CN108502984A - The positive backwashing system of pretreatment softening regeneration auxiliary salt adding and water purification machine - Google Patents
The positive backwashing system of pretreatment softening regeneration auxiliary salt adding and water purification machine Download PDFInfo
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- CN108502984A CN108502984A CN201810624804.7A CN201810624804A CN108502984A CN 108502984 A CN108502984 A CN 108502984A CN 201810624804 A CN201810624804 A CN 201810624804A CN 108502984 A CN108502984 A CN 108502984A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/02—Non-contaminated water, e.g. for industrial water supply
- C02F2103/04—Non-contaminated water, e.g. for industrial water supply for obtaining ultra-pure water
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
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- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Water By Ion Exchange (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The present invention relates to a kind of pretreatments to soften the positive backwashing system of regeneration auxiliary salt adding and water purification machine, includes the pretreatment melded system of ultrafiltration membrane and resin filter element composition;By auxiliary filter cartridge flushing, salt core, first blowdown valve and the second blowdown valve group at regeneration auxiliary salt adding system, by ultrafiltration membrane and the first blowdown valve group at positive flushing drainage, by auxiliary filter cartridge flushing and the second blowdown valve group at sewage backwash system, the present invention also provides the control methods of the system, and include the water purification machine of the pretreatment melded system, the beneficial effects of the invention are as follows the troubles that can also avoid frequently replacing resin filter element by adding salt just backwashing automatically on the basis of fully extending filter core service life at different levels, and drinking pure and more good softening water purification and soft concentrated water can be provided simultaneously.
Description
Technical field
The present invention relates to a kind of pretreatments to soften the positive backwashing system of regeneration auxiliary salt adding and water purification machine.
Background technology
With the improvement of living standards, the pure small-sized household that can directly drink of water quality and commercial water purification machine are increasingly popularized, and it is pure
The cost of water dispenser in use is mainly reflected in two aspects, is the utilization rate and filter core service life of water respectively;Water
Utilization rate is mainly reflected in the net expense ratio and concentrated water recovery utilization rate of water purification machine;The net expense ratio of water refers to water purification machine per one liter of output
The ratio of pure water and the concentrated water discharged, per 1 liter of pure water of output, its discharge concentrated water is that 2-3 rises concentrated water to common water purification machine at present,
There are many water purification machines that concentrated water recycling filtering is used to increase pure water yield to reduce concentrated water discharge, but its consequence brought is to lead
The hardness and pH value for causing pretreated water increase, and accelerate reverse osmosis membrane and filter core at different levels to block age hardening, increase filter core, pump valve more
Change this into;The main reason for influencing water purification machine concentrated water recovery utilization rate is only to penetrate water in view of reverse osmosis membrane used in water purification machine, cut
The physical characteristics of mineral ion, concentrated water pH value, ion concentration and the hardness that concentrated water pipeline is discharged are stayed to be above raw water, scale
Incrustation scale is heavier compared with tap water, as life slurry cause clothes fiber it is age hardening, stimulation skin, increase detergent use
Amount, more unsuitable breed fish are raised flowers, are wasted caused by not being suitable for being directly discharged into sewer as domestic water more.
The filter core of water purification machine is divided into two parts:Preprocessing filter element including reverse osmosis membrane and for protecting reverse osmosis membrane,
The service life of reverse osmosis membrane depends on tap water quality, preprocessing filter element category, filtering accuracy;Water quality impact reverse osmosis membrane
Principal element has the following:The hardness etc. of gel, water quality pH value, water, the wherein accumulation of gel can be in reverse osmosis membrane tables
Face forms attachment and blocks, and leads to bacterial micro-organism mass propagation, to cause biochemical corrosion contamination, water quality pH value are excessively high can lead
Cause reverse osmosis membrane hardening aging, the excessive high hardness of water can cause to form crystallization pollution, above-mentioned dirt in reverse osmosis membrane surface and film layer
Dye, which can reduce reverse osmosis membrane flux, causes water yield decline, producing water water quality to deteriorate;Preprocessing filter element is mostly to receive dirty absorbent-type at present
Cartridge combination common are polypropylene spray welding filter element and activated carbon combination, as the decline of production cost is with screening type filter core
The also more and more extensive use of pretreated cartridge combination, common are ultrafiltration membrane, ceramic element is combined with activated carbon, screening type
The characteristics of filter core is that filtering accuracy height can remove gel and bacterial micro-organism etc., reverse osmosis membrane can be more effectively protected, to dirt
Dye object carries out Physical entrapment screening, does not adsorb, and can retention pollutant discharge can fully be extended filter when being provided with drain outlet
Core service life.
The characteristics of both the above preprocessing filter element is that can effectively remove Visible pollutant, and wherein ultrafiltration membrane can also effectively be gone
Except gel microorganism, reverse osmosis membrane can be preferably protected, but cannot all change the pH value and hardness of water, so there are also
Water purification machine preprocessing filter element combination in increase resin filter element pretreated water is softened, to play absorbing calcium ions and magnesium ions,
The effect of hardness and pH value is reduced to reach better protecting effect, and by ultrafiltration membrane purification, resin filter element softening it is pre-
Discharge concentrated water turbidity, solids total content, pH value, hardness, total plate count and the body that processing soft water is retained through reverse osmosis membrane filtration
It tests sense and is superior to raw water, be good domestic water supplement, but resin filter element is easily saturated the absorption of calcium ions and magnesium ions, to
Effect is lost, need to replace in time or carries out ion exchange regeneration with sodium chloride brine, installs the small-sized pure of resin filter element additional at present
Water dispenser, resin filter element are disposable design, i.e., month are replaced by special maintenance personnel per 1-3 primary, and big are increased
Consumables cost and cost of labor bring additional financial burden and inconvenience for user.
