, charcoal canister outlet and gac, strange stone tank 9 connects, gac, strange stone tank is through accurate filter 10, second vacuum breaker is connected with airtight non-tower water supply tank 11, physical filtering tank 2 is made up of the filtrate of uniform diameter or the filter screen of uniform pore diameter, larger impurity in interception tap water, water after first step physical filtering tank filters enters second stage water demineralization tank, water demineralization tank is made up of ion exchange resin, reduce water hardness, the ozone gas produced by ozonizer by Venturi tube is sucked and mixes with water, mixed water enters third stage reaction water tank, reaction water tank is the container of band thrust-augmenting nozzle, ozone and the abundant mass transfer reaction of water in reaction water tank, kill bacteria virus, decompose larger molecular organics, remove chlorine residue, form ozone water, adopt topping-up pump by the water suction fourth stage charcoal canister in reaction water tank, the ozone water that the gac of fourth stage charcoal canister and the third stage react water tank forms ozone biological activated carbon, deep purifying is carried out to water quality, level V gac, strange stone tank adopts the pickling cocoanut active charcoal of high iodine number again to purify water quality, and improve the mouthfeel of water, strange stone filtrate is adopted to discharge far ir ray, macromolecular mass water is become small-micelle water, 6th grade of accurate filter adopts precision to be that the foldable filter element of 0.22-0.5 micron carries out secondary filter, control the opacity of water outlet, after the process of the first six grade, water purification enters in an airtight non-tower water supply tank, for user's water extraction is for certain pressure, the water outlet of non-tower water supply tank adopts overflow-type ultraviolet ray sterilizer to carry out sterilization and disinfection again to water purification, by direct-drinking water pipeline, water purification is delivered to the use water spot of user, with the sewage of water spot again from the water-in entering Venturi tube with the circulating line of water spot through motorized valve, the time switch of motorized valve 13 is controlled by programmable controller PLC, realize the water timing automatic circulation in pipeline, keep the freshness of the water in pipeline.
Running water pipe there is the second pressure transmitter 1, non-tower water supply tank outlet has the second pressure transmitter 12, reaction water tank has the 3rd pressure transmitter and overflow alarm sensor, adopts the programmable controller PLC multiway valve controlled on tank body to realize the auto-flushing of physical filtering tank, water demineralization tank, charcoal canister, gac, strange stone tank; The gap periods of rinsing and the time of flushing have pre-set in programmable controller PLC, after having arrived flushing cycle time point, programmable controller PLC sends flushes instructions to the second multiway valve on physical filtering tank, second multiway valve automatically switches to flushing state, carry out the flushing of physical filtering tank, after arriving flush time, programmable controller PLC sends and rinses END instruction to the second multiway valve on physical filtering tank, second multiway valve automatically switches to normally water state processed, terminate cleaning
After physical filtering tank has rinsed, programmable controller PLC sends flushes instructions to the second multiway valve on water demineralization tank, second multiway valve automatically switches and enters flushing state, after flush time arrives, programmable controller PLC sends softening regeneration instructions to the second multiway valve, second multiway valve automatically switches to softening reproduced state, when this state, second multiway valve will regenerate salt cellar, and (commodity selected by regeneration salt cellar, model is JYYT-60U) in salts solution suck in water demineralization tank, regeneration displacement is carried out to soften resin, after regeneration time swap arrives, programmable controller PLC sends flushes instructions again to the second multiway valve, second multiway valve automatically switches to flushing state, again rinse, after flush time arrives again, programmable controller PLC sends and rinses END instruction to the second multiway valve, second multiway valve enters normally water state processed automatically, terminate cleaning,
After water demineralization tank has rinsed, programmable controller PLC sends flushes instructions to the 3rd multiway valve on charcoal canister, 3rd multiway valve automatically switches to flushing state, programmable controller PLC sends instruction simultaneously, Controlling solenoid valve 4 is opened to the moisturizing of reaction water tank, topping-up pump starts to charcoal canister moisturizing, realize the flushing of charcoal canister, after arriving when rinsing, programmable controller PLC sends and rinses stop instruction to multiway valve, multiway valve automatically switches to normally water state processed, programmable controller PLC sends instruction shut electromagnetic valve 4 and water pump simultaneously, terminate cleaning.
After charcoal canister has rinsed, programmable controller PLC sends flushes instructions to gac, the 4th multiway valve on strange stone tank, 4th multiway valve automatically switches to flushing state, programmable controller PLC sends instruction simultaneously, Controlling solenoid valve 4 is opened to the moisturizing of reaction water tank, topping-up pump starts through the moisturizing of rear class charcoal canister, realize gac, the flushing of strange stone tank, after arriving when rinsing, programmable controller PLC sends and rinses stop instruction to the 4th multiway valve, 4th multiway valve automatically switches to normally water state processed, programmable controller PLC sends instruction shut electromagnetic valve 4 and topping-up pump 7 simultaneously, terminate cleaning.
