CN211936875U - Low-temperature plasma active oil preparation device - Google Patents
Low-temperature plasma active oil preparation device Download PDFInfo
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- CN211936875U CN211936875U CN202020149568.0U CN202020149568U CN211936875U CN 211936875 U CN211936875 U CN 211936875U CN 202020149568 U CN202020149568 U CN 202020149568U CN 211936875 U CN211936875 U CN 211936875U
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Abstract
The invention discloses a low-temperature plasma active oil preparation device, which comprises: the device comprises a low-temperature plasma reaction box, a cup-shaped grounding electrode, a high-voltage electrode, an oil storage box, an oil inlet pipe, an oil outlet pipe, an oil pump arranged on the oil inlet pipe, an air inlet pipe arranged at the top of the low-temperature plasma reaction box and a booster pump arranged on the air inlet pipe. The utility model discloses its oil curtain that utilizes low temperature plasma and plasma discharge space to form of preparation facilities of low temperature plasma active oil contacts, and the treatment effeciency is high, effectual, and the processing procedure does not have any pollutant emission, and the energy consumption is extremely low, and the active oil of preparation contains multiple active material, and peroxide number and acid number are far greater than conventional ozone oil.
Description
Technical Field
The utility model belongs to the technical field of the grease processing, concretely relates to low temperature plasma active oil preparation facilities.
Background
The ozonized oil, namely ozone oil and superoxide oil, is an extension of medical ozone treatment application. It is widely used in many countries as a natural preparation for the treatment of topical ulcers, bacterial, fungal and parasitic infections. Sedhi et al (2001) examined sunflowers trioxide (Oleozon) from cuba and found that this oil had a biocidal activity against all microorganisms tested.
The ozone oil comprises ozone and unsaturated fatty acid. Unsaturated fatty acids are divided into three main groups: omega-9 series unsaturated fatty acids represented by oleic acid contained in tea oil, omega-6 series unsaturated fatty acids represented by linoleic acid contained in vegetable oil, and omega-3 series unsaturated fatty acids represented by 20-carbon 5-olefine acid (EPA) and 22-carbon 6-olefine acid (DHA) contained in fish oil.
Conventional ozone oil is based on olive oil, which is rich in 80% oleic acid (18: in ═ 6). 1.0g of oil can absorb up to 160mg of ozone. Analysis after ozonization the modification characteristics were analyzed by Nuclear Magnetic Resonance (NMR) chromatography and the new carbon signal was found to correlate with a Criegee ozonide peak near 105 ppm. At 130ppm the olefinic carbon signal was completely absent, carbonyl compounds and carboxylic acids were absent, and the conclusion was drawn by combining resonance chromatography data, elemental analysis and High Performance Liquid Chromatography (HPLC). Long-term ozonation results in the formation of a special glycerol trimolecular ozone compound, ozone oil, of the formula:
the half-life of the ozone oil is about 3 years at normal temperature and normal pressure, the half-life is influenced by the rise and fall of the temperature, the half-life is below zero and can be prolonged to about 50 years, and the half-life is above 270 ℃, so that the ozone is immediately decomposed and does not exist any more. The ozone oil application has the following characteristics. (1) Broad spectrum property: the ozone has the effect of killing various pathogenic microorganisms such as bacteria, fungi, viruses, molds, mycoplasma, chlamydia, trichomonas vaginalis and the like. Ozone destroys the structure of the microbial membrane by oxidation to realize sterilization. Firstly, the cell membrane is acted on, so that membrane components are damaged to destroy intramembranous lipoprotein and lipopolysaccharide, the permeability of cells is changed, and the cells are dissolved and killed, thereby playing the roles of sterilization, disinfection and detoxification. (2) Rapidity: after the ozone reaches a certain degree (the content of ozone per gram is 8-9.6mg), pathogenic microorganisms can be killed within seconds to minutes, and the ozone is the fastest one of the known disinfectants. (3) Safety: the acute toxicity test of ozone shows that LD50 is more than 500mg/kg, which is nontoxic and has no stimulation to skin, mucosa and eyes. Because healthy cells have a strong oxidation balance enzyme system, ozone is harmless and nontoxic to healthy cells, and byproducts generated after pathogenic microorganisms are killed by ozone are oxygen and gaseous water molecules. (4) Penetrability: because O3 has small molecular weight and strong penetrating action on cell tissue, can penetrate 2mm into mucosa and quickly penetrate into the inner wall of pathogenic microorganism cell. (5) No drug resistance: because of the action mechanism of ozone, the genetic material of pathogenic microorganisms is directly decomposed, irreversible death occurs, and the medicine is different from common antibiotics and antiviral ointments, so that the medicine resistance is not generated. (6) The dual property: the byproducts generated by ozone killing and killing pathogenic microorganisms are oxygen and gaseous water molecules which can be absorbed by cell tissues, accelerate blood circulation and promote the healing of the skin of an affected part.
The product of the international leading ozone curing technology, namely the ozonized oil, has been greatly developed in the aspects of treatment such as antibiosis, antiphlogosis, detoxification and the like, and gradually replaces antibiotics in European medicine, and the use safety value refers to the national standard. (ozone conversion: 1 ppm-2.14 mg/m)3) The net content of the bacteriostatic ozone oil is about 30 g-30000 mg (mg), the pure ozone contained in each gram is 8.5-9.5 mg, (the ozone curing value is the highest in the industry, and the sterilization effect is greatly reduced when the ozone contained in each gram is cured by less than 6.5 mg) the ozone contained in each mg of ozone oil<0.0096 mg<0.0045ppm and the bacteriostatic ozone oil adopts Solldify ozone curing technology, and the ozone content in the ozone oil is still in a slow release state in the using process. Therefore, the safe use standard value of the bacteriostatic ozone oil is far smaller than the ozone hazard value set by the state.
The low-temperature plasma activated oil is similar to ozone oil and is a substitute of the ozone oil. The peroxide value of the low-temperature plasma activated oil is 8 times that of ozone oil, and the acid value of the low-temperature plasma activated oil is 1.7 times that of the ozone oil. The low-temperature plasma activated oil also contains rich active particles with long service life, the high-efficiency bactericidal property and the skin repair factor can reach 12 months under normal temperature storage, and the treatment process of the low-temperature plasma activated oil has no pollutant discharge, extremely low energy consumption and better application and development prospects.
SUMMERY OF THE UTILITY MODEL
To the problem, the utility model provides a preparation facilities of low temperature plasma active oil, its oil curtain that utilizes low temperature plasma and plasma discharge space to form contacts, and the treatment effeciency is high, effectual, and the processing procedure does not have any pollutant emission, and the energy consumption is extremely low, and the active oil of preparation contains multiple active material, and peroxide number and acid number are far greater than conventional ozone oil.
The utility model discloses a following technical scheme realizes.
A low temperature plasma active oil preparation facilities which characterized in that includes: the device comprises a low-temperature plasma reaction box, a cup-shaped grounding electrode, a high-voltage electrode, an oil storage box, an oil inlet pipe, an oil outlet pipe, an oil pump arranged on the oil inlet pipe, an air inlet pipe arranged at the top of the low-temperature plasma reaction box and a booster pump arranged on the air inlet pipe;
the cup-shaped grounding electrode is arranged in the low-temperature plasma reaction box and is hermetically connected with the bottom surface of the low-temperature plasma reaction box so as to form an oil curtain cavity for containing oil to be treated; the high-voltage electrode is arranged on the side wall of the low-temperature plasma reaction box in a surrounding manner around the cup-shaped grounding electrode so as to form a plasma discharge space between the high-voltage electrode and the cup-shaped grounding electrode; one end of the oil inlet pipe is communicated with the bottom of the oil storage tank, and the other end of the oil inlet pipe is communicated with the bottom of the oil curtain cavity; the oil outlet pipe is communicated with the bottom of the plasma discharge space.
As a specific technical scheme, the high-voltage electrode is a ring-shaped mesh high-voltage electrode.
As a specific technical scheme, an oil outlet pipe valve is arranged on the oil outlet pipe.
