CN205700421U - A kind of equipment efficiently produced for ozone oil - Google Patents
A kind of equipment efficiently produced for ozone oil Download PDFInfo
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- CN205700421U CN205700421U CN201620385733.6U CN201620385733U CN205700421U CN 205700421 U CN205700421 U CN 205700421U CN 201620385733 U CN201620385733 U CN 201620385733U CN 205700421 U CN205700421 U CN 205700421U
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- ozone
- oil
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- coolant
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 183
- 238000002156 mixing Methods 0.000 claims abstract description 151
- 238000012545 processing Methods 0.000 claims abstract description 13
- 230000007246 mechanism Effects 0.000 claims abstract description 12
- 239000002826 coolant Substances 0.000 claims description 86
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 64
- 239000001301 oxygen Substances 0.000 claims description 61
- 229910052760 oxygen Inorganic materials 0.000 claims description 61
- 230000004087 circulation Effects 0.000 claims description 17
- 238000001816 cooling Methods 0.000 claims description 12
- 238000005057 refrigeration Methods 0.000 claims description 11
- 230000003197 catalytic effect Effects 0.000 claims description 8
- 230000017531 blood circulation Effects 0.000 claims description 7
- 239000007789 gas Substances 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 16
- 238000000034 method Methods 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 4
- 239000003921 oil Substances 0.000 description 140
- 235000019198 oils Nutrition 0.000 description 140
- 230000009977 dual effect Effects 0.000 description 8
- 239000000284 extract Substances 0.000 description 8
- 230000037361 pathway Effects 0.000 description 8
- 238000010668 complexation reaction Methods 0.000 description 5
- 239000000110 cooling liquid Substances 0.000 description 5
- 238000004364 calculation method Methods 0.000 description 4
- 230000008676 import Effects 0.000 description 4
- 239000004006 olive oil Substances 0.000 description 3
- 235000008390 olive oil Nutrition 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 201000004624 Dermatitis Diseases 0.000 description 1
- XQFRJNBWHJMXHO-RRKCRQDMSA-N IDUR Chemical compound C1[C@H](O)[C@@H](CO)O[C@H]1N1C(=O)NC(=O)C(I)=C1 XQFRJNBWHJMXHO-RRKCRQDMSA-N 0.000 description 1
- 206010061218 Inflammation Diseases 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 208000010668 atopic eczema Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000003421 catalytic decomposition reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000004054 inflammatory process Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- WURFKUQACINBSI-UHFFFAOYSA-M ozonide Chemical group [O]O[O-] WURFKUQACINBSI-UHFFFAOYSA-M 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 238000007634 remodeling Methods 0.000 description 1
Landscapes
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
A kind of equipment efficiently produced for ozone oil, belongs to pharmacy technique with the apparatus field.It is characterized in that: include mixing arrangement (12), mixing arrangement (12) connects ozone supplied device and raw oil feeding mechanism, mixing arrangement (12) is provided with mixing arrangement ozone oil outlet (1207) and mixing arrangement ozone outlet (1205), ozone supplied device and raw oil feeding mechanism are respectively mixing arrangement (12) supply ozone and raw oil, ozone and raw oil generate ozone oil in mixing arrangement (12) mixing, and blended device ozone oil outlet (1207) output, mixing arrangement ozone outlet (1205) connects ozone processing unit.This achieves the continuous print industrialized production of ozone oil for the equipment that ozone oil efficiently produces, and the manual labor needed in work process is few, alleviates the labor intensity of workman, and production efficiency is high, improves work efficiency.
Description
Technical field
A kind of equipment efficiently produced for ozone oil, belongs to pharmacy technique with the apparatus field.
Background technology
Ozone oil is produced by olive oil and ozone reaction, and constituent is ozone carburetion unsaturated acids fat, and active component is ozonide and peroxide.For treating the inflammation such as various Mucocutaneous diseases, herpes, eczema.
