CN205062196U - Preparation facilities of disinfectant - Google Patents
Preparation facilities of disinfectant Download PDFInfo
- Publication number
- CN205062196U CN205062196U CN201520730285.4U CN201520730285U CN205062196U CN 205062196 U CN205062196 U CN 205062196U CN 201520730285 U CN201520730285 U CN 201520730285U CN 205062196 U CN205062196 U CN 205062196U
- Authority
- CN
- China
- Prior art keywords
- port
- tube
- electrode group
- solution
- electrolyte solution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Abstract
The utility model discloses a preparation facilities of disinfectant, including filter, electrolyte solution jar, electrode group, reactor, anodal solution storage tank and negative pole solution storage tank, the reactor includes anode chamber and cathode chamber, adopts the ceramic membrane to separate between anode chamber and the cathode chamber, electrode group anodal and ceramic membrane enclose into the anode chamber, and the negative pole and the ceramic membrane of electrode group enclose into the cathode chamber, the export of anode chamber links to each other with anodal solution storage tank through the export of anodal solution, the export of cathode chamber is passed through the export of negative pole solution and is linked to each other with negative pole solution storage tank. The utility model discloses a preparation facilities area is little, and salt and electricity consumption are few, but convenient operation serialization production, and production efficiency is high.
Description
Technical field
The utility model relates to sterilized water technology of preparing, particularly a kind of preparation facilities of sterilized water.
Background technology
Single oxygenant is, as clorox, dioxide peroxide etc. at present for thimerosal.
The process direction of above-mentioned oxygenant to material in water is single, and prepare the environmental requirement of clorox etc., transport, storage request are strict, high to device installation requirement, and complicated process of preparation, dangerous high, power consumption is large.
Utility model content
The purpose of this utility model is to provide that a kind of structure is simple, the preparation facilities of the low sterilized water that consumes energy.
The technical scheme realizing the utility model object is:
A preparation facilities for sterilized water, comprises strainer, electrolyte solution tank, electrode group, reactor, positive solution storage tank, negative solution storage tank and casing;
Described electrode group and reactor are arranged in casing, casing are provided with tap water inlets, electrolyte solution entrance, positive solution outlet and negative solution outlet; Described strainer is connected with tap water inlets, and tap water enters Y-tube through tap water inlets; Described electrolyte solution tank is connected with electrolyte solution entrance, and electrolyte solution enters Y-tube through electrolyte solution entrance; After Y-tube tap water mixes with electrolyte solution, enter reactor from the negative pole entrance of electrode group;
Described reactor comprises anolyte compartment and cathode compartment, adopts ceramic membrane to separate between anolyte compartment and cathode compartment; Positive pole and the ceramic membrane of described electrode group surround anolyte compartment, negative pole and the ceramic membrane of electrode group surround cathode compartment, the outlet of described anolyte compartment is connected with positive solution storage tank by positive solution outlet, and the outlet of described cathode compartment is connected with negative solution storage tank by negative solution outlet.
The utility model compared with prior art, its remarkable advantage:
(1) preparation facilities floor space of the present utility model is little, salt and electricity consumption few, existing logistics can be utilized
And electric power networks, under the condition without any design and assembly working, be installed in the place of existing chlorination;
(2) preparation facilities of the present utility model runs does not need to store, and transport and use toxic substance, ensure the safety of water sterilization process, do not need hold-up vessel and expensive charging system;
(3) preparation facilities of the present utility model not to need between chlorination house and storage chlorine " exclusionary zone " around, can be used for little, neutralize large-scale potable water treatment plants (every day supplies 500-300000 cubic meter of water or more);
(4) the utility model can improve the maximum conversion rate of salt in electrolyte solution, can reduce the erosion rate of waterpipe;
(5) preparation method of the present utility model easy to operate, can be continuously produced, save labor force.
Accompanying drawing explanation
Fig. 1 is the sterilized water preparation facilities casing external structure of the utility model embodiment.
