CN109183060A - A kind of intermittent sodium hypochlorite electrolysis generator of continuously-running - Google Patents
A kind of intermittent sodium hypochlorite electrolysis generator of continuously-running Download PDFInfo
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- CN109183060A CN109183060A CN201811328832.0A CN201811328832A CN109183060A CN 109183060 A CN109183060 A CN 109183060A CN 201811328832 A CN201811328832 A CN 201811328832A CN 109183060 A CN109183060 A CN 109183060A
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/24—Halogens or compounds thereof
- C25B1/26—Chlorine; Compounds thereof
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/02—Process control or regulation
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B15/00—Operating or servicing cells
- C25B15/08—Supplying or removing reactants or electrolytes; Regeneration of electrolytes
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
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Abstract
The present invention relates to a kind of electrolysis of the intermittent sodium hypochlorite of continuously-running to occur.The present invention mainly solves existing hypochlorite generator, and existing structure is complicated, working service is cumbersome, inefficiency and the technical issues of cooling down waste great lot of water resources.The technical solution adopted by the present invention is that: a kind of intermittent sodium hypochlorite electrolysis generator of continuously-running, including frequency conversion cooling system, electrolytic cell, medicine-sucking pump, explosive box, PLC controller and direct-current switch power supply, it further includes salt dissolving case and circulating pump, the water outlet of the siphon pipe and the salt mouth of a river of electrolytic cell connect, the cooling tube of the frequency conversion cooling system is located in the inner cavity of electrolytic cell, the electrode of the electrolytic cell is connect with direct-current switch power supply, the import of the circulating pump is connect with electrolyzer outlet, the import of the circulation pipe of the outlet and electrolytic cell of the circulating pump connects, the feeding opening of the medicine-sucking pump is connect with electrolytic cell medicine outlet, the medicine outlet of the medicine-sucking pump and the feeding opening of explosive box connect.
Description
Technical field
The present invention relates to a kind of electrolysis of the intermittent sodium hypochlorite of continuously-running to occur, it belongs to a kind of sodium hypochlorite electricity
Solve occurrence of equipment technical field.
Background technique
Sodium hypochlorite is relatively easy and cheap due to manufacturing, and disinfection bleaching effect is definite and is used widely.By
There is apparent unstability in liquor natrii hypochloritis, be easy to reduce because effective chlorine decomposes transporting and storing in use process
And influence using effect.The characteristics of sodium hypochlorite electrolysis generator has raw material and is easy to get, is prepared in situ, can precisely add determines
This production technology can effectively avoid safe warranty issues of the sodium hypochlorite in transport and use.The electricity being widely used at present
Solution hypochlorite generator mainly has continuous and clearance-type two types, and continous way is electrolysed hypochlorite generator mostly using pipe
Shape electrode, this product structure is complicated, safeguards cumbersome, unsuitable small-scale application.Clearance-type is electrolysed hypochlorite generator's knot
Structure is simple, but universal inefficient.Most of electrolysis hypochlorite generator increases to reduce course of work electrolyte temperature
Influence cooled using tap water, cause water resource waste.
Summary of the invention
Present invention aim to address structure is complicated existing for existing hypochlorite generator, cost of manufacture is high, uses dimension
The technical issues of protecting cumbersome, inefficiency and cooling down waste great lot of water resources, provides a kind of the intermittent of continuously-running
Sodium hypochlorite electrolysis occurs.
