CN205741225U - Dynamically normal pressure vertical electrode formula hypochlorite generator - Google Patents
Dynamically normal pressure vertical electrode formula hypochlorite generator Download PDFInfo
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- CN205741225U CN205741225U CN201620452691.3U CN201620452691U CN205741225U CN 205741225 U CN205741225 U CN 205741225U CN 201620452691 U CN201620452691 U CN 201620452691U CN 205741225 U CN205741225 U CN 205741225U
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- electrolyzer
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- normal pressure
- sodium hypochlorite
- vertical electrode
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Abstract
nullThe utility model discloses a kind of dynamically normal pressure vertical electrode formula hypochlorite generator，Including water softener、Salt cellar、Salt cellar tank level control system、Soft water saline matching system、Vertoro，Control system、Electrolyzer group、Hydrogen discharge pipe、Sodium hypochlorite storage tank、Aerator、Running water pipe，The water inlet of water softener connects running water pipe，Water softener connects salt cellar and soft water saline matching system by pipeline and valve，Salt cellar tank level control system connects water softener and salt cellar，Salt cellar connects soft water saline matching system，Soft water saline matching system connects electrolyzer group by valve and pipeline，Vertoro connects electrolyzer group and control system，Control system connects electrolyzer group，Electrolyzer group top connects hydrogen discharge pipe，Electrolyzer group connects sodium hypochlorite storage tank by pipeline and valve，Sodium hypochlorite storage tank top connects aerator and hydrogen discharge pipe.This utility model vertical electrode, dynamic electrolytic, normal pressure discharge hydrogen, safety, electrolytic efficiency are high.
Description
Technical field
This utility model relates to water disinfecting device field, particularly relates to a kind of dynamically normal pressure vertical electrode formula sodium hypochlorite
Generator.
Background technology
Hypochlorite generator, can occur to make liquor natrii hypochloritis at the occasion scene needing sterilization.Keep away
Exempt from buying sterilization chemical transporting, store and added the potential safety hazard of link.At water sterilization and other row
Industry is more and more applied.But the hypochlorite generator provided in the market, is electrode level
Formula is arranged, single process, pressure type structure.Its shortcoming is that efficiency is low, and structure is complicated, has pressure to run, hydrogen
Compression is assembled, and has potential safety hazard.
Utility model content
In view of this, technical problem to be solved in the utility model is: provide a kind of simple in construction, design
Rationally, normal pressure run dynamically make liquor natrii hypochloritis continuously, carry out disinfection for adding sodium hypochlorite continuously
Occasion (such as waterworks) provide the dynamic normal pressure vertical electrode formula hypochlorite generator of guarantee.
In order to achieve the above object, this utility model adopts the following technical scheme that and realizes:
A kind of dynamically normal pressure vertical electrode formula hypochlorite generator, including water softener, salt cellar, salt
Tank tank level control system, soft water saline matching system, vertoro, control system, electrolyzer group,
Hydrogen discharge pipe, sodium hypochlorite storage tank, aerator, running water pipe, the water inlet of water softener connects
Running water pipe), water softener connects salt cellar and soft water saline matching system respectively by pipeline and valve,
Described salt cellar tank level control system connects water softener and salt cellar, and described salt cellar connects soft water saline proportioning system
System, described soft water saline matching system connects electrolyzer group, described Transformer Rectifier by valve and pipeline
Device connects electrolyzer group and control system respectively, and described control system connects electrolyzer group, described electrolysis
The top of pond group connects hydrogen discharge pipe, and described electrolyzer group connects sodium hypochlorite by pipeline and valve
Storage tank, the top of described sodium hypochlorite storage tank connects aerator and hydrogen discharge pipe respectively.
Electrolyzer connects hydrogen discharge pipe and directly connects air, and system is run at ambient pressure.
Improving further, described electrolyzer group is made up of single electrolyzer.
Improving further, described electrolyzer group is in series by multiple electrolyzers.Valve is not set between each electrolyzer
Door, the dynamic continuous electrolysis of normal pressure, dynamic electrolytic step by step, until liquor natrii hypochloritis's concentration reaches to set
Requirement.
Improving further, described electrolyzer group is made up of multiple electrolyzer parallel connections.
Improving further, described electrolyzer is provided with sodium hypochlorite circulating line；Electrolysis capable of circulation is electrolysed the most completely
Saturated brine, the dynamic continuous electrolysis of normal pressure, until liquor natrii hypochloritis's concentration reach set requirement.