Fig. 2 is the sterilized water preparation facilities box inner structure figure of the utility model embodiment.
Fig. 3 is the electrode group structure figure of the utility model embodiment.
In figure: 1, power supply 2, supply lead 3, tap water inlets 4, electrolyte solution entrance 5, current adjusting knob 6, negative pole output adjusting knob button 7, magnitude of voltage indicator gauge 8, current value indicator gauge 9, positive solution outlet 10, negative solution outlet 11, casing 12, electrolyte solution storage tank 13, running water filter 14, penetrate sucking pump 15, first Y-tube 16, second Y-tube 17, 3rd Y-tube 18, 4th Y-tube 19, 5th Y-tube 20, 6th Y-tube 21, insulation covering 22, electrode group 23, 7th Y-tube 24, 8th Y-tube 25, 9th Y-tube 26, tenth Y-tube 27, 11 Y-tube 28, 12 Y-tube 29, four-way pipe 1330, positive pole product reservoir 31, negative pole product reservoir 32, the positive pole 33 of electrode group, ceramic membrane 34, the negative pole 35 of electrode group, anolyte compartment 36, cathode compartment 37, screw thread
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
Composition graphs 1, Fig. 2, a kind of preparation facilities of sterilized water, comprises strainer 13, electrolyte solution tank 12, electrode group 22, reactor, positive solution storage tank 30, negative solution storage tank 31 and casing 11;
Described electrode group and reactor are arranged in casing, casing are provided with tap water inlets, electrolyte solution entrance, positive solution outlet and negative solution outlet; Described strainer is connected with tap water inlets, and tap water enters Y-tube through tap water inlets; Described electrolyte solution tank is connected with electrolyte solution entrance, and electrolyte solution enters Y-tube through electrolyte solution entrance; After Y-tube tap water mixes with electrolyte solution, enter reactor from the negative pole entrance of electrode group;
Described reactor comprises anolyte compartment and cathode compartment, adopts ceramic membrane to separate between anolyte compartment and cathode compartment; Positive pole and the ceramic membrane of described electrode group surround anolyte compartment, negative pole and the ceramic membrane of electrode group surround cathode compartment, the outlet of described anolyte compartment is connected with positive solution storage tank by positive solution outlet, and the outlet of described cathode compartment is connected with negative solution storage tank by negative solution outlet.
The quantity of described electrode group is 4,6 or 8 groups, and electrode group is rear series connection in parallel between two, and often group comprises a plating iridium ruthenium titanium positive pole and a titanium cathode tube, and positive pole inserts in cathode tube, and described ceramic membrane is right cylinder tubular film, is arranged between negative pole and positive pole.
Described ceramic membrane is alumina doped zirconic single-tube ceramic membranes.
