CN209383861U - Sodium hypochlorite generating system - Google Patents
Sodium hypochlorite generating system Download PDFInfo
- Publication number
- CN209383861U CN209383861U CN201822148538.3U CN201822148538U CN209383861U CN 209383861 U CN209383861 U CN 209383861U CN 201822148538 U CN201822148538 U CN 201822148538U CN 209383861 U CN209383861 U CN 209383861U
- Authority
- CN
- China
- Prior art keywords
- sodium hypochlorite
- generating system
- water feeder
- salt water
- dilution proportion
- 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
- 239000005708 Sodium hypochlorite Substances 0.000 title claims abstract description 66
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 title claims abstract description 64
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 101
- 239000007788 liquid Substances 0.000 claims abstract description 72
- 150000003839 salts Chemical class 0.000 claims abstract description 69
- 239000012895 dilution Substances 0.000 claims abstract description 37
- 238000010790 dilution Methods 0.000 claims abstract description 37
- 238000001514 detection method Methods 0.000 claims abstract description 19
- 238000003860 storage Methods 0.000 claims description 33
- 239000008234 soft water Substances 0.000 claims description 23
- 230000001105 regulatory effect Effects 0.000 claims description 18
- 238000005868 electrolysis reaction Methods 0.000 claims description 12
- 239000013049 sediment Substances 0.000 claims description 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 8
- 239000001257 hydrogen Substances 0.000 claims description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims description 8
- 230000001276 controlling effect Effects 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 15
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical class O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 15
- 239000012267 brine Substances 0.000 description 14
- 239000000243 solution Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 239000008399 tap water Substances 0.000 description 3
- 235000020679 tap water Nutrition 0.000 description 3
- BZSXEZOLBIJVQK-UHFFFAOYSA-N 2-methylsulfonylbenzoic acid Chemical compound CS(=O)(=O)C1=CC=CC=C1C(O)=O BZSXEZOLBIJVQK-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 230000009897 systematic effect Effects 0.000 description 1
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model provides a kind of sodium hypochlorite generating system, it is related to sodium hypochlorite manufacturing technology field, sodium hypochlorite generating system provided by the utility model includes salt water feeder, softening water feeder and dilution proportion pump and controller, in which: salt water feeder and softening water feeder are connected to dilution proportion pump respectively；The liquid outlet of dilution proportion pump is equipped with concentration detection apparatus, controller is connect with concentration detection apparatus and salt water feeder respectively, and controller is used to receive the flow of the mixed liquid concentration information that concentration detection apparatus detects and the liquid outlet salt water for controlling salt water feeder.Sodium hypochlorite generating system provided by the utility model can the concentration real-time perfoming to salt water detect and feed back, avoid the concentration of mixed liquor from being widely varied.
Description
Technical field
The utility model relates to sodium hypochlorite manufacturing technology fields, more particularly, to a kind of sodium hypochlorite generating system.
Background technique
Sodium hypochlorite is strong oxidizer and disinfectant, it is dilute molten derived from Nacl or seawater inexpensive extensively by taking
Liquid occurs through diaphragm-free electrolysis.
But in existing sodium hypochlorite generating system, as long as the flow of softened water or the flow of saturated brine change
Become, the concentration of the mixed liquor of the online compounding system discharge of weak brine will change, and influence the production of sodium hypochlorite.
Therefore, how to provide a kind of sodium hypochlorite generating system that the concentration for avoiding mixed liquor is widely varied is this field
One of technical staff's technical problem to be solved.
Utility model content
It, being capable of concentration real-time perfoming to salt water the purpose of this utility model is to provide a kind of sodium hypochlorite generating system
It detects and feeds back, the concentration of mixed liquor is avoided to be widely varied.
To achieve the above object, the utility model the following technical schemes are provided:
The utility model provides a kind of sodium hypochlorite generating system, including salt water feeder, softening water feeder and
Dilution proportion pump and controller, in which:
The salt water feeder and the softening water feeder are connected to dilution proportion pump respectively；
The liquid outlet of the dilution proportion pump is equipped with concentration detection apparatus, and the controller is filled with the Concentration Testing respectively
It sets and is connected with the salt water feeder, the controller is for receiving the mixed liquid concentration that the concentration detection apparatus detects
Information and control the salt water feeder liquid outlet salt water flow.
