CN203474909U - Automatic electrolyte adding device for machine core of electrolysis ozone generator - Google Patents
Automatic electrolyte adding device for machine core of electrolysis ozone generator Download PDFInfo
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- CN203474909U CN203474909U CN201320523601.1U CN201320523601U CN203474909U CN 203474909 U CN203474909 U CN 203474909U CN 201320523601 U CN201320523601 U CN 201320523601U CN 203474909 U CN203474909 U CN 203474909U
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- water
- ozone generator
- electrolytic solution
- type ozone
- electrolysis type
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Abstract
The utility model discloses an automatic electrolyte adding device for a machine core of an electrolysis ozone generator, and relates to an electrolyte adding device for an ozone generator. The automatic electrolyte adding device for the machine core of the electrolysis ozone generator comprises a low-temperature distillation system, wherein the low-temperature distillation system comprises an evaporation chamber for containing water to be distillated and a heating element for heating the water to be distillated; a vapor outlet is formed in the upper part of the evaporation chamber. The device also comprises a condensation system, wherein the condensation system is provided with a condensed water passage in which a condensation pipe is arranged; the condensation pipe is provided with a water inlet which is connected with the vapor outlet and also provided with a water outlet for connecting the machine core of the electrolysis ozone generator; the water outlet is lower than the water inlet. According to the device, the water outlet of the condensation pipe is lower than the water inlet, so that the distilled water can flow down under the action of gravity; when the device is used, electrolyte can be automatically added only by connecting the water outlet to the machine core of the electrolysis ozone generator.
Description
Technical field
The utility model relates to ozonizer, is specifically related to the liquid device that adds of ozonizer.
Background technology
Ozone is the allotropic substance of oxygen, and at normal temperatures and pressures, stability extreme difference, can be decomposed into oxygen at normal temperatures voluntarily.
Ozone can be used for food purification, drink water purifying, sterilization, purifying air, preserving fruit and vegetable utilizing, mildew-resistant, bathing, beauty treatment, keeps healthy, breeds fish, waters flowers, deodorizing etc.
Aspect health care, washing ozone bath has become fashion abroad, by ozone bath, treats the existing history for many years of disease, often wash ozone bath and can get rid of vivotoxin, activate epidermal cell, eliminates acne, skin whitening, has good efficacy to rheumatosis, tetter, gynecopathy, diabetes and tinea unguium etc.In addition, ozone is poured in water, can prepare heavy-oxygen-enriched water, heavy-oxygen-enriched water is a kind of nontoxic oxygen supplement, by for oxygen supply, can improve the function of immune system of human body, promotes the metabolism of cell.And heavy-oxygen-enriched water or a kind of very strong and effective broad-spectrum sterilization, antiviral, anti-yeast and parasiticide liquid.Heavy-oxygen-enriched water can promote wound and ulcer healing, the ulcer that particularly white smear spider causes.Long-term taking heavy-oxygen-enriched water, has obvious facilitation effect to flu prevention, treating asthma, pulmonary emphysema treatment, chronic gingivitis (gum infection) recovery from illness, the treatment of chronic long sinus purulence ulcer etc.
Ozonizer is for producing the device of ozone gas (O3).Ozone is easy to decompose inconvenience and stores, and needs scene to produce on-the-spot use (in special situation, can carry out the storage of short period of time), and the place that can use ozone so every all needs to use ozonizer.It is ozoniferous by electrolysis pure water having a kind of ozonizer, it is very high to the requirement of pure water, the pure electrical conductivity of water of general requirement is less than 5us/cm or TDS value is less than 2.5ppm, this kind of ozonizer is called as electrolysis type ozone generator equipment, but the existing electrolysis type ozone generator equipment methods that adopt artificial interpolation electrolytic solution, electrolytic solution is easily polluted more.
Utility model content
The purpose of this utility model is to provide a kind of electrolysis type ozone generator movement to add electrolytic solution device with automatic powder adding, to solve the problems of the technologies described above.