Preferably, described electrode group quantity is 4 groups, four-way pipe quantity is 1, Y-tube quantity is 12, is respectively the first Y-tube, the second Y-tube, the 3rd Y-tube, the 4th Y-tube, the 5th Y-tube, the 6th Y-tube, the 7th Y-tube, the 8th Y-tube, the 9th Y-tube, the tenth Y-tube, the 11 Y-tube and the 12 Y-tube;
Described first Y-tube 15 comprises the first port, the second port and the 3rd port; Described second Y-tube 16 comprises the 4th port, five-port and the 6th port; Described 3rd Y-tube 17 comprises the 7th port, the 8th port and the 9th port; Described 4th Y-tube 18 comprises the tenth port, the tenth Single port and the tenth Two-port netwerk; Described 5th Y-tube 19 comprises the 13 port, the 14 port and the tenth five-port; Described 6th Y-tube 20 comprises the 16 port, the 17 port and the 18 port; Described 7th Y-tube 23 comprises the 19 port, the 20 port and the 20 Single port; Described 8th Y-tube 24 comprises the 20 Two-port netwerk, the 23 port and the 24 port; Described 9th Y-tube 25 comprises the 20 five-port, the 26 port and the 27 port; Described tenth Y-tube 26 comprises the 28 port, the 29 port and the 30 port; Described 11 Y-tube 27 comprises the 30 Single port, the 30 Two-port netwerk and the 33 port; Described 12 Y-tube 28 comprises the 34 port, the 30 five-port and the 36 port;
Described four-way pipe 29 comprises the 37 port, the 38 port, the 39 port, the 40 port;
Described strainer 13 is connected with tap water inlets 3, and tap water enters the first port of the first Y-tube 15 through tap water inlets; Described electrolyte solution tank 12 is connected with electrolyte solution entrance 4, and electrolyte solution enters current adjusting knob 5 through electrolyte solution entrance; Entering through current adjusting knob 5 and penetrate sucking pump 14, entering the first Y-tube 15 second port by penetrating sucking pump 14 outlet;
3rd port is connected with the 4th port, five-port is connected with the tenth port with the 7th port respectively with the 6th port, 8th port and the 9th port are connected with the negative pole mouth of the first electrode group with the 4th electrode group respectively, tenth Single port is connected with the negative pole mouth of third electrode group with the second electrode group respectively with the tenth Two-port netwerk, 13 port is just in highest terms connected with the 4th electrode group with the first electrode group respectively with the 14 port, tenth five-port is connected with the 20 five-port of the 9th Y-tube, 16 port is just in highest terms connected with third electrode group with the second electrode group respectively with the 17 port, 18 port is connected with the 26 port of the 9th Y-tube, 19 port is just in highest terms connected with the 4th electrode group with the first electrode group respectively with the 20 port, 20 Single port is connected with the 34 port of the 12 Y-tube, 20 Two-port netwerk and the 23 port are connected with the 4th electrode group negative pole mouth with the first electrode group respectively, 24 port is connected with the 38 port of four-way pipe, 27 port is connected with the 37 port of four-way pipe, 28 port is just in highest terms connected with third electrode group with the second electrode group respectively with the 29 port, 30 port is connected with the 30 five-port of the 12 Y-tube, 30 Single port and the 30 Two-port netwerk are connected with third electrode group negative pole mouth with the second electrode group respectively, 33 port is connected with the 39 port of four-way pipe, 36 port exports with positive solution and is connected, 40 port exports 10 by negative pole output adjusting knob 6 with negative solution and is connected.
Below in conjunction with specific embodiment, the utility model is described in further detail.
Embodiment 1
Composition graphs 1, Fig. 2, the preparation facilities of sterilized water comprises casing 11, electrolyte solution storage tank 12, running water filter 13, penetrates sucking pump 14, first Y-tube 15, second Y-tube 16, the 3rd Y-tube 17, the 4th Y-tube 18, the 5th Y-tube 19, the 6th Y-tube 20, insulation covering 21, electrode group 22, the 7th Y-tube 23, the 8th Y-tube 24, the 9th Y-tube 25, the tenth Y-tube the 26, the 11 Y-tube the 27, the 12 Y-tube 28, four-way pipe 29, positive pole product reservoir 30 and negative pole product reservoir 31;
