CN1188744A - Water purification system having chlorine generating function in addition to bacteriostatic function - Google Patents
Water purification system having chlorine generating function in addition to bacteriostatic function Download PDFInfo
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- CN1188744A CN1188744A CN97126020A CN97126020A CN1188744A CN 1188744 A CN1188744 A CN 1188744A CN 97126020 A CN97126020 A CN 97126020A CN 97126020 A CN97126020 A CN 97126020A CN 1188744 A CN1188744 A CN 1188744A
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Abstract
In a water purification system for purifying raw water with a first d.c. voltage is applied between a conductive adsorber portion (20) and a primary electrode in the raw water, a second d.c. voltage higher than the first d.c. voltage is applied in place of the first d.c. voltage at intervals between the adsorber portion and the primary electrode to accelerate generation of chlorine from the raw water. The primary electrode is opposite to the adsorber portion with a particular space left therebetween. It is preferable that the adsorber portion is provided with a supplementary electrode (29) which is opposite to the primary electrode so that the particular space is left therebetween.
Description
The present invention relates to the former water of a kind of purification,, provide the water purification system of civilian or commercial tap water such as tap water and underground water.
In such water purification system, the sterilization of former water is carried out in every way.As nearest technological trend, be extensive use of hollow fiber film assembly (the large quantities of supplies of energy), come the elimination of micro-organisms and bacterium, suppress its growth or propagation therefrom.Also use unit and/or another unit that produces an amount of chlorine that carries out the former water of electrolysis.
Usually, former water such as tap water and underground water, contains multiple pollutent, that is, chlorine residue is such as hypochlorous acid (HCLO
-), smell of going rotten, trichloromethane, chlorination organism, pigment or the like.In the water purification system as a water treatment system, former current are through sorbent material part (typically, activated carbon), with the form absorption of adsorbent and remove pollutent above-mentioned.Therefore, former water partly is cleaned through sorbent material, can be used as the supply of purifying waste water.In this manual, will be referred to as purification pattern to this behaviour's kind pattern.
In this purification pattern, the water requirements signal provision that produces when opening according to tap is purified waste water.When there not being the water requirements signal, purify waste water supply when stopping, because the mobile of former water is interrupted, on sorbent material part may grow various microorganisms and bacterium.In order to suppress the growth of microorganism and bacterium, this purification pattern comprises a sterilization operation that faint volts DS is put on the sorbent material part.
As time goes on, the sorbent material part will be assembled adsorbent and microorganism and bacterial product.In order to remove adsorbent and microorganism and bacterium, after this purification pattern, add a regeneration mode, in regeneration mode, a voltage of alternating current is put on the sorbent material part, come the material of desorb absorption, eliminate and desorb microorganism and bacterium.
In above-mentioned water purification system commonly used, generally as flow through sorbent material part and being cleaned of the tap water of former water.Yet when tap water was cleaned in the sorbent material part, the available chlorine composition that contains in the tap water also was removed.This is easy to cause grow in the water purification system downstream line microorganism and bacterium.In this case, microorganism and bacterium are sneaked in the water from the purification of water purification system.
For fear of problem above-mentioned, a chlorine still is installed in the downstream of water purification system.Chlorine still is to be used for producing chlorine to replenish and be adsorbed the available chlorine composition that agent is partly removed.
Yet, except that water purification system, use chlorine still in addition, not only need extra installing space, and need extra-pay.
Therefore, the object of the present invention is to provide a kind of function to have the water purification system of bacteria resistance function again with generation chlorine.
Along with the carrying out of describing, other purpose of the present invention will become very clear.
The water purification system that the present invention is suitable for is to be used for purifying former water.Water purification system comprises a conductive adsorbent part that is placed in the former water current, one in former water current conductive adsorbent part opposite and leave specific spatial primary electrode therebetween, the first voltage application portion part that is connected with primary electrode with conductive adsorbent part, be used between conductive adsorbent part and primary electrode, applying first volts DS, so that conductive adsorbent part and primary electrode are respectively as anode and negative electrode, make conductive adsorbent partly purify first volts DS of former water, with the second voltage application portion part that is connected with primary electrode with conductive adsorbent part, be used for applying second volts DS between conductive adsorbent part and primary electrode, second volts DS is higher than first volts DS and quickens the generation of chlorine in the former water.