Further, the salt water feeder includes dissolved salt case and first flow regulating valve, and the first flow is adjusted
Valve is between the dissolved salt case and dilution proportion pump, and is connect with the controller.
Further, the first sediment discharge pipe is additionally provided between the dissolved salt case and the first flow regulating valve.
Further, the dissolved salt case includes cabinet, soft water inlet valve and liquid-level switch component, and the soft water inlet valve is set
In the water inlet of the cabinet, the liquid-level switch component is connect with the soft water inlet valve, intracorporal for controlling the case
Water level.
Further, second flow regulating valve is equipped between the softening water feeder and dilution proportion pump.
It further, further include the electrolysis unit being connected to the liquid outlet of dilution proportion pump.
It further, further include the sodium hypochlorite storage device being connected to the liquid outlet of the electrolysis unit.
Further, the sodium hypochlorite storage device includes storage tank, on the storage tank setting tool have row hydrogen mouth and time
Sodium chlorate discharge line, the sodium hypochlorite discharge line are equipped with third flow control valve.
Further, the bottom of the storage tank is equipped with the second sediment being connected to the softening water feeder and is discharged
Pipe.
It further, further include the alarm being connect with the controller.
Sodium hypochlorite generating system provided by the utility model can generate it is following the utility model has the advantages that
When stating sodium hypochlorite generating system in use, salt water feeder provides strong brine for dilution proportion pump, with this
Soften water feeder simultaneously and provide softened water for dilution proportion pump, strong brine is merged in dilution proportion pump with softened water
Form mixed liquor, i.e., certain density saline solution.When concentration detection apparatus detect saline solution concentration it is higher when, control
Device can control the flow that salt water feeder reduces liquid outlet salt water, to reduce the concentration of saline solution；When Concentration Testing fills
It sets when detecting that the concentration of saline solution is lower, controller can control the flow that salt water feeder increases liquid outlet salt water,
To increase the concentration of saline solution.
For compared with the existing technology, sodium hypochlorite generating system provided by the utility model can concentration to salt water it is real
Shi Jinhang is detected and is fed back, and be ensure that the concentration of dilution proportion pump output salt water, is avoided the flow of softened water or the stream of salt water
When amount changes, the concentration generation of dilution proportion pump output salt water significantly changes, and influences the production of sodium hypochlorite.
Detailed description of the invention
It, below will be right in order to illustrate more clearly of specific embodiment of the present invention or technical solution in the prior art
Specific embodiment or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, it is described below
In attached drawing be that some embodiments of the utility model are not paying creativeness for those of ordinary skill in the art
Under the premise of labour, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is a kind of process flow diagram of sodium hypochlorite generating system provided by the embodiment of the utility model.
Icon: 1- salt water feeder；11- dissolved salt case；111- cabinet；112- soft water inlet valve；113- liquid level is opened
Close component；12- first flow regulating valve；13- the first sediment discharge pipe；2- softens water feeder；3- dilution proportion
Pump；4- controller；5- concentration detection apparatus；6- second flow regulating valve；7- electrolysis unit；8- sodium hypochlorite storage dress
It sets；81- storage tank；811- arranges hydrogen mouth；812- sodium hypochlorite discharge line；9- third flow control valve；10- second is heavy
Starch discharge pipe.
Specific embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally
Field those of ordinary skill every other embodiment obtained without making creative work belongs to practical
Novel protected range.
It is in the description of the present invention, it should be noted that term " center ", "upper", "lower", "left", "right", " perpendicular
Directly ", the orientation or positional relationship of the instructions such as "horizontal", "inner", "outside" is to be based on the orientation or positional relationship shown in the drawings, and is only
For ease of description the utility model and simplify description, rather than the device or element of indication or suggestion meaning must have it is specific
Orientation, be constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.In addition, term " the
One ", " second ", " third " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection；It can be mechanical connection, be also possible to be electrically connected；Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, above-mentioned art can be understood with concrete condition
The concrete meaning of language in the present invention.