Described first Y-tube 15 comprises the first port, the second port and the 3rd port; Described second Y-tube 16 comprises the 4th port, five-port and the 6th port; Described 3rd Y-tube 17 comprises the 7th port, the 8th port and the 9th port; Described 4th Y-tube 18 comprises the tenth port, the tenth Single port and the tenth Two-port netwerk; Described 5th Y-tube 19 comprises the 13 port, the 14 port and the tenth five-port; Described 6th Y-tube 20 comprises the 16 port, the 17 port and the 18 port; Described 7th Y-tube 23 comprises the 19 port, the 20 port and the 20 Single port; Described 8th Y-tube 24 comprises the 20 Two-port netwerk, the 23 port and the 24 port; Described 9th Y-tube 25 comprises the 20 five-port, the 26 port and the 27 port; Described tenth Y-tube 26 comprises the 28 port, the 29 port and the 30 port; Described 11 Y-tube 27 comprises the 30 Single port, the 30 Two-port netwerk and the 33 port; Described 12 Y-tube 28 comprises the 34 port, the 30 five-port and the 36 port;
Described four-way pipe 29 comprises the 37 port, the 38 port, the 39 port, the 40 port;
Described electrode group 22 and reactor are arranged in casing 11, casing are provided with tap water inlets 3, electrolyte solution entrance 4, current adjusting knob 5, negative pole output adjusting knob 6, positive solution outlet 9 and negative solution outlet 10;
Described strainer 13 is connected with tap water inlets 3, and tap water enters the first port of the first Y-tube 15 through tap water inlets; Described electrolyte solution tank 12 is connected with electrolyte solution entrance 4, and electrolyte solution enters current adjusting knob 5 through electrolyte solution entrance; Entering through current adjusting knob 5 and penetrate sucking pump 14, entering the first Y-tube 15 second port by penetrating sucking pump 14 outlet;
3rd port is connected with the 4th port, five-port and the 6th port respectively with the 7th port and the tenth port, 8th port and the 9th port are connected with the negative pole mouth of the first electrode group with the 4th electrode group respectively, tenth Single port is connected with the negative pole mouth of third electrode group with the second electrode group respectively with the tenth Two-port netwerk, 13 port is just in highest terms connected with the 4th electrode group with the first electrode group respectively with the 14 port, tenth five-port is connected with the 20 five-port of the 9th Y-tube 25, 16 port is just in highest terms connected with third electrode group with the second electrode group respectively with the 17 port, 18 port is connected with the 26 port of the 9th Y-tube 25, 19 port is just in highest terms connected with the 4th electrode group with the first electrode group respectively with the 20 port, 20 Single port is connected with the 34 port of the 12 Y-tube 28, 20 Two-port netwerk and the 23 port are connected with the 4th electrode group negative pole mouth with the first electrode group respectively, 24 port is connected with the 38 port of four-way pipe 29, 27 port is connected with the 37 port of four-way pipe, 28 port is just in highest terms connected with third electrode group with the second electrode group respectively with the 29 port, 30 port is connected with the 30 five-port of the 12 Y-tube 28, 30 Single port and the 30 Two-port netwerk are connected with third electrode group negative pole mouth with the second electrode group respectively, 33 port is connected with the 39 port of four-way pipe 29, 36 port and positive solution export 9 and are connected, and enter positive pole product reservoir 30, 40 port is connected with negative pole output adjusting knob 6, enters negative pole product reservoir 31 through negative pole output adjusting knob 6 and negative solution outlet 10,
Composition graphs 3, reactor comprises anolyte compartment 35 and cathode compartment 36, adopts ceramic membrane 33 to separate between anolyte compartment 35 and cathode compartment 36; Positive pole 32 and the ceramic membrane 33 of described electrode group surround anolyte compartment 35, negative pole 34 and the ceramic membrane 33 of electrode group surround cathode compartment 36, the outlet of described anolyte compartment 35 is connected with positive solution storage tank 30 by positive solution outlet 9, and the outlet of described cathode compartment 36 is connected with negative solution storage tank 31 by negative solution outlet 10.Described insulation covering 21 is with in highest terms positive and negative, and be fastened on electrode group 22 two ends, insulation covering 21 just in highest terms communicates with anolyte compartment 35, and negative pole mouth communicates with cathode compartment 36; Screw thread 37 connects positive pole and hold-doun nut.
The present embodiment adopts four groups of electrode groups, electrode group is rear series connection in parallel between two, often group comprises a plating iridium ruthenium titanium positive pole and a titanium cathode tube, positive pole inserts in cathode tube, described ceramic membrane is right cylinder tubular film, be arranged between negative pole and positive pole, ceramic membrane is alumina doped zirconic single-tube ceramic membranes.