Fig. 1 is the sectional view of the water purification system of first embodiment of the invention
Fig. 2 is the skeleton diagram of water purification system control section shown in Figure 1.
Fig. 3 is a red-tape operati schema of describing water purification system shown in Figure 1.
Fig. 4 describes red-tape operati time diagram shown in Figure 3.
Fig. 5 is the graphic representation of an expression with respect to the chlorine gas concentrations that chlorine ion concentration produced different in the tap water as former water.
Fig. 6 is a red-tape operati schema of describing the water purification system of second embodiment of the invention.
Fig. 7 describes red-tape operati time diagram shown in Figure 6.
Fig. 8 is the sectional view of the water purification system of third embodiment of the invention.
Fig. 9 is the decomposition diagram of electrode assembling in the expression water purification system shown in Figure 8.
Figure 10 be describe water purification system shown in Figure 8 the red-tape operati schema.
Figure 11 describes red-tape operati time diagram shown in Figure 10.
Figure 12 is the water purification system sectional view of fourth embodiment of the invention.
Now, be described with regard to several optimum examples of the present invention with reference to accompanying drawing.
At first with reference to Fig. 1, the water purification system of first embodiment of the invention is used for purifying former water, and it comprises a cylindrical water pot 10 that is used to store former water.Water pot 10 has correspondingly by the top and bottom of loam cake 11 and lower cover 12 sealings.Water pot 10, loam cake 11 and lower cover 12 all are to make with insulating material, such as, acrylic resin.Loam cake 11 has an outlet 11a who is connected with tap (not shown), and it is supplied according to well-known in the art mode and purifies waste water.Lower cover 12 has an inlet 12a who former water is introduced water pot 10.Inlet 12a is connected on the water-supply pipe 13 that has feed water valve 13a, prefilter 13B and check valve 13C.Feed water valve 13a is used for allowing and stoping former water to pass through.Check valve 13C is used for anti-sealing and refluxes from water pot 10.Inlet 12a also is connected on the delivery pipe 14 that has bleed valve 14a.
On the other hand, outlet 11a is connected on the air leading-in conduit 15 that has air importing valve 15a.Close when bleed valve 14a and air import valve 15a, when feed water valve 13a opened, former water was fed in the water pot 10.On the contrary, when bleed valve 14a and air import that valve 15a opens and feed water valve 13a when closing, former water just emits from water pot 10.
Water purification system comprises a cylindrical sorbent material part 20 of being made by the activated carbon fiber with conductivity.Cylindrical sorbent material part 20 is placed in the water pot 10.Sorbent material part 20 has a last axle head of being clamped by first electrode 21 of flat pattern by loam cake 11, and a lower shaft end of being clamped by second electrode 22 of flat pattern by electrode holder 23.The lower shaft end of sorbent material part 20 is considered to a special part.
In the sorbent material part 20 of said structure, rising pipe 27 has predetermined gap or space from the inner circumferential surface of sorbent material part 20, and vertically extends.In this case, the inner circumferential surface of sorbent material part 20 is counted as special part.
Rising pipe 27 has many discharge orifices, is used to make purify waste water flow through sorbent material part 20 arrival outlet 11a.Rising pipe 27 is made by electro-conductive material, claims that hereinafter it is the third electrode that is considered to primary electrode.The electro-conductive material of third electrode 27 is made up of the titanium utmost point, and titanium is extremely gone up and coated a kind of material that is selected from platinum, platinum iridium alloy, carbon, the mixed carbon resin selectively, and the electro-conductive material of third electrode 27 has a little chlorine overvoltage.