Control brief analysis:
1, pressure signal 1 – second pressure transmitter: detect tap water hydraulic, when hydraulic pressure is lower than 0.1MPa, carry out undervoltage warning, complete machine quits work, proterctive equipment (excessive low water level protection).
2, pressure signal-the second pressure transmitter: detect end non-tower water supply tank hydraulic pressure, when pressure is lower than set(ting)value, controls topping-up pump and runs to non-tower water supply tank ftercompction, when pressure arrives high-water, controls topping-up pump and shuts down, stop moisturizing.
3, pressure signal 3-the three pressure transmitter: the liquid level of detection reaction water tank, high-low water level drop, at about 0.5 meter, accurately controls, when the low-water level value of water level lower than setting magnetic valve 4 open, ozonizer work, to reaction Water in Water Tank moisturizing; When water level arrives high-water set(ting)value, shut electromagnetic valve 4 and ozonizer, stop moisturizing.
4, overflow alarm sensor: detection reaction water tank overflow saliva stream (defencive function of pressure signal 3), when reacting water tank overflow port spilling water, controlling shut electromagnetic valve 4, stopping water inlet.
5, internal recycle: the internal recycling of operating device, avoid " stagnant water " phenomenon, during internal recycle, PLC sends recursion instruction, motorized valve is opened, ozonizer and topping-up pump are started working, and magnetic valve 4 cuts out, and the water in the non-tower water supply tank of rear end enters reaction water tank by pipeline and carries out reprocessing, realize internal recycling, cycling time, then PLC sent loop ends instruction, and motorized valve, ozonizer and topping-up pump are closed and entered normally water state processed.
Claims (2)
1. adopt the circulation direct-drinking water advanced purification system of ozone biological activated carbon, it is characterized in that tap water enters water demineralization tank (3) after physical filtering tank (2) filters, water demineralization tank and the pipe connecting of reaction water tank (6) there are magnetic valve (4) and Venturi tube (5), reaction tank outlet is connected with charcoal canister (8) with the first vacuum breaker through topping-up pump (7), charcoal canister outlet and gac, strange stone tank (9) connects, gac, strange stone tank is through accurate filter (10), second vacuum breaker is connected with airtight non-tower water supply tank (11), physical filtering tank is made up of the filtrate of uniform diameter or the filter screen of uniform pore diameter, water after first step physical filtering tank filters enters second stage water demineralization tank, water demineralization tank is made up of ion exchange resin, reduce water hardness, the ozone gas produced by ozonizer by Venturi tube is sucked and mixes with water, mixed water enters third stage reaction water tank, reaction water tank is the container of band thrust-augmenting nozzle, ozone and the abundant mass transfer reaction of water in reaction water tank, kill bacteria virus, decompose larger molecular organics, remove chlorine residue, form ozone water, adopt topping-up pump by the water suction fourth stage charcoal canister in reaction water tank, the ozone water that the gac of fourth stage charcoal canister and the third stage react water tank forms ozone biological activated carbon, deep purifying is carried out to water quality, level V gac, strange stone tank adopts the pickling cocoanut active charcoal of high iodine number again to purify water quality, and improve the mouthfeel of water, strange stone filtrate is adopted to discharge far ir ray, macromolecular mass water is become small-micelle water, 6th grade of accurate filter adopts precision to be that the foldable filter element of 0.22-0.5 micron carries out secondary filter, control the opacity of water outlet, after the process of the first six grade, water purification enters in an airtight non-tower water supply tank, for user's water extraction is for certain pressure, the water outlet of non-tower water supply tank adopts overflow-type ultraviolet ray sterilizer to carry out sterilization and disinfection again to water purification, by direct-drinking water pipeline, water purification is delivered to the use water spot of user, with the sewage of water spot again from the water-in entering Venturi tube with the circulating line of water spot through motorized valve, the time switch of motorized valve (13) is controlled by programmable controller PLC, realize the water timing automatic circulation in pipeline, keep the freshness of the water in pipeline.