Invention content
The object of the present invention is to provide a kind of in the existing technology base using resin filter element as water purification machine pretreatment system
Increase a regeneration auxiliary salt adding and positive and negative flush loop on plinth, the new pretreatment softening regeneration auxiliary salt adding of composition just recoils
System and water purification machine are washed, which softens pretreated water using softening resin, can effectively reduce the hardness and calcium and magnesium of water
Content avoids filter core because water quality generation really up to the mark crystallization causes to block, and can fully extend making for filter core at different levels, reverse osmosis membrane and pump valve
Use the service life.Possessed auxiliary salt adding system can according to tap water quality and resin filter element use state automatically to resin filter element into
Row regeneration plus salt and positive backwash, reduce the trouble for frequently replacing resin filter element, significantly extend the replacement cycle of resin filter element.
Traditional water purification machine is only capable of this system on the basis of providing pure water or pure water, water purification and provides not only the clean drinking pure that can directly drink
High-quality softening water purification with domestic water is more suitable as, also comprehensively reduces the use cost of water purification machine while being discharged dense
The indexs such as turbidity, total plate count and the hardness of water water quality are substantially better than raw water, more worth recycling, to which overall reduction is pure
Filter core cost, pump valve loss, the consuming cost of water in water dispenser use.
Technical solution of the invention is to carry out regeneration auxiliary salt adding to pretreatment system resin filter element automatically to rinse
The pretreatment softening regeneration positive backwashing system of auxiliary salt adding, including by the first inlet pipeline, ultrafiltration membrane, the first inlet valve, resin
The pretreatment melded system of piping connection is passed sequentially through between filter core and the second inlet valve;And by the first inlet pipeline, auxiliary
Filter cartridge flushing, the first blowdown valve, the second blowdown valve and it is divided into two articles of branches through the 6th three-way pipe, all the way to be provided with salt core and salt
Saline line, the another way of water valve are that the regeneration auxiliary salt adding for the water purification backwash pipeline composition for being provided with water purification backwash valve just recoils
System is washed, is characterized in that:First inlet pipeline is divided into two branches after accessing the first three-way pipe:Pass through all the way
The water inlet of two inlet pipelines and ultrafiltration membrane connects, and the water outlet of the ultrafiltration membrane is connect with the water inlet end of the first inlet valve, institute
The water outlet for stating the first inlet valve is connected to resin filter element by being equipped with the water pipeline of the second three-way pipe and third three-way pipe
Water inlet, the water outlet of the resin filter element connects by being equipped with the softening water pipeline of the 4th three-way pipe and the 5th three-way pipe
It is connected to the water inlet end of the second inlet valve;It is to be connect with auxiliary filter cartridge flushing water inlet by third inlet pipeline all the way, it is described auxiliary
It is divided into two branches after helping the water outlet of filter cartridge flushing to access the 6th three-way pipe by pipeline:All the way by being equipped with salt core and salt
The saline line of water valve is connect with third triplate line, and another way is by being equipped with the water purification backwash pipeline and of water purification backwash valve
Five three-way pipes connect, and second three-way pipe connect the 4th three-way pipe with the second blowdown valve by the second blowoff line outward
It is connect outward with the first blowdown valve by the first blowoff line.
Further, the both ends of the ultrafiltration membrane are respectively arranged with inlet and outlet.
Further, the both ends of the resin filter element are respectively arranged with inlet and outlet.
Further, the water outlet in salt core is arranged in the brine valve, is connected between the brine valve and third three-way pipe
Saline line be additionally provided with the first check valve that can only be flowed to third three-way pipe.
Further, it is unidirectional to be additionally provided with can only be flowed to the 5th three-way pipe second for the water outlet of the water purification backwash valve
Valve.
It can also be arranged as the preferred third three-way pipe and be connected between resin filter element water outlet and the second inlet valve
Softening water pipeline on.
As preferably when the third three-way pipe is arranged when softening water pipeline, the 5th three-way pipe is arranged in salt valve
Between the first check valve.
Further, the second inlet valve of the first inlet valve first blowdown valve of brine valve water purification backwash valve and the second blowdown valve
Action controlled by control system.
In addition the present invention also provides a kind of water purification machines including the pretreatment softening regeneration positive backwashing system of auxiliary salt adding:
Including booster pump and reverse osmosis membrane, one end of the reverse osmosis membrane is equipped with feed water by reverse osmosis mouth, and the other end is provided with reverse osmosis pure
The water outlet at the mouth of a river and the reverse osmosis concentrated mouth of a river, second inlet valve passes through the water inlet end of piping connection to booster pump, the increasing
The water outlet of press pump is connected to feed water by reverse osmosis mouth by being pressurized water pipeline, and the reverse osmose pure-water mouth is by being equipped with high pressure
The pure water pipeline of switch is connect with pure water water outlet, and the reverse osmosis concentrated mouth of a river is connect by pipeline with flow-limiting valve.
Further, the pure water pipeline connected between the reverse osmose pure-water mouth and high-voltage switch gear is additionally provided with can only be to pure water
The third check valve of water outlet flowing.