Specific embodiment of the present utility model is described in detail below in conjunction with attached drawing.It should be understood that herein
Described specific embodiment is only used for describing and explaining the present invention, and is not intended to limit the utility model.
Fig. 1 is a kind of process flow diagram of sodium hypochlorite generating system provided by the embodiment of the utility model.
The purpose of the present embodiment is that a kind of sodium hypochlorite generating system is provided, as shown in Figure 1, including salt water feeder
1, soften water feeder 2 and dilution proportion pump 3 and controller 4, in which:
Salt water feeder 1 and softening water feeder 2 are connected to dilution proportion pump 3 respectively；
Dilution proportion pump 3 liquid outlet be equipped with concentration detection apparatus 5, controller 4 respectively with concentration detection apparatus 5 and salt water
Feedway 1 connects, and controller 4 is used to receive the mixed liquid concentration information that concentration detection apparatus 5 detects and controls salt water confession
To the flow of the liquid outlet salt water of device 1.
When stating sodium hypochlorite generating system in use, salt water feeder provides strong brine for dilution proportion pump, with this
Soften water feeder simultaneously and provide softened water for dilution proportion pump, strong brine is merged in dilution proportion pump with softened water
Form mixed liquor, i.e., certain density saline solution.When concentration detection apparatus detect saline solution concentration it is higher when, control
Device can control the flow that salt water feeder reduces liquid outlet salt water, to reduce the concentration of saline solution；When Concentration Testing fills
It sets when detecting that the concentration of saline solution is lower, controller can control the flow that salt water feeder increases liquid outlet salt water,
To increase the concentration of saline solution.
For compared with the existing technology, sodium hypochlorite generating system provided by the utility model can concentration to salt water it is real
Shi Jinhang is detected and is fed back, and be ensure that the concentration of dilution proportion pump output salt water, is avoided the flow of softened water or the stream of salt water
When amount changes, the concentration generation of dilution proportion pump output salt water significantly changes, and influences the production of sodium hypochlorite.
Specifically, controller 4 is electrically connected with concentration detection apparatus 5 and salt water feeder 1 respectively.
Specifically, controller 4 can be preset with a threshold value, when the numerical value of saline solution concentration information is greater than the threshold value
When, controller 4 controls alarm and alarms.
In some embodiments, above-mentioned sodium hypochlorite generating system further includes the alarm connecting with controller 4.Work as concentration
When detection device 5 detects that the concentration of saline solution is higher, controller 4 can control alarm and alarm.
In some embodiments, as shown in Figure 1, salt water feeder 1 includes dissolved salt case 11 and first flow regulating valve 12,
First flow regulating valve 12 is between dissolved salt case 11 and dilution proportion pump 3, and is connect with controller 4.Specifically, first flow
Regulating valve 12 can be electrically connected with controller 4.
Dissolved salt case 11 is connect with water supply pipe, internal to have salt particle, and the tap water in water supply pipe enters molten
Salt after in salt box 11 and in dissolved salt case 11 is fused into strong brine, and strong brine enters dilution proportion by first flow regulating valve 12
Pump 3.When the saline solution concentration that concentration detection apparatus 5 detects that dilution proportion pump 3 flows out is higher, controller 4 is directly controlled
First flow regulating valve 12 reduces the flow of strong brine output；When concentration detection apparatus 5 detects the salt of 3 outflow of dilution proportion pump
When concentration of aqueous solution is compared with height, controller 4 directly controls the flow that first flow regulating valve 12 increases strong brine output.
Wherein, controller 4 can be MCS-51 single-chip microcontroller, and concentration detection apparatus 5 can be using model SA-287's
Brine strength tester.