As mentioned above, the water purification system of Fig. 1 has first, second and third electrode 21,22 and 27.In the antibacterial operation in the purification pattern that will describe subsequently, a volts DS by second and third electrode 22 and 27 put on the sorbent material part 20 of injecting former water, suppress the growth of microorganism and bacterium.On the other hand, in the regeneration mode after purification pattern, a voltage of alternating current is put on sorbent material part 20 by first and second electrodes 21 and 22, comprise trichloromethane and various organic adsorbent with desorb, and the elimination of micro-organisms and bacterium.Purification pattern and regeneration mode hocket with pre-set time interval.
Below with reference to Fig. 2, the control section of water purification system is described.In description subsequently, the antibacterial operation in the purification pattern will be described as characteristic of the present invention.
The water purification system of present embodiment also comprises a control unit 30 of being carried out by microcomputer, and water purification system is operation automatically.Control unit 30 comprises the storer 32 of 31 and storage control programs of a central processing unit (CPU).Control unit 30 has I/ O port 33 and 34, is used to import the signal from water supply signal generation unit 35 and timing register 36, and is used for signal is outputed to feed water valve 13a, voltage-regulating circuit 38 and polarity switching 39.Water supply signal generation unit 35 produces a valve opening signal or water supply signal along with opening of feed water valve 13a.Timing register 36 produces various time signals.According to valve opening signal and time signal, control unit 30 control voltage-regulating circuit 38 and polarity switchings 39.Voltage-regulating circuit 38 is connected with a direct supply 40 with polarity switching 39, so that direct supply 40 produces selected level and selected polar volts DS.In addition, control unit 30 is controlled feed water valve 13a according to the well-known mode in present technique field.
Voltage-regulating circuit 38 is connected with control unit 30, and it is used for setting the first volts DS EA1 and the second volts DS EA2 on two different levels.The first volts DS EA1 has the low voltage that enough captures microorganism and bacterium, such as 3V.On the other hand, the second volts DS EA2 have can the former water of electrolysis to produce the higher voltage of chlorine, such as 12V.
The operation of the control section in the antibacterial operation is described now.With reference to Fig. 3 and Fig. 4, suppose that water purification system is in purification pattern.Control the supply of former water, alternately be in continuous regime and interruption status in the minimum rate of accumulation shown in Figure 4 institute target mode.
In the SA1 step, control unit 30 is with reference to having or not valve opening signal to judge whether feed water valve 13a closes.When feed water valve 13a closed, water supply signal generation unit 35 produced a water supply signal or special signal.Control unit 30 is according to the operation of special signal control voltage-regulating circuit 38 and direct supply 40.In this case, water supply signal generation unit 35 is thought a signal generation device.Control unit 30 can be according to the operation of special signal control polarity switching 39.
Under any circumstance, when feed water valve 13a closed, water purification system started antibacterial operation.Proceed to step SA2 from step SA1.At step SA2, the standard polarity voltage application time Ts of preliminary election is set in the timing register 36.Be step SA3 behind the step SA2, in this step, control unit 30 excites direct supply 40 by voltage-regulating circuit 38.As a result, the first volts DS EA1 be applied to second and third electrode 22 and 27 between, therefore, second and third electrode 22 and 27 just respectively as anode and negative electrode.Like this, microorganism and the bacterium that has a faint negative ion just become trapped in the sorbent material part 20.In addition, microorganism on the sorbent material part 20 and the growth of bacterium also are suppressed.In this case, the combination of voltage-regulating circuit 38 and direct supply 40 is called first voltage bringing device.In the process of carrying out the SA3 step, control unit 30 is referred to as first excitation apparatus.
Step SA4 behind step SA3 judges whether the standard polarity voltage application time Ts of preliminary election is over and done with.Over and done with when the standard polarity voltage application time of preliminary election, step SA4 just proceeds to step.SA5 is in the SA5 step, and polarity switching 39 is determined the polarity of the second volts DS EA2, and therefore second electrode 22 and third electrode 27 are respectively as negative electrode and anode.In addition, the opposite polarity voltage application time Tr of preliminary election is set in the timing register 36.Be step SA6 behind the step SA5, in this step, pilot circuit 40 excites direct supply 40 by voltage-regulating circuit 38.As a result, the second volts DS EA2 be applied to second and third electrode 22 and 27 between, therefore second and third electrode 22 and 27 respectively as negative electrode and anode.In this case, the combination of voltage-regulating circuit 38 and direct supply 40 is called second voltage bringing device.In the process of carrying out step SA5, pilot circuit 30 is called second excitation apparatus.The group of first and second excitation apparatus and be called excitation apparatus.
