CN205275710U - Half unfamiliar hypochlorite generator - Google Patents
Half unfamiliar hypochlorite generator Download PDFInfo
- Publication number
- CN205275710U CN205275710U CN201520948053.6U CN201520948053U CN205275710U CN 205275710 U CN205275710 U CN 205275710U CN 201520948053 U CN201520948053 U CN 201520948053U CN 205275710 U CN205275710 U CN 205275710U
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- China
- Prior art keywords
- battery lead
- lead plate
- hypochlorite generator
- barrier film
- liquid outlet
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- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model provides a half unfamiliar hypochlorite generator belongs to disinfecting equipment technical field, and it includes casing and plate electrode, and the casing has inlet and liquid outlet, and the plate electrode includes first electrode board and second electrode board, and second electrode board upper end is connected the casing upper wall and is connected with the power negative electricity, and the lower extreme forms the passageway with the casing lower wall, first electrode board lower extreme is connected the casing lower wall and is connected with the positive electricity, and the upper end forms the passageway with the casing upper wall. The utility model provides a two piece plate electrodes of half unfamiliar hypochlorite generator through setting up half diaphragm type make saline solution reciprocal flow in the electrolytic bath to changing also appears in the pH value of solution thereupon, makes the pH value of the antiseptic solution that liquid outlet department outwards spills over be in suitable scope, and contain the hypochlorite of capacity in the antiseptic solution, it is better that more traditional hypochlorite generating device, the antiseptic solution of its output disinfect the effect.
Description
Technical field
The utility model relates to sterilization equipment technical field, specifically, it relates to a kind of half barrier film hypochlorite generator.
Background technology
On engineering of water treatment, sterilization and disinfection technology almost major part depend on salt element system sterilizing agent. Particularly processing the sterilization and disinfection more than 90% in engineering at water-supply line is all use the chlorine of salt element system sterilization, clorox, Losantin etc.
Clorox is efficient, wide spectrum, and the thimerosal of safety is more and more paid attention to and popularizes, and electrolyzing hypochlorite generator is because it is easy to use, it may also be useful to field is wide, and is developed rapidly and promote.
But electrolyzing hypochlorite generator of the prior art uses sodium-chlor to be raw material, the vinegar density of sodium chlorate that electrolysis goes out is inadequate, and sterilisation effect is poor, in view of this, is badly in need of a kind of electrolyzing hypochlorite generator that can improve clorox electrolysis concentration.
Practical novel content
The utility model provides a kind of half barrier film hypochlorite generator, it is intended to improve above-mentioned technical problem.
The utility model is achieved in that
Half barrier film hypochlorite generator, comprise housing and battery lead plate, described housing has fluid inlet and liquid outlet, described fluid inlet and described liquid outlet lay respectively at the two ends, left and right of described housing, described battery lead plate comprises the first battery lead plate and the 2nd battery lead plate that arrange successively from fluid inlet to liquid outlet direction, and described battery lead plate is made up of chlorion semipermeable membrane material;
The upper end of described 2nd battery lead plate is connected to the upper inside walls of described housing and the negative pole with extraneous power supply is electrically connected, and forms, between lower end and the downside inwall of described housing, the passage circulated for liquid; The lower end of described first battery lead plate is connected to the downside inwall of described housing and the positive pole with extraneous power supply is electrically connected, and forms the passage circulated for liquid between the upper inside walls of upper end and described housing.
Mostly battery lead plate of the prior art is what the form to run through electrolyzer groove was arranged, what the battery lead plate employing in the technical program was semi-transparent arranges form, by arranging 2 pieces of semi-transparent battery lead plates, wherein near the battery lead plate connection power cathode of liquid outlet, battery lead plate near fluid inlet is connected positive source, and the benefit arranged like this is:
(1) in electrolytic process, saline solution enters electrolyzer from fluid inlet, in the first battery lead plate generation oxidizing reaction, and produce a large amount of hydrogen ion, the solution ph rapid reduction of local is made to become acid, solution flows to the 2nd battery lead plate direction through the passage between the first electrolytic zinc-coated steel sheet and housing, 2nd battery lead plate reduction reaction, the pH value of topical solutions is alkalescence, when the raw material of fluid inlet constantly pours in, solution near first battery lead plate can flow towards liquid outlet direction, and mutually neutralize with the solution near the 2nd battery lead plate, make the pH value of the thimerosal finally overflowed from liquid outlet in more suitable level.