In some embodiments, as shown in Figure 1, being additionally provided between dissolved salt case 11 and first flow regulating valve 12 for being discharged
First sediment discharge pipe 13 of the sediment in dissolved salt case 11.Specifically, the first sediment discharge pipe 13 is equipped with third stream
Adjustable valve.Third flow control valve can be closed when using above-mentioned sodium hypochlorite generating system；When needing to be discharged dissolved salt case
When sediment in 11, third flow control valve can be opened.
Specifically, in order to guarantee that the liquid in dissolved salt case 11 is no more than the highest liquid level of dissolved salt case 11, as shown in Figure 1, molten
Salt box 11 include cabinet 111, soft water inlet valve 112 and liquid-level switch component 113, soft water inlet valve 112 be set to cabinet 111 into
The mouth of a river, liquid-level switch component 113 are connect with soft water inlet valve 112, for controlling the water level in cabinet 111.
Water softener is additionally provided between soft water inlet valve 112 and water supply pipe, water softener can remove the calcium in tap water
Magnesium ion is to achieve the purpose that softening of water.Tap water in water supply pipe enters soft water inlet valve 112 after passing through water softener,
Enter cabinet 111 by soft water inlet valve 112, is merged with the salt particle in cabinet 111.When strong brine in cabinet 111
When liquid level reaches liquid-level switch 113 present position of component, liquid-level switch component 113 control soft water inlet valve 112 reduce soft water into
Enter the flow of cabinet 111, or directly control the closing of soft water inlet valve 112, until the liquid level of strong brine is lower than liquid in cabinet 111
After bit switch component 113, control soft water inlet valve 112 restores normally open state.
Specifically, liquid-level switch component 113 may include the first high level switch and the first low liquid level switch, the first high liquid
The height of bit switch is switched higher than the first low liquid level.It is corresponding, it is opened when the liquid level of strong brine in cabinet 111 reaches the first low liquid level
When closing present position, the first low liquid level switch can control soft water inlet valve 112 and reduce the flow that soft water enters cabinet 111；When
When the liquid level of strong brine reaches the first high level switch present position in cabinet 111, the first high level switch can be directly controlled
Soft water inlet valve 112 is closed.
More specifically, the first high level switch and the first low liquid level switch include the first liquid level detector and controller,
First liquid level detector is used to detect whether liquid level to reach height corresponding to it, and controller is for receiving the first liquid level detector
The liquid level information of sending and the working condition for controlling soft water inlet valve 112.Wherein, controller can be MCS-51 single-chip microcontroller.
In some embodiments, soften and be equipped with second flow regulating valve 6 between water feeder 2 and dilution proportion pump 3.?
In use process, operating personnel can manually adjust the stream into softened water in dilution proportion pump 3 by second flow regulating valve 6
Amount.
On the basis of the above embodiments, softening water feeder 2 is connect with the liquid outlet of water softener, to receive water softener
The soft water of liquid outlet discharge.Specifically, soften and be equipped with the 4th flow control valve, operation people between water feeder 2 and water softener
Member can adjust the flow for entering softened water in softening water feeder 2 by the 4th flow control valve.
Specifically, softening water feeder 2 may include softened water tank, can be equipped with and the 4th flow control valve in softened water tank
Second liquid level detector of electrical connection, the second liquid level detector may include float, and float is according to the variation of water level in softened water tank
It floats up and down, when the height of float reaches the maximum water level of softened water tank, the second liquid level detector controls the 4th flow
Regulating valve is closed, and avoids soft water in softened water tank excessive.
In order to enable above-mentioned sodium hypochlorite generating system can be to the systematic production of sodium hypochlorite, as shown in Figure 1, above-mentioned
Sodium hypochlorite generating system further includes the electrolysis unit 7 being connected to the liquid outlet of dilution proportion pump 3.
Electrolysis unit 7 includes electrolytic tube of generator for sodium hypochlorite, and the saline solution of 3 output of dilution proportion pump is directly entered secondary
Sodium chlorate generator electrolysis tube is electrolysed.
On the basis of the above embodiments, above-mentioned sodium hypochlorite generating system further includes connecting with the liquid outlet of electrolysis unit 7
Logical sodium hypochlorite storage device 8.The 5th flow tune is equipped between sodium hypochlorite storage device 8 and the liquid outlet of electrolysis unit 7
Save valve.