By applying the second volts DS EA2 of opposite polarity,, produce chlorine (hypochlorous acid (HCLO by the chlorion in the former water in third electrode 27 sides
-)), to improve the concentration of chlorine.Because third electrode 27 is to be made by above-described material with little chlorine overvoltage, so can produce chlorine efficiently by chlorion.
Be step SA7 after S steps A 6,, judge whether the opposite polarity voltage application time Tr of preliminary election is over and done with in this step.When the over and done with step of the opposite polarity voltage application time Tr of preliminary election just, SA7 turns back to step SA1.
Translate into Fig. 5, describe the variation of cl concn.Here the concentration of supposing chlorion in the former water is 15ppm, and the voltage application time equals 30 seconds.In this case, can obtain the chlorine gas concentration of about 1.0ppm.Be appreciated that when chlorine ion concentration is up to 30ppm the former water that from figure the chlorine gas concentration of about 1.0ppm can obtain in shorter voltage application time.On the contrary, when chlorine ion concentration in the former water hangs down to 10ppm, just need longer voltage application time.Therefore, the opposite polarity voltage application time Tr of preliminary election determines according to the water quality (chlorine ion concentration) of former water.
In the water purification system of this embodiment, when feed water valve 13a closes,, apply first volts DS EA1 of standard polarity and the second volts DS EA2 of opposite polarity by second and third electrode 22 and 27.Therefore, except bacteria resistance function of the prior art, also has the concentration that the function that produces chlorine improves chlorine.Therefore, need chlorine still no longer in addition.
Although control the second volts DS EA2 constant high-voltage value is arranged, such as, be 12V in the present embodiment, it be applied to first and third electrode 21 and 27 between still can produce a constant current value, such as 0.4A.
With reference to Fig. 6 and Fig. 7, the water purification system of second embodiment of the invention is described.This water purification system has the structure similar to water purification system illustrated in figures 1 and 2.Therefore, in the following description, the operation that is primarily aimed at water purification system is described.
At first step SB1, judge whether the feed water valve 13a in the purification pattern closes.If feed water valve 13a closes, step SB1 proceeds to step SB2, and the first voltage EA1 of standard polarity is applied on first and second electrodes 22 and 27.If feed water valve 13a is opening, if just generation is purified waste water and is supplied to water tap, 1 step SB proceeds to step SB3, to apply the second voltage EA2 of opposite polarity.
In a second embodiment, when the supply of former water is interrupted respectively and continued, present the function of sterilizing function and generation chlorine respectively.The content of describing among other operation and first embodiment is similar.
With reference to Fig. 8, the water purification system of third embodiment of the invention is described.Identical part marks with identical reference number, and no longer describes.
Be clear that from Fig. 8 sorbent material part 20 has a cylindrical form interior surface that extends between two axle heads, it extends to form a hollow space in vertical direction.First and second electrodes 21 and 22 are placed on the axle head of sorbent material part 20 respectively.Third electrode 27 is placed on as primary electrode in the hollow space of sorbent material part 20, leaves certain space between them.
In the 3rd embodiment water purification system, sorbent material part 20 comprises an activated carbon fiber part 20a and the 4th electrode 29.Activated carbon fiber part 20a is made cylindrical by the activated carbon fiber with electroconductibility, it has relative axle head, also has the cylindrical form interior surface that extends to form hollow space between axle head.The 4th electrode 29 is positioned at the hollow space of activated carbon fiber part 20a, and it closely contacts with the cylindrical form interior surface of activated carbon fiber part 20a.The internal surface of the 4th electrode 29 and first electrode 21 connects into an integral body, inserts in the hollow space of activated carbon fiber part 20a, facing to third electrode 27, wherein leaves a space.Therefore, the 4th electrode 29 is between the internal surface and third electrode 27 of activated carbon fiber part 20a.
