CN206613497U - Ozone vegetable oil production device and manufacturing equipment - Google Patents
Ozone vegetable oil production device and manufacturing equipment Download PDFInfo
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- CN206613497U CN206613497U CN201720370137.5U CN201720370137U CN206613497U CN 206613497 U CN206613497 U CN 206613497U CN 201720370137 U CN201720370137 U CN 201720370137U CN 206613497 U CN206613497 U CN 206613497U
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- retort
- ozone
- vegetable oil
- holding vessel
- oil production
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Abstract
The utility model is related to pharmacy technique with the apparatus field, more particularly, to ozone vegetable oil production device and manufacturing equipment.Ozone vegetable oil production device, including：Retort and holding vessel；The upper end of the retort and the holding vessel is connected by the first pipeline communication, the retort with the lower end of the holding vessel by second pipe；First pipeline is obliquely installed and first pipeline is higher than first pipeline close to the holding vessel end close to one end of the retort.With alleviate exist in the prior art ozone production yield is small and the high technical problem of cost.
Description
Technical field
The utility model is related to pharmacy technique with the apparatus field, is set more particularly, to ozone vegetable oil production device and manufacture
It is standby.
Background technology
Ozone vegetable oil has widely used, easy to use, cheap etc., is increasingly subject to the favor of people, market is needed
Ask increasing.
Vegetable oil easily absorbs ozone preferably during low temperature, but vegetable oil and ozone gas reaction are exothermic reactions, if reaction
It is larger that speed can raise soon the temperature in reaction column, and ozone easily resolves into oxygen when meeting high temperature so that ozone vegetable oil production
During needed for ozone concentration it is low, greatly reduce production efficiency, and ozone plant oil machine in the market all has production
The oily low problem of efficiency, while being possible to explode (ozone carburetion is a kind of peroxide).
Current vegetable oil typically uses single reaction post bubbling mode with ozone reaction.This reactive mode is only used in small batches
Amount production, for a large amount of production ozone vegetable oil of factory, someone is roused using cooling means to anti-post to cool, and its production cost is high,
Also do not save.
Utility model content
The purpose of this utility model is to provide a kind of ozone vegetable oil production device and manufacturing equipment, to alleviate existing skill
Exist in art ozone production yield is small and the high technical problem of cost.
A kind of ozone vegetable oil production device that the utility model is provided, including：Retort and holding vessel；
The top of the retort and the holding vessel by the first pipeline communication, the retort and the holding vessel
Bottom is connected by second pipe；
First pipeline is obliquely installed and first pipeline is managed close to one end of the retort higher than described first
Road is close to the holding vessel end.
Further, the first magnetic valve and flowmeter are disposed with the second pipe；
First magnetic valve is positioned close to one end of the holding vessel.
Further, the second pipe is connected with flowline, and the flowline is arranged on first magnetic valve and stream
Between gauge, the second magnetic valve is provided with the flowline.
Further, in addition to control the first magnetic valve and the second magnetic valve opening and closing time controller；
The time controller is provided with multiple regulation and control buttons.
Further, gas outlet and air inlet are additionally provided with the retort；
The gas outlet is arranged on the top of the retort, and the air inlet is arranged on the side wall of the retort.
Further, in addition to porous aeration head, porous aeration head enters in the retort through the air inlet, smelly
Oxygen is entered in retort by the porous aeration head.
Further, the diameter ratio of the retort and the holding vessel is 1:2-1:3.
Further, the first pipeline is higher than the connector 50-80mm of holding vessel in the connector of retort.
Further, the top of the holding vessel is provided with oil inlet.
A kind of manufacturing equipment of ozone vegetable oil, including ozone collection device and ozone vegetable oil collection device are described smelly
Oxygen collection device is connected with gas outlet, and the ozone vegetable oil collection device is connected with flowline.
A kind of ozone vegetable oil production device that the utility model is provided, including：Retort and holding vessel；The retort
With the upper end of the holding vessel by the first pipeline communication, the lower end of the retort and the holding vessel is connected by second pipe
It is logical；First pipeline is obliquely installed and first pipeline is leaned on close to one end of the retort higher than first pipeline
The nearly holding vessel end.With alleviate exist in the prior art ozone production yield is small and the high technical problem of cost.
