CN208485963U - It is a kind of for producing the electrolytic cell assembly of javelle water - Google Patents
It is a kind of for producing the electrolytic cell assembly of javelle water Download PDFInfo
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- CN208485963U CN208485963U CN201820975425.8U CN201820975425U CN208485963U CN 208485963 U CN208485963 U CN 208485963U CN 201820975425 U CN201820975425 U CN 201820975425U CN 208485963 U CN208485963 U CN 208485963U
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Abstract
The utility model discloses a kind of for producing the electrolytic cell assembly of javelle water, is equipped with secondary dilution device, simultaneous implantation secondary dilution water during weak brine is electrolysed in a cell；Secondary dilution water is not only played the role of further diluting salt water by injection electrolysis groove body, and there is cooling effect to have saved additional energy consumption so that electrolytic cell assembly does not need still further independently to set up cooling device；Simultaneously as weak brine needs to carry out secondary dilution, so the concentration of the weak brine of just injection electrolysis groove body can be greater than 3.5%, so that electrolytic efficiency is higher；The salt consumption for producing every kilogram of effective chlorine can be 3.2 kilograms, and power consumption can be 4.0kwh；The cost and energy consumption for setting up cooling system are not only saved, and salt consumption is low, power consumption is low；Reduce the technical-economic index of hypochlorite generator.
Description
Technical field
The utility model belongs to water body disinfection equipment technical field, in particular to a kind of for producing javelle water
Electrolytic cell assembly.
Background technique
2003 so far, and the disinfections such as drinking water, sanitary sewage, medical waste water are concerned, and traditional disinfection way has throwing
Liquid feeding chlorine, chlorine dioxide etc..In recent years, country payes attention to the safety problem of hazardous chemical further, and traditional sterilization process is gradually
Replaced by novel hypochlorite generator.
It is in the prior art for producing the electrolytic cell assembly (as hypochlorite generator) of javelle water, be
First by saturated brine and dilution water, (dilution water in the application, tap water or other working conditions that meet after referring to softening are used
In the water of dilution salt water) mixed diluting, it forms concentration and is filled in electrolytic cell in the weak brine of 2.5%-3.5%, then by weak brine
It is electrolysed, the salt consumption for producing every kilogram of effective chlorine is 4.0 kilograms, direct current consumption 4.5kWh, and electrolytic efficiency is lower, salt consumes
It is high with power consumption, but also need that dedicated cooling system is arranged for electrolytic cell assembly and cool down, production cost is more high；
Our company has been devoted to research and development hypochlorite generator's corollary apparatus, and it is raw to reduce salt consumption, power consumption of hypochlorite generator etc.
Produce cost.
Utility model content
In order to overcome the shortcomings of the prior art, the utility model provides a kind of for producing javelle water
Electrolytic cell assembly, without in addition setting up cooling system, electrolytic efficiency is high, reduces salt consumption and energy consumption.
The utility model is to achieve the goal, and used technical solution is:
It is a kind of that for producing the electrolytic cell assembly of javelle water, the electrolytic cell assembly includes electrolysis groove body,
The secondary dilution device for carrying out multi-point injection dilution water into electrolysis groove body is equipped in the electrolysis groove body, it is described
Secondary dilution device connection the first dilution water pipe；One end of the electrolysis groove body is equipped with salt water inlet, and the other end is equipped with
Liquid mouth；The salt water inlet is communicated with weak brine pipeline.Weak brine pipeline, which is used to be passed through concentration into electrolysis groove body, to be greater than
3.5% weak brine.
Preferably, the weak brine pipeline has been respectively communicated with saturated common salt water pipe and second far from one end of salt water inlet
Dilute water pipe.Saturated salt solution and the second dilution water, which cross, be mixed to form a certain proportion of dilution salt water, we pass through control
Make the concentration of the dilution salt water of the i.e. controllable injection electrolytic cell of flow of each pipeline.