(2) owing to battery lead plate and housing all exist passage, completely housing is not separated, and battery lead plate adopts chlorion semipermeable membrane material to make, this just makes the ion of chloride element in solution can only flow in passage, the process that such solution flows from fluid inlet to liquid outlet, in the passage back and forth arranged, flowing, substantially prolongs its flowing-path, make in solution, have the sufficient reaction times to produce enough clorox, it is to increase from the sterilisation effect of the thimerosal that liquid outlet overflows.
(3) namely salts solution generates NaClO, pH value about 6.5 �� 0.5 after the electrolysis of the first battery lead plate and the 2nd battery lead plate.
Further, by regulating and controlling electric current and the voltage of battery lead plate, it is possible to the electrolysis amount of each battery lead plate place of accurate control, make to generate in electrolyzer more clorox.
Further, described fluid inlet is connected with input duct, and described input duct is provided with volume pump.
To liquid inlet volume by volume pump and enter liquid speed and control accurately, and combine with each battery lead plate electric energy control, it is possible to realize the accurate control of the clorox concentration that whole hypochlorite generator produces.
Further, the width of described passage is no more than the half of the inwall spacing of two ends up and down of described housing.
Namely the width of passage is the spacing between one end of the non-closure casing of battery lead plate and housing, and the size of this width determines the path length of Chlorine in Solution ion flow. Specifically, the width of passage is more big, and the flowing-path of chlorion is more short, otherwise then more long.
More preferably, through practicality novel people repeatedly experimental summary, when the width of described passage be described housing the inwall spacing of two ends up and down three/for the moment, the electrolysis effectiveness in whole hypochlorite generator is best.
Further, also comprise PLC control system and the surveymeter for detecting pH value, described surveymeter is arranged on liquid outlet place, and described surveymeter is electrically connected with described PLC control system, the electric current that institute's PLC control system is powered to described battery lead plate for controlling power supply and voltage.
PLC control system forms circuit with all battery lead plates and is connected, and is accurately controlled the electricity of each circuit card by built-in program, it is achieved to the accurate control of electrolytic process. In addition, PLC control system can also carry out connection control with volume pump.
Further, described liquid outlet is provided with magnetic valve, and described magnetic valve is electrically connected with described PLC control system. When the thimerosal existed in electrolyzer does not reach the situation of service requirements, PLC control system Controlling solenoid valve is closed, and extends electrolysis time.
Further, described fluid inlet is positioned at the lower end of sidewall on the left of described housing.
Further, described liquid outlet is positioned at the upper end of described housing right sidewall.
Fluid inlet and liquid outlet are separately positioned on the lower end of sidewall and the upper end of right sidewall on the left of housing, do the flowing-path that can extend the solution entering in electrolyzer from fluid inlet equally like this.
Specifically, fluid inlet near the lower end of the first battery lead plate, and then away from the passage between the first battery lead plate and housing; Liquid outlet then near the upper end of the 4th battery lead plate, and then away from the passage between the first battery lead plate and housing.
Further, described housing is made up of insulating material, and the inwall of described housing is provided with corrosion-resistant coating.
In cell operation process, local can in acid or alkaline. Housing can be produced violent corrosion, and the setting of corrosion-resistant coating is the corrodibility of the anti-acid in order to strengthen whole housing, alkali, salt, extends its work-ing life.
Further, described corrosion-resistant coating thickness is not less than 3mm.
The beneficial effects of the utility model are: the novel half barrier film hypochlorite generator that the utility model provides is by arranging four electrode plate of half diaphragm type, the flowing making saline solution reciprocal in electrolyzer, and also there is change in the pH value of solution thereupon, directly generate clorox, and outwards overflow from liquid outlet, and the pH value of the thimerosal generated is in relatively suitable scope, containing enough clorox in thimerosal, more traditional hypochlorite element generating unit, the thimerosal sterilisation effect of its output is better.
Accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme of the utility model embodiment, it is briefly described to the accompanying drawing used required in embodiment below, it is to be understood that, the following drawings illustrate only some embodiment of the present utility model, therefore should not be counted as is the restriction to scope, for those of ordinary skill in the art, under the prerequisite not paying creative work, it is also possible to obtain other relevant accompanying drawings according to these accompanying drawings.
Fig. 1 is the structural representation of the half barrier film hypochlorite generator that the utility model embodiment provides;
Fig. 2 is the workflow diagram of the half barrier film hypochlorite generator that the utility model provides.
Figure acceptance of the bid note is respectively:
Saline solution storage pool 101; Volume pump 102; Housing 103; Fluid inlet 104; Liquid outlet 105; First battery lead plate 111; 2nd battery lead plate 112.
Embodiment
On engineering of water treatment, sterilization and disinfection technology almost major part depend on salt element system sterilizing agent. Particularly processing the sterilization and disinfection more than 90% in engineering at water-supply line is all use the chlorine of salt element system sterilization, clorox, Losantin etc.
Clorox is efficient, wide spectrum, and the thimerosal of safety is more and more paid attention to and popularizes, and electrolyzing hypochlorite generator is because it is easy to use, it may also be useful to field is wide, and is developed rapidly and promote.
But electrolyzing hypochlorite generator of the prior art uses sodium-chlor to be raw material, the vinegar density of sodium chlorate that electrolysis goes out is inadequate, and sterilisation effect is poor, in view of this, is badly in need of a kind of electrolyzing hypochlorite generator that can improve clorox electrolysis concentration.
In view of this, those skilled in the art are seeking a kind of instrument or the method for improving this problem for a long time always.
For making the object of the utility model embodiment, technical scheme and advantage clearly, below in conjunction with the accompanying drawing in the utility model embodiment, technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is the utility model part embodiment, instead of whole embodiments. Therefore, below to the detailed description of the embodiment of the present utility model provided in the accompanying drawings and the claimed scope of the present utility model of not intended to be limiting, but only represent selected embodiment of the present utility model. Based on the embodiment in the utility model, those of ordinary skill in the art are not making other embodiments all obtained under creative work prerequisite, all belong to the scope of the utility model protection.
It should be noted that: similar label and letter accompanying drawing below represents similar item, therefore, once a certain Xiang Yi accompanying drawing is defined, then do not need it carries out definition further and explains in accompanying drawing subsequently.
In description of the present utility model, it should be noted that, term " " center ", " on ", D score, " left side ", " right side ", " vertically ", " level ", " interior ", it is based on orientation shown in the drawings or position relation that the orientation of the instruction such as " outward " or position are closed, or this practicality novel product orientation usually put or position relation when using, it is only the utility model and simplified characterization for convenience of description, instead of indicate or imply that the device referred to or element must have specific orientation, with specific orientation structure and operation, therefore can not be interpreted as restriction of the present utility model. in addition, term " first ", " the 2nd ", " the 3rd " etc. are only for distinguishing description, and can not be interpreted as instruction or hint relative importance.
In description of the present utility model, in addition it is also necessary to explanation, unless otherwise clearly defined and limited, term " setting ", " installation ", " being connected ", " connection " should be interpreted broadly, such as, it is possible to be fixedly connected with, can also be removably connect, or connect integratedly; Can be mechanically connected, it is also possible to be electrical connection; Can be directly be connected, it is also possible to be indirectly connected by intermediary, it is possible to be the connection of two element internals. For the ordinary skill in the art, it is possible to particular case understands the concrete implication of above-mentioned term in the utility model.
Embodiment
As depicted in figs. 1 and 2, present embodiments provide a kind of half barrier film hypochlorite generator, comprise housing 103, PLC control system and saline solution storage pool 101. In the present embodiment, housing 103 is rectangular-shaped, and housing 103 adopts insulating material to make, and the inwall of described housing 103 is provided with corrosion-resistant coating, and the setting of corrosion-resistant coating is the corrodibility of the anti-acid in order to strengthen whole housing 103, alkali, salt, extends its work-ing life.
