CN206599615U - Sodium hypochlorite generators - Google Patents
Sodium hypochlorite generators Download PDFInfo
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- CN206599615U CN206599615U CN201720036715.1U CN201720036715U CN206599615U CN 206599615 U CN206599615 U CN 206599615U CN 201720036715 U CN201720036715 U CN 201720036715U CN 206599615 U CN206599615 U CN 206599615U
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- sodium hypochlorite
- tube
- branch pipe
- import
- dosing pump
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Abstract
A kind of sodium hypochlorite generators, including softening hydrophone, dissolved salt case, sodium hypochlorite generating unit and sodium hypochlorite storage tank, sodium hypochlorite generating unit includes ratio dosing pump, one-level electrolytic cell and second electrolyser, soften the outlet of hydrophone by softening import of the waterpipe respectively with dissolved salt case, first import of ratio dosing pump and the import connection of second electrolyser, the outlet of dissolved salt case is connected by the second import of pipeline and ratio dosing pump, the outlet of ratio dosing pump is connected by pipeline with the import of one-level electrolytic cell, the outlet of one-level electrolytic cell and the import of second electrolyser are connected, the outlet of second electrolyser is connected by pipeline with the import of sodium hypochlorite storage tank.Sodium hypochlorite generators of the present utility model form salinity gradient between one-level electrolytic cell and the electrolyte of second electrolyser, can individually improve the electrolyte salinity of one-level electrolytic cell, so that while device electrolytic efficiency is improved, it is possible to decrease power consumption and salt consumption.
Description
Technical field
The utility model is related to water disinfecting device field, especially with regard to a kind of sodium hypochlorite generators.
Background technology
Hypochlorite generator is one kind of Water Disinfection disinfection equipment, and the equipment is led to using saline solution as raw material
Cross cell reaction and produce liquor natrii hypochloritis, so as to make liquor natrii hypochloritis, application in the occasion for needing to sterilize
Extensively.However, no matter whether electrolytic cell is divided into firsts and seconds to existing hypochlorite generator, electrolyte salt solution used is dense
Degree is 3% or so, and low brine strength make it that the electrical conductivity of electrolyte is low, correspondingly, and the voltage of required electrolysis power is high, and
Chlorine in Solution ion concentration is low also to cause analysis chlorine relative difficulty, so as to cause hypochlorite generator to exist, power consumption is high, be electrolysed effect
The problem of rate is low.
Utility model content
The purpose of this utility model is to provide a kind of sodium hypochlorite generators, can improve electrolytic efficiency, reduce energy consumption.
The utility model provides a kind of sodium hypochlorite generators, including list occurs for softening hydrophone, dissolved salt case, sodium hypochlorite
Member and sodium hypochlorite storage tank, the sodium hypochlorite generating unit include ratio dosing pump, one-level electrolytic cell and second electrolyser, institute
The outlet of softening hydrophone is stated by softening import of the waterpipe respectively with the dissolved salt case, the first import of the ratio dosing pump
And the import connection of the second electrolyser, the outlet of the dissolved salt case passes through the second import of pipeline and the ratio dosing pump
Connection, the outlet of the ratio dosing pump is connected by pipeline with the import of the one-level electrolytic cell, the one-level electrolytic cell
Outlet is connected with the import of the second electrolyser, and the outlet of the second electrolyser passes through pipeline and the sodium hypochlorite storage tank
Import connection.
Further, it is described softening waterpipe include main pipeline, the first branch pipe(tube), the second branch pipe(tube), the 3rd branch pipe(tube) and
4th branch pipe(tube), the entrance of the main pipeline is connected with the outlet of the softening hydrophone, and first branch pipe(tube) connects the master
The outlet and the import of the dissolved salt case of pipeline, second branch pipe(tube) connect the outlet of the main pipeline and the 3rd branch pipe
The entrance in road, the 4th branch pipe(tube), the outlet of the 3rd branch pipe(tube) is connected with the first import of the ratio dosing pump, institute
The outlet for stating the 4th branch pipe(tube) is connected with the import of the second electrolyser.