Improving further, be provided with battery lead plate in described electrolyzer, described battery lead plate is arranged vertically.
Tap water supply pipe is connected with water softener；Water softener outlet connects with salt cellar and soft water saline matching system
Connect；Salt cellar flows out saturated brine, and also and soft water enters input electricity after the mixing of soft water saline matching system proportioning
Xie Chi group；Mixed solution is electrolysed in electrolyzer, produce hydrogen floated by natural buoyancy, and with drum
Nature is entered through hydrogen discharge bank of tubes after the air mixed diluting that blower fan blows.
Further, the described many water of salt cellar inner salt is few.Salt cellar tank level control system is according to water consumption to salt cellar certainly
The dynamic compensation water yield.
Further, described soft water saline matching system adjusts proportioning (salinity) automatically, changes electrical conductivity,
Realize the constant electrode electric current in electrolyzer.
Further, described electrolyzer upper end is provided with temperature sensor and liquid level sensor.
Further, described sodium hypochlorite storage tank sets liquid level sensor.Liquid level reaches the upper limit, system autostop；
Liquid level reaches lower limit, system Auto Power On.
Further, described electrolyzer is demountable structure.In many cell system, dismantle an electrolyzer
After, system still can work.
In electrolyzer, battery lead plate is vertical parallel arrangement, the solution flowed out in soft water saline matching system from
Electrolyzer bottom entrance enters, from bottom to top direction flowing, and ie in solution is hung down from bottom to top in electrolyzer
Direct current moves.It is electrolysed time in the middle of battery lead plate.By the solution after being electrolysed from electrolyzer upper end outlet stream
Go out, through outermost loops pipeline, again come electrolyzer bottom entrance and enter electrolyzer, be again electrolysed,
Again flow out from upper end outlet.So can repeatedly circulate, sodium hypochlorite concentration gradually raises.
Electrolyzer can arrange multiple in parallel or series, go into different qualities system.Parallel electrolytic pond is,
System can multiple electrolyzers in parallel, each electrolyzer can under low voltage power supply repeatedly cyclic electrolysis output
Liquor natrii hypochloritis；Series connection electrolysis pond is, system can be connected multiple electrolyzer, under High Voltage Power Supply,
After solution circulates in each electrolyzer, entering back into next electrolyzer cyclic electrolysis, normal pressure dynamically connects
Continuous electrolysis, to the last one, output liquor natrii hypochloritis.
Producing hydrogen during electrolyzer electrolytic solution, hydrogen leans on natural buoyancy emersion liquid level the most easily, and
After the Dilution air of aerator output, enter hydrogen discharge bank of tubes empty.Hydrogen produces at any time, floats at any time
Go out, discharge at any time.Electrolyzer, pipeline do not have hydrogen to gather.Meanwhile, the hydrogen of floating washes away electricity
Pole plate, reduces the electrode blind spot produced on battery lead plate because of bubbles attached, improves electrolytic efficiency.On
Floating hydrogen promotes liquid flows upwards, go into the power that solution in electrolyzer circulates.
As shown from the above technical solution, the beneficial effects of the utility model are:
Compared to existing technology, the utility model has the advantages that, system footprint area is little, and normal pressure is dynamically the most electric
Solution, battery lead plate vertical out-fall, the hydrogen of floating washes away battery lead plate, reduces because of bubbles attached at electrode
The electrode blind spot produced on plate, improves electrolytic efficiency, and automaticity is high.Under normal circumstances, system
Startup and stopping need not personnel participate in.When restoring electricity after on-the-spot accident power-off, system is the most extensive
Multiple operation.According to electrolyzer capacity and the quantity of electrolyzer serial or parallel connection, can form and vary in size
Sodium hypochlorite production capacity, meet the needs of user of varying in size；The discharge of hydrogen normal pressure and air blast
After the air mixed diluting that machine blows, discharge improves the safety of hydrogen discharge (hydrogen accounting height is explosive
Fried).
Accompanying drawing explanation
Fig. 1 is this utility model structural representation；
Fig. 2 is this utility model embodiment one structural representation；
Fig. 3 is the electrolyzer group structural representation that circulating line was connected and be provided with to multiple electrolyzer；
Fig. 4 is this utility model embodiment two structural representation；
Fig. 5 is the parallel connection of multiple electrolyzer the electrolyzer group structural representation being provided with circulating line.