As a specific technical scheme, a ventilation valve is arranged on the air inlet pipe.
As a specific technical scheme, the oil pump is a bidirectional oil pump.
As a specific technical scheme, a detachable box cover is arranged at the top of the low-temperature plasma reaction box, and the air inlet pipe is arranged on the box cover.
The utility model has the advantages that: the utility model discloses low temperature plasma active oil preparation facilities's simple structure, the cost of manufacture is low, and it contacts through the oil curtain of low temperature plasma and plasma discharge space formation, can increase the area of contact reaction of low temperature plasma and grease by a wide margin to can carry out continuous processing to the grease, have the characteristics that the treatment effeciency is high, the treatment effect is good, and the processing procedure does not have any pollutant emission, and the energy consumption is extremely low, has better popularization application prospect.
Drawings
FIG. 1 is a schematic structural view of a low-temperature plasma active oil preparation apparatus of the present invention;
FIG. 2 is a cross-sectional view A-A of FIG. 1;
the meanings of the marks in the above figures are as follows: 1-low temperature plasma reaction box, 101-box cover, 2-cup-shaped grounding electrode, 3-high voltage electrode, 4-oil storage box, 5-oil inlet pipe, 6-oil outlet pipe, 601-oil outlet pipe valve, 7-oil pump, 8-air inlet pipe, 9-oil curtain cavity, 10-plasma discharge space, 11-oil curtain, 12-booster pump and 13-raw oil.
Detailed Description
The technical solution of the present invention will be described clearly and completely with reference to the accompanying drawings, and obviously, the described embodiments are some, but not all embodiments of the present invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of 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", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," "third," and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
Example 1
A low-temperature plasma active oil preparation device, please refer to fig. 1 and fig. 2, which comprises: the device comprises a low-temperature plasma reaction box 1, a cup-shaped grounding electrode 2, a high-voltage electrode 3, an oil storage box 4 (the oil storage box 4 is used for storing raw oil 13 to be treated), an oil inlet pipe 5, an oil outlet pipe 6, an oil pump 7 arranged on the oil inlet pipe 5, an air inlet pipe 8 arranged at the top of the low-temperature plasma reaction box 1 and a booster pump 12 arranged on the air inlet pipe 8;
the cup-shaped grounding electrode 2 is arranged in the low-temperature plasma reaction box 1 and is hermetically connected with the bottom surface of the low-temperature plasma reaction box 1 to form an oil curtain cavity 9 for containing oil to be treated; the high-voltage electrode 3 is arranged on the side wall of the low-temperature plasma reaction box 1 around the cup-shaped grounding electrode 2 so as to form a plasma discharge space 10 between the high-voltage electrode 3 and the cup-shaped grounding electrode 2; one end of the oil inlet pipe 5 is communicated with the bottom of the oil storage tank 4, and the other end of the oil inlet pipe is communicated with the bottom of the oil curtain cavity 9; the oil outlet pipe 6 is communicated with the bottom of the plasma discharge space 10;
the utility model discloses low temperature plasma active oil preparation facilities's theory of operation as follows:
starting a booster pump 12 to enable the pressure in the plasma discharge space 10 to reach working pressure, then starting an oil pump 7 to pump raw oil 13 into an oil curtain cavity 9, with the continuous pumping of the raw oil 13, filling the oil in the oil curtain cavity 9 with the oil, then slowly overflowing the raw oil from the oil curtain cavity 9, forming an oil curtain 11 on the outer side surface of the oil curtain cavity 9, namely the surface of the cup-shaped grounding electrode 2, then starting the cup-shaped grounding electrode 2 and the high-voltage electrode 3 to enable low-temperature plasma to be formed in the plasma discharge space 10, enabling the low-temperature plasma to be in contact reaction with the continuously flowing oil curtain 11, after the reaction is finished, generating low-temperature plasma active oil at the bottom of the plasma discharge space 10, and collecting and transferring the low-temperature plasma active oil through the oil outlet pipe 6.
Further, in a preferred embodiment, the high voltage electrode 3 is a ring-mesh high voltage electrode.