Further, second branch pipe(tube) is in the position close to the 3rd branch pipe(tube) and the entrance of the 4th branch pipe(tube)
Put place and be provided with temperature controller, the temperature controller is the integral constant temperature water dispenser of air-cooled cold-hot, the temperature of the temperature controller
It is 5-20 DEG C to spend control range.
Further, the 3rd branch pipe(tube) is described soft with being respectively equipped with softening water regulating valve in the 4th branch pipe(tube)
Change the ratio that water regulating valve is used to control the softened water into the ratio dosing pump and the softened water into the second electrolyser
Example is 4:5.
Further, the production fluid of the one-level electrolytic cell is discharged into the second electrolyser, the 4th branch pipe(tube)
Softening water regulating valve is additionally operable to control and enters production fluid of the softened water of the second electrolyser with entering the second electrolyser
Ratio be 1:1.
Further, the ratio dosing pump is waterpower ratio dosing pump, and the first import of the ratio dosing pump is water
Power drive end.
Further, the dissolved salt case is used to prepare saturated salt solution, and the ratio dosing pump is used to control saturated salt molten
The mixed proportion of liquid and softened water is 1:4.
Further, the sodium hypochlorite storage tank is provided with row's hydrogen blower fan and row's hydrogen mouthful, and row's hydrogen blower fan is used to dilute institute
State the hydrogen in sodium hypochlorite storage tank.
Further, in addition to sodium hypochlorite dosing pump, the sodium hypochlorite dosing pump and the sodium hypochlorite storage tank
Outlet connection.
Further, the charging aperture of the dissolved salt case is connected with screw feeding machine.
In the sodium hypochlorite generators of the utility model embodiment, adoption rate dosing pump prepares salting liquid and is used as one-level
The electrolyte of electrolytic cell, and softened water is it is possible to additionally incorporate to be used as two grades with the mixing of the production fluid of one-level electrolytic cell to second electrolyser
The electrolyte of electrolytic cell, in this way, the electrolyte salinity of one-level electrolytic cell can be improved individually, and is electrolysed in one-level electrolytic cell and two grades
Salinity gradient is formed between the electrolyte of groove so that is being improved electrolytic efficiency, is especially being improved the electrolytic efficiency of one-level electrolytic cell
While, it is possible to decrease overall power consumption and salt consumption.
Brief description of the drawings
Fig. 1 is the structural representation of sodium hypochlorite generators in the utility model one embodiment.
Embodiment
Further to illustrate that the utility model is to reach technological means and effect that predetermined utility model purpose is taken,
Below in conjunction with accompanying drawing and preferred embodiment, to embodiment of the present utility model, structure, feature and its effect, specifically
It is bright as after.
Fig. 1 is the structural representation of sodium hypochlorite generators in the utility model one embodiment.As shown in figure 1, this
The sodium hypochlorite generators of utility model embodiment include the softening hydrophone 1, dissolved salt case 2, temperature being connected with each other by pipeline
Controller 3, sodium hypochlorite generating unit 4, sodium hypochlorite storage tank 5 and sodium hypochlorite dosing pump 6, sodium hypochlorite generating unit 4 are wrapped
Include ratio dosing pump 41, one-level electrolytic cell 42 and second electrolyser 43.
Soften the import connection running water of hydrophone 1, running water itself come under effect of water pressure to enter softening hydrophone 1 with
The calcium ions and magnesium ions for making the hardness of running water reduce and go in water removal, so that mitigate electrolytic tank electrode scale formation, softening hydrophone 1
Export by softening import of the waterpipe respectively with dissolved salt case 2, the first import of ratio dosing pump 41 and second electrolyser 43
Import is connected.Specifically, softening waterpipe includes main pipeline 7, the first branch pipe(tube) 71, the second branch pipe(tube) 72, the 3rd branch pipe(tube) 73
And the 4th branch pipe(tube) 74, outlet of the entrance of main pipeline 7 with softening hydrophone 1 be connected, and the first branch pipe(tube) 71 connects going out for main pipeline 7
Mouthful with the import of dissolved salt case 2, the outlet of the second branch pipe(tube) 72 connection main pipeline 7 and the 3rd branch pipe(tube) 73, the 4th branch pipe(tube) 74
First import of entrance, the outlet of the 3rd branch pipe(tube) 73 and ratio dosing pump 41 is connected, the outlet of the 4th branch pipe(tube) 74 with two grades
The import connection of electrolytic cell 43.Further, it is respectively equipped with softening water regulating valve in the 3rd branch pipe(tube) 73 and the 4th branch pipe(tube) 74
(not shown), in the present embodiment, in the 3rd branch pipe(tube) 73 and the 4th branch pipe(tube) 74 soften water regulating valve be used for control enter than
The ratio of the softened water of example dosing pump 41 and the softened water into second electrolyser 43 is 4:5.