With reference to Fig. 9, the 4th electrode 29 has many discharge orifice 29a on its circumferential edge wall in addition.The discharge orifice 29a of the 4th electrode 29 is flow through in purifying waste water of the activated carbon fiber part of flowing through 20a, flows to third electrode 27.The 4th electrode 29 is regarded a supporting electrode as.
As first, second and third electrode 21,22 and 27, the 4th electrode 29 is made by electro-conductive material, electro-conductive material by scribble platinum, platinum iridium alloy, carbon selectively, mix carbon resin wherein a kind of titanium utmost point of material form, the 4th electrode has a little chlorine overvoltage.
In the antibacterial operation in purification pattern, a volts DS is put on the sorbent material part 20 of injecting former water by first electrode 21 (with the 4th electrode 29) and third electrode 27, suppress the growth of microorganism and bacterium, this point will be described in detail subsequently.On the other hand, in the regeneration mode after purification pattern, a voltage of alternating current is put on sorbent material part 20 by first electrode 21 (with the 4th electrode 29) and second electrode 22, comprise trichloromethane and various organic adsorbent with desorb, with the elimination of micro-organisms and bacterium.Described in first embodiment, purification pattern and regeneration mode hocket with pre-set time interval.
The water purification system of the 3rd embodiment and the control section 30 that analog structure is arranged together with the water purification system shown in Figure 2 of first embodiment.In the following description, the operation of antibacterial operation in the purification pattern and generation chlorine will be described as characteristic.
Voltage-regulating circuit 38 by direct supply 40 first and third electrode 21 and 27 between set the first volts DS EA1, the second volts DS EA2 and the 3rd volts DS EA3.The first volts DS EA1 has the low voltage that enough captures microorganism and bacterium, such as 3V.On the other hand, second with the 3rd volts DS EA2 and EA3 have respectively can electrolysis former water to produce the relative higher voltage of chlorine, such as 12V.The first and the 3rd volts DS EA1 and EA3 are standard polarities.The second volts DS EA2 is an opposite polarity.
Water supply signal generation unit 35 is to be used for producing when feed water valve 13a opens valve opening signal.The water supply signal is sent to control unit 30.CPU31 calculates the number of times that produces the chlorine operation.
With reference to Figure 10 and Figure 11 and Fig. 2, the operation of control section in the antibacterial operation is described.Under the continuous regime of former water supply, first, second that applies and tertiary voltage EA1, EA2 and EA3 are interrupted.Suppose that water purification system operates in the purification pattern.At step SC1, with reference to having or not valve opening signal to judge whether feed water valve 13a closes.13a closes when feed water valve, and step SC1 just carries out step SC2.At step SC2, whether the timed interval Tc of judgement generation chlorine begins to calculate over and done with from the operation of purification pattern.If the timed interval Tc that produces chlorine is not also not in the past, step SC2 just proceeds to step SC3, in this step, the first volts DS EA1 of standard polarity be applied to first and third electrode 21 and 27 between.Here note, standard polarity refer to first and third electrode 21 and 27 respectively as anode and negative electrode.Therefore, microorganism and the bacterium that has a faint negative ion just become trapped in the sorbent material part 20.And microorganism in the sorbent material part 20 and the growth of bacterium also are suppressed.Therefore, antibacterial operation has just been carried out.When carrying out step SC3, the combination of voltage-regulating circuit 38, polarity switching 39 and direct supply 40 is referred to as first voltage bringing device.
