CN206940640U - A kind of water treatment system with renewable filtrate fluorine removal - Google Patents
A kind of water treatment system with renewable filtrate fluorine removal Download PDFInfo
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- CN206940640U CN206940640U CN201720771676.XU CN201720771676U CN206940640U CN 206940640 U CN206940640 U CN 206940640U CN 201720771676 U CN201720771676 U CN 201720771676U CN 206940640 U CN206940640 U CN 206940640U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 118
- 239000011737 fluorine Substances 0.000 title claims abstract description 49
- 229910052731 fluorine Inorganic materials 0.000 title claims abstract description 49
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 title claims abstract description 45
- 239000000706 filtrate Substances 0.000 title claims abstract description 22
- 239000003814 drug Substances 0.000 claims abstract description 72
- 230000008929 regeneration Effects 0.000 claims abstract description 37
- 238000011069 regeneration method Methods 0.000 claims abstract description 37
- 229940079593 drug Drugs 0.000 claims abstract description 34
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 10
- 230000000740 bleeding effect Effects 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 5
- 230000001172 regenerating effect Effects 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 20
- 239000000463 material Substances 0.000 description 8
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 7
- 229910052782 aluminium Inorganic materials 0.000 description 7
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 238000006115 defluorination reaction Methods 0.000 description 5
- 235000020188 drinking water Nutrition 0.000 description 5
- 239000003651 drinking water Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000001179 sorption measurement Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000004411 aluminium Substances 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000007726 management method Methods 0.000 description 4
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical compound [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 description 3
- 210000000988 bone and bone Anatomy 0.000 description 3
- CADZRPOVAQTAME-UHFFFAOYSA-L calcium;hydroxy phosphate Chemical compound [Ca+2].OOP([O-])([O-])=O CADZRPOVAQTAME-UHFFFAOYSA-L 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical class O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 2
- 235000012206 bottled water Nutrition 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- 238000000909 electrodialysis Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 206010016818 Fluorosis Diseases 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- KBQPEQMZFVCZKQ-UHFFFAOYSA-N [F].OP(O)(O)=O Chemical group [F].OP(O)(O)=O KBQPEQMZFVCZKQ-UHFFFAOYSA-N 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000000675 anti-caries Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 208000004042 dental fluorosis Diseases 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000004334 fluoridation Methods 0.000 description 1
- BCQZXOMGPXTTIC-UHFFFAOYSA-N halothane Chemical compound FC(F)(F)C(Cl)Br BCQZXOMGPXTTIC-UHFFFAOYSA-N 0.000 description 1
- 229960003132 halothane Drugs 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000001727 in vivo Methods 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000035790 physiological processes and functions Effects 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 230000005180 public health Effects 0.000 description 1
- 230000002940 repellent Effects 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Landscapes
- Physical Water Treatments (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses a kind of water treatment system with renewable filtrate fluorine removal, including filter, the water inlet of the filter is connected by water intaking valve with inlet pipeline, the delivery port of the filter is connected by outlet valve with outlet pipeline, the water inlet of the filter is connected by entering medicine valve with drug-feeding tube road, the delivery port of the filter passes through drug valve and drug pipeline connection, the filter at least two.The upstream of the inlet pipeline is serially connected with pipe-line mixer.The pipe-line mixer is communicated with PH adjusters.The downstream of the outlet pipeline is serially connected with ultraviolet sterilizer.Regeneration Teat pipette is serially connected between the upstream on the drug-feeding tube road and the medicine outlet for regenerating medicine-chest.It is serially connected between the feeding opening of the medicine outlet of the regeneration medicine-chest and the regeneration Teat pipette into medicine main valve.The downstream of the drug pipeline connects with the feeding opening of the regeneration medicine-chest.The utility model can realize continuous water supply, not interfere with the just conventional water of user.
Description
Technical field
It the utility model is related to a kind of water treatment system, more particularly to a kind of water process system with renewable filtrate fluorine removal
System.