In order to solve the above technical problems, the technical solution adopted by the present invention is that:
A kind of intermittent sodium hypochlorite electrolysis generator of continuously-running, including frequency conversion cooling system, electrolytic cell, pumping medicine
Pump, explosive box, PLC controller and direct-current switch power supply further include salt dissolving case and circulating pump, and the salt dissolving case is by cabinet, note
Water pipe, partition, salt water floating ball, siphon pipe sleeve, siphon pipe and the first solenoid valve are constituted, and the partition is located in cabinet and by cabinet
Inner cavity is divided into storage salt tank and brine drum, and the water injection pipe is located in storage salt tank, and the siphon pipe is located in brine drum and siphon
The water inlet of pipe is 30mm lower than upper liquid level, and the siphon pipe sleeve covers on siphon pipe and the import of siphon pipe sleeve and lower liquid level are flat
Together, the salt water floating ball is located in brine drum, and the water outlet of first solenoid valve and the water inlet of water injection pipe connect；The rainbow
The water outlet of suction pipe and the salt mouth of a river of electrolytic cell connect, and the water inlet of the electrolytic cell passes through the water outlet of pipeline and second solenoid valve
Mouth connection, the cooling tube of the frequency conversion cooling system are located in the inner cavity of electrolytic cell, the electrode and dc switch of the electrolytic cell
Power supply connection, the import of the circulating pump are connect with the outlet that one side lower part of electrolytic cell is arranged, the outlet of the circulating pump and electricity
The import connection of the circulation pipe of slot internal upper part setting is solved, another side lower part setting of the feeding opening and electrolytic cell of the medicine-sucking pump goes out
The feeding opening of the connection of medicine mouth, the medicine outlet of the medicine-sucking pump and explosive box connects, the PLC controller and the first solenoid valve, the
Two solenoid valves, the frequency-changeable compressor in frequency conversion cooling system, circulating pump, the temperature sensor in electrolytic cell, direct-current switch power supply
It is connected with medicine-sucking pump.
Further, the electrolytic cell by shell, at least one electrode cavity, seal cover board, exhaust pipe, temperature sensor and
Electrolyte floating ball is constituted, and the seal cover board is located in the electrode cavity inlet and outlet of the upper surface setting of shell, and the electrode cavity is set
In the inner cavity of shell and electrode is stretched out from the electrode hole that seal cover board is arranged, and the exhaust pipe is located at the one of shell upper surface
Side, the temperature sensor are located on the side wall of housing cavity, and the electrolyte floating ball is located at the side of housing cavity.
Further, the electrode cavity is made of electrode case, two electrode plates and several intermediate electrode plates, the electrode case
For the rectangle case of front and back opening, left and right sides upper part that the electrode plate is located at electrode case is stretched from the upper surface of electrode case
Out, the intermediate electrode plate is located at the centre of two electrode plates.
Further, the electrode plate and intermediate electrode plate are titanium plate and are equipped with ruthenium iridium coating layer on the surface of titanium plate.
Due to present invention employs above-mentioned technical proposal, solve existing hypochlorite generator it is existing structure is complicated,
Cost of manufacture is high, working service is cumbersome, inefficiency and the technical issues of cooling down waste great lot of water resources.With background technique
It compares, the invention has the advantages that 1) using frequency conversion compress technique for cold source, C.P.Ti tube production evaporation cooling coil is directly cooling
Electrode and electrolytic solution, good cooling results have fundamentally prevented the loss waste of water resource；2) it is thrown using bushing type siphon device
The amount of reordering saturated brine is then diluted to optimised process concentration, and solving clearance-type hypochlorite generator needs artificial ingredient
Problem greatly extends equipment application model so that clearance-type hypochlorite generator realizes continuous production without manual intervention
It encloses；3) electrolytic cell built-in electrode chamber of the present invention, plays the efficiency of specification Electrolyte Electric Field, has effectively obstructed partial short-circuit between electrode
Phenomenon reduces side reaction consumption electric energy.Actual power consumption reduces a quarter, and electrolyte temperature rise reduces 2/3rds, significantly mentions
Rise electrolysis efficiency.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention；
Fig. 2 is the structural schematic diagram of salt dissolving case of the present invention；
Fig. 3 is the structural schematic diagram of electrode cavity of the present invention；
Fig. 4 is the left view of Fig. 3；
In figure: 1- salt dissolving case, 2- frequency conversion cooling system, 3- circulating pump, 4- electrolytic cell, 5- medicine-sucking pump, 6- explosive box, 7-
PLC controller, 8- direct-current switch power supply, 9- second solenoid valve；
1-1- cabinet, 1-2- water injection pipe, 1-3- partition, 1-4- salt water floating ball, 1-5- siphon pipe sleeve, 1-6- siphon pipe, 1-
The first solenoid valve of 7-；
2-1- frequency-changeable compressor, 2-2- condenser, 2-3- titanium evaporate cooling coil；
4-1- shell, 4-2- electrode cavity, 4-3- seal cover board, 4-4- exhaust pipe, 4-5- temperature sensor, 4-6- electrolyte
Floating ball；4-2-1- electrode case, 4-2-2- electrode plate, 4-2-3- intermediate electrode plate；
6-1- dosing pump, 6-2- drug storage floating ball.