After operation in purification pattern begins, when produce chlorine the timed interval, Tc was over and done with the time, step SC2 just proceeds to step SC4.In step SC4, on timing register 36, set preliminary election voltage application time Tv.Be step SC5 behind step SC4, in this step, the crust opposite polarity the second volts DS EA2 be applied to second and third electrode 22 and 27 between.Applying of the second volts DS EA2 of opposite polarity continues to reach preliminary election voltage application time Tv.Step SC6 after step SC5 judges whether over and done with preliminary election voltage application time Tv begins to calculate from applying the second volts DS EA2.Here notice that opposite polarity refers to by first electrode 21 as the 4th electrode 29 of negative electrode and polarity as anodic third electrode 27.By applying the second volts DS EA2,, quicken to produce chlorine (hypochlorous acid (HCLO by the chlorion of the 4th electrode 29 those sides such as 12V
-)), to increase chlorine gas concentration.Like this, the operation that produces chlorine has just been carried out effectively.When carrying out step SC5, voltage-regulating circuit 38, polarity switching 39 are called second voltage bringing device with the combination of direct supply 40.
Here, the variation of chlorine gas concentration is to similar together with the content that first embodiment describes with reference to Fig. 5.
Repeat if in opposite polarity, produce the operation of chlorine,, will accumulate scale at the 4th electrode 29 places as negative electrode such as 10 times.Therefore, among the step SC7 after step SC6, calculate the times N 1 that the second volts DS EA2 applies.Among the step SC8 after step SC7, judge whether times N 1 equals 10.If times N 1 equals 10, step SC8 just proceeds to step SC9.In step SC9, judge whether feed water valve 13a closes.If feed water valve 13a closes, step SC9 just carries out step SC10, in this step, judges whether the timed interval Tc that produces chlorine is over and done with.Also do not have in the past if produce the timed interval Tc of chlorine, step SC10 just proceeds to step SC11, in this step, applies the first volts DS EA1 of standard polarity.On the other hand, if it is over and done with to produce the timed interval Tc of chlorine, step SC10 just proceeds to step SC12, in this step, applies the 3rd volts DS EA3 of standard polarity.Especially, polarity switching 39 becomes the 3rd volts DS EA3 to the second volts DS EA2.When carrying out step SC12, the combination of voltage-regulating circuit 38, polarity switching 39 and direct supply 40 is as second voltage bringing device, it is used for applying the 3rd volts DS EA3 between the 4th electrode 29 and third electrode 27, therefore the 4th electrode and third electrode 29 and 27 are just respectively as anode and negative electrode.
After the step SC12 is step SC13, in this step, judges whether over and done with preliminary election voltage application time Tv begins to calculate from applying tertiary voltage EA3.If Tv is over and done with for preliminary election voltage application time, step SC13 just proceeds to step SC14, in this step, calculates the times N 2 that the 3rd volts DS EA3 of standard polarity applies.After the step SC14 is step SC15.In step SC15, judge whether times N 2 equals 5, such as.If times N 2 equals 5, step SC15 just turns back to step SC9.Like this, the disagreeable scale that is accumulated on the 4th electrode 29 has just been removed.
In above-described the 3rd embodiment, the times N 2 that times N 1 that the second volts DS EA2 of opposite polarity applies and the 3rd volts DS EA3 of standard polarity apply equals 10 and 5 respectively.Therefore, the times N 2 of times N 1 to the three volts DS EA3 of the second volts DS EA2 is big.This is because in the antibacterial operation of the first volts DS EA1 by applying standard polarity, and scale is sticking and be accumulated on the third electrode 27.Consider this point, will increase by the times N 1 of the second volts DS EA2, come to remove disagreeable scale from third electrode 27 effectively.Although control the second and the 3rd volts DS EA2 and EA3 higher constant voltage values is arranged, first and third electrode 21 and 27 between also to apply and keep the controllable current value of constant, such as 0.4A.
According to above-described the 3rd embodiment, in each opposite polarity and standard polarity, can both produce chlorine.Therefore can remove the scale on third and fourth electrode 27 and 29 reliably, guarantee that antibacterial and chlorine steady in a long-term produces function.
The 4th electrode 29 is positioned at the inside of sorbent material part 20, produces chlorine between third and fourth electrode 27 and 29.Adopt this structure, can prevent that the sorbent material part 20 of activated carbon is subjected to producing the disadvantageous effect of chlorine.Like this, can prevent that activated carbon part 20 is damaged.