Background technology
Fluorine is one of the essential trace elements of the human body, and endangers the accumulation element of human body.Fluorine in human body
Ion is essentially from drinking water.Fluorine has important physiological function to human body, is the part of tooth and bone.Holding is drunk
A certain amount of fluorine in water, can pre- anti-caries.But the high-fluorine water that fluorinated volume is more than 1.0mg/L is drunk for a long time, fluorine will be in people
Accumulation in vivo, causes fluorine poisoning.
The standard GB/T 5749-2006 that the Ministry of Public Health of China and the Ministry of Construction work out jointly《Standards for drinking water quality》In
Regulation fluorine content of drinking water cannot be greater than 1.0mg/L.When Oil repellent is more than 1.0mg/L or higher in drinking water, need to consider to remove
Fluorine.
According to incompletely statistics, China's high-fluorine water is widely distributed, there are about 26 provinces, municipalities and autonomous regions, individual cities and towns, township more than 50000
Village, more than 7,000 ten thousand people drink high-fluorine water.Therefore, in face of the Halothane gene of getting worse, lacking the area in low fluorine water source, solving drink
It is imperative with water fluoridation problem, it is extremely urgent.
However, people always seem unable to do what one wishes that the people and animals of most of fluorosis still exist during fluorine is dropped for many years
Drink high-fluorine water.Its reason is mainly：First, understanding deficiency.Fluorine is objective reality in water, and it is voluntarily to disappear not handle
Lose, but to handle and will consider equipment investment, also to undertake the high equipment operating cost of comparison, many local common people are not
Accreditation.Although equipment, operation a period of time just have stopped getting off in many place countries and governmental investments, particularly before that
A little water factories that defluorination material must be just changed using one or two years, common people are seldom raised funds replacings, then drop fluorine interruption, not
It.Second, fluorine is extremely intractable material in water.What harmful substance present in water was easily processed is all the thing that can be aoxidized
Matter, such as the generation chemical substance such as oxide precipitation, ammonia nitrogen can be combined with oxygen for most metal ions and the overwhelming majority is organic
Material can be biodegradable, and fluorine can neither be oxidized, again can not be biodegradable.For many years, fluorine workers drop earnestly
Thinking, it is also difficult to find low a kind of efficiency high, small investment, cost, long lifespan and will not make to increase new harmful components in water
Material, this is also the reason for drop fluorine work is seldom successful.
Water process is carried out using renewable filtrate in the prior art.1. continuous operating time is short, it is easy to occurs false
Fatigue, operation will be interrupted 4~6 hours same time in 4~6 hours and set up；2. being recovery time length, regeneration is complicated, pipe
Reason is complicated.
It is difficult to control, causes because medicament mixes uneven, filtered water inlet pH value in common Defluorination water treatment equipment application
System operation it is unstable, be extremely difficult to the problem of predetermined defluorination effect.
Main reducing fluoride method domestic at present has negative resin ion-exchange, active carbon adsorption, calcium hydroxy phosphate (bone carbon)
Absorption method, activated alumina absorption method, electroosmose process, hyperfiltration, hydroxyl polymeric aluminum coagulant sedimentation, Activated Zeolite Adsorption etc..
(1) ion-exchange：The anion energy that negative resin is gone in water removal is very big, but to fluoride ion removing rate very
It is low, because the selecting sequence of negative resin is：Sulfate radical ＞ chlorine root ＞ bicarbonate radical ＞ fluorine, behind fluorine comes, therefore fluorine removing rate
Very low and expensive, regeneration is extremely complex, it is difficult to manage, seldom uses.
(2) active carbon adsorption：Activated carbon has king-sized specific surface area, but its aperture is also very big, fluorine below
After ion enters hole, the fluorine ion above entered is easily run out, therefore very low to fluorine ion adsorbance, and is not done
Method regenerates, and can only be discarded after adsorption saturation.High operating cost typically seldom comes into operation.
