CN216168916U - Preparation device of ozonized oil - Google Patents
Preparation device of ozonized oil Download PDFInfo
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- CN216168916U CN216168916U CN202122541403.5U CN202122541403U CN216168916U CN 216168916 U CN216168916 U CN 216168916U CN 202122541403 U CN202122541403 U CN 202122541403U CN 216168916 U CN216168916 U CN 216168916U
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Abstract
The utility model belongs to the technical field of ozonized oil, and discloses a preparation device of ozonized oil, which comprises an ozone output assembly, a mixing generation assembly and a dryer, wherein the ozone output assembly is used for producing ozone gas and outputting the ozone gas to the dryer, the dryer is respectively connected with the ozone output assembly and the mixing generation assembly and used for drying the ozone gas, the mixing generation assembly is used for receiving the ozone gas and producing and outputting ozonized oil, the mixing generation assembly comprises a mixing injection pump and a gas-liquid separation kettle, an ozone inlet pipe is arranged at a first input end of the mixing injection pump and is connected and communicated with an output end of the dryer, and an output end of the mixing injection pump is connected and communicated with a top inlet end of the gas-liquid separation kettle. The utility model improves the production efficiency of the ozonized oil preparation device, and improves the cost performance and market competitiveness of the device.
Description
Technical Field
The utility model belongs to the technical field of ozonized oil, and particularly relates to a preparation device of ozonized oil.
Background
Ozone oil or superoxide oil, which is ozone gas and vegetable oil, is formed by mixing and dissolving ozone gas and vegetable oil, is an extension of medical ozone treatment application, is a natural preparation, is widely applied to the treatment of local ulcer, bacterial infection, fungal infection and parasitic infection in many countries, and researches show that the ozone oil has the effect of killing activity on common microorganisms, so that corresponding equipment for producing the ozone oil is widely applied.
SUMMERY OF THE UTILITY MODEL
The present invention has been made to solve the above-mentioned problems occurring in the prior art, and an object of the present invention is to provide an apparatus for producing an ozonized oil.
For realizing the purpose of the above utility model, the technical scheme adopted is as follows:
the ozonized oil preparation device comprises an ozone output assembly, a mixing generation assembly and a dryer, wherein the ozone output assembly is used for producing ozone gas and outputting the ozone gas to the dryer, the dryer is respectively connected with the ozone output assembly and the mixing generation assembly and used for drying the ozone gas, the mixing generation assembly is used for receiving the ozone gas and producing and outputting ozonized oil, the mixing generation assembly comprises a mixing injection pump and a gas-liquid separation kettle, an ozone inlet pipe is arranged at a first input end of the mixing injection pump and connected and communicated with an output end of the dryer, and an output end of the mixing injection pump is connected and communicated with a top inlet end of the gas-liquid separation kettle.
The utility model is further configured to: the mixed generation assembly is provided with a circulating pump for forced circulation, the input end of the circulating pump is provided with a circulating input pipe, the circulating input pipe is connected and communicated with the bottom inlet end of the gas-liquid separation kettle, the output end of the circulating pump is provided with a circulating output pipe, and the circulating output pipe is connected and communicated with the second input end of the mixed jet pump.
The utility model is further configured to: the mixed generating assembly is provided with a decomposer for tail gas treatment, the top of the gas-liquid separation kettle is provided with a tail gas output pipe, and the tail gas output pipe is connected and communicated with the input end of the decomposer.
The utility model is further configured to: the ozone output assembly comprises an electrolyzed water type ozone generator, a first output water tank and a second output water tank, wherein an ozone output end of the electrolyzed water type ozone generator is provided with an ozone output pipe, the ozone output pipe is connected and communicated with the first output water tank, a hydrogen output pipe is arranged at a cathode output end of the electrolyzed water type ozone generator, and the hydrogen output pipe is connected and communicated with the second output water tank.
The utility model is further configured to: the output end of the first output water tank is provided with an ozone gas supply pipe, and the ozone gas supply pipe is connected and communicated with the input end of the dryer and is used for drying the ozone gas.