With reference to Figure 12, a fourth embodiment in accordance with the invention is described water purification system.Identical parts are adopted and are denoted by like references.
In the water purification system of the 4th embodiment, the 4th electrode 29 is columniform, and separates with the inner circumferential surface of activated carbon fiber part 20a, leaves an annular space 28 between them.The position that each discharge orifice 29a of the 4th electrode 29 makes and each discharge orifice 27a of third electrode 27 are inconsistent along the position that the radial direction of sorbent material part 20 is made.
Thus much, related several embodiment are described the present invention, concerning those skilled in the art, are easy to implement the present invention according to other variety of way.For example, third and fourth electrode can be by two half-cylindrical electrodes in conjunction with forming.The discharge orifice can be the Any shape except that circular port shown in Figure 9.The valve (end marks) that is opposite to terminal (water tap) can use different valve opening signals.If water purification system is installed in the vending machine, can use from the beverage of the switch signal of selling goods of selling goods of the beverage in the vending machine.In addition, can be placed on flow sensor the downstream of water purification system, detect the flow of purifying waste water.In this case, can use flow detecting signal from flow sensor.Equally, can be placed on pressure transmitter the downstream of water purification system, detect the water flow pressure of purifying waste water.In this case, can use pressure detecting signal from pressure transmitter.
Claims (15)
1, a kind of water purification system that purifies former water comprises:
A conductive adsorbent part (20) that is placed in the described former water current;
One is arranged on conductive adsorbent opposite partly in the described former water current, and leaves the primary electrode (27) of particular space therebetween;
The first voltage application portion part (38 that is connected with described primary electrode with described conductive adsorbent part, 40), be used between described conductive adsorbent part and described primary electrode, applying first volts DS, so that described conductive adsorbent part and described primary electrode are respectively as anode and negative electrode, and described first volts DS makes conductive adsorbent partly purify described former water; And
The second voltage application portion part (38 that is connected with described primary electrode with described conductive adsorbent part, 40), be used between described conductive adsorbent part and described primary electrode, applying second volts DS, described second volts DS is higher than described first volts DS, quickens the generation of chlorine in the described former water.
2, a kind of according to the described water purification system of claim 1, it is characterized in that also comprising: link to each other with the described second voltage application portion part and be used for definite described second volts DS polar polarity and determine parts (39), thereby described conductive adsorbent part and described primary electrode are respectively as described negative electrode and anode.
3, a kind of according to the described water purification system of claim 2, it is characterized in that also comprising; Being used for of being connected with described conductive adsorbent part and described primary electrode applies the 3rd volts DS between described conductive adsorbent part and described primary electrode tertiary voltage applies parts (38,40), thereby described conductive adsorbent part and described primary electrode be respectively as described anode and negative electrode, the described first volts DS height of described the 3rd DirectCurrent Voltage Ratio.
4, a kind of according to the described water purification system of claim 1, it is characterized in that also comprising: with described first be connected with the described second voltage application portion part excite parts (30), when described former water current interrupt, in a specific time length, excite parts to be used for alternately exciting described first and the described second voltage application portion part.
5, a kind of according to the described water purification system of claim 4, it is characterized in that also comprising: a timing register (36) of in the described specific time length, determining for first and second time length, the described parts that excite comprise:
Be connected with the described first voltage application portion part with described timing register, in described first time length, be used to excite first of the described first voltage application portion part to excite parts (30); And
Be connected with the described second voltage application portion part with described timing register, in described second time length, be used to excite second of the described second voltage application portion part to excite parts (30).
6, a kind of according to the described water purification system of claim 1, it is characterized in that also comprising: be connected with the described first and second voltage application portion parts, be used to excite the described first voltage application portion part at described former water current intercourse, and between described former water current continuing phase, be used to excite the described second voltage application portion part excite parts (30).
7, a kind of according to the described water purification system of claim 1, it is characterized in that: described primary electrode by scribble selectively platinum, platinum iridium alloy, carbon and mixed carbon resin wherein a kind of titanium utmost point of material form.