The present invention also provides it is a kind of pretreatment softening regeneration the positive backwashing system of auxiliary salt adding control method, it is no electricity or
The first inlet valve is shown in a fully open operation when standby mode, second inlet valve the first blowdown valve of brine valve water purification backwash valve and second row
Dirty valve is in full-shut position, tap water by first the first three-way pipe of inlet pipeline respectively enter the second inlet pipeline and third into
Water lines enter ultrafiltration membrance filter output ultrafiltration water purification, then the first inlet valve of water outlet through ultrafiltration membrane by the second inlet pipeline
Output softens water purification and comes together in softening water pipeline after water pipeline enters the softening of resin filter flask;Entered by third inlet pipeline
The water purification of auxiliary filter cartridge flushing purification output is divided into two-way through the 6th three-way pipe, enters salt core all the way and is mixed with the dissolving of soft water salt,
Water purification backwash pipeline is flowed to all the way, and when third three-way pipe is arranged in water pipeline and is connected to resin filter element water inlet, startup is pre-
When the processing softening regeneration positive backwashing system of auxiliary salt adding:Control system control the first inlet valve valve close, brine valve and the
One blowdown valve valve is opened, and tap water enters the filtering of auxiliary filter cartridge flushing only by the first inlet pipeline and third inlet pipeline
Change, output water purification enters salt core, output brine after mix with the dissolving of soft water salt, by brine valve the first check valve saline line with
Third three-way pipe enters resin filter element by resin filter element water inlet and carries out immersion and calcium and magnesium displacement, and slow rinse water is filtered by resin
Core water outlet and the discharge of the first blowdown valve;Brine valve is closed the first inlet valve and is opened, and carries out water purification and just rinses, tap water passes through the
One the first three-way pipe of inlet pipeline and the second inlet pipeline introduce ultrafiltration membrance filter output ultrafiltration water purification, then through the first inlet valve into
Enter to enter resin filter element by resin filter element water inlet with water pipeline and be rinsed, calcium-magnesium-containing remaining waste is through soft in resin filter element
Change water pipeline and the discharge of the first blowdown valve, the first blowdown valve and the first inlet valve are closed, and water purification backwash valve opens the second blowdown
Valve is opened, through assisting the water purification of filter cartridge flushing purification to pass through water purification backwash pipeline and softening water pipeline and resin filter element water outlet
It is redirected back into resin filter element and carries out depth flushing, and remaining waste is discharged by the second sewage draining exit, when third three-way pipe is arranged
It is arranged in the saline line between brine valve and the first check valve in softening water pipeline, the 5th three-way pipe, starts pretreatment
When the softening regeneration positive backwashing system of auxiliary salt adding:The control method of the pretreatment softening regeneration positive backwashing system of auxiliary salt adding:
Control system controls that the first inlet valve valve is closed, brine valve and the second blowdown valve valve are opened, by the first inlet pipeline and
The water purification that third inlet pipeline introduces auxiliary filter cartridge flushing filtration, purification output enters salt core, output after being mixed with the dissolving of soft water salt
Saline solution is redirected back into resin filter element by brine valve the first check valve saline line and third three-way pipe by resin filter element water outlet
Impregnate and replaced with calcium and magnesium, slow rinse water is discharged by resin filter element water inlet and the second blowdown valve;Brine valve closes the
One inlet valve is opened, and the second blowdown valve is closed, and the first blowdown valve is opened, and is carried out water purification and is just rinsed, and tap water passes through the first water inlet
The first three-way pipe of pipeline and the second inlet pipeline introduce ultrafiltration membrance filter output ultrafiltration water purification, then enter through the first inlet valve and net
Water lines enter resin filter element by resin filter element water inlet and are rinsed, the softened water purification of calcium-magnesium-containing remaining waste in resin filter element
Pipeline and the discharge of the first blowdown valve;First blowdown valve and the first inlet valve are closed, and water purification backwash valve is opened the second blowdown valve and opened,
Through assisting the water purification of filter cartridge flushing purification to pass through water purification backwash pipeline the second check valve the first check valve saline line third threeway
Pipe and resin filter element water outlet, which are redirected back into resin filter element, carries out depth flushing, and remaining waste is arranged by the second sewage draining exit
Go out.This method have the advantage that the water purification of water purification backwash pipeline can be residual between brine valve and the first check valve when backwash softens resin
The saline solution stayed is rinsed, and avoids the corrosion of the first check valve of brine pair.Described regeneration adds salt to refer to resin filter in the present invention
The efficiency for wicking attached calcium and magnesium saturation removal calcium ions and magnesium ions continuously decreases, and the sodium chloride brine using salt core middle and high concentration passes through tree
Fat again cements out the calcium ions and magnesium ions on resin, is discharged outside filter core with regeneration liquid waste, the resin of failure is made to reform into sodium
The process of type resin and softening function of exchange;Positive rinse refers to that the second blowdown valve closes the first blowdown valve opening, and tap water is through super
Entered by resin filter element water inlet after membrane filtration and resin filter element is rinsed, the mistake that flushing waste is discharged by the first blowdown valve
Journey;Backwash refers to that the first inlet valve closes the second blowdown valve opening tap water through assisting filter cartridge flushing water purification backwash pipeline and tree
Fat filter core water outlet, which enters, is rinsed resin filter element, the process that flushing waste is discharged through the second blowdown valve.
In addition the present invention also provides the control methods for the water purification machine for softening regeneration auxiliary salt adding system comprising pretreatment:System
Control system controls the second inlet valve valve and opens, is pressurized pump operation when pure water, comes together in the softening water purification of softening water pipeline
Enter reverse osmosis membrane after booster pump is pressurized and carry out Pure water preparation, the pure water of output is flowed to by pure water outlet and pure water pipeline
The concentrated water of pure water water outlet, generation is discharged through concentrated water pipeline and flow-limiting valve.
Compared with prior art, the invention has the advantages and positive effects that:It will be into using ultrafiltration membrane and resin filter element
The tap water improvement for entering filter core is the soft water of soft, can significantly extend the physical life of filter core reverse osmosis membranes and pump valve at different levels;
The resin filter element add automatically salt and positive backwashing function science solve the easy adsorption saturation of resin filter element, lose it is soft
Change function, needs professional unpicks and washes manually plus salt flushing is regenerated or frequently replaced cost of labor trouble and material cost;
Poor, the big panel height of turbidity organic matter microbial impurities hardness calcium-magnesium content in water with traditional water purification machine discharge concentrated water water quality
It is unsuitable for being recycled again as domestic water using can only compare as waste water is discarded in tap water, water purification machine of the present invention is arranged
The concentrated water turbidity organic matter microbial impurities hardness calcium-magnesium content gone out is below tap water, is good domestic water, more worth
It recycles.