Specifically, the thickness of corrosion-resistant coating should be not less than 3mm, and in the present embodiment, corrosion-resistant coating is made up of high molecule plastic PVDF, and the thickness of corrosion-resistant coating is 4mm.
As shown in Figure 1, described housing 103 has fluid inlet 104 and liquid outlet 105, and described fluid inlet 104 and described liquid outlet 105 lay respectively at the two ends, left and right of described housing 103. Saline solution storage pool 101 is connected with fluid inlet 104 by input duct, and is provided with volume pump 102 in input duct, and volume pump 102 can accurately control saline solution and enter the flow in housing 103 and flow velocity. Volume pump 102 is electrically connected with PLC control system, and PLC control system is by the unlatching of built-in time variable control volume pump 102, closedown and flow.
Liquid outlet 105 place is provided with pH value surveymeter, pH value surveymeter is for detecting the pH value of liquid outlet 105 place solution, and liquid outlet 105 place is also provided with magnetic valve, pH value surveymeter and magnetic valve are all electrically connected with PLC control system, the opening and closing of the output control magnetic valve that PLC control system detects according to pH value surveymeter, ensures that the pH value of the thimerosal from liquid outlet 105 spilling all can be up to standard.
The cavity of housing 103 inside forms electrolyzer, and the top and bottom sidewall of housing 103 is provided with opening. Being provided with two electrode plate in electrolyzer, battery lead plate is that the opening by arranging on top and bottom sidewall stretches into electrolyzer inside.
Battery lead plate is made up of chlorion semipermeable membrane material, and this kind of chlorion semipermeable membrane material can stop chloride elemental substance to pass through.
In the present embodiment, described battery lead plate comprises the first battery lead plate 111 and the 2nd battery lead plate 112 that arrange successively from fluid inlet 104 to liquid outlet 105 direction.
Specifically, the upper end of the 2nd battery lead plate 112 is all connected to the upper inside walls of described housing 103 and the negative pole with extraneous power supply is electrically connected, and forms, between lower end and the downside inwall of described housing 103, the passage circulated for liquid; The lower end of described first battery lead plate 111 is all connected to the downside inwall of described housing 103 and the positive pole with extraneous power supply is electrically connected, and forms the passage circulated for liquid between the upper inside walls of upper end and described housing 103.
First battery lead plate 111, the 2nd battery lead plate 112 and extraneous power supply are all electrically connected with PLC control system, and PLC control system can control the first battery lead plate 111, the instantaneous input voltage of the 2nd battery lead plate 112 and electric current.
In actual use procedure, saline solution enters electrolyzer from fluid inlet 104, there is oxidizing reaction in the first battery lead plate 111, and produce a large amount of hydrogen ion, the solution ph rapid reduction of local is made to become acid, solution flows to the 2nd battery lead plate 112 direction through the passage between the first battery lead plate 111 and housing 103, there is reduction reaction in the 2nd battery lead plate 112, the pH value of topical solutions is alkalescence, when the raw material of fluid inlet 104 constantly pours in, solution near first battery lead plate 111 can flow towards liquid outlet 105 direction, and first with the 2nd battery lead plate 112 near solution neutralization, in slightly acidic after neutralization, the pH value of the thimerosal finally overflowed from liquid outlet 105 is in more suitable level.
The present embodiment provides a kind of preferred electrolyzer pH value control program, specifically, solution ph near first battery lead plate 111 is 2.5 �� 0.2, solution ph near 2nd battery lead plate 112 is 6 �� 0.5, the pH value of the thimerosal overflowed from liquid outlet 105 like this is slightly acidic, is suitable for use of sterilizing.
The width of the passage between battery lead plate and housing 103 is extremely important for the control path length of solution in electrolyzer, and in the present embodiment, the width of described passage is 1/3rd of the inwall spacing of two ends up and down of described housing 103.
Passage is under this width, and flow of solution is comparatively suitable through the path of electrolyzer, and the working efficiency of electrolyzer is the highest.