8, a kind of according to the described water purification system of claim 1, it is characterized in that also comprising:
Be used to produce a signal generator part (35) about described former water current distinctive signal; And
Be connected with described signal generator part, the described first voltage application portion part and the described second voltage application portion part, control described first and the parts of the operation of the described second voltage application portion part according to described distinctive signal.
9, a kind of according to the described water purification system of claim 1, it is characterized in that also comprising:
Be used to produce a signal generator part (35) about described former water current distinctive signal; And
Determine what parts were connected with described signal generator part with described polarity, control the parts that described polarity is determined the operation of parts according to described distinctive signal.
10, a kind of according to the described water purification system of claim 1, it is characterized in that: described conductive adsorbent is partly made cylindrical, axle head respect to one another and an inner circumferential surface that extends to form a hollow space between described axle head are arranged, described primary electrode is positioned at described hollow space, thereby stays described particular space between described inner circumferential surface and described primary electrode.
11, a kind of according to the described water purification system of claim 1, it is characterized in that: described conductive adsorbent partly comprises:
An activated carbon fiber part of making by activated carbon fiber with conductivity;
A supporting electrode that partly is connected with described activated carbon fiber facing to described primary electrode, thereby stays described particular space between described elementary and described supporting electrode.
12, a kind of according to the described water purification system of claim 11, it is characterized in that: described activated carbon fiber is partly made cylindrical, axle head respect to one another and an inner circumferential surface that extends to form a hollow space between described axle head are arranged, described primary electrode is positioned at described hollow space, thereby stay described particular space between described inner circumferential surface and described primary electrode, the described supporting electrode in described particular space leaves a space between described primary electrode and described supporting electrode.
13, a kind of according to the described water purification system of claim 12, it is characterized in that: described supporting electrode is columniform, and closely contacts with the described inner circumferential surface of activated carbon fiber part.
14, a kind of according to the described water purification system of claim 12, it is characterized in that: described supporting electrode is columniform, and separates with the described inner circumferential surface of activated carbon fiber part.
15, a kind of according to the described water purification system of claim 12, it is characterized in that: described supporting electrode extends along the wherein said axle head of activated carbon fiber part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97126020A CN1188744A (en) | 1996-11-05 | 1997-11-05 | Water purification system having chlorine generating function in addition to bacteriostatic function |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP292890/96 | 1996-11-05 | ||
| JP292909/96 | 1996-11-05 | ||
| CN97126020A CN1188744A (en) | 1996-11-05 | 1997-11-05 | Water purification system having chlorine generating function in addition to bacteriostatic function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1188744A true CN1188744A (en) | 1998-07-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN97126020A Pending CN1188744A (en) | 1996-11-05 | 1997-11-05 | Water purification system having chlorine generating function in addition to bacteriostatic function |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1188744A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102897874A (en) * | 2011-07-29 | 2013-01-30 | 通用电气公司 | Method for preparing bactericide |
| CN105849050A (en) * | 2013-12-23 | 2016-08-10 | 豪威株式会社 | CDI-type water treatment device |
| CN108602690A (en) * | 2016-01-29 | 2018-09-28 | 格伦倍克水处理有限公司 | For carrying out clean cylinder to water by electroactive sorbing material (Zeta electric potential) |
-
1997
- 1997-11-05 CN CN97126020A patent/CN1188744A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102897874A (en) * | 2011-07-29 | 2013-01-30 | 通用电气公司 | Method for preparing bactericide |
| CN105849050A (en) * | 2013-12-23 | 2016-08-10 | 豪威株式会社 | CDI-type water treatment device |
| CN105849050B (en) * | 2013-12-23 | 2019-06-14 | 豪威株式会社 | CDI formula water treatment facilities |
| US11084740B2 (en) | 2013-12-23 | 2021-08-10 | Coway Co., Ltd. | CDI-type water treatment method |
| CN108602690A (en) * | 2016-01-29 | 2018-09-28 | 格伦倍克水处理有限公司 | For carrying out clean cylinder to water by electroactive sorbing material (Zeta electric potential) |
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