(3) calcium hydroxy phosphate (bone carbon) absorption method：Calcium hydroxy phosphate is very big to the adsorbance of fluorine, and China was in seven, 80 years
In generation, has many water factories to use.Its weak point one is material price height；Second, intensity difference, broken；Third, operating is complicated, management
Difficulty is very high, and when especially regenerating, regeneration solution concentration control is bad；Fourth, water outlet has stench taste, mouthfeel is very poor, or even has
The exceeded possibility of ammonia nitrogen.These shortcomings are restricted its application, are not used substantially at present.
(4) activated alumina absorption method：The method does not especially find aluminium ion to people within a period of time in people
Before body health has huge detrimental effect, China and it is universally acknowledged for activated alumina be maximally effective reducing fluoride method.But pass through
For many years it was verified that the method is there is also following six problems, first, continuous operating time is short, it is easy to false fatigue, operation 4 occur
To be interrupted 4~6 hours same time within~6 hours to set up；Second, the recovery time is grown, regeneration is complicated, complex management.Third,
Easily there is hardened phenomenon in filtrate, makes water distribution uneven with catchmenting, has a strong impact on service life.Fourth, effluent quality is poor, it is only capable of dropping
Fluorine and the harmful substance such as the colourity to being coexisted sometimes in water body, turbidity, heavy metal ion can not remove.Coexisted fifth, fearing in water
Phosphate, because phosphorus is combined very firm with aluminium, it can not elute, the surface area of activated alumina removes once being occupied by phosphate
Fluorine function is that announcement finishes；Sixth, water outlet has the exceeded possibility of aluminium ion, China GB5749-2006《Drinking Water health mark
It is accurate》Provide that aluminium ion standard is 0.2mg/L.Therefore, in terms of developing direction, the prospect of aluminium system defluorination material is suspicious.
(5) electroosmose process.The method is a kind of defluorination method ionized with electrode aluminium sheet to material in water, and fluorine removal is totally thorough
Bottom, effluent characteristics are fine, can automation mechanized operation, management is easier.Shortcoming is that investment is high, and operating cost is high, electrodialysis plant
Referred to as electric-tiger, under current electric rate, water cost per ton wants more than 6 yuan, and general economic condition is not afforded to do.
(6) hyperfiltration.This method fluorine removal is totally thorough, and effluent characteristics are good, and its shortcoming is similar with electrodialysis, operating cost
Height, average producing water ratio is low, and therefore, counter-infiltration is being suitable only for industrial high purity water preparation and bottled water, bottled water at present, is not suitable for big
Medium-sized waterworks.
(7) hydroxyl polymeric aluminum coagulant sedimentation.This method is that raw water is mixed into hydroxyl polymeric aluminum, is precipitated subsequently into sedimentation basin
Clarification, the extremely difficult control of chemical feeding quantity, and when fluorine is removed, exceeded tens times of aluminium.At present, the method is eliminated substantially.
(8) Activated Zeolite Adsorption.Directly very low using zeolite drop fluorine energy, cost performance is poor, seldom application.
Above reducing fluoride method, material are all not fully up to expectations, therefore, people be badly in need of seeking it is a kind of cheap, it is easy to use,
Management is simple, and long lifespan, multi-functional and water outlet do not increase the processing method of any harmful substance, to meet the need of reducing fluoride content and improving water quality
Will.
The defluoridation filter material that my company uses is renewable filtrate, such filtrate, by can repeatedly be weighed after regeneration treatment
It is multiple to use.Therefore, employ the water treatment system with renewable filtrate fluorine removal.A kind of as shown in figure 1, renewable filtrate fluorine removal
Water treatment system, including a filter 1, the water inlet of the filter 1 connected by water intaking valve 2-1 with inlet pipeline 2,
The delivery port of the filter 1 is connected by outlet valve 3-1 with outlet pipeline 3, and the water inlet of the filter 1 is by entering medicine valve
4-1 is connected with drug-feeding tube road 4, and the delivery port of the filter 1 is connected by drug valve 5-1 with drug pipeline 5.Such fluorine removal
Water treatment system must shut off the outlet valve of the filter during regeneration treatment is carried out to filter, therefore, it is impossible to real
Existing continuous water supply, influence the just conventional water of user.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of water treatment system with renewable filtrate fluorine removal, and this is
System can not interfere with the just conventional water of user in the process of regeneration treatment with continuous water supply.