Brief description of the drawings
, below will be right in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
The accompanying drawing used required in embodiment or description of the prior art is briefly described, it should be apparent that, describe below
In accompanying drawing be some embodiments of the present utility model, for those of ordinary skill in the art, do not paying creativeness
On the premise of work, other accompanying drawings can also be obtained according to these accompanying drawings.
The front view for the ozone vegetable oil production device that Fig. 1 provides for the utility model embodiment；
The front view of the holding vessel for the ozone vegetable oil production device that Fig. 2 provides for the utility model embodiment；
The front view of the retort for the ozone vegetable oil production device that Fig. 3 provides for the utility model embodiment；
The top view for the ozone vegetable oil production device that Fig. 4 provides for the utility model embodiment.
Icon：1- retort；2- holding vessels；11- gas outlets；12- air inlets；21- oil inlets；The pipelines of 100- first；
200- second pipes；The porous aeration heads of 300-；The magnetic valves of 210- first；220- flowmeters；The magnetic valves of 230- second.
Embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with accompanying drawing, it is clear that described
Embodiment is a part of embodiment of the utility model, rather than whole embodiments.Based on the embodiment in the utility model, sheet
The every other embodiment that field those of ordinary skill is obtained under the premise of creative work is not made, belongs to this reality
With novel protected scope.
, it is necessary to explanation in description of the present utility model, term " " center ", " on ", " under ", it is "left", "right", " perpendicular
Directly ", the orientation or position relationship of the instruction such as " level ", " interior ", " outer " are, based on orientation shown in the drawings or position relationship, to be only
Described for the ease of description the utility model and simplifying, rather than to indicate or imply that signified device or element must have specific
Orientation, with specific azimuth configuration and operation, therefore it is not intended that to limitation of the present utility model.In addition, term " the
One ", " second ", " the 3rd " are only used for describing purpose, and it is not intended that indicating or implying relative importance.
, it is necessary to which explanation, unless otherwise clearly defined and limited, term " are pacified in description of the present utility model
Dress ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or integratedly
Connection；Can be mechanical connection or electrical connection；Can be joined directly together, can also be indirectly connected to by intermediary,
It can be the connection of two element internals.For the ordinary skill in the art, above-mentioned art can be understood with concrete condition
Concrete meaning of the language in the utility model.
Embodiment 1
The front view for the ozone vegetable oil production device that Fig. 1 provides for the utility model embodiment, Fig. 2 is the utility model
The front view of the holding vessel for the ozone vegetable oil production device that embodiment is provided；Fig. 3 for the utility model embodiment provide it is smelly
The front view of the retort of oxygen vegetable oil production device；The ozone vegetable oil production dress that Fig. 4 provides for the utility model embodiment
The top view put.As Figure 1-4, a kind of ozone vegetable oil production device that the utility model is provided, including：The He of retort 1
Holding vessel 2；
The retort 1 is connected with the upper end of the holding vessel by the first pipeline 100, the retort 1 and the storage
The lower end for depositing tank is connected by second pipe 200；
First pipeline 100 be obliquely installed and first pipeline 100 close to one end of the retort 1 higher than described
First pipeline 100 is close to the end of holding vessel 2.
Wherein, retort 1 and the shape of holding vessel 2 can have diversified forms, for example：Toot, cylinder are described
Device or square etc., and retort 1 and the shape of storage tank 2 can be different.
Wherein, the material of the first pipeline 100 and second pipe 200 can have a variety of, for example：Stainless steel, synthetic resin material
Material, aluminium alloy and plastics etc..
Wherein, a diameter of 200MM of retort 1, a diameter of 500MM of holding vessel 2, plus the height of vegetable oil is 800MM, once
About 180L ozone carburetion can be produced, flow is being passed through for 5M3/h, when ozone concentration is 40G/M3 ozone gas, is needing 15-20 small
When.
Wherein, the first pipeline 100 and second pipe 200 on be provided with anticorrosive coat, anticorrosive coat can be in the first pipeline
100 and second pipe 200 on be painted with raw lacquer, urushiol resin paint, phenolic resin coating, epoxy-phenolic paint, chlorinated polyvinyl chloride paints and
Inorganic zinc rich paint etc.；
Wherein, raw lacquer (also referred to as lacquer).Taupe thick liquid, with acid resistance, solvent resistance, water-resistance, oil resistivity,
The advantages of wearability and strong adhesive force.