Casing is also provided with current value display instrument 8 and magnitude of voltage display instrument 7, is respectively used to current value and magnitude of voltage in display reactor.
To prepare chlorine (85%), dioxide peroxide (12%), ozone (2.5%) and in the total concn of solution be 0.5% the aqueous antiseptic solution of hydrogen compound be example, sterilized water pH is 6.8, ORP is 1000mV, and described hydrogen compound is H
2o, Industrial Salt solution is electrolyte solution, and by percentage to the quality, preparation method is above-mentioned component:
(1) room temperature tap water filters through filter 13;
(2) electrolyte solution is prepared: the pure water 10L selecting specific conductivity < 10 μ s/cm, temperature, at 20 DEG C, takes the Industrial Salt of 1000g, and obtained concentration is at 100g/L, temperature, at the electrolyte solution of 20 DEG C, is placed in electrolyte solution storage tank 12;
(3) input reactor: by tap water, electrolyte solution enters from the tap water inlets 3 casing 11, electrolyte solution entrance 4 respectively by throughput ratio 3:37, sucking pump 14 is penetrated through current adjusting knob 5, converge through the first Y-tube 15 again, shunt through the second Y-tube 16 again, through the 3rd Y-tube 17, the 4th Y-tube 18, enter reactor from electrode group 22 negative pole mouth;
(4) switch on power, start preparation: be connected with supply lead 2 by power supply 1, magnitude of voltage indicator gauge 7 shows 48V and regulates current adjusting knob 5, and current value indicator gauge 8 shows 12A, electrolytic solution;
(5) negative solution is collected: the solution gone out by electrode group negative pole lower port converges through the 8th Y-tube the 24, the 11 Y-tube 27, electrode group positive pole upper port goes out solution through the 5th Y-tube 19,6th Y-tube 20 converges to the 9th Y-tube 25, converge through four-way pipe 29, enter negative solution storage tank 31 through negative solution outlet 10;
(6) positive solution is collected: the solution gone out by electrode group positive pole lower port converges through the 7th Y-tube 23, the tenth Y-tube 26 respectively, positive solution storage tank 30 is entered through positive solution outlet 9, regulate negative pole output adjusting knob 6, control negative pole quantum of output 10-12L/h; Solution in positive solution storage tank is sterilized water.
Embodiment 2
The preparation facilities of the present embodiment is identical with embodiment 1, to prepare chlorine (70%), dioxide peroxide (20%), ozone (8%) and in the total concn of solution be 2% the aqueous antiseptic solution of hydrogen compound be example, the pH of sterilized water is 8, ORP is 800mV, and described hydrogen compound is H
2o, adopt Industrial Salt solution to be electrolyte solution, preparation method is:
(1) room temperature tap water filters through filter 13;
(2) prepare electrolyte solution: the pure water 10L selecting specific conductivity < 10 μ s/cm, temperature, at 20 DEG C, takes the Industrial Salt of 500g, and obtained concentration is at 50g/L, and temperature, at the electrolyte solution of 20 DEG C, is placed in electrolyte solution storage tank 12;
(3) input reactor: by tap water, electrolyte solution enters from the tap water inlets 3 casing 11, electrolyte solution entrance 4 respectively by throughput ratio 13:27, through current adjusting knob 5, penetrate sucking pump 14, converge through the first Y-tube 15 again, shunt through the second Y-tube 16 again, through the 3rd Y-tube 17, the 4th Y-tube 18, enter reactor from electrode group 22 negative pole mouth;
(4) switch on power, start preparation: be connected with supply lead 2 by power supply 1, magnitude of voltage indicator gauge 7 shows 45V and regulates current adjusting knob 5, and current value indicator gauge 8 shows 8A, electrolytic solution;
(5) negative solution is collected: the solution gone out by electrode group negative pole lower port converges through the 8th Y-tube the 24, the 11 Y-tube 27, electrode group positive pole upper port goes out solution through the 5th Y-tube 19,6th Y-tube 20 converges to the 9th Y-tube 25, converge through four-way pipe 29, enter negative solution storage tank 31 through negative solution outlet 10;
(6) positive solution is collected: the solution gone out by electrode group positive pole lower port converges through the 7th Y-tube 23, the tenth Y-tube 26 respectively, positive solution storage tank 30 is entered through positive solution outlet 9, regulate negative pole output adjusting knob 6, control negative pole quantum of output 9-10L/h; Solution in positive solution storage tank is sterilized water.