Description of the drawings
Fig. 1 is the structural schematic diagram of the present invention pretreatment softening regeneration positive backwashing system of auxiliary salt adding.
Fig. 2 is the structural schematic diagram of another pretreatment softening regeneration positive backwashing system of auxiliary salt adding of the invention.
Fig. 3 is the structural representation of water purification machine of the present invention comprising the pretreatment softening regeneration positive backwashing system of auxiliary salt adding
Figure.
Fig. 4 is the circuit diagram of the positive backwashing system of present invention pretreatment softening regeneration auxiliary salt adding and water purification machine.
Primary clustering symbol description:
First inlet pipeline 1, the second inlet pipeline 2, third inlet pipeline 3, ultrafiltration membrane 4,5 first inlet valve 6 of reverse osmosis membrane,
One three-way pipe 701, the second three-way pipe 702, third three-way pipe 703, the 4th three-way pipe 704, the 5th three-way pipe 705, the 6th threeway
Pipe 706, resin filter element 8, auxiliary filter cartridge flushing 9, the second inlet valve 10, water pipeline 11, softening water pipeline 12, booster pump
13, salt core 14, brine valve 15, the first check valve 16, saline line 17, the first blowdown valve 18, the first blowoff line 19, second row
Dirty pipeline 20, the second blowdown valve 21, water purification backwash pipeline 22, water purification backwash valve 23, the second check valve 24, pure water water outlet 25,
High-voltage switch gear 26,27 control system 28 of supercharging water pipeline, third check valve 29, high-voltage switch gear 30, pure water pipeline 31, concentrated water pipe
Road 32, flow-limiting valve 33, pure water water outlet 34, ultrafiltration membrane water inlet 401, ultrafiltration membrane water outlet 402, resin filter element water inlet 801,
Resin filter element water outlet 802, reverse osmosis membrane water inlet 501, reverse osmosis membrane pure water mouth 502, reverse osmosis membrane concentrated water spout 503.
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation describes, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, those of ordinary skill in the art are obtained every other without creative efforts
Embodiment shall fall within the protection scope of the present invention.
Term " first ", " second " in description and claims of this specification and above-mentioned attached drawing etc. are to be used for area
Not different objects, rather than for describing particular order.In addition, term " comprising " and " having " and their any deformations,
It is intended to cover and non-exclusive includes.Such as it contains the process of series of steps or unit, method, system, product or sets
Standby the step of being not limited to list or unit, but further include the steps that optionally not listing or unit, or optionally
Further include for other intrinsic steps of these processes, method, product or equipment or unit.Referenced herein " embodiment "
It is meant that a particular feature, structure, or characteristic described may be embodied at least one embodiment of the present invention in conjunction with the embodiments.
The phrase, which occurs, in each position in the description might not each mean identical embodiment, nor mutual with other embodiments
The independent or alternative embodiment of reprimand.Those skilled in the art explicitly and implicitly understand, reality described herein
Applying example can be combined with other embodiments.
The structural schematic diagram of the pretreatment softening regeneration positive backwashing system of auxiliary salt adding as shown in Figure 1, including by first
The pre- of piping connection is passed sequentially through between inlet pipeline 1, ultrafiltration membrane 4, the first inlet valve 6, resin filter element 8 and the second inlet valve 10
Handle melded system;And by the first inlet pipeline 1, auxiliary filter cartridge flushing 9, the first blowdown valve 18, the second blowdown valve 21 and warp
6th three-way pipe 706 is divided to for two articles of branches, and saline line 17, the another way for being provided with salt core 14 and brine valve 15 all the way are provided with
The positive backwashing system of regeneration auxiliary salt adding that the water purification backwash pipeline 22 of water purification backwash valve 23 is constituted, first inlet pipeline 1
It is divided into two branches after accessing the first three-way pipe 701:The water inlet 401 for passing through the second inlet pipeline 2 and ultrafiltration membrane 4 all the way connects
It connects, the water outlet 402 of the ultrafiltration membrane 4 is connect with the water inlet end of the first inlet valve 6, and the water outlet of first inlet valve 6 is logical
It crosses and the water pipeline 11 of the second three-way pipe 702 and third three-way pipe 703 is installed is connected to the water inlet 801 of resin filter element 8, institute
The water outlet 802 of resin filter element 8 is stated by being equipped with the softening water pipeline 12 of the 4th three-way pipe 704 and the 5th three-way pipe 705
It is connected to the water inlet end of the second inlet valve 10;Another way connects by third inlet pipeline 3 with the water inlet of filter cartridge flushing 9 is assisted
It connects, the water outlet of the auxiliary filter cartridge flushing 9 after pipeline the 6th three-way pipe 706 of access by being divided into two branches:Pass through all the way
The saline line 17 for being equipped with salt core 14 and brine valve 15 is connect with third three-way pipe 703, and the brine valve 15 is arranged in salt core
14 water outlet, the saline line 17 connected between the brine valve 15 and third three-way pipe 703 is additionally provided with can only be to third
The first check valve 16 that three-way pipe 703 flows, another way is by being equipped with the water purification backwash pipeline 22 and the of water purification backwash valve 23
Five three-way pipes 705 connect, and the water purification backwash pipeline 22 connected between 23 and the 5th three-way pipe 705 of the water purification backwash valve is also set up
There are the second check valve 24 that can only be flowed to the 5th three-way pipe 705, second three-way pipe 702 to pass through the second blowoff line outward
20 connect with the second blowdown valve 21, and the 4th three-way pipe 704 is connected by the first blowoff line 19 and the first blowdown valve 18 outward
It connects, the circuit diagram of the positive backwashing system of softening regeneration auxiliary salt adding and water purification machine is pre-processed with reference to figure 4, the pretreatment softening is again
Control system 28 controls 6 second inlet valve 10 of the first inlet valve by the following course of work in the positive backwashing system of raw auxiliary salt adding
The action of 15 water purification backwash valve of brine valve 23 first blowdown valve 18 and the second blowdown valve 21:
When without electric or standby when state:First inlet valve 6 is opened, 10 brine valve of the second inlet valve, 15 water purification backwash valve 23 first
Blowdown valve 18 and the second blowdown valve 21 are in full-shut position, and tap water divides through the first three-way pipe 701 for two-way, passes through ultrafiltration all the way
Film 4 and the filtering softening of resin filter element 8 come together in softening water pipeline 12;Through the 6th after being filtered all the way by auxiliary filter cartridge flushing 9
Three-way pipe 706 divides for two-way, and a-road-through crosses saline line 17 and enters that salt core 14 and soft water salt mixed dissolution, to flow to water purification all the way anti-
Wash pipeline 22.