Specific embodiment
The present invention is described in further detail with reference to the accompanying drawings and examples.
As shown in Figure 1 to 4, the intermittent sodium hypochlorite electrolysis generator of one of the present embodiment continuously-running,
Including frequency conversion cooling system 2, electrolytic cell 4, medicine-sucking pump 5, explosive box 6, PLC controller 7 and direct-current switch power supply 8, further include
Salt dissolving case 1 and circulating pump 3, the salt dissolving case 1 is by cabinet 1-1, water injection pipe 1-2, partition 1-3, salt water floating ball 1-4, siphon pipe sleeve
1-5, siphon pipe 1-6 and the first solenoid valve 1-7 are constituted, and the partition 1-3 is located in cabinet 1-1 and separates the inner cavity cabinet 1-1
For storage salt tank and brine drum, the water injection pipe 1-2 is located in storage salt tank, and the siphon pipe 1-6 is located in brine drum and siphon pipe
The water inlet of 1-6 is 30mm lower than upper liquid level, the siphon pipe sleeve 1-5 cover on siphon pipe 1-6 and the import of siphon pipe sleeve 1-5 with
Lower liquid level is concordant, and the salt water floating ball 1-4 is located in brine drum, and the water outlet of the first solenoid valve 1-7 is with water injection pipe 1-2's
Water inlet connection；The water outlet of the siphon pipe 1-6 is connect with the salt mouth of a river of electrolytic cell 4, and the water inlet of the electrolytic cell 4 passes through
Pipeline is connect with the water outlet of second solenoid valve 9, and the titanium evaporation cooling coil of the frequency conversion cooling system 2 is located at electrolytic cell 4
In inner cavity, the electrode of the electrolytic cell 4 is connect with direct-current switch power supply 8, under the import of the circulating pump 3 and 4 side of electrolytic cell
The import of the circulation pipe of the circulating outlet connection of portion's setting, the outlet of the circulating pump 3 and the setting of 4 internal upper part of electrolytic cell connects
It connects, the feeding opening of the medicine-sucking pump 5 is connect with the medicine outlet that another side lower part of electrolytic cell 4 is arranged, the medicine outlet of the medicine-sucking pump 5
It is connect with the feeding opening of explosive box 6, the PLC controller 7 and the first solenoid valve 1-7, second solenoid valve 9, frequency conversion cooling system 2
In frequency-changeable compressor, circulating pump 3, the temperature sensor in electrolytic cell 4, direct-current switch power supply 8 and medicine-sucking pump 5 connect.It is described
Partition 1-3 is equipped with the through-hole that several diameters are 8 millimeters.
As shown in Figure 1, the electrolytic cell 4 is by shell 4-1, at least one electrode cavity 4-2, seal cover board 4-3, exhaust pipe 4-
4, temperature sensor 4-5 and electrolyte floating ball 4-6 is constituted, the electricity that the seal cover board 4-3 is arranged mounted in the upper surface of shell 4-1
In pole chamber inlet and outlet, the electrode cavity 4-2 is located at the electrode hole that in the inner cavity of shell 4-1 and electrode is arranged from seal cover board 4-3
Middle stretching, the exhaust pipe 4-4 are located at one side of the upper surface shell 4-1, and the temperature sensor 4-5 is located at the inner cavity shell 4-1
Side wall on, the electrolyte floating ball 4-6 is located at the side of the inner cavity shell 4-1.The another side of the upper surface the shell 4-1 is equipped with
Water inlet, the salt mouth of a river and cooling tube inlet and outlet, the upper and lower part of the shell 4-1 one side is respectively equipped with the installation of circulation pipe
Hole and circulating outlet, the another side shell 4-1 lower part are provided with medicine outlet.