The utility model is further configured to: the ozone inlet pipe, the circulation input pipe and the circulation output pipe are all provided with a flowmeter and a pressure gauge.
The utility model is further configured to: the ozone production pipe, the hydrogen production pipe and the ozone gas supply pipe are all provided with a concentration monitoring meter and a differential pressure meter.
The utility model is further configured to: the mixing jet pump is arranged at the top end of the gas-liquid separation kettle and is in sealing connection with the gas-liquid separation kettle.
In summary, compared with the prior art, the utility model discloses a preparation device of ozonized oil, which comprises an ozone output assembly, a mixing generation assembly and a dryer, wherein the ozone output assembly is used for producing ozone gas and outputting the ozone gas to the dryer, the dryer is respectively connected with the ozone output assembly and the mixing generation assembly and used for drying the ozone gas, the mixing generation assembly is used for receiving the ozone gas and producing and outputting ozonized oil, the mixing generation assembly comprises a mixing injection pump and a gas-liquid separation kettle, an ozone inlet pipe is arranged at a first input end of the mixing injection pump and is connected and communicated with an output end of the dryer, and an output end of the mixing injection pump is connected and communicated with a top inlet end of the gas-liquid separation kettle. Through this setting, improve the production efficiency of ozonization oil preparation facilities, improve device price/performance ratio and market competition.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and other drawings can be obtained by those skilled in the art without creative efforts.
Fig. 1 is a schematic view of the overall structure of an ozonized oil production apparatus according to this embodiment.
Reference numerals: 1. an ozone output assembly; 2. a mix generation component; 21. a resolver; 3. a dryer; 4. a mixing jet pump; 41. an ozone inlet pipe; 5. a gas-liquid separation kettle; 51. a tail gas output pipe; 6. a circulation pump; 61. a circulating input pipe; 62. circulating an output pipe; 7. an electrolytic water type ozone generator; 71. an ozone production pipe; 72. a hydrogen production pipe; 8. a first output water tank; 81. an ozone supply pipe; 9. and a second output water tank.
Detailed Description
For the purpose of making the objects, technical solutions and advantages of the present invention more apparent, the present invention will be further described in detail with reference to the accompanying drawings and embodiments, it being understood that the specific embodiments described herein are merely illustrative of the present invention and are not intended to limit the present invention.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it should be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; the two elements may be directly connected or indirectly connected through an intermediate medium, or may be communicated with each other inside the two elements, or may be wirelessly connected or wired connected. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
Furthermore, the technical features mentioned in the different embodiments of the present invention described above may be combined with each other as long as they do not conflict with each other.
A preparation device of ozonized oil is shown in figure 1, and comprises an ozone output component 1, a mixing generation component 2 and a dryer 3, wherein the ozone output component 1 is used for producing ozone gas and outputting the ozone gas to the dryer 3, the dryer 3 is respectively connected with the ozone output component 1 and the mixing generation component 2 and is used for drying the ozone gas, the mixing generation component 2 is used for receiving the ozone gas and generating and outputting the ozonized oil, the mixing generation component 2 comprises a mixing injection pump 4 and a gas-liquid separation kettle 5, a first input end of the mixing injection pump 4 is provided with an ozone inlet pipe 41, the ozone inlet pipe 41 is connected and communicated with an output end of the dryer 3 and is used for feeding the dried ozone gas into the mixing injection pump 4, an output end of the mixing injection pump 4 is connected and communicated with a top inlet end of the gas-liquid separation kettle 5, namely, the ozonized oil is obtained by mixing the ozone gas and vegetable oil at one time through the mixing injection pump 4, and the primarily mixed ozonized oil is injected into the gas-liquid separation kettle 5 to complete secondary mixing so as to improve the generation efficiency of the ozonized oil.