Ozone oil has of many uses, easy to use, low price etc., is increasingly subject to the favor of people, and the market demand is increasing.Substantial amounts of heat energy all can be produced when ozone and olive oil course of reaction and ozonator work, ozone easily resolves into oxygen when meeting high temperature, make ozone concentration required in ozone oil production process low, greatly reduce production efficiency, and ozone oil machine in the market all exists the problems such as oil-producing efficiency is low.
Summary of the invention
The technical problems to be solved in the utility model is: overcome the deficiencies in the prior art, it is provided that a kind of production efficiency is high, realize ozone oil industrialized production, the easy to operate equipment efficiently produced for ozone oil.
This utility model solves its technical problem and be the technical scheme is that this is for equipment that ozone oil efficiently produces, it is characterized in that: include mixing arrangement, mixing arrangement connects ozone supplied device and raw oil feeding mechanism, mixing arrangement is provided with the outlet of mixing arrangement ozone oil and mixing arrangement ozone outlet, ozone supplied device and raw oil feeding mechanism are respectively mixing arrangement supply ozone and raw oil, ozone and raw oil generate ozone oil in mixing arrangement mixing, and the outlet output of blended device ozone oil, mixing arrangement ozone outlet connects ozone processing unit.
Preferably, it is equipped with ozone concentration sensor between described mixing arrangement and ozone supplied device and between mixing arrangement and described ozone processing unit.
Preferably, described ozone processing unit is catalytic destroyer.
Preferably, described ozone supplied device includes source of oxygen and ozonator, connects with described mixing arrangement after the gas outlet series connection ozonator of source of oxygen.
Preferably, oxygen flow sensor it is provided with between described source of oxygen and ozonator.
Preferably, described raw oil feeding mechanism includes raw oil container and oil feed pump, and the oil-in of oil feed pump and raw oil reservoir, oil-out connects with described mixing arrangement.
Preferably, described mixing arrangement connects the blood circulation for making raw oil circulate.
Preferably, described blood circulation includes oil circulating pump, the bottom of described mixing arrangement is provided with mixing arrangement circulation output interface, top is provided with mixing arrangement circulation input interface, the oil-in of oil circulating pump connects with mixing arrangement circulation output interface, and oil-out connects with mixing arrangement circulation input interface.
Preferably, the cooling system for described mixing arrangement and ozone supplied device are cooled down also is included.
Preferably, described cooling system includes coolant casing and refrigeration compressor set, and the coolant in refrigeration compressor set makes the coolant in tank for coolant body lower the temperature by putting in the heat exchange coil in tank for coolant body；Being provided with the heat exchange coil connected with coolant casing in described mixing arrangement, described ozone supplied device connects with the heat exchange coil being arranged in tank for coolant body.
Compared with prior art, the equipment efficiently produced for ozone oil of the present utility model is had the beneficial effect that
1, ozone supplied device and the raw oil of this equipment efficiently produced for ozone oil is respectively mixing arrangement delivery of ozone and raw oil for device, ozone and raw oil mix in mixing arrangement, generate ozone oil, and from the outlet output of mixing arrangement ozone oil, achieve the continuous print industrialized production of ozone oil, and the manual labor needed in work process is few, alleviate the labor intensity of workman, production efficiency is high, improves work efficiency；Unnecessary ozone can be decomposed by the ozone processing unit that mixing arrangement ozone outlet connects, it is to avoid pollutes environment in unnecessary ozone discharge to air.
2, ozone concentration sensor is for measuring input mixing arrangement and the concentration of ozone exported by mixing arrangement, facilitates the complexation concentration of follow-up accurate survey calculation ozone oil.
3, ozone processing unit is catalytic destroyer, and catalytic destroyer makes ozone decomposed become oxygen, and is discharged in air, to free of air pollution.
4, the oxygen that source of oxygen provides is converted into ozone by ozonator, and flows to mixing arrangement, makes this be capable of the production process of whole ozone oil for the equipment that ozone oil efficiently produces, improves automaticity.
5, oxygen flow sensor can measure the flow of the oxygen entered in ozonator, thus conveniently controls the generation speed of ozone, and then the convenient ozone that controls enters the speed of mixing arrangement.
6, in raw oil is contained in raw oil container, raw oil is also transported in mixing arrangement by oil feed pump extraction raw oil, achieve the automatic interpolation of raw oil, oil feed pump can use dosing pump, thus conveniently control amount and the transporting velocity of the raw oil of input mixing arrangement, facilitate the complexation concentration of follow-up survey calculation ozone oil.
7, the raw oil flowing in blood circulation makes mixing arrangement, makes raw oil more fully contact with ozone, thus improves the production efficiency of ozone oil.
8, circulating pump extracts raw oil from mixing arrangement bottom, and in being again inputted into mixing arrangement, makes raw oil form circulation, make raw oil be fully contacted with ozone.
9, mixing arrangement and ozone supplied device are cooled down by cooling system, can effectively reduce mixing arrangement and the temperature of ozone supplied device, it is ensured that ozone concentration is stable, improve the production efficiency of ozone oil.
10, refrigeration compressor set is to the coolant cooling down in tank for coolant body, and the coolant in tank for coolant body is to mixing arrangement and ozone supplied device cooling down, good cooling results, and simple in construction.
Accompanying drawing explanation
Fig. 1 is the structural representation of the equipment efficiently produced for ozone oil.
Fig. 2 is the structural representation of mixing arrangement.
Fig. 3 is the structural representation of coolant casing.
In figure: 1, source of oxygen 2, oxygen valve 3, oxygen flow sensor 4, ozonator 5, ozone oil output interface 6, ozone oil delivery valve 7, raw oil container 8, raw oil input interface 9, oil feed pump 10, delivery valve 11, oil circulating pump 12, mixing arrangement 1201, mixing arrangement circulation input interface
1202, mixing arrangement raw oil import 1203, mixing arrangement coolant inlet 1204, mixing arrangement cooling liquid outlet
1205, mixing arrangement ozone outlet 1206, mixing arrangement ozone inlet 1207, the outlet of mixing arrangement ozone oil
1208, mixing arrangement circulation output interface 13, cabinet
14, dual pathways ozone concentration sensor 15, coolant recirculation pump
16, refrigeration compressor set 17, catalytic destroyer
18, coolant casing 1801, coolant casing oxygen inlet 1802, coolant casing oxygen outlet
1803, the cold entrance of tank for coolant system 1804, the cold outlet of tank for coolant system 1805, coolant loop head
1806, coolant loop exit 19, oxygen input interface.
Detailed description of the invention
Fig. 1 ~ 3 are most preferred embodiments of the present utility model, and 1 ~ 3 pair of this utility model is described further below in conjunction with the accompanying drawings.
A kind of equipment efficiently produced for ozone oil, including mixing arrangement 12, mixing arrangement 12 connects ozone supplied device and raw oil feeding mechanism, mixing arrangement 12 is provided with mixing arrangement ozone oil outlet 1207 and mixing arrangement ozone outlet 1205, ozone supplied device and raw oil feeding mechanism are respectively mixing arrangement 12 and supply ozone and raw oil, ozone and raw oil generate ozone oil in mixing arrangement 12 mixing, and blended device ozone oil outlet 1207 output, mixing arrangement ozone outlet 1205 connects ozone processing unit.Ozone supplied device and the raw oil of this equipment efficiently produced for ozone oil are respectively mixing arrangement 12 delivery of ozone and raw oil for device, ozone and raw oil mix in mixing arrangement 12, generate ozone oil, and from mixing arrangement ozone oil outlet 1207 output, achieve the continuous print industrialized production of ozone oil, and the manual labor needed in work process is few, alleviate the labor intensity of workman, production efficiency is high, improves work efficiency；Unnecessary ozone can be decomposed by the ozone processing unit that mixing arrangement ozone outlet 1205 connects, it is to avoid pollutes environment in unnecessary ozone discharge to air.
Concrete: as shown in Figure 1: mixing arrangement 12 is arranged in cabinet 13, cabinet 13 is rectangular box body, and mixing arrangement 12 is arranged on the top of cabinet 13.