Further, in a preferred embodiment, referring to fig. 1, a drain pipe valve 601 is disposed on the drain pipe 6.
Further, in a preferred embodiment, a vent valve 801 is provided on the air inlet pipe 8.
Further, in a preferred embodiment, the oil pump 7 is a bi-directional oil pump; after the work is finished, the oil in the oil curtain cavity 9 can be pumped back to the oil storage tank 4, so that the oil curtain cavity 9 can be cleaned conveniently.
Further, in order to facilitate maintenance of the apparatus and cleaning of the inside, in a preferred embodiment, referring to fig. 1, a detachable cover 101 is provided on the top of the low temperature plasma reaction chamber 1, and the air inlet pipe 8 is provided on the cover 101.
Claims (6)
1. A low temperature plasma active oil preparation facilities which characterized in that includes: the device comprises a low-temperature plasma reaction box (1), a cup-shaped grounding electrode (2), a high-voltage electrode (3), an oil storage box (4), an oil inlet pipe (5), an oil outlet pipe (6), an oil pump (7) arranged on the oil inlet pipe (5), an air inlet pipe (8) arranged at the top of the low-temperature plasma reaction box (1), and a booster pump (12) arranged on the air inlet pipe (8);
the cup-shaped grounding electrode (2) is arranged in the low-temperature plasma reaction box (1) and is hermetically connected with the bottom surface of the low-temperature plasma reaction box (1) to form an oil curtain cavity (9) for containing oil to be treated; the high-voltage electrode (3) is arranged on the side wall of the low-temperature plasma reaction box (1) in a surrounding manner of the cup-shaped grounding electrode (2) so as to form a plasma discharge space (10) between the high-voltage electrode (3) and the cup-shaped grounding electrode (2); one end of the oil inlet pipe (5) is communicated with the bottom of the oil storage tank (4), and the other end of the oil inlet pipe is communicated with the bottom of the oil curtain cavity (9); the oil outlet pipe (6) is communicated with the bottom of the plasma discharge space (10).
2. A low-temperature plasma active oil production apparatus according to claim 1, wherein said high voltage electrode (3) is a ring-mesh high voltage electrode.
3. A low-temperature plasma active oil production apparatus according to claim 1, wherein an oil outlet pipe valve (601) is provided on the oil outlet pipe (6).
4. A low temperature plasma active oil production apparatus as claimed in claim 1, wherein said air introducing pipe (8) is provided with a ventilation valve (801).
5. A low-temperature plasma active oil production apparatus according to claim 1, wherein said oil pump (7) is a bidirectional oil pump.
6. A low-temperature plasma active oil preparation device as claimed in any one of claims 1 to 5, characterized in that a detachable box cover (101) is arranged on the top of the low-temperature plasma reaction box (1), and the air inlet pipe (8) is arranged on the box cover (101).
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| CN202020149568.0U CN211936875U (en) | 2020-01-30 | 2020-01-30 | Low-temperature plasma active oil preparation device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111167389A (en) * | 2020-01-30 | 2020-05-19 | 李智 | Low-temperature plasma active oil preparation device and preparation method |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111167389A (en) * | 2020-01-30 | 2020-05-19 | 李智 | Low-temperature plasma active oil preparation device and preparation method |
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Effective date of registration: 20210621 Address after: 423600 Zhongshan formation, Hexi village, Chengping Township, Anren County, Chenzhou City, Hunan Province Patentee after: Li Guang Address before: 410000 No.97 Jiefang East Road, Furong district, Changsha City, Hunan Province Patentee before: Li Zhi |
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Effective date of registration: 20211110 Address after: 410699 rooms 304, 305 and 306, 3 / F, building 6, Miaosheng international business incubation port, Xinkang Avenue, economic development zone, Ningxiang County, Changsha City, Hunan Province Patentee after: Hunan Daren Flour Industry Co.,Ltd. Address before: 423600 Zhongshan Group, Hexi village, Chengping Township, Anren County, Chenzhou City, Hunan Province Patentee before: Li Guang |
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