The technical problem that the utility model solves can realize by the following technical solutions:
Electrolysis type ozone generator movement adds electrolytic solution device with automatic powder adding, comprise a low temperature distillation system, described low temperature distillation system comprises that one for holding evaporation of water chamber to be distilled, for heating the heating unit of water to be distilled, the top of described evaporator room is provided with a vapor outlet port, it is characterized in that, also comprise a condenser system, described condenser system is provided with a condensation water channel, in described condensation water channel, be provided with a prolong, described prolong is provided with a water-in, and described water-in connects described vapor outlet port;
Described prolong is also provided with one for connecting the water outlet of electrolysis type ozone generator movement, and the height of described water outlet is lower than the height of described water-in.The water outlet of prolong of the present utility model is lower than water-in, and distilled water can flow down under the effect of gravity.During use, as long as water outlet is connected on electrolysis type ozone generator movement, so just can automatically realize the interpolation of electrolytic solution.
Described condenser system comprises a hollow cavity, using the hollow space of described hollow cavity as described condensation water channel, the lower end of described hollow cavity has a lower opening, using the condensing water inlet of described lower opening as described condensation water channel, the upper end of described hollow cavity has a upper shed, usings the condensation-water drain of described upper shed as described condensation water channel.Adopt the simple in structure of this technical scheme, can reduce manufacture difficulty.
The part that described prolong is positioned at described condensation water channel in the shape of a spiral.Spirrillum is conducive to increase the action time of the water of condensation of distilled water in prolong and outside, can make distilled water fully cooling.
In described evaporator room, be provided with a water inlet pipe, the water outlet of described water inlet pipe is provided with a fluid level controller.Fluid level controller can limit the height of former water in evaporator room.Described fluid level controller can be polarity formula liquid level switch controller, float switch controller, liquid level relay etc.
The height of the water outlet of described water inlet pipe is higher than the height of described heating unit.To avoid heating unit dry combustion method to cause evaporator room outer wall or heating unit to damage.
The bottom of described evaporator room is provided with one to the groove to recessed, and described heating unit is positioned at described groove.With fixing heating unit.Described groove is preferably placed at the central authorities of evaporator room, and for example, described evaporator room is preferably an evaporator room that is " U ", described in be evaporator room opening down of " U ", described opening is in-built described heating unit.
As a kind of preferred version, the glass hollow cavity that the glass evaporator room that described evaporator room preferred glass is made, described hollow cavity preferred glass are made.
The water entering in the water inlet pipe of described evaporator room can be pure water, as primary reverse osmosis water or commercially available bottled pure water, can also be to adopt the method for low-temperature distillation to be met the ultra-pure water of requirement.
The electrical conductivity of water that the water outlet of described prolong flows out is less than 5us/cm or TDS value is less than 2.5ppm.
The preferred an electric heating element of described heating unit, as nichrome wire (Ni-Cr), Fe-Cr-Al wire (Fe-Cr-Al), nickel-iron wire (Ni-Fe), nickel-copper wire (Ni-Cu)), silicon carbide, Si-Mo rod, PTC electrical heating element, electric-heating coatings etc.
Described an electric heating element can be automatic constant-temperature an electric heating element, also can connect one and add thermal control units, described in add thermal control units and connect a temperature sensor.The working temperature of described an electric heating element is 60-80 degree.
Accompanying drawing explanation
Fig. 1 is part-structure schematic diagram of the present utility model.
Embodiment
For technique means, creation characteristic that the utility model is realized, reach object with effect is easy to understand, below in conjunction with the further elaboration the utility model of concrete diagram.
With reference to Fig. 1, electrolysis type ozone generator movement adds electrolytic solution device with automatic powder adding, comprise a low temperature distillation system, low temperature distillation system comprises that one for holding evaporation of water chamber to be distilled 1, for heating the heating unit 3 of water to be distilled, and the top of evaporator room 1 is provided with a vapor outlet port, also comprises a condenser system, condenser system is provided with a condensation water channel, in condensation water channel, be provided with a prolong, prolong is provided with a water-in, and water-in connects vapor outlet port; Prolong is also provided with one for connecting the water outlet of electrolysis type ozone generator movement, and the height of water outlet is lower than the height of water-in.The water outlet of prolong of the present utility model is lower than water-in, and distilled water can flow down under the effect of gravity.During use, as long as water outlet is connected on electrolysis type ozone generator movement, so just can automatically realize the interpolation of electrolytic solution.