Embodiment 3
The preparation facilities of the present embodiment is identical with embodiment 1, to prepare chlorine (80%), dioxide peroxide (16%), ozone (3%) and in the total concn of solution be 1 the aqueous antiseptic solution of hydrogen compound be example, sterilized water pH7.3, ORP900mV, described hydrogen compound is H
2o, adopts Industrial Salt solution to be electrolyte solution; Preparation method is:
(1) room temperature tap water filters through filter 13;
(2) prepare electrolyte solution: the pure water 10L selecting specific conductivity < 10 μ s/cm, temperature, at 20 DEG C, takes the Industrial Salt of 800g, and obtained concentration is at 80g/L, and temperature, at the electrolyte solution of 20 DEG C, is placed in electrolyte solution storage tank 12;
(3) input reactor: by tap water, electrolyte solution enters from the tap water inlets 3 casing 11, electrolyte solution entrance 4 respectively by throughput ratio 10:30, enter through current adjusting knob 5 and penetrate sucking pump 14, converge through the first Y-tube 15 again, shunt through the second Y-tube 16 again, through the 3rd Y-tube 17, the 4th Y-tube 18, enter reactor from electrode group 22 negative pole mouth;
(4) switch on power, start preparation: be connected with supply lead 2 by power supply 1, magnitude of voltage indicator gauge 7 shows 47V and regulates current adjusting knob 5, and current value indicator gauge 8 shows 10A, electrolytic solution;
(5) negative solution is collected: the solution gone out by electrode group negative pole lower port converges through the 8th Y-tube the 24, the 11 Y-tube 27, electrode group positive pole upper port goes out solution through the 5th Y-tube 19,6th Y-tube 20 converges to the 9th Y-tube 25, converge through four-way pipe 29, enter negative solution storage tank 31 through negative solution outlet 10;
(6) positive solution is collected: the solution gone out by electrode group positive pole lower port converges through the 7th Y-tube 23, the tenth Y-tube 26 respectively, positive solution storage tank 30 is entered through positive solution outlet 9, regulate negative pole output adjusting knob 6, control negative pole quantum of output 10L/h; Solution in positive solution storage tank is sterilized water.
Claims (4)
1. the preparation facilities of a sterilized water, it is characterized in that, comprise strainer (13), electrolyte solution tank (12), electrode group (22), reactor, positive solution storage tank (30), negative solution storage tank (31) and casing (11);
Described electrode group (22) and reactor are arranged in casing (11), casing are provided with tap water inlets (3), electrolyte solution entrance (4), positive solution outlet (9) and negative solution outlet (10); Described strainer (13) is connected with tap water inlets (3), and tap water enters Y-tube through tap water inlets (3); Described electrolyte solution tank (12) is connected with electrolyte solution entrance (4), and electrolyte solution enters Y-tube through electrolyte solution entrance; After Y-tube tap water mixes with electrolyte solution, enter reactor from the negative pole entrance of electrode group;
Described reactor comprises anolyte compartment and cathode compartment, adopts ceramic membrane to separate between anolyte compartment and cathode compartment; Positive pole and the ceramic membrane of described electrode group surround anolyte compartment, negative pole and the ceramic membrane of electrode group surround cathode compartment, the outlet of described anolyte compartment is connected with positive solution storage tank by positive solution outlet, and the outlet of described cathode compartment is connected with negative solution storage tank by negative solution outlet.
2. the preparation facilities of sterilized water according to claim 1, it is characterized in that, the quantity of described electrode group is 4,6 or 8 groups, electrode group is rear series connection in parallel between two, often group comprises a plating iridium ruthenium titanium positive pole and a titanium cathode tube, positive pole inserts in cathode tube, and described ceramic membrane is right cylinder tubular film, is arranged between negative pole and positive pole.
3. the preparation facilities of sterilized water according to claim 1 or 2, it is characterized in that, described ceramic membrane is alumina doped zirconic single-tube ceramic membranes.
4. the preparation facilities of sterilized water according to claim 3, it is characterized in that, described electrode group quantity is 4 groups, four-way pipe quantity is 1, Y-tube quantity is 12, is respectively the first Y-tube, the second Y-tube, the 3rd Y-tube, the 4th Y-tube, the 5th Y-tube, the 6th Y-tube, the 7th Y-tube, the 8th Y-tube, the 9th Y-tube, the tenth Y-tube, the 11 Y-tube and the 12 Y-tube;
Described first Y-tube (15) comprises the first port, the second port and the 3rd port; Described second Y-tube (16) comprises the 4th port, five-port and the 6th port; Described 3rd Y-tube (17) comprises the 7th port, the 8th port and the 9th port; Described 4th Y-tube (18) comprises the tenth port, the tenth Single port and the tenth Two-port netwerk; Described 5th Y-tube (19) comprises the 13 port, the 14 port and the tenth five-port; Described 6th Y-tube (20) comprises the 16 port, the 17 port and the 18 port; Described 7th Y-tube (23) comprises the 19 port, the 20 port and the 20 Single port; Described 8th Y-tube (24) comprises the 20 Two-port netwerk, the 23 port and the 24 port; Described 9th Y-tube (25) comprises the 20 five-port, the 26 port and the 27 port; Described tenth Y-tube (26) comprises the 28 port, the 29 port and the 30 port; Described 11 Y-tube (27) comprises the 30 Single port, the 30 Two-port netwerk and the 33 port; Described 12 Y-tube (28) comprises the 34 port, the 30 five-port and the 36 port;
Described four-way pipe (29) comprises the 37 port, the 38 port, the 39 port, the 40 port;
Described strainer (13) is connected with tap water inlets (3), and tap water enters the first port of the first Y-tube (15) through tap water inlets; Described electrolyte solution tank (12) is connected with electrolyte solution entrance (4), and electrolyte solution enters current adjusting knob (5) through electrolyte solution entrance; Entering through current adjusting knob (5) and penetrate sucking pump (14), entering the first Y-tube (15) second port by penetrating sucking pump (14) outlet;
3rd port is connected with the 4th port, five-port is connected with the tenth port with the 7th port respectively with the 6th port, 8th port and the 9th port are connected with the negative pole mouth of the first electrode group with the 4th electrode group respectively, tenth Single port is connected with the negative pole mouth of third electrode group with the second electrode group respectively with the tenth Two-port netwerk, 13 port is just in highest terms connected with the 4th electrode group with the first electrode group respectively with the 14 port, tenth five-port is connected with the 20 five-port of the 9th Y-tube, 16 port is just in highest terms connected with third electrode group with the second electrode group respectively with the 17 port, 18 port is connected with the 26 port of the 9th Y-tube, 19 port is just in highest terms connected with the 4th electrode group with the first electrode group respectively with the 20 port, 20 Single port is connected with the 34 port of the 12 Y-tube, 20 Two-port netwerk and the 23 port are connected with the 4th electrode group negative pole mouth with the first electrode group respectively, 24 port is connected with the 38 port of four-way pipe, 27 port is connected with the 37 port of four-way pipe, 28 port is just in highest terms connected with third electrode group with the second electrode group respectively