Temperature controller 3 is located in the second branch pipe(tube) 72 close to the position of the 3rd branch pipe(tube) 73 and the entrance of the 4th branch pipe(tube) 74
Place is put, softened water is after temperature controller 3, and water temperature is adjusted to suitable scope, then according to 4:5 ratio is respectively enterd
Ratio dosing pump 41 and second electrolyser 43.In the present embodiment, temperature controller 3 is the integral constant temperature water dispenser of air-cooled cold-hot,
The temperature controlling range of temperature controller 3 is 5-20 DEG C, so as to be down to the temperature of water by cooling when summer, water temperature was high
Less than 20 DEG C, water temperature is risen to more than 5 DEG C by heating when water temperature is low in the winter time, the scope of application of water temperature is extended to 0-40
℃。
The charging aperture of dissolved salt case 2 is connected with screw feeding machine 8, adds excess into dissolved salt case 2 using screw feeding machine 8
Table salt, soaks salt solution of the dissolving as saturation, the outlet of dissolved salt case 2 passes through pipeline and ratio dosing by softened water
The second import connection of pump 41.
The outlet of ratio dosing pump 41 is connected by pipeline with the import of one-level electrolytic cell 42, enters ratio through the first import
The softened water of dosing pump 41 and the saturated common salt solution for entering ratio dosing pump 41 through the second import are pressed in ratio dosing pump 41
Outlet discharge through ratio dosing pump 41 after setting ratio mixing, use ratio dosing pump 41 can make matched proportion density pass through graduated scale
It can directly obtain, and concentration is adjustable, proportioning is not influenceed by flow in pipeline and pressure, proportioning lasting accuracy is high.In the present embodiment
In, ratio dosing pump 41 is used to control the mixed proportion of saturated salt solution and softened water to be 1:4, so that it is about 6% to obtain concentration
Salting liquid, the salting liquid enter one-level electrolytic cell 42 in, due to the electrolyte of one-level electrolytic cell 42 be concentration be 6% salt
Water, is 2 times of 3% salinity that usual electrolyte is used, and higher salinity causes the electrolytic process of one-level electrolytic cell 42 to have
There are higher electrolytic efficiency and relatively low power consumption.Further, the ratio dosing pump 41 in the present embodiment is that waterpower ratio adds
Teat pipette, the first import of ratio dosing pump 41 is hydro powered end, so that pressure of the ratio dosing pump 41 in softened water water
It can be worked under effect, without electricity consumption, upstream need not be equipped with kinetic energy equipment, save the energy.
The outlet of one-level electrolytic cell 42 is connected with the import of second electrolyser 43, and the production fluid of one-level electrolytic cell 42 is discharged into two
Level electrolytic cell 43, the production fluid is effective chlorine density 10000ppm or so sodium hypochlorite and the mixed solution of salt.One-level electricity
The flow that the production fluid of solution groove 42 is discharged into second electrolyser 43 keeps constant after setting, in the present embodiment, the 4th branch pipe(tube)
Softening water regulating valve in 74 is additionally operable to control the softened water for entering second electrolyser 43 in the 4th branch pipe(tube) 74 with entering two grades
The ratio of the production fluid of electrolytic cell 43 is 1:1, that is, the electrolyte of second electrolyser 43 for one-level electrolytic cell 42 production fluid and
Softened water is with 1:The mixed liquor of 1 mixing.It is appreciated that into ratio dosing pump 41 softened water and enter second electrolyser 43
The ratio and entrance of the ratio of softened water, the softened water into second electrolyser 43 with the production fluid into second electrolyser 43
The ratio of the softened water of ratio dosing pump 41 and the softened water of entrance second electrolyser 43 is not limited with above-mentioned, and can be according to reality
Border needs to be adjusted, so that forming suitable salinity ladder between the electrolyte of one-level electrolytic cell 42 and second electrolyser 43
Degree.