The sodium hypochlorite that electrolysis unit 7 generates after being electrolysed is directly entered sodium hypochlorite storage device 8, sodium hypochlorite storage dress
8 pairs of sodium hypochlorite are set store and transport sodium hypochlorite to next station.
In some embodiments, as shown in Figure 1, sodium hypochlorite storage device 8 includes storage tank 81, setting tool on storage tank 81
There are row's hydrogen mouth 811 and sodium hypochlorite discharge line 812, sodium hypochlorite discharge line 812 is equipped with third flow control valve 9.
Hydrogen can be generated when being electrolysed due to salt water, this allows for there is a certain amount of hydrogen in liquor natrii hypochloritis
Gas, row's hydrogen mouth 811 on storage tank 81 are used to for the hydrogen of this part being discharged.Third stream on sodium hypochlorite discharge line 812
Adjustable valve 9 can be used for controlling the discharge rate of sodium hypochlorite.
At least one liquid-level switch can be equipped on storage tank 81 specifically can be equipped with one, two on storage tank 81
A, three, the liquid-level switches such as four.In at least one embodiment, liquid-level switch there are three being set on storage tank 81.
Set on storage tank 81 there are three being specifically described for liquid-level switch, three liquid-level switches can be respectively the
Two high level switches, middle liquid-level switch and the second low liquid level switch.
When the liquid level of the liquor natrii hypochloritis in storage tank 81 reaches the second low liquid level switch present position, the second low liquid
Bit switch can control the 5th flow control valve and reduce the flow that sodium hypochlorite enters storage tank 81 by a small margin；
When the liquid level of the liquor natrii hypochloritis in storage tank 81 reaches middle liquid-level switch present position, middle liquid-level switch can
Reduce the flow that sodium hypochlorite enters storage tank 81 to control amplitude in the 5th flow control valve；
When the liquid level of the liquor natrii hypochloritis in storage tank 81 reaches the second high level switch present position, the second high liquid
Bit switch can control the 5th flow control valve and significantly reduce the flow that sodium hypochlorite enters storage tank 81.
In some embodiments, as shown in Figure 1, in order to can be smoothly when not using above-mentioned sodium hypochlorite generating system
Storage tank 81 is discharged and softens the precipitated impurities in water feeder 2, the bottom of storage tank 81 is equipped with to supply with softened water and fill
Set the second sediment discharge pipe 10 of 2 connections, the precipitated impurities in storage tank 81 and softening water feeder 2 can be by the
Two sediment discharge pipes 10 drain into the external world jointly.
Finally, it should be noted that the above various embodiments is only to illustrate the technical solution of the utility model, rather than it is limited
System；Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should
Understand: it is still possible to modify the technical solutions described in the foregoing embodiments, or to some or all of
Technical characteristic is equivalently replaced；And these are modified or replaceed, it does not separate the essence of the corresponding technical solution, and this is practical new
The range of each embodiment technical solution of type.
Claims (10)
1. a kind of sodium hypochlorite generating system, which is characterized in that including salt water feeder (1), softening water feeder (2) and
Dilution proportion pumps (3) and controller (4), in which:
The salt water feeder (1) and the softening water feeder (2) are connected to dilution proportion pump (3) respectively；
The liquid outlet of dilution proportion pump (3) is equipped with concentration detection apparatus (5), the controller (4) respectively with the concentration
Detection device (5) and the salt water feeder (1) connection, the controller (4) is for receiving the concentration detection apparatus (5)
The flow of the mixed liquid concentration information that detects and the liquid outlet salt water for controlling the salt water feeder (1).
2. sodium hypochlorite generating system according to claim 1, which is characterized in that the salt water feeder (1) includes
Dissolved salt case (11) and first flow regulating valve (12), the first flow regulating valve (12) be in the dissolved salt case (11) with it is described
Dilution proportion pumps between (3), and connect with the controller (4).