Note: in figure, the direction of arrow represents the flow direction of fluid (liquid or gas).
Detailed description of the invention
In order to make those skilled in the art can be further understood that feature of the present utility model and technology contents, please
Refering to below in connection with detailed description of the present utility model and accompanying drawing.
Refer to Fig. 1, Fig. 2, Fig. 4, one dynamically normal pressure vertical electrode formula hypochlorite generator, including
Water softener 1, salt cellar 2, salt cellar tank level control system 3, soft water saline matching system 4, Transformer Rectifier
Device 5, control system 6, electrolyzer group 11, hydrogen discharge pipe 8, sodium hypochlorite storage tank 9, air blast
Machine 10, running water pipe 12, the water inlet of water softener 1 connects running water pipe 12, and water softener 1 passes through
Pipeline and valve connect salt cellar 2 and soft water saline matching system 4 respectively, described salt cellar Liquid level system
System 3 connection water softener 1 and salt cellar 2, described salt cellar 2 connects soft water saline matching system 4, described
Soft water saline matching system 4 connects electrolyzer group 11, described vertoro 5 by valve and pipeline
Connecting electrolyzer group 11 and control system 6 respectively, described control system 6 connects electrolyzer group 11,
The top of described electrolyzer group 11 connects hydrogen discharge pipe 8, described electrolyzer group 11 by pipeline and
Valve connects sodium hypochlorite storage tank 9, and the top of described sodium hypochlorite storage tank 9 connects air blast respectively
Machine 10 and hydrogen discharge pipe 8.
As in figure 2 it is shown, running water pipe 12 connects water softener 1；Water softener 1 outlet and salt cellar 2
And soft water saline matching system 4 connects；Vertoro 5 High Voltage Power Supply is in battery lead plate 72, salt cellar
Tank level control system 3 compensates the water yield according to water consumption automatically to salt cellar 2；Salt cellar 2 flows out saturated salt
Water is also and soft water enters input electrolyzer group 11 after the mixing of soft water saline matching system 4 proportioning；Soft water salt
Water matching system 4 adjusts proportioning (salinity) automatically, changes electrical conductivity, it is achieved in electrolyzer 7
Constant electrode electric current；Mixed solution is electrolysed in electrolyzer 7, and electrolyzer 7 upper end is provided with temperature and passes
Sensor and liquid level sensor, produce hydrogen and floated by natural buoyancy, and aerator 10 is when system is run
All the time delivery air, enters sodium hypochlorite storage tank 9, diluter with the hydrogen mixing that electrolyzer 7 produces
After releasing, it is discharged in air through hydrogen discharge pipe 8.The sodium hypochlorite being electrolysed generation in electrolyzer 7 is molten
Liquid enters sodium hypochlorite storage tank 9 through delivery pipe, is then fed into each liquor natrii hypochloritis's demand station 13.Secondary
Liquid level sensor is set in sodium chlorate storage tank 9.Liquid level reaches the upper limit, system autostop；Liquid level is as little as
Lower limit, system Auto Power On.Control system 6 is according to the temperature in system, liquid level, flow, electric current
Etc. parameter, the operation of control system.As regulated softening water and saturated brine proportioning, control electrode
Current constant in pond 7；According to the height of liquid level in sodium hypochlorite storage tank 9, automatically turn on or close
Closed system；Power-off or restore electricity, system is resumed work automatically；Electrolyzer pipeline leakage, system is certainly
Dynamic closedown；Aerator 10 is blown fault, and system is automatically switched off.
Follow as it is shown on figure 3, electrolyzer group 11 is provided with sodium hypochlorite for each electrolyzer 7 in Fig. 2
Behind endless tube road 71 in series.Vertoro 5 High Voltage Power Supply to battery lead plate 72, solution big
Part produces interior circulation at each electrolyzer 7 through sodium hypochlorite circulating line 71, and small part enters
Next electrolyzer 7, the solution after cyclic electrolysis enters back into next electrolyzer 7 cyclic electrolysis, directly
To last electrolyzer 7, output solubility meets the liquor natrii hypochloritis of design.
As shown in Figure 4, running water pipe 12 connects water softener 1；Water softener 1 outlet and salt cellar 2
And soft water saline matching system 4 connects；Vertoro 5 low voltage power supply is in battery lead plate 72, salt cellar
Tank level control system 3 compensates the water yield according to water consumption automatically to salt cellar 2；Salt cellar 2 flows out saturated salt
Water is also and soft water enters input electrolyzer group 11 after the mixing of soft water saline matching system 4 proportioning；Soft water salt
Water matching system 4 adjusts proportioning (salinity) automatically, changes electrical conductivity, it is achieved in electrolyzer 7
Constant electrode electric current；Mixed solution is electrolysed in electrolyzer 7, and electrolyzer 7 upper end is provided with temperature and passes
Sensor and liquid level sensor, produce hydrogen and floated by natural buoyancy, and aerator 10 is when system is run
All the time delivery air, enters sodium hypochlorite storage tank 9, diluter with the hydrogen mixing that electrolyzer 7 produces
After releasing, it is discharged in air through hydrogen discharge pipe 8.The sodium hypochlorite being electrolysed generation in electrolyzer 7 is molten
Liquid enters sodium hypochlorite storage tank 9 through delivery pipe, is then fed into each liquor natrii hypochloritis's demand station 13.Secondary
Liquid level sensor is set in sodium chlorate storage tank 9.Liquid level reaches the upper limit, system autostop；Liquid level is as little as
Lower limit, system Auto Power On.Control system 6 is according to the temperature in system, liquid level, flow, electric current
Etc. parameter, the operation of control system.As regulated softening water and saturated brine proportioning, control electrode
Current constant in pond 7；According to the height of liquid level in sodium hypochlorite storage tank 9, automatically turn on or close
Closed system；Power-off or restore electricity, system is resumed work automatically；Electrolyzer pipeline leakage, system is certainly
Dynamic closedown；Aerator 10 is blown fault, and system is automatically switched off.
Follow as it is shown in figure 5, electrolyzer group 11 is provided with sodium hypochlorite for each electrolyzer 7 in Fig. 4
Composition in parallel behind endless tube road 71.Vertoro 5 High Voltage Power Supply is to battery lead plate 72, and solution is often
Individual electrolyzer 7 is after sodium hypochlorite circulating line 71 produces interior circulation, and output meets what design was wanted
The liquor natrii hypochloritis of solubility.
Such as Fig. 3, Fig. 5, in loop structure, hydrogen buoyancy drives liquid flows upwards, hypochlorous acid
Sodium circulating line 71, is again introduced into electrolyzer 7 and is electrolysed.When being again electrolysed, produce again hydrogen,
Hydrogen is floated by natural buoyancy again, enters hydrogen discharge pipe 8 and discharges.So iterative cycles, in solution
Liquor natrii hypochloritis's concentration constantly raises.Repeatedly after circulation, liquor natrii hypochloritis's concentration reaches to set to be wanted
Ask, enter sodium hypochlorite storage tank 9 through discharge connecting tube.
But the foregoing is only preferable possible embodiments of the present utility model, and be not used to limit to this utility model
The scope of the claims, therefore all utilization this utility model description and accompanying drawing content made equivalent structure change, all
In like manner it is included in the range of this utility model.
Claims (9)
1. a dynamic normal pressure vertical electrode formula hypochlorite generator, including water softener (1), salt
Tank (2), salt cellar tank level control system (3), soft water saline matching system (4), Transformer Rectifier
Device (5), control system (6), electrolyzer group (11), hydrogen discharge pipe (8), sodium hypochlorite
Storage tank (9), aerator (10), running water pipe (12), it is characterised in that: water softener (1)
Water inlet connect running water pipe (12), water softener (1) connects salt respectively by pipeline and valve
Tank (2) and soft water saline matching system (4), described salt cellar tank level control system (3) connects soft
Hydrophone (1) and salt cellar (2), described salt cellar (2) connects soft water saline matching system (4), institute
State soft water saline matching system (4) and connect electrolyzer group (11), described change by valve and pipeline
Pressure commutator (5) connects electrolyzer group (11) and control system (6), described control system (6) respectively
Connecting electrolyzer group (11), the top of described electrolyzer group (11) connects hydrogen discharge pipe (8),
Described electrolyzer group (11) connects sodium hypochlorite storage tank (9) by pipeline and valve, described secondary
The top of sodium chlorate storage tank (9) connects aerator (10) and hydrogen discharge pipe (8) respectively.
Dynamic normal pressure vertical electrode formula hypochlorite generator the most according to claim 1, its
Being characterised by, described electrolyzer group (11) is made up of single electrolyzer (7).
Dynamic normal pressure vertical electrode formula hypochlorite generator the most according to claim 1, its
Being characterised by, described electrolyzer group (11) is in series by multiple electrolyzers (7).
Dynamic normal pressure vertical electrode formula hypochlorite generator the most according to claim 1, its
Being characterised by, described electrolyzer group (11) is made up of multiple electrolyzers (7) parallel connection.
5. send out according to the arbitrary described dynamic normal pressure vertical electrode formula sodium hypochlorite in claim 2-4
Raw device, it is characterised in that described electrolyzer (7) is provided with sodium hypochlorite circulating line (71).
6. send out according to the arbitrary described dynamic normal pressure vertical electrode formula sodium hypochlorite in claim 2-4
Raw device, it is characterised in that be provided with battery lead plate (72), described battery lead plate in described electrolyzer (7)
Arranged vertically.
7. occur according to arbitrary described dynamic normal pressure vertical electrode formula sodium hypochlorite in claim 2-4
Device, it is characterised in that described electrolyzer (7) upper end is provided with temperature sensor and liquid level sensor.
8. occur according to arbitrary described dynamic normal pressure vertical electrode formula sodium hypochlorite in claim 2-4
Device, it is characterised in that set liquid level sensor in described sodium hypochlorite storage tank (9).
9. occur according to arbitrary described dynamic normal pressure vertical electrode formula sodium hypochlorite in claim 3-4
Device, it is characterised in that described electrolyzer (7) is demountable structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620452691.3U CN205741225U (en) | 2016-05-17 | 2016-05-17 | Dynamically normal pressure vertical electrode formula hypochlorite generator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620452691.3U CN205741225U (en) | 2016-05-17 | 2016-05-17 | Dynamically normal pressure vertical electrode formula hypochlorite generator |
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| CN205741225U true CN205741225U (en) | 2016-11-30 |
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| CN201620452691.3U Expired - Fee Related CN205741225U (en) | 2016-05-17 | 2016-05-17 | Dynamically normal pressure vertical electrode formula hypochlorite generator |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108193223A (en) * | 2018-02-11 | 2018-06-22 | 广东卓信环境科技股份有限公司 | A kind of hypochlorite production system |
| CN106498439B (en) * | 2017-01-12 | 2018-09-25 | 青岛双瑞海洋环境工程股份有限公司 | Sodium hypochlorite generators |
| CN108588756A (en) * | 2018-06-29 | 2018-09-28 | 山东新日电气设备有限公司 | A kind of row's hydrogen fan operation state control device |
| CN109081482A (en) * | 2018-09-30 | 2018-12-25 | 四川省威沃敦化工有限公司 | A kind of shale gas fracturing outlet liquid electrolytic sterilizing apparatus sledge |
| CN112111754A (en) * | 2020-10-15 | 2020-12-22 | 山东新日电气设备有限公司 | Intelligent disinfection device control system |
| CN113215601A (en) * | 2020-01-19 | 2021-08-06 | 北京奇清水处理技术有限公司 | Device that sodium hypochlorite generator is used for hydrogen to discharge and solution to carry |
-
2016
- 2016-05-17 CN CN201620452691.3U patent/CN205741225U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106498439B (en) * | 2017-01-12 | 2018-09-25 | 青岛双瑞海洋环境工程股份有限公司 | Sodium hypochlorite generators |
| CN108193223A (en) * | 2018-02-11 | 2018-06-22 | 广东卓信环境科技股份有限公司 | A kind of hypochlorite production system |
| CN108193223B (en) * | 2018-02-11 | 2023-12-15 | 广东卓信环境科技股份有限公司 | Hypochlorite production system |
| CN108588756A (en) * | 2018-06-29 | 2018-09-28 | 山东新日电气设备有限公司 | A kind of row's hydrogen fan operation state control device |
| CN109081482A (en) * | 2018-09-30 | 2018-12-25 | 四川省威沃敦化工有限公司 | A kind of shale gas fracturing outlet liquid electrolytic sterilizing apparatus sledge |
| CN113215601A (en) * | 2020-01-19 | 2021-08-06 | 北京奇清水处理技术有限公司 | Device that sodium hypochlorite generator is used for hydrogen to discharge and solution to carry |
| CN112111754A (en) * | 2020-10-15 | 2020-12-22 | 山东新日电气设备有限公司 | Intelligent disinfection device control system |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161130 Termination date: 20170517 |
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| CF01 | Termination of patent right due to non-payment of annual fee |