Salinity ladder is formed in the utility model embodiment, between the electrolyte of one-level electrolytic cell 42 and second electrolyser 43
Degree, can individually improve the electrolyte salinity of one-level electrolytic cell 42, so that while electrolytic efficiency is improved, it is possible to decrease power consumption and salt
Consumption.Specifically, the one-level electrolyte in one-level electrolytic cell 42 is higher (about for the concentration for preparing acquisition by ratio dosing pump 41
6%) salting liquid so that electrical conductivity of solution is higher in one-level electrolytic cell 42, and Chlorine in Solution ion concentration is also higher, so that
Electrolytic process has higher electrolytic efficiency.On this basis, one-level electrolysis can be reduced by introducing softened water to second electrolyser 43
The production fluid temperature of groove 42 and makes the salt of the electrolyte of second electrolyser 43 dense to the temperature for being more suitable for the electrolysis of second electrolyser 43
Versus primary electrolytic cell 42 declines to form salinity gradient degree (about 3%), while also causing the porch of second electrolyser 43
Sodium hypochlorite concentration is reduced, and can be reduced time by reducing the temperature and sodium hypochlorite concentration of the porch electrolyte of second electrolyser 43
Sodium chlorate decomposes the low-producing influence of drop, and makes the salinity of electrolyte in second electrolyser 43 moderate and have relatively low gas
Content (H2) with the higher electrolytic efficiency of guarantee.
Connect above-mentioned, the import of sodium hypochlorite storage tank 5 is connected by pipeline with the outlet of second electrolyser 43, sodium hypochlorite storage
Tank 5 is electrolysed obtained liquor natrii hypochloritis and flows into sodium hypochlorite storage tank 5, hydrogen is secondary provided with row's hydrogen blower fan 51 and row's hydrogen mouthful 52
Separated upwards in sodium chlorate storage tank 5, and by row's hydrogen blower fan 51 be diluted to concentration below 1% after by being stored up positioned at sodium hypochlorite
Row's hydrogen mouthful 52 on the top of tank 5 drains into outdoor, and the outlet of sodium hypochlorite storage tank 5 is connected with sodium hypochlorite dosing pump 6, and sodium hypochlorite is molten
Liquid is stored in sodium hypochlorite storage tank 5 takes to carry out water sterilization for sodium hypochlorite dosing pump 6.
Next, the work with a specific sodium hypochlorite preparation process to sodium hypochlorite generators of the present utility model
Process describes in detail as follows.
As shown in figure 1, running water coming under effect of water pressure by softening hydrophone 1 at itself, softened hydrophone 1 softens
To softened water respectively enter in dissolved salt case 2 and temperature controller 3, dissolved salt case 2 added using screw feeding machine 8 it is excessive refined
Salt, salt solution of the dissolving as saturation is soaked by softened water, and the temperature into the softened water of temperature controller 3 is conditioned
The 3rd branch pipe(tube) 73 and the 4th branch pipe(tube) 74 are respectively enterd after to suitable scope (5-20 DEG C), in the 3rd branch pipe(tube) 73 and the 4th
Under softening water regulating valve effect in branch pipe(tube) 74, the softened water in the 3rd branch pipe(tube) 73 and the 4th branch pipe(tube) 74 is according to 4:5
Ratio respectively enters the first import (hydro powered end) and the second electrolyser 43 of ratio dosing pump 41.Then, ratio dosing pump
41 rely on the saturated aqueous common salt in the pressure duty of softened water water, dissolved salt case 2 under the suction of ratio dosing pump 41, with
Softened water is in ratio dosing pump 41 according to 1:4 ratios are mixed, and form salting liquid and entrance one-level electrolytic cell 42 that concentration is 6%
It is middle to be electrolysed.Electrolyte after electrolysis is effective chlorine density 10000ppm or so sodium hypochlorite and the mixed solution of salt,
The mixed solution and the softened water 1 from the 4th branch pipe(tube) 74:Enter after 1 mixing and be electrolysed in second electrolyser 43, is electrolysed
Liquor natrii hypochloritis afterwards flows into sodium hypochlorite storage tank 5, and hydrogen is separated upwards in sodium hypochlorite storage tank 5, and hydrogen is secondary
Pass through row 52 rows of hydrogen mouthful on the top of sodium hypochlorite storage tank 5 after being diluted to concentration below 1% by row's hydrogen blower fan 51 in sodium chlorate storage tank 5
To outdoor, liquor natrii hypochloritis is stored in sodium hypochlorite storage tank 5 to take for sodium hypochlorite dosing pump 6.Pass through the utility model
The current efficiency that can be electrolysed sodium hypochlorite generators improves 10% or so, power consumption reduction by 15% or so, salt consumption reduction
10% or so, floor space reduces 20% or so, and the scope of application of water temperature is extended to 0-40 DEG C.