Phenolic resin coating.With good electrical insulating property and oil resistivity, 60% sulfuric acid, hydrochloric acid, certain density vinegar are resistant to
The dielectric corrosion such as acid and phosphoric acid, most of salts and organic solvent, remaining is not enumerated secondary.
In the present embodiment, retort 1 is connected with the upper end of holding vessel by the first pipeline 100, retort 1 and the storage
The lower end of tank is connected by second pipe 200；First pipeline 100 is obliquely installed and the first pipeline 100 is close to one end of retort 1
Higher than the first pipeline 100 close to the end of holding vessel 2；When retort 1 is reacted, the reaction solution of part passes through the first pipeline
100 enter in holding vessel 2, and the liquid levels rise in holding vessel 2, liquid is being back to retort 1 by second pipe 200
In, to increase the speed of reaction, improve the output of ozone carburetion and reduce the cost of production.
On the basis of above-described embodiment, further, the first magnetic valve is disposed with the second pipe 200
210 and flowmeter 220；
First magnetic valve 210 is positioned close to one end of the holding vessel 2.
In the present embodiment, first magnetic valve 210, flowmeter 220 are set close to one end of holding vessel 2 in second pipe 200
It is arranged between the first magnetic valve 210 and retort 1, holding vessel 2 is adjusted to retort by the setting of the first magnetic valve 210
The regulation of the break-make of liquid and flow in 1, then show by flowmeter 220 fluid flow of the holding vessel 2 into retort 1
Statistics, in order to preferably adjust the first magnetic valve 210, so as to proper amount of liquid ensure that in retort 1, to increase
The speed of reaction, improves the speed of production, circulation primary when regulation flow velocity makes whole liquid per 1-2.
On the basis of above-described embodiment, further, the second pipe 200 is connected with flowline, the flowline
It is arranged between first magnetic valve 210 and flowmeter 220, the second magnetic valve 230 is provided with the flowline.
In the present embodiment, second pipe 200 is connected with flowline, and be arranged on the first magnetic valve 210 and flowmeter 220 it
Between, after the reaction solution in retort 1 and holding vessel 2 is reacted to the defined time, by the second magnetic valve 230 and the first electromagnetism
Valve 210 is opened simultaneously, the ozone carburetion that reaction completes to produce is flowed out by the second battery valve.
On the basis of above-described embodiment, further, in addition to the first magnetic valve 210 of control and the second magnetic valve 230
The time controller of opening and closing；
The time controller is provided with multiple regulation and control buttons.
Wherein, time controller be it is a kind of connecting or disconnecting for circuit can be controlled according to the time of setting, also
It is the switching device of control apparatus, with following advantages：
1. the open and close time is arbitrarily adjustable；
2. the open and close time mixed up is not power failure influence, automatic Memory；
3. can be automatic, it is also manually controllable, provided with automatic safety device；
4. interior consumption power is low.
In the present embodiment, the first magnetic valve 210 and the control of the second magnetic valve 230 passage time controller are specifically being given birth to
Staff that can be according to scene during production or the requirement of reaction, so as to enter to the regulation and control knob on time controller
Row regulation, so that the reaction solution in retort 1 and holding vessel 2 can obtain in time sufficiently reaction, control retort 1 and storage
Reaction solution circulation in tank 2, also, do not need staff to nurse reactor always, to reduce the operating pressure of staff.
The front view of the retort for the ozone vegetable oil production device that Fig. 3 provides for the utility model embodiment.Such as Fig. 3 institutes
Show, on the basis of above-described embodiment, further, gas outlet 11 and air inlet 12 are additionally provided with the retort 1；
The gas outlet 11 is arranged on the top of the retort 1, and the air inlet 12 is arranged on the side of the retort 1
On wall.
In the present embodiment, the top of retort 1 is provided with gas outlet 11, air inlet is provided with the side wall of retort 1
Mouth 12, reacting gas is entered in retort 1 by air inlet 12, because gas can not carry out sufficient with reaction solution
Reaction, the complete gas of unreacted is discharged by gas outlet 11, and gas treatment equipment can be connected outside outlet, with
Reacted gas is handled, meanwhile, gas outlet 11 is also shed a part of heat produced by reaction, Ke Yiyou
Effect slows down the heat in retort 1, improves the efficiency of reaction.
On the basis of above-described embodiment, further, in addition to porous aeration head 300, porous aeration head 300 passes through institute
State air inlet 12 to enter in the retort 1, ozone is entered in retort 1 by the porous aeration head 300.