with the 29 port, 30 port is connected with the 30 five-port of the 12 Y-tube, 30 Single port and the 30 Two-port netwerk are connected with third electrode group negative pole mouth with the second electrode group respectively, 33 port is connected with the 39 port of four-way pipe, 36 port exports with positive solution and is connected, 40 port exports (10) by negative pole output adjusting knob (6) and is connected with negative solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520730285.4U CN205062196U (en) | 2015-09-20 | 2015-09-20 | Preparation facilities of disinfectant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520730285.4U CN205062196U (en) | 2015-09-20 | 2015-09-20 | Preparation facilities of disinfectant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205062196U true CN205062196U (en) | 2016-03-02 |
Family
ID=55388776
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520730285.4U Expired - Fee Related CN205062196U (en) | 2015-09-20 | 2015-09-20 | Preparation facilities of disinfectant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205062196U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105165890A (en) * | 2015-09-20 | 2015-12-23 | 连云港龙卷风环保技术有限公司 | Disinfectant fluid and preparation method and device thereof |
-
2015
- 2015-09-20 CN CN201520730285.4U patent/CN205062196U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105165890A (en) * | 2015-09-20 | 2015-12-23 | 连云港龙卷风环保技术有限公司 | Disinfectant fluid and preparation method and device thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104003580B (en) | A kind of process sanitary sewage wetland electrogenesis and for the system of wetland effluent electrochemical disinfection | |
| CN106430451A (en) | Method and device for producing subacid electrolyzed water | |
| US20110108437A1 (en) | Disinfection method and disinfection device | |
| CN101531411A (en) | Method for electrochemically disinfecting gas diffusion electrode system | |
| CN203222623U (en) | Electrolytic ozone generation device | |
| CN219731071U (en) | Preparation and supply system for offshore wind power hydrogen production electrolysis water | |
| CN205329172U (en) | Device of hydrogen and oxygen is prepared to solar energy electrolysis sea water | |
| CN111349945A (en) | Small non-diaphragm weak acid oxidation potential water maker | |
| CN203833683U (en) | Electrolysis cup | |
| CN205062196U (en) | Preparation facilities of disinfectant | |
| CN204125535U (en) | A kind of device and slightly acidic electrolyzed oxidizing water spray disinfection system preparing slightly acidic electrolyzed oxidizing water | |
| CN103305862B (en) | High-basicity polymerize aluminum chloride and Al 13muriatic electrochemical production device and manufacture method thereof | |
| CN209065489U (en) | It is a kind of for handling the three-dimensional electrocatalysis oxidation apparatus of ammonia nitrogen waste water | |
| CN206219283U (en) | Produce the device of subacidity electrolysis water | |
| CN111377535A (en) | Anaerobic forward osmosis membrane bioreactor process for oxidizing ammonia nitrogen by coupling electrochemistry | |
| CN204958479U (en) | Drinking cup is separated to electricelectric | |
| CN204529992U (en) | Water treatment system disinfectant preparation apparatus | |
| CN105165890A (en) | Disinfectant fluid and preparation method and device thereof | |
| CN205556329U (en) | Swimming pool circulating water electrolysis type purifier | |
| CN213203226U (en) | Ion membrane electrolysis method hypochlorous acid disinfectant takes place processing system | |
| CN212334687U (en) | Device for preparing hypochlorous acid water | |
| CN212223118U (en) | Sodium hypochlorite generating device based on ion membrane method | |
| CN206986285U (en) | A kind of hypochlorite generator of less salt consumption | |
| CN210176966U (en) | Hydrogen-rich water generating device based on aluminum-air battery | |
| CN106835189A (en) | A kind of sodium hypochlorite electrolytic cell assembly of multi-channel structure |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160302 Termination date: 20170920 |