2. the circulation direct-drinking water advanced purification system of employing ozone biological activated carbon according to claim 1, it is characterized in that running water pipe there is the first pressure transmitter (1), non-tower water supply tank outlet has the second pressure transmitter (12), reaction water tank has the 3rd pressure transmitter and overflow alarm sensor, adopts the programmable controller PLC multiway valve controlled on tank body to realize the auto-flushing of physical filtering tank, water demineralization tank, charcoal canister, gac, strange stone tank, the gap periods of rinsing and the time of flushing have pre-set in programmable controller PLC, after having arrived flushing cycle time point, programmable controller PLC sends flushes instructions to the first multiway valve on physical filtering tank, first multiway valve automatically switches to flushing state, carry out the flushing of physical filtering tank, after arriving flush time, programmable controller PLC sends and rinses END instruction to the first multiway valve on physical filtering tank, first multiway valve automatically switches to normally water state processed, terminate cleaning, after physical filtering tank has rinsed, programmable controller PLC sends flushes instructions to the second multiway valve on water demineralization tank, second multiway valve automatically switches and enters flushing state, after flush time arrives, programmable controller PLC sends softening regeneration instructions to the second multiway valve, second multiway valve automatically switches to softening reproduced state, when this state, salts solution in regeneration salt cellar sucks in water demineralization tank by the second multiway valve, regeneration displacement is carried out to soften resin, after regeneration time swap arrives, programmable controller PLC sends flushes instructions again to the second multiway valve, second multiway valve automatically switches to flushing state, again rinse, after flush time arrives again, programmable controller PLC sends and rinses END instruction to the second multiway valve, second multiway valve enters normally water state processed automatically, terminate cleaning, after water demineralization tank has rinsed, programmable controller PLC sends flushes instructions to the 3rd multiway valve on charcoal canister, 3rd multiway valve automatically switches to flushing state, programmable controller PLC sends instruction simultaneously, Controlling solenoid valve (4) is opened to the moisturizing of reaction water tank, topping-up pump starts to charcoal canister moisturizing, realize the flushing of charcoal canister, after arriving when rinsing, programmable controller PLC sends and rinses stop instruction to multiway valve, multiway valve automatically switches to normally water state processed, programmable controller PLC sends instruction shut electromagnetic valve and water pump simultaneously, terminate cleaning, after charcoal canister has rinsed, programmable controller PLC sends flushes instructions to gac, the 4th multiway valve on strange stone tank, 4th multiway valve automatically switches to flushing state, programmable controller PLC sends instruction simultaneously, Controlling solenoid valve (4) is opened to the moisturizing of reaction water tank, topping-up pump starts through the moisturizing of rear class charcoal canister, realize gac, the flushing of strange stone tank, after arriving when rinsing, programmable controller PLC sends and rinses stop instruction to the 4th multiway valve, 4th multiway valve automatically switches to normally water state processed, programmable controller PLC sends instruction shut electromagnetic valve and topping-up pump simultaneously, terminate cleaning.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520834095.7U CN205170610U (en) | 2015-10-27 | 2015-10-27 | Circulation of adopting ozone biological activity charcoal deep purification system of directly drinking water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520834095.7U CN205170610U (en) | 2015-10-27 | 2015-10-27 | Circulation of adopting ozone biological activity charcoal deep purification system of directly drinking water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205170610U true CN205170610U (en) | 2016-04-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520834095.7U Withdrawn - After Issue CN205170610U (en) | 2015-10-27 | 2015-10-27 | Circulation of adopting ozone biological activity charcoal deep purification system of directly drinking water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205170610U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152497A (en) * | 2015-10-27 | 2015-12-16 | 成都川力智能流体设备股份有限公司 | Circulation direct drinking water deep purification system using ozone biological activated carbon |
| CN106430752A (en) * | 2016-12-15 | 2017-02-22 | 中建水务（深圳）有限公司 | Water tank |
| CN112723626A (en) * | 2020-12-22 | 2021-04-30 | 成都川力智能流体设备股份有限公司 | Remote-monitoring advanced direct drinking water treatment equipment and water purification process |
| CN112755634A (en) * | 2020-12-30 | 2021-05-07 | 苏州碧清源环保技术有限公司 | Distilled water filtering equipment and filtering method |
-
2015
- 2015-10-27 CN CN201520834095.7U patent/CN205170610U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105152497A (en) * | 2015-10-27 | 2015-12-16 | 成都川力智能流体设备股份有限公司 | Circulation direct drinking water deep purification system using ozone biological activated carbon |
| CN106430752A (en) * | 2016-12-15 | 2017-02-22 | 中建水务（深圳）有限公司 | Water tank |
| CN112723626A (en) * | 2020-12-22 | 2021-04-30 | 成都川力智能流体设备股份有限公司 | Remote-monitoring advanced direct drinking water treatment equipment and water purification process |
| CN112755634A (en) * | 2020-12-30 | 2021-05-07 | 苏州碧清源环保技术有限公司 | Distilled water filtering equipment and filtering method |
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