Wherein, aeration head is higher than the bottom 15-20cm of retort 1.
Wherein, aeration head principle is：Aeration is a kind of means for making air be contacted strongly with water, and its object is to by air
In oxygen be dissolved in the water, or unwanted gas and volatile materials in water are banished in air；It is to promote gas
A kind of means of mass exchange between liquid.
Feature is：
1. producing and maintaining effective air-water to contact, and protected in the case where biological oxidation constantly consumes oxygen
Certain dissolved oxygen concentration in water holding；
2. circulating for enough immixture and water is produced in aeration zone.
In the present embodiment, porous aeration head 300 is provided with the air inlet 12 of retort 1, when ozone passes through aeration head
Enter in reaction solution, ozone can be made sufficiently to be reacted with reaction solution, so as to add the speed of ozone reaction liquid reaction
Spend, and the utilization of ozone is also improved simultaneously, to reduce the cost of production.
The top view for the ozone vegetable oil production device that Fig. 4 provides for the utility model embodiment.As shown in figure 4, upper
State on the basis of embodiment, further, the diameter ratio of the retort 1 and the holding vessel 2 is 1:2-1:Between 3.
In the present embodiment, the diameter ratio of retort 1 and holding vessel 2 is 1:2-1:Between 3, so, when reacting one in retort 1
After the section time, the partially liq in retort 1 is entered in holding vessel 2 by the first pipeline 100, and the diameter of holding vessel 2 is big
In the diameter of retort 1, the liquid after being reacted in holding vessel 2 can be made not to be back to again in retort 1 as far as possible, with
Improve the speed of production of ozone carburetion.
On the basis of above-described embodiment, further, the first pipeline 100 is higher than holding vessel 2 in the connector of retort 1
Connector 50-80mm.
In the present embodiment, the first pipeline 100 is higher than the connector 50-80mm of holding vessel 2 in the connector of retort 1, when
After ozone and reaction solution carry out blistering reaction in retort 1, partially liq is entered in holding vessel 2 by the first pipeline 100,
Because the first pipeline 100 is higher than the connector 50-80mm of holding vessel 2 in the connector of retort 1, when liquid liquid in holding vessel 2
When face is higher than the liquid level of liquid in retort 1, backflow will not be produced, and the liquid between retort 1 and holding vessel 2 will not be made
It is that drop is too high to flow through, to improve the stability of single unit system reaction.
The front view of the holding vessel for the ozone vegetable oil production device that Fig. 2 provides for the utility model embodiment.Such as Fig. 2 institutes
Show, on the basis of above-described embodiment, further, the top of the holding vessel 2 is provided with oil inlet 21.
In the present embodiment, the top of holding vessel 2 is provided with oil inlet 21, so, can according to the speed of reaction or
It is after reaction is completed successively, holding vessel 2 to be carried out more facilitating during injection reaction solution again.
The overall work process of device, the porous aeration head 300 that ozone gas is entered in retort 1 by air inlet 12 exposes
Gas head height is in reaction pot bottom 15-20cm, because the effect liquid level rise of air-flow makes partially liq overflow through upper first pipeline 100
Flow into holding vessel 2.First pipeline 100 is higher than the connection end of holding vessel 2 in the connection end of retort 1, and its liquid level is in holding vessel 2 during charging
Below connection end, liquid is set not flow back.
Retort 1 is connected with the recessed bottom bottom second pipe 200 of holding vessel 2, and being also due to the effect of air-flow makes
Liquid passes back into retort 1 from holding vessel 2.Reacted waste gas is discharged by gas outlet 11.The inside of bottom second pipe 200 is set
There are the first magnetic valve 210 and flowmeter 220, for adjusting flow velocity and viewing flow, regulation flow velocity is followed when making whole liquid per 1-2
Ring is once.Retort 1 and a diameter of the 1 of holding vessel 2:2-1:3, a diameter of 200mm of retort, a diameter of 500mm of holding vessel 2,
Plus the height of vegetable oil is 800mm, can once produce about 180L ozone carburetion, flow is being passed through for 5M3/h, ozone concentration is
During 40G/M3 ozone gas, need 15-20 hours.
Embodiment 2
A kind of manufacturing equipment of ozone vegetable oil, including ozone collection device and ozone vegetable oil collection device are described smelly
Oxygen collection device is connected with gas outlet 11, and the ozone vegetable oil collection device is connected with flowline.