Preferably, the saturated common salt water pipe, the first dilution water pipe, second, which dilute, is equipped with spinner flowmeter on water pipe；
Shut-off valve is equipped on the first dilution water pipe and the second dilution water pipe.Convenient for control flow and concentration.
Preferably, the ratio between the water flow of the first dilution water pipe and the second dilution water pipe is 10:1.Electrolytic efficiency is higher,
Salt consumption and energy consumption are lower.
The beneficial effects of the utility model are: the utility model discloses a kind of for producing the electricity of javelle water
Slot device is solved, is equipped with secondary dilution device, simultaneous implantation secondary dilution water during weak brine is electrolysed in a cell；
Secondary dilution water is not only played the role of further diluting salt water by injection electrolysis groove body, and has cooling effect, makes
It obtains electrolytic cell assembly not needing still further independently to set up cooling device, has saved additional energy consumption；Simultaneously as weak brine needs
Secondary dilution is carried out, so the concentration of the weak brine of just injection electrolysis groove body can be greater than 3.5%, so that electrolytic efficiency
It is higher；The salt consumption for producing every kilogram of effective chlorine can be 3.2 kilograms, and power consumption can be 4.0kwh；Not only saved set up it is cold
But the cost and energy consumption of system, and salt consumption is low, power consumption is low；Reduce the technical-economic index of hypochlorite generator.
Detailed description of the invention
The present invention will be further described with reference to the accompanying drawings and examples.
Fig. 1 is described in the utility model a kind of for producing the structural representation of the electrolytic cell assembly of javelle water
Figure.
Specific embodiment
The utility model is described in further detail presently in connection with attached drawing.These attached drawings are simplified schematic diagram,
Only illustrate the basic structure of the utility model in a schematic way, therefore it only shows composition related with the utility model.
As shown in Figure 1 is a kind of for producing the electrolytic cell assembly of javelle water, and the electrolytic cell assembly includes
It is electrolysed groove body 1, two for carrying out multi-point injection dilution water into electrolysis groove body 1 are equipped in the electrolysis groove body 1
Secondary dilution device 2, first dilution of the connection of secondary dilution device 2 water pipe 3；Secondary dilution device 2 is one in the present embodiment
Pipeline, one end connection the first dilution water pipe 3 of the pipeline, is intervally distributed with several water outlet openings on the side wall of the pipeline etc.,
These water outlet openings are the water filling point of dilution water.In other embodiments, it can also will be filled the water using other settings
Point carries out distribution, for example the first dilution tube 3 is connected more water distributors, fill the water in different water distribution points etc..
In the present embodiment, one end of electrolysis groove body 1 is equipped with salt water inlet, and the other end is equipped with liquid outlet 4；Liquid outlet 4
For exporting the electrolyte after being electrolysed, i.e. javelle water；The salt water inlet is communicated with weak brine pipeline 5.It is dilute
Brine pipeline 5 is used to be passed through the weak brine that concentration is greater than 3.5% into electrolytic cell.
In the present embodiment, the weak brine pipeline 5 has been respectively communicated with saturated common salt water pipe far from one end of salt water inlet
51 and second dilute water pipe 52.Saturated salt solution crosses with the second dilution water be mixed to form a certain proportion of concentration and is greater than
3.5% dilution salt water, dilution salt water passes through again to be electrolysed in the entrance electrolysis groove body of weak brine pipeline 5；We pass through control
The flow of each pipeline is the concentration of the dilution salt water of controllable injection electrolytic cell.
In the present embodiment, the saturated common salt water pipe 51, first, which dilutes water pipe 3, second and dilutes to be equipped on water pipe 52, to be turned
Subflow meter 6；Shut-off valve 7 is equipped on the first dilution water pipe 3 and the second dilution water pipe 52.Convenient for control flow and dilution
The concentration of salt water.In automated production, these spinner flowmeters 6 and shut-off valve 7 can also be electrically connected to the control system, from
And realize automation manipulation.