When starting auxiliary salt adding regeneration, the first inlet valve closes 6, brine valve 15 and the first blowdown valve 18 is opened, salt core
Interior 14 brine enters resin filter element 8 by salt valve 15, resin filter element water inlet 801 and carries out the displacement of sodium and calcium ions and magnesium ions again
Raw, the waste liquid of displacement is discharged through the first blowdown valve 18.
When starting water purification and just rinsing resin filter element 8, the first blowdown valve 18 is opened, and the water purification filtered through ultrafiltration membrane 4 is through the
One inlet valve 6 and resin filter element water inlet 802 enter resin filter element 8, are just being rinsed to resin filter element 8, and flushing waste is through the
One blowdown valve 18 is discharged.
When starting water purification backwash resin filter element 8, water purification backwash valve 23, the second blowdown valve 21 are opened, and auxiliary rinses filter
Core 9 filter water purification by 23 resin filter element water outlet 802 of water purification backwash valve be redirected back into resin filter element 8 to resin filter element 8 into
Row rinses, and flushing waste is discharged through resin filter element water inlet 801 and the second blowdown valve 21.
The structural schematic diagram of another pretreatment softening regeneration positive backwashing system of auxiliary salt adding as shown in Figure 2, reference
Fig. 1, third three-way pipe described in this structural schematic diagram 703 are arranged in the softening pure water pipe being connect with resin filter element water outlet 802
On road 12, the 5th three-way pipe 705 is arranged in the saline line 17 connected between brine valve 15 and the first check valve 16,
It is remaining that identical as Fig. 1 details are not described herein again;
When described in this structural schematic diagram without electric or standby mode, control system 28 controls the course of work and Fig. 1 one kind of pump valve
The course of work of the pretreatment softening regeneration positive backwashing system of auxiliary salt adding is identical, except that when starting auxiliary salt adding regeneration
When:First inlet valve 6 is closed, and brine valve 15 and the second blowdown valve 21 are opened, and the brine of salt core 14 passes through brine valve 15 and resin
Filter core water outlet 802 is redirected back into resin filter element 8 and is rinsed, and flushing waste is through resin filter element water inlet 801 and the second blowdown
Valve 21 is discharged.
The water purification machine for including the pretreatment softening regeneration positive backwashing system of auxiliary salt adding as shown in Figure 3, including booster pump
13 and reverse osmosis membrane 5, one end of the reverse osmosis membrane 5 is equipped with feed water by reverse osmosis mouth 501, and the other end is provided with reverse osmose pure-water mouth
502 and the reverse osmosis concentrated mouth of a river 503, the water outlet of second inlet valve 10 by piping connection to the water inlet end of booster pump 13,
The water outlet of the booster pump 13 is connected to feed water by reverse osmosis mouth 501, the reverse osmose pure-water mouth by being pressurized water pipeline 27
502 by be equipped with the pure water pipeline 31 of the third check valve 29 and high-voltage switch gear 30 that can only be flowed to pure water water outlet 25 with it is pure
Water water outlet 25 connects, and the reverse osmosis concentrated mouth of a river 503 is connect by concentrated water pipeline 32 with flow-limiting valve 33.Tap water through first into
Water pipe 1 and the second water inlet pipe 2 introduce 4 filtration, purification of ultrafiltration membrane, then carry out water purification sofening treatment to tap water through resin filter element 8,
The colloid and organic matter and calcium ions and magnesium ions that go in water removal reduce the hardness of water, and obtained softening water purification is passed through by softening pure water pipe
Road 12 and the second inlet valve 10 opened introduce booster pump 13, then are introduced after the supercharging of booster pump 13 by being pressurized water pipeline 27
Reverse osmosis membrane 5 filters, and goes the pure water of output after water removal intermediate ion to be drawn by reverse osmose pure-water mouth 502, through pure water pipeline 31 the
Three check valves 29 and high-voltage switch gear 30 flow to pure water water outlet 25;The concentrated water containing high concentration ion being trapped passes through concentrated water spout
503, concentrated water pipeline 32 and flow-limiting valve 33 are discharged.
It below by embodiment 1 and combines shown in Fig. 1 and Fig. 2, it is positive and negative that pretreatment softening regeneration auxiliary salt adding is described in detail
The control method of rinse-system, with reference to figure 4, no electricity or the first inlet valve 6 is shown in a fully open operation when standby mode, the second inlet valve
10, brine valve 15, water purification backwash valve 23, the first blowdown valve 18 and the second blowdown valve 21 are in full-shut position, and tap water passes through
One inlet pipeline 1 is divided into two-way after introducing the first three-way pipe 701, respectively enters the second inlet pipeline 2 and third inlet pipeline 3,
Ultrafiltration membrane 4 is entered by the second inlet pipeline 2 and filters output ultrafiltration water purification, then through ultrafiltration membrane water outlet 402, the first inlet valve 6, net
Water lines 11 enter output softening water purification after resin filter element 8 softens and come together in softening water pipeline 12;By third inlet pipeline 3
It introduces auxiliary filter cartridge flushing 9 and purifies the water purification of output and divide again for two-way through the 6th three-way pipe 706, enter salt core 14 and soft water all the way
Salt dissolving mixing, flows to water purification backwash pipeline 22 all the way.