Condenser system comprises a hollow cavity 2, using the hollow space of hollow cavity 2 as condensation water channel, the lower end of hollow cavity 2 has a lower opening, using the condensing water inlet of lower opening as condensation water channel, the upper end of hollow cavity 2 has a upper shed, usings the condensation-water drain of upper shed as condensation water channel.Adopt the simple in structure of this technical scheme, can reduce manufacture difficulty.The part 6 that prolong is positioned at condensation water channel in the shape of a spiral.Spirrillum is conducive to increase the action time of the water of condensation of distilled water in prolong and outside, can make distilled water fully cooling.
In evaporator room 1, be provided with a water inlet pipe 4, the water outlet of water inlet pipe 4 is provided with a fluid level controller 5.Fluid level controller can limit the height of former water in evaporator room 1.Fluid level controller 5 can be polarity formula liquid level switch controller, float switch controller, liquid level relay etc.The height of the water outlet of water inlet pipe 4 is higher than the height of heating unit 3.To avoid heating unit 3 dry combustion methods to cause evaporator room 1 outer wall or heating unit 3 to damage.
The bottom of evaporator room 1 is provided with one to the groove to recessed, and heating unit 3 is positioned at groove.With fixing heating unit 3.Groove is preferably placed at the central authorities of evaporator room 1, and for example, evaporator room 1 is preferably an evaporator room that is " U ", is evaporator room opening down of " U ", and heating unit 3 is housed in opening.As a kind of preferred version, the glass hollow cavity that the glass evaporator room that evaporator room 1 preferred glass is made, hollow cavity 2 preferred glass are made.
The water entering in the water inlet pipe 4 of evaporator room 1 can be pure water, as primary reverse osmosis water or commercially available bottled pure water, can also be to adopt the method for low-temperature distillation to be met the ultra-pure water of requirement.The electrical conductivity of water that the water outlet of prolong flows out is less than 5us/cm or TDS value is less than 2.5ppm.
The preferred an electric heating element of heating unit 3, as nichrome wire (Ni-Cr), Fe-Cr-Al wire (Fe-Cr-Al), nickel-iron wire (Ni-Fe), nickel-copper wire (Ni-Cu)), silicon carbide, Si-Mo rod, PTC electrical heating element, electric-heating coatings etc.An electric heating element is automatic constant-temperature an electric heating element preferably, also can connect one and add thermal control units, adds thermal control units and connects a temperature sensor.The working temperature of an electric heating element is 60-80 degree.
More than show and described ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; that in above-described embodiment and specification sheets, describes just illustrates principle of the present utility model; do not departing under the prerequisite of the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (10)
1. electrolysis type ozone generator movement adds electrolytic solution device with automatic powder adding, comprise a low temperature distillation system, described low temperature distillation system comprises that one for holding evaporation of water chamber to be distilled, for heating the heating unit of water to be distilled, the top of described evaporator room is provided with a vapor outlet port, it is characterized in that, also comprise a condenser system, described condenser system is provided with a condensation water channel, in described condensation water channel, be provided with a prolong, described prolong is provided with a water-in, and described water-in connects described vapor outlet port;
Described prolong is also provided with one for connecting the water outlet of electrolysis type ozone generator movement, and the height of described water outlet is lower than the height of described water-in.
2. electrolysis type ozone generator movement according to claim 1 adds electrolytic solution device with automatic powder adding, it is characterized in that: described condenser system comprises a hollow cavity, using the hollow space of described hollow cavity as described condensation water channel, the lower end of described hollow cavity has a lower opening, using the condensing water inlet of described lower opening as described condensation water channel, the upper end of described hollow cavity has a upper shed, usings the condensation-water drain of described upper shed as described condensation water channel.