In the present embodiment, the ratio between the water flow of the first dilution water pipe 3 and the second dilution water pipe 52 is 10:1.Second is dilute
The water and saturated brine mixing, saturated brine released in water pipe 52 carry out first time dilution, dense through diluted saturated brine for the first time
Degree is greater than or much larger than 3.5%, then injects in electrolysis groove body 1 through weak brine pipeline 5, the water in the first dilution water pipe 3, warp
Secondary dilution device mix with the weak brine after diluting in electrolysis groove body 1 into first time, carries out second dilution；
In this course, first weak brine of the concentration greater than 3.5% is filled in electrolysis groove body 1, in these weak brines
Simultaneous implantation secondary dilution water during being electrolysed；Secondary dilution water is not only played further dilute by injection electrolysis groove body
The effect of salt water is released, and there is cooling effect, so that electrolytic cell assembly does not need still further independently to set up cooling device, is saved
Additional energy consumption；Simultaneously as the concentration of weak brine injection electrolytic cell is greater than 3.5%, so electrolytic efficiency is higher；Production is every
The salt consumption of kilogram effective chlorine can be 3.2 kilograms, and power consumption can be 4.0kwh；Salt consumption is low, power consumption is low, reduces sodium hypochlorite
The technical-economic index of generator.
It is enlightenment, through the above description, related work people with the above-mentioned desirable embodiment according to the utility model
Member can carry out various changes and amendments in the range of without departing from this item utility model technical idea completely.This item is real
It is not limited to the contents of the specification with novel technical scope, it is necessary to its technology is determined according to scope of the claims
Property range.
Claims (4)
1. a kind of for producing the electrolytic cell assembly of javelle water, it is characterised in that: the electrolytic cell assembly includes electricity
Groove body is solved, the secondary dilution for carrying out multi-point injection dilution water into electrolysis groove body is equipped in the electrolysis groove body
Device, the first dilution of secondary dilution device connection water pipe；One end of the electrolysis groove body is equipped with salt water inlet, another
End is equipped with liquid outlet；The salt water inlet is communicated with weak brine pipeline.
2. according to claim 1 a kind of for producing the electrolytic cell assembly of javelle water, it is characterised in that: institute
It states weak brine pipeline and has been respectively communicated with saturated common salt water pipe and the second dilution water pipe far from one end of salt water inlet.
3. according to claim 2 a kind of for producing the electrolytic cell assembly of javelle water, it is characterised in that: institute
State saturated common salt water pipe, first dilution water pipe, second dilution water pipe on be equipped with spinner flowmeter；It is described first dilution water pipe and
Shut-off valve is equipped on second dilution water pipe.
4. according to claim 2 a kind of for producing the electrolytic cell assembly of javelle water, it is characterised in that: institute
The ratio between water flow of the first dilution water pipe and the second dilution water pipe is stated as 10:1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820975425.8U CN208485963U (en) | 2018-06-22 | 2018-06-22 | It is a kind of for producing the electrolytic cell assembly of javelle water |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820975425.8U CN208485963U (en) | 2018-06-22 | 2018-06-22 | It is a kind of for producing the electrolytic cell assembly of javelle water |
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| CN208485963U true CN208485963U (en) | 2019-02-12 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108468064A (en) * | 2018-06-22 | 2018-08-31 | 广州新奥环境技术有限公司 | A kind of electrolysis method for production and its electrolytic cell assembly of javelle water |
-
2018
- 2018-06-22 CN CN201820975425.8U patent/CN208485963U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108468064A (en) * | 2018-06-22 | 2018-08-31 | 广州新奥环境技术有限公司 | A kind of electrolysis method for production and its electrolytic cell assembly of javelle water |
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Legal Events
| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: An electrolytic cell device for producing sodium hypochlorite disinfectant Effective date of registration: 20201021 Granted publication date: 20190212 Pledgee: China Co. truction Bank Corp Guangzhou economic and Technological Development Zone sub branch Pledgor: NEAO GUANGZHOU ENVIRONMENTAL TECHNOLOGY Co.,Ltd. Registration number: Y2020440000331 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |