CN206352062U - A kind of water treatment facilities - Google Patents
A kind of water treatment facilities Download PDFInfo
- Publication number
- CN206352062U CN206352062U CN201621230844.6U CN201621230844U CN206352062U CN 206352062 U CN206352062 U CN 206352062U CN 201621230844 U CN201621230844 U CN 201621230844U CN 206352062 U CN206352062 U CN 206352062U
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- China
- Prior art keywords
- water
- tank
- collection
- treatment facilities
- water treatment
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Abstract
The utility model provides a kind of water treatment facilities, it is characterised in that including：Tank, the tank has the exterior contour of pyramid tetrapyamid shape and the internal cavities of pyramid tetrapyamid shape, the conical top of tank passes in and out in the opening of the tank, the internal cavities of tank provided with permission water and is filled with ceramic packing.The utility model further relates to a kind of electrolysis water treatment facilities including the water treatment facilities, wherein the water treatment facilities activated water and can improve the effect of water electrolysis.
Description
Technical field
The utility model is related to a kind of water treatment facilities, especially a kind of water treatment facilities for activated water.
Background technology
As the improvement of people's living standards, requirement to water quality also more and more higher.Light water is become into active water, can be made
The penetration of water, extension, dissolving power, metabolism power enhancing, and produce water conservation film.But work of the existing water treatment facilities to water
Propertyization is not enough, it is impossible to meet demand of the people to active water.Therefore there is still a need for the improved water treatment facilities for activated water.
The content of the invention
To solve problems of the prior art, the technical solution of the utility model is：
1st, a kind of water treatment facilities, it is characterised in that including：Tank, the tank has pyramid four
The exterior contour of pyramid-shaped and the internal cavities of pyramid tetrapyamid shape, the conical top of the tank is provided with permission water
Pass in and out and ceramic packing is filled with the opening of the tank, the internal cavities of the tank.
2nd, according to the water treatment facilities of technical scheme 1, it is characterised in that the bottom surface of the exterior contour of the tank with
The angle of side is 52 ± 2 degree, and the ratio on hypotenuse and base is 0.95-0.97；The bottom surface of the internal cavities of the tank
Angle with side is also 52 ± 2 degree, and the ratio on hypotenuse and base is 0.95-0.97；The side wall thickness of the tank is
The 0.1-2% of exterior contour base length.
3rd, according to any one of technical scheme 1-2 water treatment facilities, it is characterised in that the ceramic packing is spherical pottery
Porcelain filling or pyramid tetrapyamid shape ceramic packing.
4th, according to the water treatment facilities of technical scheme 3, it is characterised in that the pyramid tetrapyamid shape ceramic packing is
Solid, the angle of bottom surface and side is 52 ± 2 degree, and the ratio on hypotenuse and base is 0.95-0.97；Base length is 0.5-
0.8 centimetre.
5th, a kind of electrolysis wetting system, it is characterised in that including：According to technical scheme 1-4 any one water treatment facilities,
Electrolytic water device and power supply；Wherein, the electrolytic water device further comprise water funnel, the collection oxygen pipe for collecting oxygen and
Collection hydrogen pipe for collecting hydrogen；The bottom of the water funnel is connected with the lower flow of collection oxygen pipe and collection hydrogen pipe, for inciting somebody to action
The water injection collection oxygen pipe and the collection hydrogen pipe in water funnel；The bottom of the collection hydrogen pipe is provided with the positive pole with the power supply
The negative electrode of electrical connection, the bottom of the collection oxygen pipe is provided with the anode electrically connected with the negative pole of the power supply；Under the collection hydrogen pipe
Portion and the bottom of the collection oxygen pipe and the open fluid communication of the tank of the water treatment facilities, so as to the water storage
The water turnover collection hydrogen pipe and the collection oxygen pipe in container.
Tank and ceramic packing of the present utility model including the activity selected from following at least one above composition by making pottery
Porcelain is made：15% far-infrared powder, 5% negative ion powder, 4% germanium powder, 5% Rare Earth Lanthanum, 5% medical stone, 5% wood
Fish stone, 5% Tourmaline stone flour.
Active ceramic described in the utility model, wherein, the far-infrared powder at least includes in following component：Si、Ai、K、
Na、Fe、Ti、Mg、C、SiO2、Al2O3、Fe2O3、K2O、Na2O、MnO、CaO、MgO、P2O5、Ge10-6、TiO2、ZnO、Mo、
Se。
The preparation method of active ceramic of the present utility model comprises the following steps：
Step A：Respectively by potassium feldspar, albite, stone needle, agate, mullite, periclase, calcite, fluorite, quartz,
Medical stone, tourmaline calcine 3.5-4.5h at 840-860 DEG C, and are cooled to grinding after normal temperature, cross 90-120 mesh sieves, standby；
Step B：Kaolin, bentonite, clay are calcined into 3.5-4.5h at 620-650 DEG C respectively respectively, and are cooled to often
Ground after temperature, cross 90-120 mesh sieves, it is standby；
Step C：By weight, kaolin 11-13%, clay 31-33%, bentonite 8-10% is taken to be used as porcelain mud raw material stone
Diamond stone 9-10%, albite 4-6%, bone meal 7-10%, mullite 2.5-3.5%, tourmaline 8-8.5%, medical stone 5-
5.5%, rare earth element 3.2-4.5%, knock down ball mill, plus the 80-100% of porcelain mud raw material gross weight water, be ground 30-
36h, then 24h is stood, water float thing is removed, then using magnet removal of impurities, then except hydraulic pressure mud, pugging to pug wet weight hundred
Divide than being 15-18%, porcelain mud is made；
Step D：By weight, kaolin 3-3.5%, bentonite 7.5-8.5%, potassium feldspar 30-35%, calcite 5- are taken
6.5%, zinc oxide 8-9.5%, barium carbonate 3.2-4.5%, titanium oxide 1.5-2.%, quartz 6.8-7.5%, frit 2.5-
3%, lithium carbonate 4-5.5%, fluorite 4.5-5.5%, rare earth element 5.5-6.8%, tourmaline 12.8-13.2%, far-infrared powder
2.5-3.5% nano-silver ionics 1-1.5% knocks down ball mill as enamel raw material, plus enamel raw material gross weight 80-100%
Water, be ground 30-36h, then put 24h only, remove water float thing, then using magnet removal of impurities, then except hydraulic pressure mud, pugging
It is 15-18% to pug wet weight percentage, enamel is made；
Step E：The porcelain mud is molded by traditional ceramics production method, dried, then the biscuiting at 840-860 DEG C
2.5-3.h, and normal temperature is naturally cooled to, obtain biscuiting product；
Step F：By traditional ceramics production method, glazing is carried out to the biscuiting product using the enamel, is subsequently placed in
Burnt till in kiln.
It is first reducing atmosphere in control kiln, and the temperature in kiln is warming up to 850-900 DEG C in 3-4h, then at 5-
6h is warming up to 1215-1225 DEG C；Kiln temperature is warming up to 50-65 DEG C per hour of speed in 100-120min again
1280-1300 DEG C, and come out of the stove after 25-35min is kept, then normal temperature is naturally cooled to, obtain product.
It is related in the porcelain mud raw material and the enamel raw material with the step A identicals raw material using by described
The raw material of processing of step A.
Light water preferably can be converted into activated water by water treatment facilities of the present utility model, and the activated water of gained has
The electrolytic speed increased substantially.
Brief description of the drawings
Fig. 1 is electrolysis water treatment facilities schematic diagram of the present utility model.
Embodiment
To make the purpose of this utility model, technical scheme and advantage clearer, the utility model will be made with reference to accompanying drawing
Further it is described in detail；This description is to describe by way of example, and not limitation and principle phase one of the present utility model
The embodiment of cause, the description of these embodiments is detailed enough, to enable those skilled in the art to put into practice
The utility model, other embodiment can be used in the case where not departing from scope and spirit of the present utility model and can be with
Change and/or replace the structure of each key element；Therefore, the following detailed description should not be understood from restrictive, sense；
As shown in figure 1, a kind of electrolysis water treatment facilities that the utility model is provided, it is characterised in that including：Tank
1, tank 1 has the exterior contour of pyramid tetrapyamid shape and the internal cavities of pyramid tetrapyamid shape, and water storage holds
The conical top of device 1 is passed in and out provided with permission water fills out in the opening of tank, the internal cavities of tank 1 filled with ceramics
Material.The bottom surface of the exterior contour of tank 1 and the angle of side are 52 ± 2 degree, and the ratio on hypotenuse and base is 0.95-
0.97.The bottom surface of the internal cavities of tank 1 and the angle of side are also 52 ± 2 degree, and the ratio on hypotenuse and base is 0.95-
0.97.The side wall thickness of tank 1 is the 0.1-2% of exterior contour base length.Ceramic packing be spherical ceramic packing or
Pyramid tetrapyamid shape ceramic packing.Pyramid tetrapyamid shape ceramic packing is solid, and the angle of bottom surface and side is
52 ± 2 degree, the ratio on hypotenuse and base is 0.95-0.97.Base length is 0.5-0.8 centimetres.Electrolytic water device is further wrapped
Include water funnel 2, the collection oxygen pipe 3 for collecting oxygen, collection hydrogen pipe 4 and power supply 5 for collecting hydrogen.Under water funnel 2
Portion is connected with the lower flow of collection oxygen pipe 3 and collection hydrogen pipe 4, for the water injection in water funnel 2 to be collected into oxygen pipe 3 and collection hydrogen pipe 4.
The bottom of collection hydrogen pipe 4 is provided with the negative electrode electrically connected with the positive pole of power supply 5, and the bottom of collection oxygen pipe 3 is electrically connected provided with the negative pole with power supply
The anode connect.Collect the open fluid communication of the tank 1 of the bottom of hydrogen pipe 4 and the bottom of collection oxygen pipe 3 and water treatment facilities, with
Just the water turnover in tank 1 collects hydrogen pipe and collection oxygen pipe.
The ceramic tank of pyramid of the present utility model can have pyramid with activated water through of the present utility model
The water of the water treatment facilities activation of ceramic tank has the electrolytic speed increased substantially., will in order to investigate this phenomenon
Water electrolysis equipment shown in Fig. 1 and after the ceramic tank of pyramid in the water electrolysis equipment shown in Fig. 1 is removed
Water electrolysis equipment has carried out contrast experiment, as a result as shown in table 1.
Table 1：The relation of hydrogen generation amount (mL) and electrolysis time
As can be seen from Table 1, it is not added with electrolytic speed during pyramid tank very slow, but has added ceramic pyramid to store up
After water receptacle, electrolytic speed was promptly accelerated after one day or so, will enter the metastable stage until two days or so.
But decomposition rate is still more faster than the not added-time in time per unit.
In addition, according to disclosed specification of the present utility model, skill of other realizations of the present utility model for this area
Art personnel are obvious；The various aspects of embodiment and/or embodiment can be used for this reality individually or with any combinations
With in new system and method；Specification and example therein should only be regarded solely as exemplary, reality of the present utility model
Scope and spirit are represented by appended claims.
Claims (5)
1. a kind of water treatment facilities, it is characterised in that including：Tank, the tank has pyramid rectangular pyramid
The exterior contour of shape and the internal cavities of pyramid tetrapyamid shape, the conical top of the tank are passed in and out provided with permission water
Ceramic packing is filled with the opening of the tank, the internal cavities of the tank.
2. water treatment facilities according to claim 1, it is characterised in that the bottom surface of the exterior contour of the tank with
The angle of side is 52 ± 2 degree, and the ratio on hypotenuse and base is 0.95-0.97；The bottom surface of the internal cavities of the tank
Angle with side is also 52 ± 2 degree, and the ratio on hypotenuse and base is 0.95-0.97；The side wall thickness of the tank is
The 0.1-2% of exterior contour base length.
3. the water treatment facilities according to any one of claim 1-2, it is characterised in that the ceramic packing is spherical pottery
Porcelain filling or pyramid tetrapyamid shape ceramic packing.
4. water treatment facilities according to claim 3, it is characterised in that the pyramid tetrapyamid shape ceramic packing is
Solid, the angle of bottom surface and side is 52 ± 2 degree, and the ratio on hypotenuse and base is 0.95-0.97；Base length is 0.5-
0.8 centimetre.
5. one kind electrolysis wetting system, it is characterised in that including：Water treatment facilities according to claim any one of 1-4, electricity
Solve water installations and power supply；Wherein, the electrolytic water device further comprises water funnel, the collection oxygen pipe for collecting oxygen and use
In the collection hydrogen pipe for collecting hydrogen；The bottom of the water funnel is connected with the lower flow of collection oxygen pipe and collection hydrogen pipe, for that will note
The water injection collection oxygen pipe and the collection hydrogen pipe in hyponome；The bottom of the collection hydrogen pipe is provided with the positive pole electricity with the power supply
The negative electrode of connection, the bottom of the collection oxygen pipe is provided with the anode electrically connected with the negative pole of the power supply；The bottom of the collection hydrogen pipe
Bottom and the open fluid communication of the tank of the water treatment facilities with the collection oxygen pipe, so that the water storage holds
The water turnover collection hydrogen pipe and the collection oxygen pipe in device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621230844.6U CN206352062U (en) | 2016-11-14 | 2016-11-14 | A kind of water treatment facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621230844.6U CN206352062U (en) | 2016-11-14 | 2016-11-14 | A kind of water treatment facilities |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206352062U true CN206352062U (en) | 2017-07-25 |
Family
ID=59346373
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621230844.6U Expired - Fee Related CN206352062U (en) | 2016-11-14 | 2016-11-14 | A kind of water treatment facilities |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206352062U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110157566A (en) * | 2018-02-13 | 2019-08-23 | 方厉远 | Alkalescent multielement active health preserving wine and preparation method thereof |
-
2016
- 2016-11-14 CN CN201621230844.6U patent/CN206352062U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110157566A (en) * | 2018-02-13 | 2019-08-23 | 方厉远 | Alkalescent multielement active health preserving wine and preparation method thereof |
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|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170725 Termination date: 20171114 |
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| CF01 | Termination of patent right due to non-payment of annual fee |