As shown in Figure 3 and Figure 4, the electrode cavity 4-2 is by electrode case 4-2-1, two electrode plate 4-2-2 and several intermediate electricity
Pole plate 4-2-3 is constituted, and the electrode case 4-2-1 is the rectangle case of front and back opening, and the electrode plate 4-2-2 is located at electrode case
Left and right sides upper part of 4-2-1 is stretched out from the upper surface of electrode case 4-2-1, and the intermediate electrode plate 4-2-3 is located at two blocks of electricity
The centre of pole plate 4-2-2.The electrode plate 4-2-2 and intermediate electrode plate 4-2-3 is titanium plate and is equipped with ruthenium iridium on the surface of titanium plate
Coating.The size and number of the electrode plate 4-2-2 and intermediate electrode plate 4-2-3 are according to the yield of hypochlorite generator and straight
Stream supply voltage is different and determines.The direct current power source voltage determined in the present embodiment is in 15-36 volt ranges, corresponding electrode plate
The quantity of 4-2-2 and intermediate electrode plate 4-2-3 are chosen in 5-10 pieces of ranges, and every electrode plate is wide having a size of long 450mm
200mm, 1.5-3mm of thickness.
The salt dissolving case 1 is manufactured with anti-corrosion reinforced PVC anti-corrosion material, is stored up and is passed through 8 millimeters of diameter between salt tank and brine drum
Through-hole connection.100 millimeters the bottom of from positions in water injection pipe 1-2 insertion storage salt tank, bore 3 millimeters of apertures by salt water submerged part.
Salt dissolving case 1 and electrolytic cell 4 keep liquid level difference required by siphon.
The frequency conversion cooling system 2 is made of frequency-changeable compressor 2-1, condenser 2-2 and titanium evaporation cooling coil 2-3, is become
The outlet of frequency compressor 2-1 is connect with the import of titanium evaporation cooling coil 2-3, and the outlet of titanium evaporation cooling coil 2-3 passes through hair
Tubule is connect with the import of condenser 2-2, and the outlet of condenser 2-2 is connect with the import of frequency-changeable compressor 2-1.
The course of work of the invention are as follows:
1, strong brine is deployed；The first solenoid valve of strong brine 1-7 is opened, injects tap water into salt dissolving case 1, in salt dissolving case 1
Liquid level reaches high liquid level state, closes the first solenoid valve 1-7, impregnates 1 endoparticle salt of salt dissolving case for a long time and is dissolved to saturation, this
When 1 solution concentration of salt dissolving case close to 26.5%.
2, the weak brine of 3-3.5% concentration is deployed；When 6 drug storage floating ball 6-2 of finished product explosive box is down to scarce medical fluid position, PLC control
Device 7 processed issues starting work order.The first solenoid valve of strong brine 1-7 is opened, injects tap water into salt dissolving case 1.In salt dissolving case 1
Liquid level, which exceeds quickly at the top of bushing type siphoning installation, reaches upper liquid level；Strong brine is due to salt dissolving case 1 and electrolytic cell 4 in salt dissolving case 1
Difference in height driving strong brine is entered in siphon pipe 1-6 by siphon pipe sleeve 1-5, and strong brine flows into while extracting siphon pipe sleeve 1-5 out
Interior air makes to form vacuum in siphon pipe, quickly forms siphon, and strong brine is added to electrolytic cell 4, causes 1 liquid level of salt dissolving case quick
Lower liquid level is dropped to, siphon pipe sleeve 1-5, which enters large quantity of air, makes siphon pipe 1-6 stop siphon.Salt dissolving case 1 is discharged into electrolytic cell 4 and sets
After quantitative strong brine, the first solenoid valve of strong brine 1-7 of opening, which continues to inject tap water in salt dissolving case 1, dissolves granulated salt,
The supreme fluid level condition until 1 liquid level of salt dissolving case is gone up, the salt water floating ball 1-4 in salt dissolving case 1 issue signal-off strong brine first
Solenoid valve 1-7 stops filling the water to salt dissolving case 1, and salt dissolving case 1 keeps upper liquid level continued dissolution granulated salt to be ready for siphon next time
Quantitative strong brine is added to electrolytic cell 4.
