CN213060335U - Spiral backward flow formula ozone water machine - Google Patents
Spiral backward flow formula ozone water machine Download PDFInfo
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- CN213060335U CN213060335U CN202021363559.8U CN202021363559U CN213060335U CN 213060335 U CN213060335 U CN 213060335U CN 202021363559 U CN202021363559 U CN 202021363559U CN 213060335 U CN213060335 U CN 213060335U
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- ozone
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- dissolving tank
- spiral
- liquid mixture
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Abstract
The utility model discloses a spiral backward flow formula ozone water machine uses in the field of ozone water machine, has solved current ozone water machine and has produced the unstable technical problem of ozone water dissolved concentration, and its technical scheme main points are including ozone dissolving tank, characterized by: one side intercommunication of ozone dissolving tank has the gas-liquid mixture inlet pipe, the intercommunication has the gas-liquid mixture pump on the gas-liquid mixture inlet pipe, still be connected with the inlet tube on the gas-liquid mixture pump, be connected with the back flow between the one end of inlet tube and ozone dissolving tank, the one end that the back flow was kept away from to the ozone dissolving tank is equipped with the blast pipe, the one end lateral wall that the gas-liquid mixture inlet pipe was kept away from to the ozone dissolving tank is equipped with the delivery port, the inside of ozone dissolving tank still is equipped with the spiral-up pipeline, the middle part of spiral-up pipeline is equipped with central back flow, the one end and the back flow intercommunication of central back flow.
Description
Technical Field
The utility model relates to an ozone water machine field, in particular to spiral backward flow formula ozone water machine.
Background
The ozone water machine is a device which continuously dissolves high-concentration ozone in water to the maximum extent and outputs ozone water for the purposes of disinfection and the like, and the higher the concentration of the ozone dissolved by the ozone water is, the better the disinfection effect is. In order to increase the ozone concentration of the ozone water, it is important to adopt higher ozone concentration, higher pressure in the dissolving container and increase the contact area between the ozone gas and water, however, the existing ozone water machine equipment generally has the condition of low ozone water concentration caused by insufficient dissolution in the actual operation process.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a, its advantage is can ensure stable ozone water concentration, ensures abundant stable air water dissolution emergence process.
The above technical purpose of the present invention can be achieved by the following technical solutions: the utility model provides a spiral backward flow formula ozone water machine, includes ozone dissolving tank, characterized by: one side intercommunication of ozone dissolving tank has the gas-liquid mixture inlet pipe, the intercommunication has the gas-liquid mixture pump on the gas-liquid mixture inlet pipe, still be connected with the inlet tube on the gas-liquid mixture pump, be connected with the back flow between the one end of inlet tube and ozone dissolving tank, the one end that the back flow was kept away from to the ozone dissolving tank is equipped with the blast pipe, the one end lateral wall that the gas-liquid mixture inlet pipe was kept away from to the ozone dissolving tank is equipped with the delivery port, the inside of ozone dissolving tank still is equipped with the spiral-up pipeline, the middle part of spiral-up pipeline is equipped with central back flow, the.
Preferably: and the inlet end of the water inlet pipe is also provided with a water inlet control valve.
Preferably: the water inlet pipe is positioned on the return pipe and the pipe body of the gas-liquid mixing pump and is also provided with an ozone negative pressure regulating valve.
Preferably: and a pressure limiting exhaust valve is arranged on the exhaust pipe.
Preferably: and a circulating water check valve is arranged on the return pipe.
Preferably: and an ozone input socket is arranged on the gas-liquid mixing pump.
To sum up, the utility model discloses following beneficial effect has:
1. the spiral ascending pipeline and the central reflux pipe inside the dissolving tank form a multi-time aeration mixing structure, a spiral ascending spiral surface formed between the central reflux pipe and the tank wall realizes a spiral tubular water flow channel, gas-liquid mixed water at an inlet reaches an outlet through the spiral pipe, and a large amount of residual water returns to the mixing pump from the central pipe for secondary aeration because the flow of the gas-liquid mixing pump is greater than the flow of water, so that the full dissolving effect is improved.
Drawings
Fig. 1 is a sectional view for showing the structure inside the ozonated water machine in the embodiment.
Reference numerals: 1. an ozone dissolving tank; 2. a gas-liquid mixing feeding pipe; 3. a gas-liquid mixing pump; 4. a water inlet pipe; 5. a return pipe; 6. an exhaust pipe; 7. a water outlet; 8. a spiral rising pipe; 9. a central return pipe; 10. an inlet control valve; 11. an ozone negative pressure regulating valve; 12. a pressure limiting exhaust valve; 13. a circulating water check valve; 14. ozone input socket.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings.