To sum up, the sodium hypochlorite generators of the utility model embodiment at least have the advantages that:
(1) adoption rate dosing pump prepares salting liquid as the electrolyte of one-level electrolytic cell, and to second electrolyser in addition
Electrolyte of the softened water using the production fluid mixing with one-level electrolytic cell as second electrolyser is added, in this way, one can individually be improved
The electrolyte salinity of level electrolytic cell, and form salinity gradient between one-level electrolytic cell and the electrolyte of second electrolyser so that
While improving electrolytic efficiency, especially improving the electrolytic efficiency of one-level electrolytic cell, it is possible to decrease overall power consumption and salt consumption；
(2) salting liquid is prepared using waterpower ratio dosing pump online, matched proportion density can directly be obtained by graduated scale, and concentration can
Adjust and easy to operate, proportioning is not influenceed by flow in pipeline and pressure, proportioning lasting accuracy is high, and only needs by running water
Pressure-driven, without electricity consumption, upstream need not be equipped with kinetic energy equipment, save the energy；
(3) temperature that can adjust water using temperature controller makes water when summer water temperature is high in 5-20 DEG C by cooling
Temperature be down to less than 20 DEG C, water temperature is risen to more than 5 DEG C by heating when water temperature in winter is low, broad application temperature range, reduction
Dependence to environment temperature；
(4) water softening tank or weak brine storage tank need not be set, and equipment and floor space are saved in thin device configuration.
It is described above, only it is preferred embodiment of the present utility model, not makees any formal to the utility model
Limitation, although the utility model is disclosed above with preferred embodiment, but is not limited to the utility model, any ripe
Professional and technical personnel is known, is not being departed from the range of technical solutions of the utility model, when in the technology using the disclosure above
Hold the equivalent embodiment made a little change or be modified to equivalent variations, as long as being without departing from technical solutions of the utility model
Hold, any simple modification, equivalent variations and the modification made according to technical spirit of the present utility model to above example, still
Belong in the range of technical solutions of the utility model.
Claims (10)
1. a kind of sodium hypochlorite generators, it is characterised in that occur including softening hydrophone (1), dissolved salt case (2), sodium hypochlorite
Unit (4) and sodium hypochlorite storage tank (5), the sodium hypochlorite generating unit (4) include ratio dosing pump (41), one-level electrolytic cell
(42) and second electrolyser (43), the outlet of the softening hydrophone (1) by soften waterpipe respectively with the dissolved salt case (2)
Import, the first import of the ratio dosing pump (41) and the import of the second electrolyser (43) connection, the dissolved salt case (2)
Outlet connected by the second import of pipeline and the ratio dosing pump (41), the outlet of the ratio dosing pump (41) passes through
Pipeline is connected with the import of the one-level electrolytic cell (42), outlet and the second electrolyser of the one-level electrolytic cell (42)
(43) import connection, the outlet of the second electrolyser (43) is connected by the import of pipeline and the sodium hypochlorite storage tank (5)
Connect.