3, when salt dissolving case 1 issues siphon end signal, PLC controller 7 starts second solenoid valve 9 and injects into electrolytic cell 4
Tap water, electrolysis floating ball 4-6 stops filling the water to electrolytic cell 4 when monitoring liquid level in the liquid level to electrolytic cell 4, while opening direct current and opening
Powered-down source 8 and circulating pump 3, into electrowinning process.Concentration is maintained between 3.0-3.5% when electrolytic cell 4 is normally electrolysed, generally
Situation is 3.2%.When 4 temperature sensor 4-5 of electrolytic cell detects that electrolyte temperature rises to 36 degree in electrolytic process, start frequency conversion
Frequency-changeable compressor 2-1 in cooling system 2 starts to work, and electrolyte temperature is made to be maintained at 42 degree or less.Circulating pump 3 is from electrolytic cell
Electrolyte is extracted in the lower part of 4 sides, by overcoming electrode cavity 4-2 to electrolyte in circulation pipe input electrode chamber 4-2 after pressurization
The barrier of flowing accelerates electrolyte to flow in electrode surface and updates, further improves electrode working efficiency.
4, after electrolytic cell 4 is electrolysed 120 minutes, DC power supply 8 is automatically closed and stops electrolysis, simultaneously close off circulating pump 3 and become
Frequency compressor 2-1 opens medicine-sucking pump 5, sodium hypochlorite in electrolytic cell 4 is pumped into explosive box 6,4 electrolyte inside floating ball of electrolytic cell
When 4-6 drops to lower liquid level, medicine-sucking pump 5 is closed.After dosing pumps 6-1 work, drug storage floating ball 6-2 drops to storage in explosive box 6
Under medicine when liquid level, into next course of work.
The present invention is electrolysed preferable operating condition are as follows: and electrolysis time is 2 hours, and electrolyte salt concentration is 3.0~3.5%,
36~42 degree of electrolyte temperature.The sodium hypochlorite effective chlorine density that is produced in such operating condition stablize 8500mg/L with
On.Effective chlorine can be kept close to the optimum level of 10g/L, salt consumption and power consumption at this time is held at lower water.
To verify beneficial effects of the present invention, following comparative experiments is made.
The electrolytic cell specification that experimental group of the present invention uses is height 550mm* length 420mm* width 400mm, actual volume
92.5 liters, 2.5 kg particles salt are added, DC power supply exports 15V.Electrode cavity 4-2 is by electrode case, two electrode plates and three pieces
Between electrode plate constitute.Its electrode plate size are as follows: long 450mm* wide 200mm* thickness 1.5mm, interval 10mm are evenly distributed.Electrode case two
The electrode plate of side draws conductive lead wire plate upwards, and conductive lead wire plate takes high 150mm* wide 200mm* thickness 3mm titanium plate, its underpart and electricity
Pole plate is integrally welded, and the closed cover board of electrolytic cell is stretched out in the upper end, passes through fastening bolt and DC power output end connection.
The electrode web plate that control group uses five pieces of general gap formula electrolysis generators, connects and composes group using plastic bolt
Composite electrode group.The electrode network plate matter of this electrode group, the electrode of size, lead pattern and type of array all with experimental group of the present invention
Plate is identical.
Two groups are successively electrolysed 120 minutes under the conditions of identical, respectively test job electric current, voltage value and final solution
Effective chlorine density, as a result such as following table.
As seen from the above table, present invention reduces current drains, improve effective chlorine density, it was demonstrated that the present invention is more common than existing
Clearance-type electrolysis generator is superior.
Claims (4)
1. a kind of intermittent sodium hypochlorite electrolysis generator of continuously-running, including frequency conversion cooling system (2), electrolytic cell (4),
Medicine-sucking pump (5), explosive box (6), PLC controller (7) and direct-current switch power supply (8), it is characterised in that: further include salt dissolving case (1)
With circulating pump (3), the salt dissolving case (1) is by cabinet (1-1), water injection pipe (1-2), partition (1-3), salt water floating ball (1-4), siphon
Pipe sleeve (1-5), siphon pipe (1-6) and the first solenoid valve (1-7) are constituted, and the partition (1-3) is located in cabinet (1-1) and by case
The inner cavity body (1-1) is divided into storage salt tank and brine drum, and the water injection pipe (1-2) is located in storage salt tank, and the siphon pipe (1-6) sets
In brine drum and the water inlet of siphon pipe (1-6) is 30mm lower than upper liquid level, and the siphon pipe sleeve (1-5) covers in siphon pipe (1-
6) on and the import of siphon pipe sleeve (1-5) is concordant with lower liquid level, and the salt water floating ball (1-4) is located in brine drum, and described first
The water outlet of solenoid valve (1-7) is connect with the water inlet of water injection pipe (1-2)；The water outlet and electrolytic cell of the siphon pipe (1-6)
(4) salt mouth of a river connection, the water inlet of the electrolytic cell (4) is connect by pipeline with the water outlet of second solenoid valve (9), described
The cooling tube of frequency conversion cooling system (2) is located in the inner cavity of electrolytic cell (4), electrode and the dc switch electricity of the electrolytic cell (4)
Source (8) connection, the import of the circulating pump (3) are connect with the outlet that (4) one side lower part of electrolytic cell is arranged, the circulating pump (3)
The import of circulation pipe that is arranged of outlet and electrolytic cell (4) internal upper part connect, the feeding opening and electrolytic cell of the medicine-sucking pump (5)
(4) the medicine outlet connection of another side lower part setting, the medicine outlet of the medicine-sucking pump (5) are connect with the feeding opening of explosive box (6), institute
State PLC controller (7) and the first solenoid valve (1-7), second solenoid valve (9), the frequency-changeable compressor in frequency conversion cooling system (2),
Circulating pump (3), the temperature sensor in electrolytic cell (4), direct-current switch power supply (8) and medicine-sucking pump (5) connection.