In order to solve the above-mentioned technical problem, the water treatment system of the renewable filtrate fluorine removal of the utility model, including filtering
Device, the water inlet of the filter are connected by water intaking valve with inlet pipeline, the delivery port of the filter by outlet valve with
Outlet pipeline is connected, and the water inlet of the filter is connected by entering medicine valve with drug-feeding tube road, and the delivery port of the filter leads to
Cross drug valve and drug pipeline connection, the filter at least two.
The filter has two, and the water inlet of two filters is connected by water intaking valve with inlet pipeline respectively,
The delivery port of two filters is connected by outlet valve with outlet pipeline respectively, the water inlet difference of two filters
Connected by entering medicine valve with drug-feeding tube road, the delivery port of two filters passes through drug valve and drug pipeline connection respectively.
The filter has three, and the water inlet of three filters is connected by water intaking valve with inlet pipeline respectively,
The delivery port of three filters is connected by outlet valve with outlet pipeline respectively, the water inlet difference of three filters
Connected by entering medicine valve with drug-feeding tube road, the delivery port of three filters passes through drug valve and drug pipeline connection respectively.
The upstream of the inlet pipeline is serially connected with pipe-line mixer.
The pipe-line mixer is communicated with PH adjusters.
The downstream of the outlet pipeline is serially connected with ultraviolet sterilizer.
The delivery port of the ultraviolet sterilizer is provided with pressure gauge.
Water outlet main valve is serially connected between the water inlet of the downstream of the outlet pipeline and the ultraviolet sterilizer.
The water inlet of the water outlet main valve connects with blowoff line.
The blowoff line is serially connected with blowoff valve.
Bypass line is communicated between the downstream of the inlet pipeline and the downstream of the outlet pipeline.
The bypass line is serially connected with by-passing valve.
Regeneration Teat pipette is serially connected between the upstream on the drug-feeding tube road and the medicine outlet for regenerating medicine-chest.
It is serially connected between the feeding opening of the medicine outlet of the regeneration medicine-chest and the regeneration Teat pipette into medicine main valve.
The medicine outlet of the regeneration medicine-chest is communicated with discharge pipe.
The discharge pipe is serially connected with powder removing valve.
The downstream of the drug pipeline connects with the feeding opening of the regeneration medicine-chest.
The exhaust outlet of the filter is serially connected with air bleeding valve.
The utility model is had the advantages that compared with prior art with the water treatment system of renewable filtrate fluorine removal.
1st, the technical program as a result of the filter at least two technological means, so, when to wherein one
Individual filter need to only be closed during regeneration treatment the outlet valve of the filter, and other filters may continue to work, therefore,
Continuous water supply can be achieved, do not interfere with the just conventional water of user.
2nd, the technical program has two as a result of the filter, and the water inlet of two filters passes through respectively
Water intaking valve is connected with inlet pipeline, and the delivery port of two filters is connected by outlet valve with outlet pipeline respectively, two
The water inlet of the filter is connected by entering medicine valve with drug-feeding tube road respectively, and the delivery port of two filters passes through respectively
The technological means of drug valve and drug pipeline connection, so, only need to close when carrying out regeneration treatment to one of filter
The outlet valve of the filter, another filter may continue to work, therefore, continuous water supply can be achieved, do not interfering with user just
Conventional water, meanwhile, equipment cost is minimum.