In the specific implementation process, the mixing generation assembly 2 is provided with a circulating pump 6 for forced circulation, the input end of the circulating pump 6 is provided with a circulating input pipe 61, the circulating input pipe 61 is connected and communicated with the bottom inlet end of the gas-liquid separation kettle 5, the output end of the circulating pump 6 is provided with a circulating output pipe 62, the circulating output pipe 62 is connected and communicated with the second input end of the mixing injection pump 4, and by the design of the circulating pump 6, working media in the gas-liquid separation kettle 5 are kept to circulate continuously and are combined with the primary mixing ozonized oil of the mixing injection pump 4, so that the purpose of enhancing the preparation efficiency of the ozonized oil is achieved.
Further, mix and generate subassembly 2 and be equipped with the resolver 21 that is used for tail gas treatment, the top of gas-liquid separation cauldron 5 is equipped with tail gas output tube 51, and tail gas output tube 51 is connected and communicates with the input that decomposes the ware 21, will accomplish the ozone tail gas recovery decomposition of mixing work in gas-liquid separation cauldron 5 through decomposing the ware 21 promptly, improves the practicality.
In this embodiment, the ozone output assembly 1 includes an electrolyzed water type ozone generator 7, a first output water tank 8 and a second output water tank 9, an ozone output pipe 71 is disposed at an anode output end of the electrolyzed water type ozone generator 7, the ozone output pipe 71 is connected and communicated with the first output water tank 8, a hydrogen output pipe 72 is disposed at a cathode output end of the electrolyzed water type ozone generator 7, the hydrogen output pipe 72 is connected and communicated with the second output water tank 9, wherein an ozone supply pipe 81 is disposed at an output end of the first output water tank 8, and the ozone supply pipe 81 is connected and communicated with an input end of the dryer 3 for drying ozone gas.
That is, in the working process of the electrolyzed water type ozone generator 7, ozone gas generated at the anode output end thereof overflows from the first output water tank 8 and enters the dryer 3, and the ozone gas output is ensured to be pure through the design of the first output water tank 8, and on the other hand, hydrogen gas generated at the cathode output end of the electrolyzed water type ozone generator 7 is output to the second output water tank 9, that is, the electrolyzed water type ozone generator 7 is used as a supply source of ozone gas, so as to facilitate the preparation of ozone oxidation oil.
In the specific implementation process, the ozone inlet pipe 41, the circulation input pipe 61 and the circulation output pipe 62 are all provided with a flowmeter and a pressure gauge so as to improve the practicability.
Further, a concentration monitoring meter and a differential pressure meter are provided on the ozone-producing pipe 71, the hydrogen-producing pipe 72, and the ozone-feeding pipe 81, to improve safety.
Wherein, the mixing jet pump 4 is arranged at the top end of the gas-liquid separation kettle 5 and is hermetically connected with the gas-liquid separation kettle 5 so as to keep the whole structure stable.
During the working process of the ozonized oil preparation device, the ozone gas is sent into the dryer 3 by the electrolytic water type ozone generator 7 through the first output water tank 8 to be dried, the dried ozone gas enters the mixing injection pump 4 through the ozone inlet pipe 41, meanwhile, under the action of the circulating pump 6, the vegetable oil at the bottom layer in the gas-liquid separation kettle 5 is conveyed into the mixing injection pump 4 by the circulating output pipe 62 and is sprayed out to the gas-liquid separation kettle 5 through the mixing injection pump 4, in the process, the ozone gas is sucked by the negative pressure generated by the mixing injection pump 4, namely, the primary mixing of the ozone gas and the vegetable oil is completed in the mixing injection pump 4 or a jet device thereof, the ozone gas is output and sprayed into the gas-liquid separation kettle 5 at a high speed through the mixing injection pump 4, the secondary mixing is further completed, the aim of preparing the ozonized oil with high efficiency is achieved, and the production efficiency is improved.