Example (b): the utility model provides a spiral backward flow formula ozone water machine, as shown in figure 1, including ozone dissolving tank 1, one side intercommunication at ozone dissolving tank 1 has gas-liquid mixture inlet pipe 2, the intercommunication has gas-liquid mixture pump 3 on the gas-liquid mixture inlet pipe 2, still be connected with inlet tube 4 on the gas-liquid mixture pump 3, the entrance point of inlet tube 4 still is equipped with into water control valve 10, a control input for carrying out the water, be equipped with ozone input socket 14 on the gas-liquid mixture pump 3, then can realize ozone's input, mix ozone and water recently and input to ozone dissolving tank 1 in and dissolve, the one end lateral wall that gas-liquid mixture inlet pipe 2 was kept away from to ozone dissolving tank 1 is equipped with delivery port 7, ozone water after dissolving is discharged from delivery port 7.
Be connected with the back flow pipe 5 between the one end of inlet tube 4 and ozone dissolving tank 1, the one end that ozone dissolving tank 1 kept away from back flow pipe 5 is equipped with blast pipe 6, discharge from blast pipe 6 after the gas gathering that overflows from the aquatic, be equipped with voltage limiting discharge valve 12 on blast pipe 6, can restrict the pressure of discharge gas, satisfy the inside atmospheric pressure requirement of normal dissolving mixing in-process, in case gathering gas leads to pressure too high, discharge from voltage limiting discharge valve 12 promptly, discharge after blast pipe 6 handles.
Because can't realize fully dissolving in the actual gas-liquid mixing process, still be equipped with spiral rising pipeline 8 in ozone dissolving tank 1's inside, gas-liquid mixture water reaches delivery port 7 through this spiral rising pipeline, the middle part of spiral rising pipeline 8 is equipped with central back flow 9, the one end and the back flow 5 intercommunication of central back flow 9, because 3 flows of gas-liquid mixing pump are greater than the discharge flow, a large amount of surplus water returns gas-liquid mixing pump 3 through back flow 5 from the central pipe and carries out the secondary aeration, be equipped with circulating water check valve 13 on the back flow 5, can prevent the refluence.
In order to ensure the stable input of ozone gas, the water inlet pipe 4 is also provided with an ozone negative pressure regulating valve 11 on the return pipe 5 and the pipe body of the gas-liquid mixing pump 3, so that negative pressure can be formed at the ozone inlet part of the gas-liquid mixing pump 3, and the stable input pumping effect of ozone is ensured.
The present embodiment is only for explaining the present invention, and it is not limited to the present invention, and those skilled in the art can make modifications to the present embodiment without inventive contribution as required after reading the present specification, but all of them are protected by patent laws within the scope of the claims of the present invention.
Claims (6)
1. The utility model provides a spiral backward flow formula ozone water machine, includes ozone dissolving tank (1), characterized by: one side intercommunication of ozone dissolving tank (1) has gas-liquid mixture inlet pipe (2), the intercommunication has gas-liquid mixture pump (3) on gas-liquid mixture inlet pipe (2), still be connected with inlet tube (4) on gas-liquid mixture pump (3), be connected with back flow (5) between the one end of inlet tube (4) and ozone dissolving tank (1), the one end that back flow (5) were kept away from in ozone dissolving tank (1) is equipped with blast pipe (6), the one end lateral wall that gas-liquid mixture inlet pipe (2) were kept away from in ozone dissolving tank (1) is equipped with delivery port (7), the inside of ozone dissolving tank (1) still is equipped with spiral rising pipeline (8), the middle part of spiral rising pipeline (8) is equipped with central back flow (9), the one end and back flow (5) the intercommunication of central back flow (9).
2. The spiral backflow type ozone water machine as claimed in claim 1, wherein: and the inlet end of the water inlet pipe (4) is also provided with a water inlet control valve (10).
3. The spiral backflow type ozone water machine as claimed in claim 1, wherein: the water inlet pipe (4) is positioned on the return pipe (5) and the pipe body of the gas-liquid mixing pump (3) and is also provided with an ozone negative pressure regulating valve (11).
4. The spiral backflow type ozone water machine as claimed in claim 1, wherein: and a pressure-limiting exhaust valve (12) is arranged on the exhaust pipe (6).
5. The spiral backflow type ozone water machine as claimed in claim 1, wherein: and a circulating water check valve (13) is arranged on the return pipe (5).
6. The spiral backflow type ozone water machine as claimed in claim 1, wherein: the gas-liquid mixing pump (3) is provided with an ozone input socket (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021363559.8U CN213060335U (en) | 2020-07-13 | 2020-07-13 | Spiral backward flow formula ozone water machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021363559.8U CN213060335U (en) | 2020-07-13 | 2020-07-13 | Spiral backward flow formula ozone water machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213060335U true CN213060335U (en) | 2021-04-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021363559.8U Active CN213060335U (en) | 2020-07-13 | 2020-07-13 | Spiral backward flow formula ozone water machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213060335U (en) |
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2020
- 2020-07-13 CN CN202021363559.8U patent/CN213060335U/en active Active
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