2. a kind of intermittent sodium hypochlorite electrolysis generator of continuously-running according to claim 1, it is characterised in that:
The electrolytic cell (4) is passed by shell (4-1), at least one electrode cavity (4-2), seal cover board (4-3), exhaust pipe (4-4), temperature
Sensor (4-5) and electrolyte floating ball (4-6) are constituted, and the seal cover board (4-3) is located at the electricity of the upper surface setting of shell (4-1)
In pole chamber inlet and outlet, the electrode cavity (4-2) is located in the inner cavity of shell (4-1) and electrode is arranged from seal cover board (4-3)
It is stretched out in electrode hole, the exhaust pipe (4-4) is located at one side of the upper surface shell (4-1), and the temperature sensor (4-5) is located at
On the side wall of the inner cavity shell (4-1), the electrolyte floating ball (4-6) is located at the side of the inner cavity shell (4-1).
3. a kind of intermittent sodium hypochlorite electrolysis generator of continuously-running according to claim 1 or 2, feature exist
In: the electrode cavity (4-2) is by electrode case (4-2-1), two electrode plates (4-2-2) and several intermediate electrode plates (4-2-3) structure
At the electrode case (4-2-1) is the rectangle case of front and back opening, and the electrode plate (4-2-2) is located at electrode case (4-2-1)
Left and right sides upper part stretched out from the upper surface of electrode case (4-2-1), the intermediate electrode plate (4-2-3) is located at two pieces of electrodes
The centre of plate (4-2-2).
4. a kind of intermittent sodium hypochlorite electrolysis generator of continuously-running according to claim 3, it is characterised in that:
The electrode plate (4-2-2) and intermediate electrode plate (4-2-3) are titanium plate and are equipped with ruthenium iridium coating layer on the surface of titanium plate.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201811328832.0A CN109183060A (en) | 2018-11-09 | 2018-11-09 | A kind of intermittent sodium hypochlorite electrolysis generator of continuously-running |
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| CN201811328832.0A CN109183060A (en) | 2018-11-09 | 2018-11-09 | A kind of intermittent sodium hypochlorite electrolysis generator of continuously-running |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110820009A (en) * | 2019-11-27 | 2020-02-21 | 苏州希克曼物联技术有限公司 | Sodium hypochlorite generating device regulated and controlled through frequency conversion and application |
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| CN207619020U (en) * | 2017-12-12 | 2018-07-17 | 江苏唯达水处理技术股份有限公司 | A kind of equipment of automatic production liquor natrii hypochloritis |
| CN108658184A (en) * | 2018-05-15 | 2018-10-16 | 廊坊市凯翔工贸有限公司 | Sulphur removal sterilizing unit |
| CN209128551U (en) * | 2018-11-09 | 2019-07-19 | 太原卫安环保科技股份有限公司 | A kind of intermittent sodium hypochlorite electrolysis generator of continuously-running |
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| CN110820009A (en) * | 2019-11-27 | 2020-02-21 | 苏州希克曼物联技术有限公司 | Sodium hypochlorite generating device regulated and controlled through frequency conversion and application |
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