3. electrolysis type ozone generator movement according to claim 2 adds electrolytic solution device with automatic powder adding, it is characterized in that: the part that described prolong is positioned at described condensation water channel in the shape of a spiral.
4. electrolysis type ozone generator movement according to claim 2 adds electrolytic solution device with automatic powder adding, it is characterized in that: in described evaporator room, be provided with a water inlet pipe, the water outlet of described water inlet pipe is provided with a fluid level controller.
5. electrolysis type ozone generator movement according to claim 4 adds electrolytic solution device with automatic powder adding, it is characterized in that: the height of the water outlet of described water inlet pipe is higher than the height of described heating unit.
6. electrolysis type ozone generator movement according to claim 5 adds electrolytic solution device with automatic powder adding, it is characterized in that: described evaporator room is one to be the evaporator room of " U ", the evaporator room of described being " U " opening down, described opening is in-built described heating unit.
7. according to the electrolysis type ozone generator movement described in any one in claim 2 to 6, with automatic powder adding, add electrolytic solution device, it is characterized in that: described evaporator room is that glass evaporator room, the described hollow cavity that glass is made is the glass hollow cavity that glass is made.
8. according to the electrolysis type ozone generator movement described in any one in claim 1 to 6, with automatic powder adding, add electrolytic solution device, it is characterized in that: the electrical conductivity of water that the water outlet of described prolong flows out is less than 5us/cm or TDS value is less than 2.5ppm.
9. according to the electrolysis type ozone generator movement described in any one in claim 1 to 6, with automatic powder adding, add electrolytic solution device, it is characterized in that: described heating unit is an electric heating element.
10. electrolysis type ozone generator movement according to claim 9 adds electrolytic solution device with automatic powder adding, it is characterized in that: described an electric heating element is that a working temperature is the automatic constant-temperature an electric heating element of 60-80 degree.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320523601.1U CN203474909U (en) | 2013-08-26 | 2013-08-26 | Automatic electrolyte adding device for machine core of electrolysis ozone generator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320523601.1U CN203474909U (en) | 2013-08-26 | 2013-08-26 | Automatic electrolyte adding device for machine core of electrolysis ozone generator |
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| CN203474909U true CN203474909U (en) | 2014-03-12 |
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| CN201320523601.1U Expired - Fee Related CN203474909U (en) | 2013-08-26 | 2013-08-26 | Automatic electrolyte adding device for machine core of electrolysis ozone generator |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106881055A (en) * | 2017-04-10 | 2017-06-23 | 安徽嘉宝诺生物科技有限公司 | Ozone solidifies emulsifier unit and the sterilized agent and process for producing same of ozone solidification emulsification |
| CN114097584A (en) * | 2021-12-02 | 2022-03-01 | 南通大学 | Desert water-making drip irrigation system and method utilizing solar energy |
-
2013
- 2013-08-26 CN CN201320523601.1U patent/CN203474909U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106881055A (en) * | 2017-04-10 | 2017-06-23 | 安徽嘉宝诺生物科技有限公司 | Ozone solidifies emulsifier unit and the sterilized agent and process for producing same of ozone solidification emulsification |
| CN114097584A (en) * | 2021-12-02 | 2022-03-01 | 南通大学 | Desert water-making drip irrigation system and method utilizing solar energy |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190122 Address after: 201415 No. 1299 Juting Road, Zhuanghang Town, Fengxian District, Shanghai Patentee after: SHANGHAI VM ELECTRIC POWER TECHNOLOGY Co.,Ltd. Address before: Room 101, 549 Sanmin Road, Zhuangxing Town, Fengxian District, Shanghai Patentee before: SHANGHAI VM ENVIRONMENT PROTECTION TECHNOLOGY CO.,LTD. |
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| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140312 Termination date: 20210826 |
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| CF01 | Termination of patent right due to non-payment of annual fee |