Soften the regeneration positive backwashing system of auxiliary salt adding with reference to pretreatment shown in FIG. 1, third three-way pipe 703 is arranged net
Water lines 11 and the structural schematic diagram for being connected to resin filter element water inlet 801, when starting pretreatment softening regeneration auxiliary salt adding:Control
System 28 processed controls the closing of the first inlet valve 6, brine valve 15 and 18 valve of the first blowdown valve and opens, and passes through the first inlet pipeline 1
Enter auxiliary 9 filtration, purification of filter cartridge flushing with third inlet pipeline 3, the water purification of output enters salt core 14, mixed with the dissolving of soft water salt
Output brine after conjunction, by brine valve 15, the first check valve 16, saline line 17 and third three-way pipe 703 by resin filter element into
The mouth of a river 801 enters resin filter element 8, to resin filter element 8 impregnate and be replaced with calcium and magnesium, displacement waste liquid passes through resin filter element water outlet
802 and first blowdown valve 18 be discharged;Regeneration auxiliary salt adding terminate, starts water purification just rinse soften resin when:The closing of brine valve 15,
First inlet valve 6 is opened, and tap water introduces ultrafiltration membrane 4 by first the first three-way pipe of inlet pipeline and the second inlet pipeline and filters
Output ultrafiltration water purification, then carried out into resin filter element 8 by resin filter element water inlet 801 through the first inlet valve 6 and water pipeline 11
It rinses, softened 12 and first blowdown valve 18 of water pipeline of calcium-magnesium-containing remaining waste is discharged in resin filter element 8, and knot is just being rinsed in water purification
When beam, startup water purification backwash softening resin:First blowdown valve 18 and the first inlet valve 6 are closed, and water purification backwash valve 23 opens, the
Two blowdown valves 21 are opened, through assisting the water purification that filter cartridge flushing 9 purifies to pass through water purification backwash pipeline 22, softening water pipeline 12 and tree
Fat filter core water outlet 802, which is redirected back into resin filter element 8, carries out depth flushing, and by remaining waste by resin filter element water inlet
801, the second three-way pipe 702, the second blow-off pipe 20 and the discharge of the second blowdown valve 21.
With reference to another pretreatment softening regeneration positive backwashing system of auxiliary salt adding shown in Fig. 2, third three-way pipe 703 is set
It sets on softening water pipeline 12, the saline line that the 5th three-way pipe 705 is arranged between brine valve 15 and the first check valve 16
On 17, when starting pretreatment softening regeneration auxiliary salt adding:Control system 28 control the first inlet valve 6 close, brine valve 15 and the
Two blowdown valves 21 are opened, and auxiliary 9 filtration, purification output of filter cartridge flushing is introduced by the first inlet pipeline 1 and third inlet pipeline 3
Water purification enter salt core 14, with soft water salt dissolving mix after output brine, through brine valve 15, the first check valve 16, Brine Pipe
Road 17, third three-way pipe 703 are redirected back into resin filter element 8 by resin filter element water outlet 802, to resin filter element 8 carry out impregnate with
Calcium and magnesium is replaced, and displacement waste liquid is discharged by resin filter element water inlet 801 and the second blowdown valve 21;Regeneration auxiliary salt adding terminates, opens
When resin filter element is just being rinsed in dynamic water purification:Brine valve 15 is closed, the first inlet valve 6 is opened, and the second blowdown valve 21 is closed, the first blowdown
Valve 18 is opened, and is carried out water purification and is just rinsed, tap water passes through the first inlet pipeline 1, the first three-way pipe 701 and the second inlet pipeline 2
Introduce ultrafiltration membrane 4 and filter output ultrafiltration water purification, then through the first inlet valve 6 and water pipeline 11 by resin filter element water inlet 801 into
Enter resin filter element 8 to be rinsed, softened 12 and first blowdown valve of water pipeline, 18 row of calcium-magnesium-containing remaining waste in resin filter element 8
Go out;When water purification just flushing terminates, starts water purification backwash softening resin:First blowdown valve 18 and the first inlet valve 6 are closed, water purification
Backwash valve 23 is opened, the second blowdown valve 21 is opened, through assisting the water purification that filter cartridge flushing 9 purifies to pass through water purification backwash pipeline 22, the
Two check valves 24, the first check valve 16, saline line 17, third three-way pipe 701 and resin filter element water outlet 802 are redirected back into tree
Depth flushing is carried out in fat filter core 8, and by remaining waste by 801 11 second blow-off pipe of water pipeline of resin filter element water inlet, 20 He
Second blowdown valve 21 is discharged.This method have the advantage that the water purification of water purification backwash pipeline 22 can be to brine valve when backwash softens resin 8
15 and first remaining brine between check valve 16 be rinsed, avoid the corrosion of the first check valve of brine pair 16.
It below by embodiment 2 and combines shown in Fig. 3, detailed description pretreatment softening regeneration auxiliary salt adding, which just backwashes, is
It unites the control method of water purification machine, control system 28 controls that the second inlet valve 10 is opened, booster pump 13 is run, tap water when pure water processed
4 filtration, purification of ultrafiltration membrane is introduced through the first water inlet pipe 1 and the second water inlet pipe 2, goes removing rust, silt, gel, organic matter output
Water purification, then through resin filter element 8 to tap water carry out water purification sofening treatment, water pipeline 11 enter resin filter element 4 soften, through tree
Fat filter core 4 removes removing calcium and magnesium, reduces the softening water purification of hardness by softening water pipeline 12, the second inlet valve 10 introducing booster pump
13, softening water purification after supercharged by be pressurized water pipeline 27 introduce reverse osmosis membrane 5 carry out Pure water preparation, go deionization and other
The pure water of inorganic salts output comes together in after pure water outlet 502 and flows to pure water water outlet 25 by pure water pipeline 31, is trapped
Concentrated water containing high concentration ion, inorganic salts is discharged through concentrated water water outlet 503, concentrated water pipeline 32 and flow-limiting valve 33.