The novel half barrier film hypochlorite generator that the present embodiment provides is by arranging two electrode plate of half diaphragm type, the flowing making saline solution reciprocal in electrolyzer, and also there is change in the pH value of solution thereupon, directly generate clorox, and outwards overflow from liquid outlet 105, and the pH value of the thimerosal generated is in relatively suitable scope, containing enough clorox in thimerosal, more traditional hypochlorite element generating unit, the thimerosal sterilisation effect of its output is better.
The foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, for a person skilled in the art, the utility model can have various modifications and variations. All within spirit of the present utility model and principle, any amendment of doing, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (10)
1. half barrier film hypochlorite generator, it is characterized in that, comprise housing and battery lead plate, described housing has fluid inlet and liquid outlet, described fluid inlet and described liquid outlet lay respectively at the two ends, left and right of described housing, described battery lead plate comprises the first battery lead plate and the 2nd battery lead plate that arrange successively from fluid inlet to liquid outlet direction, and described battery lead plate is made up of chlorion semipermeable membrane material;
The upper end of described 2nd battery lead plate is connected to the upper inside walls of described housing and the negative pole with extraneous power supply is electrically connected, and forms, between lower end and the downside inwall of described housing, the passage circulated for liquid; The lower end of described first battery lead plate is connected to the downside inwall of described housing and the positive pole with extraneous power supply is electrically connected, and forms the passage circulated for liquid between the upper inside walls of upper end and described housing.
2. half barrier film hypochlorite generator according to claim 1, it is characterised in that, described fluid inlet is connected with input duct, and described input duct is provided with volume pump.
3. half barrier film hypochlorite generator according to claim 1, it is characterised in that, the width of described passage is no more than the half of the inwall spacing of two ends up and down of described housing.
4. half barrier film hypochlorite generator according to claim 3, it is characterised in that, the width of described passage is 1/3rd of the inwall spacing of two ends up and down of described housing.
5. half barrier film hypochlorite generator according to claim 1, it is characterized in that, also comprise PLC control system and the surveymeter for detecting pH value, described surveymeter is arranged on liquid outlet place, described surveymeter is electrically connected with described PLC control system, the electric current that institute's PLC control system is powered to described battery lead plate for controlling power supply and voltage.
6. half barrier film hypochlorite generator according to claim 5, it is characterised in that, described liquid outlet is provided with magnetic valve, and described magnetic valve is electrically connected with described PLC control system.
7. half barrier film hypochlorite generator according to claim 1, it is characterised in that, described fluid inlet is positioned at the lower end of sidewall on the left of described housing.
8. half barrier film hypochlorite generator according to claim 1, it is characterised in that, described liquid outlet is positioned at the upper end of described housing right sidewall.
9. half barrier film hypochlorite generator according to claim 1, it is characterised in that, described housing is made up of insulating material, and the inwall of described housing is provided with corrosion-resistant coating.
10. half barrier film hypochlorite generator according to claim 9, it is characterised in that, described corrosion-resistant coating thickness is not less than 3mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520948053.6U CN205275710U (en) | 2015-11-24 | 2015-11-24 | Half unfamiliar hypochlorite generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520948053.6U CN205275710U (en) | 2015-11-24 | 2015-11-24 | Half unfamiliar hypochlorite generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205275710U true CN205275710U (en) | 2016-06-01 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520948053.6U Withdrawn - After Issue CN205275710U (en) | 2015-11-24 | 2015-11-24 | Half unfamiliar hypochlorite generator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205275710U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105332001A (en) * | 2015-11-24 | 2016-02-17 | 成都百鸥飞达生物科技有限公司 | Semi-membrane sodium hypochlorite generator |
-
2015
- 2015-11-24 CN CN201520948053.6U patent/CN205275710U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105332001A (en) * | 2015-11-24 | 2016-02-17 | 成都百鸥飞达生物科技有限公司 | Semi-membrane sodium hypochlorite generator |
| CN105332001B (en) * | 2015-11-24 | 2017-10-27 | 成都百鸥飞达生物科技有限公司 | Half barrier film hypochlorite generator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160601 Effective date of abandoning: 20171027 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20160601 Effective date of abandoning: 20171027 |