3rd, the technical program has three as a result of the filter, and the water inlet of three filters passes through respectively
Water intaking valve is connected with inlet pipeline, and the delivery port of three filters is connected by outlet valve with outlet pipeline respectively, three
The water inlet of the filter is connected by entering medicine valve with drug-feeding tube road respectively, and the delivery port of three filters passes through respectively
The technological means of drug valve and drug pipeline connection, so, only need to close when carrying out regeneration treatment to one of filter
The outlet valve of the filter, another two filter may continue to work, therefore, continuous water supply can be achieved, it is ensured that user is just conventional
Water, meanwhile, equipment cost is relatively low.
4th, the technical program is serially connected with the technological means of pipe-line mixer, institute as a result of the upstream of the inlet pipeline
With, be advantageous to adjust current pH value.
5th, the technical program is communicated with the technological means of PH adjusters as a result of the pipe-line mixer, so, can
Adjust the pH value of current.
6th, the technical program is serially connected with the technological means of ultraviolet sterilizer as a result of the downstream of the outlet pipeline,
So sterilization processing can be carried out to current.
7th, the technical program is provided with the technological means of pressure gauge as a result of the delivery port of the ultraviolet sterilizer,
So pressure change of convenient monitoring current.
8th, the technical program as a result of downstream and the ultraviolet sterilizer of the outlet pipeline water inlet it
Between be serially connected with the technological means of water outlet main valve, so, the current of outlet pipeline can be controlled.
9th, the technological means that the technical program connects as a result of the water inlet of the water outlet main valve with blowoff line, institute
To be advantageous to discharge in sewage.
10th, the technical program is serially connected with the technological means of blowoff valve as a result of the blowoff line, so, can be to dirt
The discharge of water is controlled.
11st, the technical program connects as a result of between the downstream and the downstream of the outlet pipeline of the inlet pipeline
There is the technological means of bypass line, so, it can directly utilize undressed current.
12nd, the technical program is serially connected with the technological means of by-passing valve as a result of the bypass line, so, can be to side
Siphunculus road is controlled.
13rd, the technical program is serially connected with as a result of between the upstream on the drug-feeding tube road and the medicine outlet of regeneration medicine-chest
The technological means of Teat pipette being regenerated, so, regrowth liquid medicine can be transported in pending filter.
14th, the technical program is as a result of between the medicine outlet of the regeneration medicine-chest and the feeding opening of the regeneration Teat pipette
The technological means into medicine main valve being serially connected with, so, drug-feeding tube road can be controlled.
15th, the technical program is communicated with the technological means of discharge pipe as a result of the medicine outlet of the regeneration medicine-chest,
So be advantageous to discharge useless regrowth liquid medicine.
16th, the technical program is serially connected with the technological means of powder removing valve as a result of the discharge pipe, so, can be to row
Pipeline is put to be controlled.
17th, the technical program connects as a result of the downstream of the drug pipeline with the feeding opening of the regeneration medicine-chest
The section of technology, so, used regrowth liquid medicine can be discharged into regeneration medicine-chest.
18th, the technical program is serially connected with the technological means of air bleeding valve as a result of the exhaust outlet of the filter, so,
The discharge of air in controllable filter.
Brief description of the drawings
The utility model is made with the water treatment system of renewable filtrate fluorine removal with reference to the accompanying drawings and detailed description
It is described in further detail.
Fig. 1 is the structural representation of the single-filter water treatment system of renewable filtrate fluorine removal in the prior art.
Fig. 2 is the structural representation of the utility model twinfilter water treatment system of renewable filtrate fluorine removal.
Fig. 3 is the structural representation of the filter of the utility model three water treatment system of renewable filtrate fluorine removal.
Description of reference numerals is as follows.
1~filter；
1-1~air bleeding valve；
2~inlet pipeline；
2-1~water intaking valve；
3~outlet pipeline；
3-1~outlet valve；
3-2~water outlet main valve；
4~drug-feeding tube road；
4-1~enter medicine valve；
4-2~enter medicine main valve；
5~drug pipeline；
5-1~drug valve；
6~regeneration medicine-chest；
7~regeneration Teat pipette；
8~pipe-line mixer；
9~PH adjusters；
10~ultraviolet sterilizer；
11~pressure gauge；
12~bypass line；
12-1~by-passing valve；
13~blowoff line；
13-1~blowoff valve；
14~discharge pipe；
14-1~powder removing valve.
Embodiment
As shown in Figure 2 to Figure 3, present embodiments provide for a kind of water treatment system with renewable filtrate fluorine removal, including
Filter 1, the water inlet of the filter 1 are connected by water intaking valve 2-1 with inlet pipeline 2, and the delivery port of the filter 1 leads to
Cross outlet valve 3-1 to connect with outlet pipeline 3, the water inlet of the filter 1 connects by entering medicine valve 4-1 with drug-feeding tube road 4, institute
The delivery port for stating filter 1 is connected by drug valve 5-1 with drug pipeline 5, the filter 1 at least two.
As shown in Fig. 2 the filter 1 has two, the water inlet of two filters 1 passes through water intaking valve 2-1 respectively
Connected with inlet pipeline 2, the delivery port of two filters 1 is connected by outlet valve 3-1 with outlet pipeline 3 respectively, two
The water inlet of the filter 1 is connected by entering medicine valve 4-1 with drug-feeding tube road 4 respectively, the delivery port point of two filters 1
Do not connected by drug valve 5-1 with drug pipeline 5.
As shown in figure 3, the filter 1 has three, the water inlet of three filters 1 passes through water intaking valve 2-1 respectively
Connected with inlet pipeline 2, the delivery port of three filters 1 is connected by outlet valve 3-1 with outlet pipeline 3 respectively, three
The water inlet of the filter 1 is connected by entering medicine valve 4-1 with drug-feeding tube road 4 respectively, the delivery port point of three filters 1
Do not connected by drug valve 5-1 with drug pipeline 5.
Various improvement explanation as present embodiment is as above.
As shown in Figure 2 to Figure 3, the upstream of the inlet pipeline 2 is serially connected with pipe-line mixer 8.
As shown in Figure 2 to Figure 3, the pipe-line mixer 8 is communicated with PH adjusters 9.
As shown in Figure 2 to Figure 3, the downstream of the outlet pipeline 3 is serially connected with ultraviolet sterilizer 10.
As shown in Figure 2 to Figure 3, the delivery port of the ultraviolet sterilizer 10 is provided with pressure gauge 11.
As shown in Figure 2 to Figure 3, gone here and there between the downstream of the outlet pipeline 3 and the water inlet of the ultraviolet sterilizer 10
It is connected to water outlet main valve 3-2.
As shown in Figure 2 to Figure 3, the water inlet of the water outlet main valve 3-2 connects with blowoff line 13.
As shown in Figure 2 to Figure 3, the blowoff line 13 is serially connected with blowoff valve 13-1.
As shown in Figure 2 to Figure 3, it is communicated with bypass between the downstream of the inlet pipeline 2 and the downstream of the outlet pipeline 3
Pipeline 12.
As shown in Figure 2 to Figure 3, the bypass line 12 is serially connected with by-passing valve 12-1.
As shown in Figure 2 to Figure 3, it is serially connected with crude drug again between the upstream on the drug-feeding tube road 4 and the medicine outlet for regenerating medicine-chest 6
Pump 7.
As shown in Figure 2 to Figure 3, it is serially connected between the feeding opening of the medicine outlet of the regeneration medicine-chest 6 and the regeneration Teat pipette 7
Enter medicine main valve 4-2.
As shown in Figure 2 to Figure 3, the medicine outlet of the regeneration medicine-chest 6 is communicated with discharge pipe 14.
As shown in Figure 2 to Figure 3, the discharge pipe 14 is serially connected with powder removing valve 14-1.
As shown in Figure 2 to Figure 3, the downstream of the drug pipeline 5 connects with the feeding opening of the regeneration medicine-chest 6.
As shown in Figure 2 to Figure 3, the exhaust outlet of the filter 1 is serially connected with air bleeding valve 1-1.