It should be noted that for each embodiment of the method above-mentioned, for simple description, therefore it is all expressed as to a system
The combination of actions of row, but those skilled in the art should understand that, the present invention is not limited by the described action sequence, because
For according to the present invention, certain some step can be performed in other orders or simultaneously.Secondly, those skilled in the art also should
Know, embodiment described in this description belongs to preferred embodiment, involved action and module not necessarily this hair
Necessary to bright.
In the above-described embodiments, it all emphasizes particularly on different fields to the description of each embodiment, is not described in some embodiment
Part, may refer to the associated description of other embodiment.Specific case used herein is to the principle of the present invention and implementation
Mode is expounded, and the explanation of above example is only intended to facilitate the understanding of the method and its core concept of the invention;Meanwhile
For those of ordinary skill in the art, according to the thought of the present invention, has change in specific embodiments and applications
Become place, in conclusion the content of the present specification should not be construed as limiting the invention.
Claims (7)
1. the pretreatment softening regeneration positive backwashing system of auxiliary salt adding, including by the first inlet pipeline(1), ultrafiltration membrane(4), first
Inlet valve(6), resin filter element(8)With the second inlet valve(10)Between pass sequentially through the pretreatment melded system of piping connection;By
First inlet pipeline(1), auxiliary filter cartridge flushing(9), through assist filter cartridge flushing(9)Filtering introduces the 6th three-way pipe(706)After divide
It Jin Ru not salt core(14), and pass through saline line(17)With third three-way pipe(703)Connection, and flow to the 5th three-way pipe
(705)Water purification backwash pipeline(22)The positive and negative flush loop of regeneration auxiliary salt adding of composition, it is characterised in that:First water inlet
Pipeline(1)Access the first three-way pipe(701)After be divided into two branches:Pass through the second inlet pipeline all the way(2)With ultrafiltration membrane 4 into
The mouth of a river(401)Connection, the water outlet of the ultrafiltration membrane 4(402)Pass through pipeline and the first inlet valve(6)Water inlet end connection, institute
State the first inlet valve(6)Water outlet by being provided with the second three-way pipe(702)With third three-way pipe(703)Water pipeline
(11)It is connected to resin filter element water inlet(801), the resin filter element water outlet(802)By being provided with the 4th three-way pipe
(804)With the 5th three-way pipe(805)Softening water pipeline(12)With the second inlet valve(10)Water inlet end connection;Another way passes through
Cross third inlet pipeline(703)With auxiliary filter cartridge flushing(9)Water inlet connects, the auxiliary filter cartridge flushing(9)Water outlet it is logical
It crosses pipeline and accesses the 6th three-way pipe(706)After be divided into two branches:Pass through pipeline and salt core all the way(14)Water inlet connection, institute
State salt core(14)Water outlet be provided with brine valve(15)The brine valve(15)Pass through saline line(17)It is connected to the three or three
Siphunculus(703), all the way by being equipped with water purification backwash valve(23)Water purification backwash pipeline(22)It is connected to the 5th three-way pipe
(705)And by the second three-way pipe(702)Pass through the second blowoff line(20)Second blowdown valve of connection(21)With the four or three
Siphunculus(704)Pass through the first blowoff line(19)First blowdown valve of connection(18)The regeneration auxiliary salt adding of composition just backwashes back
Road.
2. the pretreatment softening regeneration positive backwashing system of auxiliary salt adding according to claim 1, it is characterised in that:Described
Three three-way pipes(703)It can also be arranged in resin filter flask water outlet(802)With the second inlet valve(10)The softening pure water pipe of connection
Road(12)On.
3. the pretreatment softening regeneration positive backwashing system of auxiliary salt adding according to claim 1, it is characterised in that:The salt
Water valve(15)Water outlet and third three-way pipe(703)Between the saline line that connects(17)Being additionally provided with can only be to third threeway
Pipe(703)First check valve of flowing(16).
4. the pretreatment softening regeneration positive backwashing system of auxiliary salt adding according to claim 1, it is characterised in that:It is described net
Water backwash valve(23)With the 5th three-way pipe(705)Between the water purification backwash pipeline that connects(22)Being additionally provided with can only be to the 5th threeway
Pipe(705)Second check valve of flowing(24).
5. the pretreatment softening regeneration positive backwashing system of auxiliary salt adding according to claim 1,2,3, it is characterised in that:Institute
State third three-way pipe(703)Mounted on softening water pipeline(12)When, the 5th three-way pipe(705)It can also be arranged in brine
Valve(15)With the first check valve(16)Between the saline line that connects(17)On.
6. the water purification machine according to claim 1 for including the pretreatment softening regeneration positive backwashing system of auxiliary salt adding, including
Booster pump(13)And reverse osmosis membrane(5), the reverse osmosis membrane(5)One end be equipped with feed water by reverse osmosis mouth(501), other end setting
There is reverse osmose pure-water mouth(502)With the reverse osmosis concentrated mouth of a river(503), second inlet valve(10)Water outlet pass through piping connection
To booster pump(13)Water inlet end, the booster pump(13)Water outlet pass through be pressurized water pipeline(27)Reverse osmosis is connected to penetrate into
The mouth of a river(501), the reverse osmose pure-water mouth(502)It can only be to pure water water outlet by being equipped with(25)The third check valve of flowing
(29)And high-voltage switch gear(30)Pure water pipeline(31)With pure water water outlet(25)Connection, the reverse osmosis concentrated mouth of a river(503)It is logical
Overrich water lines(32)With flow-limiting valve(33)Connection.
7. a kind of control method of pretreatment softening regeneration positive backwashing system of auxiliary salt adding as described in claim 1-5,
It is characterized in that:First inlet valve when without electric or standby mode(6)It is shown in a fully open operation, the second inlet valve(10)Brine valve(15)
Water purification backwash valve(23)First blowdown valve(18)With the second blowdown valve(21)In full-shut position, tap water is through the first inlet pipeline
(1)Access the first three-way pipe(701)After respectively enter the second inlet pipeline(2)With third inlet pipeline(3), by the second water inlet pipe
Road(2)Into ultrafiltration membrane(4)Output ultrafiltration water purification is filtered, then through ultrafiltration membrane(4)Water outlet(401)First inlet valve(6)Only
Water lines(11)Into resin filter element(8)Output softens water purification after softening, and comes together in softening water pipeline(12);By third into
Water lines(3)Into auxiliary filter cartridge flushing(9)The water purification of output is purified through the 6th three-way pipe(706)It is divided into two-way, introduces all the way
Salt core(14)With soft water salt mixed dissolution, flow to water purification backwash valve all the way(23);
When third three-way pipe(703)It is arranged in water pipeline(11)And it is connected to resin filter element water inlet(801), start pretreatment
When softening regeneration auxiliary salt adding:Control system(28)Control the first inlet valve(6)It closes, brine valve(15)With the first blowdown valve
(18)It opens, tap water passes through the first inlet pipeline(1)With third inlet pipeline(3)Into auxiliary filter cartridge flushing(9)Filtering is net
Change, output water purification enters salt core(14), output brine after mixing is dissolved with soft water salt, passes through brine valve(15), the first check valve
(16)Saline line(17)With third three-way pipe(703)By resin filter element water inlet(801)Into resin filter element(8), to resin
Filter core(8)Impregnate and replaced with calcium and magnesium, displacement waste liquid passes through resin filter element water outlet(802)With the first blowdown valve(18)Row
Go out, regeneration auxiliary salt adding terminates, starts water purification and just rinse resin filter element(8)When:Brine valve(15)It closes, the first inlet valve(6)
It opens, tap water passes through the first inlet pipeline(1), the first three-way pipe(701)With the second inlet pipeline(2)Introduce ultrafiltration membrane(8)
Output ultrafiltration water purification is filtered, then through the first inlet valve(6), water pipeline(11)By resin filter element water inlet(801)Into resin
Filter core(8)It is rinsed, resin filter element(8)The interior softened water pipeline of calcium-magnesium-containing remaining waste(12)With the first blowdown valve
(18)Discharge, when water purification just flushing terminates, starts water purification backwash softening resin:First blowdown valve(18)With the first inlet valve
(6)It closes, water purification backwash valve(23), the second blowdown valve(21)It opens, through assisting filter cartridge flushing(9)The water purification of purification passes through water purification
Backwash valve(23), water purification backwash pipeline(22)With softening water pipeline(12)By resin filter element water outlet(802)It is redirected back into tree
Fat filter core(8)Interior progress depth flushing, flushing waste water pass through resin filter element water inlet(801)With the second blowdown valve(21)Discharge;
When third three-way pipe(703)Setting with resin filter element water outlet(802)The softening water pipeline of connection(12)Above, the 5th
Three-way pipe(705)It is arranged in brine valve(15)With the first check valve(16)Between the saline line that connects(17)On, start pre- place
When reason softening regeneration auxiliary salt adding system:Control system(28)Control the first inlet valve(6)It closes, brine valve(15)And second row
Dirty valve(21)It opens, passes through the first inlet pipeline(1)With third water inlet pipe(3)Pass enters to assist filter cartridge flushing(9)Filtration, purification
The water purification of output enters salt core(14), output brine after mixing is dissolved with soft water salt, passes through brine valve(15), the first check valve
(16), saline line(17)With third three-way pipe(703)By resin filter element water outlet(902)It is redirected back into resin filter element(8), right
Resin filter element(8)It carries out plus salt is impregnated and replaced with calcium and magnesium, displacement waste liquid passes through resin filter element water inlet(801)With the second blowdown valve
(21)Discharge, regeneration auxiliary salt adding terminate, starts water purification just rinse soften resin when:Brine valve(15)It closes, the first inlet valve
(6)It opens, the second blowdown valve(21)It closes, the first blowdown valve(18)It opens, tap water passes through the first inlet pipeline(1)One or three
Siphunculus(701)With the second water inlet pipe(2)Pass enters ultrafiltration membrane(4)Output ultrafiltration water purification is filtered, then through the first inlet valve(6), it is net
Water lines(11)By resin filter element water inlet(801)Into resin filter element(8)It is rinsed, resin filter element(8)Interior calcium-magnesium-containing is residual
Stay waste liquid through resin filter element water outlet(802), softening water pipeline(12)With the first blowdown valve(18)Knot is just being rinsed in discharge, water purification
When beam, startup water purification backwash resin filter element:First blowdown valve(18)With the first inlet valve(6)It closes, water purification backwash valve(23)、
Second blowdown valve(21)It opens, through assisting filter cartridge flushing(9)The water purification of purification passes through water purification backwash valve(23), water purification backwash pipeline
(22), saline line(17), the first check valve(16)With resin filter element water outlet(802)It is redirected back into resin filter element(8)It is interior into
Row depth is rinsed, and by flushing water by resin filter element water inlet(801), the second blowdown valve(21)Discharge.
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CN111559779A (en) * | 2020-05-28 | 2020-08-21 | 佛山市顺德区美的饮水机制造有限公司 | Water purifying device and method for activating ion resin filter element of water purifying device |
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Cited By (1)
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CN111559779A (en) * | 2020-05-28 | 2020-08-21 | 佛山市顺德区美的饮水机制造有限公司 | Water purifying device and method for activating ion resin filter element of water purifying device |
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Application publication date: 20180907 |