Raw oil feeding mechanism is arranged on cabinet 13 top, and raw oil feeding mechanism includes expecting oil vessel 7 and oil feed pump 9.Oil feed pump 9 is arranged in cabinet 13, and the oil-out of oil feed pump 9 is connected with mixing arrangement 12 by pipeline, and the oil-out of oil feed pump 9 connects with the raw oil input interface 8 being arranged on cabinet 13, and raw oil input interface 8 is fixed on cabinet 13.It is outside that raw oil container 7 is arranged on cabinet 13, and the oil-out of raw oil container 7 is connected with raw oil input interface 8 by pipeline, and raw oil input interface 8 facilitates the dismounting of raw oil container 7 and oil feed pump 9.Oil feed pump 9 extracts the raw oil in raw oil container 7, and is transported in mixing arrangement 12.Oil feed pump 9 can be dosing pump, is convenient for measuring the amount of raw oil in input mixing arrangement 12, thus facilitates the complexation concentration of the ozone oil that follow-up survey calculation produces.Raw oil in the present embodiment is olive oil.
Being provided with delivery valve 10 between the oil-out and mixing arrangement 12 of oil feed pump 9, delivery valve 10 can control the break-make of raw oil, the convenient addition accurately controlling raw oil.
Ozone supplied device is arranged on the bottom at cabinet 13, and ozone supplied device includes source of oxygen 1 and ozonator 4.The ozone outlet of ozonator 4 is connected with mixing arrangement 12 by pipeline, and the oxygen intake of ozonator 4 connects with oxygen input interface 19, and oxygen input interface 19 is fixed on cabinet 13.The oxygen outlet of source of oxygen 1 connects with oxygen input interface 19, and oxygen input interface 19 facilitates the connection of source of oxygen 1 and ozonator 4.Source of oxygen 1 can be oxygen tank.
It is provided with ozone concentration sensor between ozonator 4 and mixing arrangement 12, ozone concentration sensor is dual pathways ozone concentration sensor 14, connects with mixing arrangement 12 after a passage of the ozone outlet series connection dual pathways ozone concentration sensor 14 of ozonator 4；Connect with mixing arrangement ozone oil outlet 1207 after another passage of ozone processing unit series connection dual pathways ozone concentration sensor 14.Ozone processing unit is catalytic destroyer 17, and catalytic destroyer 17 can carry out catalytic decomposition to the ozone of discharge and become oxygen, is then directly discharged in air, will not be to environment.
Oxygen valve 2 and oxygen flow sensor 3 it is provided with between ozonator 4 and oxygen input interface 19, oxygen input interface 19 is sequentially connected in series oxygen valve 2 and connects with oxygen intake with ozonator 4 after oxygen flow sensor 3, oxygen valve 2 can control the break-make of oxygen, thus control the break-make of ozone, oxygen flow sensor 3 can measure the flow of oxygen, and then measures the flow of ozone.Oxygen flow sensor 3 coordinates dual pathways ozone concentration sensor 14, it is possible to the accurately complexation concentration of the ozone oil that survey calculation produces.
Being connected by pipeline bottom mixing arrangement 12 has ozone oil output interface 5, ozone oil output interface 5 to be fixed on cabinet 13, the convenient pipeline that connects of ozone oil output interface 5, thus is transported to the ozone oil of production specify position.Being provided with ozone oil delivery valve 6 between mixing arrangement 12 and ozone oil output interface 5, ozone oil delivery valve 6 can control the break-make of ozone oil output.
Mixing arrangement 12 is provided with blood circulation, blood circulation includes oil circulating pump 11, the oil-in of oil circulating pump 11 connects bottom mixing arrangement 12, the oil-out of oil circulating pump 11 connects with the top of mixing arrangement 12, oil circulating pump 11 extracts the raw oil bottom mixing arrangement 12 and is re-injected in mixing arrangement 12 from top, increase the contact area of raw oil and ozone, greatly improve the production efficiency of ozone oil.