Claims (4)
1. a kind of water treatment system with renewable filtrate fluorine removal, including filter (1), the water inlet of the filter (1) leads to
Cross water intaking valve (2-1) to connect with inlet pipeline (2), the delivery port of the filter (1) passes through outlet valve (3-1) and outlet pipeline
(3) connect, the water inlet of the filter (1) is connected by entering medicine valve (4-1) with drug-feeding tube road (4), the filter (1)
Delivery port is connected by drug valve (5-1) with drug pipeline (5), it is characterised in that：The filter (1) at least two.
2. according to claim 1 with the water treatment system of renewable filtrate fluorine removal, it is characterised in that：The filter (1)
There are two, the water inlet of two filters (1) is connected by water intaking valve (2-1) with inlet pipeline (2) respectively, described in two
The delivery port of filter (1) is connected by outlet valve (3-1) with outlet pipeline (3) respectively, the water inlet of two filters (1)
Mouth is connected by entering medicine valve (4-1) with drug-feeding tube road (4) respectively, and the delivery port of two filters (1) passes through drug respectively
Valve (5-1) connects with drug pipeline (5).
3. according to claim 1 with the water treatment system of renewable filtrate fluorine removal, it is characterised in that：The filter (1)
There are three, the water inlet of three filters (1) is connected by water intaking valve (2-1) with inlet pipeline (2) respectively, described in three
The delivery port of filter (1) is connected by outlet valve (3-1) with outlet pipeline (3) respectively, the water inlet of three filters (1)
Mouth is connected by entering medicine valve (4-1) with drug-feeding tube road (4) respectively, and the delivery port of three filters (1) passes through drug respectively
Valve (5-1) connects with drug pipeline (5).
4. according to one of claims 1 to 3 water treatment system with renewable filtrate fluorine removal, it is characterised in that：
The upstream of the inlet pipeline (2) is serially connected with pipe-line mixer (8)；
The pipe-line mixer (8) is communicated with PH adjusters (9)；
The downstream of the outlet pipeline (3) is serially connected with ultraviolet sterilizer (10)；
The delivery port of the ultraviolet sterilizer (10) is provided with pressure gauge (11)；
Water outlet main valve (3- is serially connected between the downstream of the outlet pipeline (3) and the water inlet of the ultraviolet sterilizer (10)
2)；
The water inlet of the water outlet main valve (3-2) connects with blowoff line (13)；
The blowoff line (13) is serially connected with blowoff valve (13-1)；
Bypass line (12) is communicated between the downstream of the inlet pipeline (2) and the downstream of the outlet pipeline (3)；
The bypass line (12) is serially connected with by-passing valve (12-1)；
Regeneration Teat pipette (7) is serially connected between the upstream of the drug-feeding tube road (4) and the medicine outlet of regeneration medicine-chest (6)；
It is serially connected between the medicine outlet of the regeneration medicine-chest (6) and the feeding opening of the regeneration Teat pipette (7) into medicine main valve (4-2)；
The medicine outlet of the regeneration medicine-chest (6) is communicated with discharge pipe (14)；
The discharge pipe (14) is serially connected with powder removing valve (14-1)；
The downstream of the drug pipeline (5) connects with the feeding opening of the regeneration medicine-chest (6)；
The exhaust outlet of the filter (1) is serially connected with air bleeding valve (1-1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720771676.XU CN206940640U (en) | 2017-06-29 | 2017-06-29 | A kind of water treatment system with renewable filtrate fluorine removal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720771676.XU CN206940640U (en) | 2017-06-29 | 2017-06-29 | A kind of water treatment system with renewable filtrate fluorine removal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206940640U true CN206940640U (en) | 2018-01-30 |
Family
ID=61366516
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720771676.XU Expired - Fee Related CN206940640U (en) | 2017-06-29 | 2017-06-29 | A kind of water treatment system with renewable filtrate fluorine removal |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206940640U (en) |
-
2017
- 2017-06-29 CN CN201720771676.XU patent/CN206940640U/en not_active Expired - Fee Related
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