In conclusion, the utility model has the following beneficial effects: the utility model discloses a preparation device of ozonized oil, which comprises an ozone output component 1, a mixing generation component 2 and a dryer 3, wherein the ozone output component 1 outputs ozone gas to the dryer 3, the dryer 3 is respectively connected with the ozone output component 1 and the mixing generation component 2, the mixing generation component 2 is used for receiving the ozone gas and generating and outputting ozonized oil, the preparation device comprises a mixing injection pump 4 and a gas-liquid separation kettle 5, an ozone inlet pipe 41 is arranged at a first input end of the mixing injection pump 4, the ozone inlet pipe 41 is connected and communicated with an output end of the dryer 3, and an output end of the mixing injection pump 4 is connected and communicated with a top inlet end of the gas-liquid separation kettle 5. Through the arrangement, the production efficiency of the ozonized oil preparation device is improved, and the cost performance and market competitiveness of the device are improved.
It should be understood that the above examples are only for clarity of illustration and are not intended to limit the embodiments. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. And are neither required nor exhaustive of all embodiments. And obvious variations or modifications therefrom are within the scope of the utility model.
Claims (8)
1. The preparation device of the ozonized oil is characterized by comprising an ozone output assembly, a mixing generation assembly and a dryer, wherein the ozone output assembly is used for producing ozone gas and outputting the ozone gas to the dryer, the dryer is respectively connected with the ozone output assembly and the mixing generation assembly and used for drying the ozone gas, the mixing generation assembly is used for receiving the ozone gas and producing and outputting ozonized oil, the mixing generation assembly comprises a mixing injection pump and a gas-liquid separation kettle, an ozone inlet pipe is arranged at a first input end of the mixing injection pump and is connected and communicated with an output end of the dryer, and an output end of the mixing injection pump is connected and communicated with a top inlet end of the gas-liquid separation kettle.
2. The ozonized oil producing apparatus according to claim 1, wherein the mixing and generating unit has a circulating pump for forced circulation, and an input end of the circulating pump has a circulation inlet pipe connected to and communicating with a bottom inlet end of the gas-liquid separation tank, and an output end of the circulating pump has a circulation outlet pipe connected to and communicating with a second input end of the mixing and injecting pump.
3. The apparatus of claim 1 or 2, wherein the mixing and generating module comprises a decomposer for treating off-gas, and the gas-liquid separation tank comprises an off-gas outlet pipe at the top thereof, the off-gas outlet pipe being connected to and communicating with an input end of the decomposer.
4. The apparatus of claim 1, wherein the ozone output module comprises an electrolyzed water ozone generator, a first output water tank, and a second output water tank, wherein an ozone output pipe is disposed at an anode output end of the electrolyzed water ozone generator, the ozone output pipe is connected to and communicated with the first output water tank, and a hydrogen output pipe is disposed at a cathode output end of the electrolyzed water ozone generator, the hydrogen output pipe is connected to and communicated with the second output water tank.
5. The ozonated oil preparation apparatus of claim 4, wherein an output end of the first output water tank is provided with an ozone feed pipe, the ozone feed pipe being connected to and communicating with an input end of the dryer for drying the ozone gas.
6. The apparatus of claim 2, wherein the ozone inlet pipe, the circulation inlet pipe, and the circulation outlet pipe are provided with a flow meter and a pressure gauge.
7. The apparatus of claim 5, wherein the ozone-producing pipe, the hydrogen-producing pipe, and the ozone-feeding pipe are provided with a concentration monitoring meter and a differential pressure meter.
8. The apparatus of claim 1, wherein the jet mixer is disposed at a top end of the gas-liquid separation tank and is hermetically connected to the gas-liquid separation tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122541403.5U CN216168916U (en) | 2021-10-21 | 2021-10-21 | Preparation device of ozonized oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122541403.5U CN216168916U (en) | 2021-10-21 | 2021-10-21 | Preparation device of ozonized oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216168916U true CN216168916U (en) | 2022-04-05 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122541403.5U Active CN216168916U (en) | 2021-10-21 | 2021-10-21 | Preparation device of ozonized oil |
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| Country | Link |
|---|---|
| CN (1) | CN216168916U (en) |
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2021
- 2021-10-21 CN CN202122541403.5U patent/CN216168916U/en active Active
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