In the present embodiment, the manufacturing equipment of ozone vegetable oil includes ozone collection device and ozone vegetable oil collection device,
Ozone collection device is by the unreacted gas collection in retort 1, in order to avoid being polluted to air, ozone vegetable oil is collected
Device is connected with flowline is collected reacted ozone carburetion.
Finally it should be noted that：Various embodiments above is only limited to illustrate the technical solution of the utility model, rather than to it
System；Although the utility model is described in detail with reference to foregoing embodiments, one of ordinary skill in the art should
Understand：It can still modify to the technical scheme described in foregoing embodiments, or to which part or whole
Technical characteristic carries out equivalent substitution；And these modifications or replacement, the essence of appropriate technical solution is departed from this practicality newly
The scope of each embodiment technical scheme of type.
Claims (10)
1. a kind of ozone vegetable oil production device, it is characterised in that including：Retort (1) and holding vessel (2)；
The retort (1) is connected with the top of the holding vessel (2) by the first pipeline (100), the retort (1) and institute
The bottom for stating holding vessel (2) is connected by second pipe (200)；
First pipeline (100) is obliquely installed, and first pipeline (100) is higher than close to one end of the retort (1)
First pipeline (100) is held close to the holding vessel (2).
2. ozone vegetable oil production device according to claim 1, it is characterised in that in the second pipe (200) according to
It is secondary to be provided with the first magnetic valve (210) and flowmeter (220)；
First magnetic valve (210) is positioned close to one end of the holding vessel (2).
3. ozone vegetable oil production device according to claim 2, it is characterised in that the second pipe (200) is with going out
Oil pipe is connected, and the flowline is arranged between first magnetic valve (210) and flowmeter (220), set on the flowline
It is equipped with the second magnetic valve (230).
4. ozone vegetable oil production device according to claim 3, it is characterised in that also including controlling the first magnetic valve
(210) and the second magnetic valve (230) opening and closing time controller；
The time controller is provided with multiple regulation and control buttons.
5. ozone vegetable oil production device according to claim 4, it is characterised in that also set up on the retort (1)
There are gas outlet (11) and air inlet (12)；
The gas outlet (11) is arranged on the top of the retort (1), and the air inlet (12) is arranged on the retort (1)
Side wall on.
6. ozone vegetable oil production device according to claim 5, it is characterised in that also including porous aeration head (300),
Porous aeration head (300) enters in the retort (1) through the air inlet (12), and ozone passes through the porous aeration head
(300) enter in retort (1).
7. ozone vegetable oil production device according to claim 6, it is characterised in that the retort (1) and the storage
The diameter ratio for depositing tank (2) is 1:2-1:3.
8. ozone vegetable oil production device according to claim 1, it is characterised in that the first pipeline (100) is in retort
(1) connector is higher than the connector 50-80mm of holding vessel (2).
9. ozone vegetable oil production device according to claim 1, it is characterised in that the top of the holding vessel (2) is set
It is equipped with oil inlet (21).
10. a kind of manufacturing equipment of ozone vegetable oil, with the ozone vegetable oil production dress as described in claim any one of 1-9
Put, it is characterised in that including ozone collection device and ozone vegetable oil collection device, the ozone collection device and gas outlet
(11) connect, the ozone vegetable oil collection device is connected with flowline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720370137.5U CN206613497U (en) | 2017-04-10 | 2017-04-10 | Ozone vegetable oil production device and manufacturing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720370137.5U CN206613497U (en) | 2017-04-10 | 2017-04-10 | Ozone vegetable oil production device and manufacturing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206613497U true CN206613497U (en) | 2017-11-07 |
Family
ID=60236035
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720370137.5U Active CN206613497U (en) | 2017-04-10 | 2017-04-10 | Ozone vegetable oil production device and manufacturing equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN206613497U (en) |
Cited By (2)
| 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 |
| CN107989830A (en) * | 2017-11-21 | 2018-05-04 | 佛山汇众森泰科技有限公司 | A kind of novel environment friendly Pulp pump overcurrent equipment |
-
2017
- 2017-04-10 CN CN201720370137.5U patent/CN206613497U/en active Active
Cited By (2)
| 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 |
| CN107989830A (en) * | 2017-11-21 | 2018-05-04 | 佛山汇众森泰科技有限公司 | A kind of novel environment friendly Pulp pump overcurrent equipment |
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