2. sodium hypochlorite generators as claimed in claim 1, it is characterised in that the softening waterpipe includes main pipeline
(7), the first branch pipe(tube) (71), the second branch pipe(tube) (72), the 3rd branch pipe(tube) (73) and the 4th branch pipe(tube) (74), the main pipeline
(7) entrance is connected with the outlet of the softening hydrophone (1), and first branch pipe(tube) (71) connects going out for main pipeline (7)
Mouthful with the import of the dissolved salt case (2), second branch pipe(tube) (72) connect the main pipeline (7) outlet and described 3rd
Pipeline (73), the entrance of the 4th branch pipe(tube) (74), the outlet of the 3rd branch pipe(tube) (73) and the ratio dosing pump
(41) the first import connection, the outlet of the 4th branch pipe(tube) (74) is connected with the import of the second electrolyser (43).
3. sodium hypochlorite generators as claimed in claim 2, it is characterised in that second branch pipe(tube) (72) is close to institute
The 3rd branch pipe(tube) (73) is stated with being provided with temperature controller (3), the temperature at the position of the entrance of the 4th branch pipe(tube) (74)
Controller (3) is the integral constant temperature water dispenser of air-cooled cold-hot, and the temperature controlling range of the temperature controller (3) is 5-20 DEG C.
4. sodium hypochlorite generators as claimed in claim 2, it is characterised in that the 3rd branch pipe(tube) (73) and described the
Softening water regulating valve is respectively equipped with four branch pipe(tube)s (74), the softening water regulating valve is used to control to enter the ratio dosing pump
(41) ratio of softened water and the softened water into the second electrolyser (43) is 4:5.
5. sodium hypochlorite generators as claimed in claim 4, it is characterised in that the production fluid of the one-level electrolytic cell (42)
The softening water regulating valve being discharged into the second electrolyser (43), the 4th branch pipe(tube) (74) is additionally operable to control and enters described two
The ratio of production fluid of the softened water of level electrolytic cell (43) with entering the second electrolyser (43) is 1:1.
6. sodium hypochlorite generators as claimed in claim 1, it is characterised in that the ratio dosing pump (41) is waterpower ratio
Example dosing pump, the first import of the ratio dosing pump (41) is hydro powered end.
7. sodium hypochlorite generators as claimed in claim 1, it is characterised in that the dissolved salt case (2) is used to prepare saturation
Salting liquid, the ratio dosing pump (41) is used to control the mixed proportion of saturated salt solution and softened water to be 1:4.
8. sodium hypochlorite generators as claimed in claim 1, it is characterised in that the sodium hypochlorite storage tank (5) is provided with row
Hydrogen blower fan (51) and row's hydrogen mouthful (52), row's hydrogen blower fan (51) are used to dilute the hydrogen in the sodium hypochlorite storage tank (5).
9. sodium hypochlorite generators as claimed in claim 1, it is characterised in that also including sodium hypochlorite dosing pump (6), institute
The outlet that sodium hypochlorite dosing pump (6) is stated with the sodium hypochlorite storage tank (5) is connected.
10. sodium hypochlorite generators as claimed in claim 1, it is characterised in that the charging aperture and spiral shell of the dissolved salt case (2)
Revolve feeder (8) connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720036715.1U CN206599615U (en) | 2017-01-12 | 2017-01-12 | Sodium hypochlorite generators |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720036715.1U CN206599615U (en) | 2017-01-12 | 2017-01-12 | Sodium hypochlorite generators |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206599615U true CN206599615U (en) | 2017-10-31 |
Family
ID=60149957
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| Application Number | Title | Priority Date | Filing Date |
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| CN201720036715.1U Withdrawn - After Issue CN206599615U (en) | 2017-01-12 | 2017-01-12 | Sodium hypochlorite generators |
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Cited By (1)
| 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 |
-
2017
- 2017-01-12 CN CN201720036715.1U patent/CN206599615U/en not_active Withdrawn - After Issue
Cited By (1)
| 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 |
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Granted publication date: 20171031 Effective date of abandoning: 20180925 |