The bottom of cabinet 13 is additionally provided with cooling system, and cooling system includes coolant casing 18 and refrigeration compressor set 16.Coolant casing 18 is fixed on cabinet 13, and coolant casing 18 built with coolant, oxygen input interface 19 enters in oxygen flow sensor 3 after the oxygen cooled liquid inputted cooling, reduces the temperature of ozonator 4, it is ensured that the temperature of ozone concentration.Refrigeration compressor set 16 is arranged on the top of coolant casing 18, and the coolant in coolant casing 18 is lowered the temperature by refrigeration compressor set 16.
Coolant casing 18 is connected with mixing arrangement 12 also by coolant recirculation pump 15, and form circulation, coolant recirculation pump 15 extracts the coolant in coolant casing 18, and make coolant turn again to after mixing arrangement 12 in coolant casing 18, so that mixing arrangement 12 is lowered the temperature by the coolant in coolant casing 18, with the temperature in guarantee mixing arrangement 12, thus ensure the ozone concentration in mixing arrangement 12.
As shown in Figure 2: mixing arrangement 12 is the casing of cuboid, the top of mixing arrangement 12 is sequentially provided with mixing arrangement circulation input interface 1201, mixing arrangement raw oil import 1202, mixing arrangement coolant inlet 1203, mixing arrangement cooling liquid outlet 1204 and mixing arrangement ozone outlet 1205 from left to right；The bottom of mixing arrangement 12 is sequentially provided with mixing arrangement circulation output interface 1208, mixing arrangement ozone oil outlet 1207 and mixing arrangement ozone inlet 1206 from left to right.Mixing arrangement 12 can also be the cylinder of closed at both ends.
Mixing arrangement circulation input interface 1201 connects with the oil-out of oil circulating pump 11, and mixing arrangement circulation output interface 1208 connects with the oil-in of oil circulating pump 11, so that the raw oil in mixing arrangement 12 forms circulation.Mixing arrangement raw oil import 1202 connects with delivery valve 10, and raw oil is entered in mixing arrangement 12 by mixing arrangement raw oil import 1202.
Mixing arrangement coolant inlet 1203 connects with the liquid outlet of coolant recirculation pump 15, and mixing arrangement cooling liquid outlet 1204 connects with coolant casing 18.Mixing arrangement coolant inlet 1203 be positioned at mixing arrangement 12 with mixing arrangement cooling liquid outlet 1204 within one end connected by heat exchange coil, coolant recirculation pump 15 extracts the coolant in coolant casing 18, make coolant again be back in coolant casing 18 behind mixing arrangement 12 inside, thus mixing arrangement 12 is lowered the temperature.
Mixing arrangement ozone outlet 1205 connect dual pathways ozone concentration sensor 14 a passage after connect with catalytic destroyer 17；Mixing arrangement ozone inlet 1206 connect dual pathways ozone concentration sensor 14 another passage after connect with ozonator 4.Mixing arrangement ozone oil outlet 1207 is connected with ozone oil delivery valve 6 by pipeline.
As shown in Figure 3: coolant casing 18 is rectangular box, the left side of coolant casing 18 is sequentially provided with coolant casing oxygen inlet 1801 and coolant casing oxygen outlet 1802 from the bottom to top, coolant casing oxygen inlet 1801 connects with oxygen input interface 19, and coolant casing oxygen outlet 1802 connects with oxygen valve 2.One end that coolant casing oxygen inlet 1801 is positioned at coolant casing 18 with coolant casing oxygen outlet 1802 is connected by heat exchange coil, oxygen enters in oxygen flow sensor 3 after heat exchange coil with coolant heat exchange, thus reduces the temperature of ozonator 4.
The top of coolant casing 18 be sequentially provided with from left to right the cold entrance of tank for coolant system 1803 and the cold outlet of tank for coolant system 1804, the cold entrance of tank for coolant system 1803 and the cold outlet of tank for coolant system 1804 respectively with refrigerant exit and the coolant inlet communication of refrigeration compressor set 16.One end that the cold entrance of tank for coolant system 1803 outlet cold with tank for coolant system 1804 is positioned at coolant casing 18 is connected by heat exchange coil, and the coolant in refrigeration compressor set 16 carries out cooling down by heat exchange coil to the coolant in coolant casing 18.
From top to bottom being sequentially provided with coolant loop head 1805 and coolant loop exit 1806 on the right side of coolant casing 18, coolant loop head 1805 connects with mixing arrangement cooling liquid outlet 1204, and coolant loop exit 1806 connects with coolant recirculation pump 15.
This work process being used for the equipment that ozone oil efficiently produces is as follows, oil feed pump 9 extracts the raw oil in raw oil container 7 and is transported in mixing arrangement 12, oxygen in source of oxygen 1 generates ozone after ozonator 4, also in mixing arrangement 12, oil circulating pump 11 extracts the raw oil in mixing arrangement 12 and is again input in mixing arrangement 12 from top, raw oil is made to increase with the contact area of ozone, improve the production efficiency of ozone oil, ozone oil blended device ozone oil outlet 1207 discharge of generation.
Coolant recirculation pump 15 extracts the coolant in coolant casing 18, mixing arrangement 12 is lowered the temperature, oxygen in source of oxygen 1 enters in ozonator 4 after coolant casing 18, effectively reduces mixing arrangement 12 and the temperature of ozonator 4, it is ensured that stablizing of ozone concentration.
Dual pathways ozone concentration sensor 14 can measure the concentration of the ozone entering mixing arrangement 12 and outflow mixing arrangement 12, such that it is able to draw the flow of ozone gas, and then according to flowing into and out the flow of ozone of mixing arrangement 12 and the amount of raw oil in mixing arrangement 12 can be entered, can accurately calculate the complexation concentration of ozone oil.
The above, it it is only preferred embodiment of the present utility model, being not the restriction that this utility model is made other form, any those skilled in the art are changed possibly also with the technology contents of the disclosure above or are modified as the Equivalent embodiments of equivalent variations.But every without departing from technical solutions of the utility model content, any simple modification, equivalent variations and remodeling above example made according to technical spirit of the present utility model, still fall within the protection domain of technical solutions of the utility model.
Claims (10)
1. the equipment efficiently produced for ozone oil, it is characterized in that: include mixing arrangement (12), mixing arrangement (12) connects ozone supplied device and raw oil feeding mechanism, mixing arrangement (12) is provided with mixing arrangement ozone oil outlet (1207) and mixing arrangement ozone outlet (1205), ozone supplied device and raw oil feeding mechanism are respectively mixing arrangement (12) supply ozone and raw oil, ozone and raw oil generate ozone oil in mixing arrangement (12) mixing, and blended device ozone oil outlet (1207) output, mixing arrangement ozone outlet (1205) connects ozone processing unit.
The equipment efficiently produced for ozone oil the most according to claim 1, it is characterised in that: it is equipped with ozone concentration sensor between described mixing arrangement (12) and ozone supplied device and between mixing arrangement (12) and described ozone processing unit.
The equipment efficiently produced for ozone oil the most according to claim 1 and 2, it is characterised in that: described ozone processing unit is catalytic destroyer (17).
The equipment efficiently produced for ozone oil the most according to claim 1 and 2, it is characterized in that: described ozone supplied device includes source of oxygen (1) and ozonator (4), gas outlet series connection ozonator (4) of source of oxygen (1) connects with described mixing arrangement (12) afterwards.
The equipment efficiently produced for ozone oil the most according to claim 4, it is characterised in that: it is provided with oxygen flow sensor (3) between described source of oxygen (1) and ozonator (4).
The equipment efficiently produced for ozone oil the most according to claim 1, it is characterized in that: described raw oil feeding mechanism includes raw oil container (7) and oil feed pump (9), the oil-in of oil feed pump (9) connects with raw oil container (7), and oil-out connects with described mixing arrangement (12).
The equipment efficiently produced for ozone oil the most according to claim 1, it is characterised in that: described mixing arrangement (12) connects the blood circulation for making raw oil circulate.
The equipment efficiently produced for ozone oil the most according to claim 7, it is characterized in that: described blood circulation includes oil circulating pump (11), the bottom of described mixing arrangement (12) is provided with mixing arrangement circulation output interface (1208), top is provided with mixing arrangement circulation input interface (1201), the oil-in of oil circulating pump (11) connects with mixing arrangement circulation output interface (1208), and oil-out connects with mixing arrangement circulation input interface (1201).
The equipment efficiently produced for ozone oil the most according to claim 1, it is characterised in that: also include the cooling system for described mixing arrangement (12) and ozone supplied device are cooled down.
The equipment efficiently produced for ozone oil the most according to claim 9, it is characterized in that: described cooling system includes coolant casing (18) and refrigeration compressor set (16), the coolant in refrigeration compressor set (16) makes the coolant in coolant casing (18) lower the temperature by putting in the heat exchange coil in coolant casing (18)；Being provided with the heat exchange coil connected with coolant casing (18) in described mixing arrangement (12), described ozone supplied device connects with the heat exchange coil being arranged in coolant casing (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620385733.6U CN205700421U (en) | 2016-05-03 | 2016-05-03 | A kind of equipment efficiently produced for ozone oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620385733.6U CN205700421U (en) | 2016-05-03 | 2016-05-03 | A kind of equipment efficiently produced for ozone oil |
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| CN205700421U true CN205700421U (en) | 2016-11-23 |
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| CN201620385733.6U Active CN205700421U (en) | 2016-05-03 | 2016-05-03 | A kind of equipment efficiently produced for ozone oil |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106861592A (en) * | 2017-04-10 | 2017-06-20 | 安徽嘉宝诺生物科技有限公司 | Ozone oil process units and manufacturing equipment |
| CN106861369A (en) * | 2017-04-12 | 2017-06-20 | 湖北润德堂生物科技有限公司 | A kind of exhaust gas processing device for producing ozone oil |
| CN107335367A (en) * | 2017-09-07 | 2017-11-10 | 深圳欧威奇科技有限公司 | Ozone oil blending tank |
| CN109121278A (en) * | 2018-09-20 | 2019-01-01 | 华中科技大学 | A kind of plasma-activated oil treatment provisions |
| CN109234021A (en) * | 2018-09-26 | 2019-01-18 | 西安科技大学 | A kind of preparation method of medical ozone carburetion |
| CN109589812A (en) * | 2018-12-20 | 2019-04-09 | 常州大学 | A kind of device preparing ozonated water emulsion and preparation process |
| CN110559189A (en) * | 2019-08-20 | 2019-12-13 | 安徽氧趣生物科技有限公司 | Preparation method of dimer and polymer ozone ointment |
-
2016
- 2016-05-03 CN CN201620385733.6U patent/CN205700421U/en active Active
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106861592A (en) * | 2017-04-10 | 2017-06-20 | 安徽嘉宝诺生物科技有限公司 | Ozone oil process units and manufacturing equipment |
| CN106861369A (en) * | 2017-04-12 | 2017-06-20 | 湖北润德堂生物科技有限公司 | A kind of exhaust gas processing device for producing ozone oil |
| CN107335367A (en) * | 2017-09-07 | 2017-11-10 | 深圳欧威奇科技有限公司 | Ozone oil blending tank |
| CN109121278A (en) * | 2018-09-20 | 2019-01-01 | 华中科技大学 | A kind of plasma-activated oil treatment provisions |
| CN109234021A (en) * | 2018-09-26 | 2019-01-18 | 西安科技大学 | A kind of preparation method of medical ozone carburetion |
| CN109234021B (en) * | 2018-09-26 | 2021-10-08 | 陕西福科原力健康科技有限公司 | Preparation method of medical ozonized oil |
| CN109589812A (en) * | 2018-12-20 | 2019-04-09 | 常州大学 | A kind of device preparing ozonated water emulsion and preparation process |
| CN110559189A (en) * | 2019-08-20 | 2019-12-13 | 安徽氧趣生物科技有限公司 | Preparation method of dimer and polymer ozone ointment |
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