3. sodium hypochlorite generating system according to claim 2, which is characterized in that the dissolved salt case (11) and described first
The first sediment discharge pipe (13) is additionally provided between flow control valve (12).
4. sodium hypochlorite generating system according to claim 2, which is characterized in that the dissolved salt case (11) includes cabinet
(111), soft water inlet valve (112) and liquid-level switch component (113), the soft water inlet valve (112) are set to the cabinet (111)
Water inlet, the liquid-level switch component (113) connect with the soft water inlet valve (112), for controlling the cabinet (111)
Interior water level.
5. sodium hypochlorite generating system according to claim 1, which is characterized in that the softening water feeder (2) with
Second flow regulating valve (6) are equipped between the dilution proportion pump (3).
6. sodium hypochlorite generating system according to claim 1, which is characterized in that further include being pumped with the dilution proportion
(3) electrolysis unit (7) of liquid outlet connection.
7. sodium hypochlorite generating system according to claim 6, which is characterized in that further include and the electrolysis unit (7)
Liquid outlet connection sodium hypochlorite storage device (8).
8. sodium hypochlorite generating system according to claim 7, which is characterized in that the sodium hypochlorite storage device (8)
Including storage tank (81), setting tool has row hydrogen mouth (811) and sodium hypochlorite discharge line (812) on the storage tank (81), described
Sodium hypochlorite discharge line (812) is equipped with third flow control valve (9).
9. sodium hypochlorite generating system according to claim 8, which is characterized in that the bottom of the storage tank (81) is equipped with
The second sediment discharge pipe (10) being connected to softening water feeder (2).
10. -9 described in any item sodium hypochlorite generating systems according to claim 1, which is characterized in that further include and the control
The alarm of device (4) connection processed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822148538.3U CN209383861U (en) | 2018-12-20 | 2018-12-20 | Sodium hypochlorite generating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822148538.3U CN209383861U (en) | 2018-12-20 | 2018-12-20 | Sodium hypochlorite generating system |
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| Publication Number | Publication Date |
|---|---|
| CN209383861U true CN209383861U (en) | 2019-09-13 |
Family
ID=67873106
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822148538.3U Expired - Fee Related CN209383861U (en) | 2018-12-20 | 2018-12-20 | Sodium hypochlorite generating system |
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| Country | Link |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110904466A (en) * | 2019-11-12 | 2020-03-24 | 江苏乾宝生物科技有限公司 | Electrolytic sodium hypochlorite generator system and operation method |
| CN111517425A (en) * | 2020-05-22 | 2020-08-11 | 广东新洁生物科技有限公司 | Hypochlorous acid disinfectant fluid intelligent manufacturing application system |
| CN111876791A (en) * | 2020-08-04 | 2020-11-03 | 湖南匡楚科技有限公司 | Control method for preparing hypochlorous acid water |
| CN112723503A (en) * | 2021-01-25 | 2021-04-30 | 青岛双瑞海洋环境工程股份有限公司 | Tap water disinfection system |
| CN113186551A (en) * | 2021-05-08 | 2021-07-30 | 潍坊思源环保设备有限公司 | Sodium hypochlorite generator and production method thereof |
-
2018
- 2018-12-20 CN CN201822148538.3U patent/CN209383861U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110904466A (en) * | 2019-11-12 | 2020-03-24 | 江苏乾宝生物科技有限公司 | Electrolytic sodium hypochlorite generator system and operation method |
| CN111517425A (en) * | 2020-05-22 | 2020-08-11 | 广东新洁生物科技有限公司 | Hypochlorous acid disinfectant fluid intelligent manufacturing application system |
| CN111876791A (en) * | 2020-08-04 | 2020-11-03 | 湖南匡楚科技有限公司 | Control method for preparing hypochlorous acid water |
| CN112723503A (en) * | 2021-01-25 | 2021-04-30 | 青岛双瑞海洋环境工程股份有限公司 | Tap water disinfection system |
| CN113186551A (en) * | 2021-05-08 | 2021-07-30 | 潍坊思源环保设备有限公司 | Sodium hypochlorite generator and production method thereof |
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