CN208660428U - A kind of volatilization oil recovery apparatus - Google Patents
A kind of volatilization oil recovery apparatus Download PDFInfo
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- CN208660428U CN208660428U CN201821212373.5U CN201821212373U CN208660428U CN 208660428 U CN208660428 U CN 208660428U CN 201821212373 U CN201821212373 U CN 201821212373U CN 208660428 U CN208660428 U CN 208660428U
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Abstract
The utility model discloses a kind of volatilization oil recovery apparatus, the device includes separator, collector, extractor and condenser, separator includes inlet, liquid outlet and separator body, extractor, condenser, inlet, liquid outlet and extractor are sequentially connected, the one side wall of separator is provided with collection port, and collecting pipe crosses collection port；Inlet is arranged with protection cap close to one end of condenser；Inlet includes glass inlet, and inlet is provided with graduation mark, and graduation mark includes the first graduation mark, the second graduation mark and third graduation mark；Baffle is additionally provided with inside inlet, one end of baffle is fixedly connected on the inner wall of inlet, and the other end of baffle is hanging；The inner wall of separator is provided with insulating layer, adherent layer, and adherent layer, insulating layer, inner wall are successively mutually adhered.In the utility model, by the way that graduation mark, baffle is arranged in inlet and coating is arranged in separator inner wall, it is separated from water oil more thorough, the recycling of volatile oil is also more thorough.
Description
Technical field
The utility model relates to the field of environment protection equipment of recycling more particularly to a kind of volatilization oil recovery apparatus.
Background technique
Volatile oil refers to the solvent flashing that extraction is steamed from crude oil.The volatile oil of Chinese herbal medicine or extraction containing volatile oil is big
Has the effects that sweating, qi-regulating, analgesic, antibacterial more.
The acquisition process of volatile oil can mainly be distilled out jointly using volatile oil with water vapour.Existing volatile oil recycling
Device includes inlet, liquid outlet and overflow port.In use process, the oil mixing with water gas evaporated from extractor is through being subcooled
Solidifying pipework condensation becomes oil mixing with water liquid, and oil mixing with water liquid enters through the inlet of device, after static separation, volatile oil
It flows out by overflow port, is collected through collection device；And water reenters in extractor by liquid outlet.
In the prior art, it is not thorough since volatile oil is separated from water, unsegregated volatile oil comes back to by liquid outlet
Extractor, so that volatile oil recycling is not thorough.More thorough in order to recycle volatile oil, the utility model provides one kind and waves
Hair oil recyclable device.
Utility model content
The utility model provides a kind of volatilization oil recovery apparatus, is asked with solving the halfway technology of existing volatile oil recycling
Topic.
To solve the above-mentioned problems, the utility model provides technical solution below:
A kind of volatilization oil recovery apparatus, including separator, collector, extractor and condenser, in which: separator include into
One end of liquid mouth, liquid outlet and separator body, inlet and condenser by inlet tube connect, the other end of condenser with mention
The gas outlet of tank is taken to connect by connecting tube, the refluxing opening of extractor is connect with liquid outlet by outlet tube, the side of separator
Wall is provided with collection port, and collecting pipe crosses collection port, and both ends are separately connected separator and collector；Inlet and separator sheet
Body is fixedly connected, and liquid outlet and separator body are integrally formed, and inlet one end close to condenser is arranged with protection cap, is protected
Base face is provided with gas vent and inlet opening；Inlet includes glass inlet, and inlet is provided with graduation mark, and graduation mark includes
First graduation mark, the second graduation mark and third graduation mark, the first graduation mark and third graduation mark are respectively arranged at the two of inlet
End, the second graduation mark includes multiple graduation marks, and is set between the first graduation mark and third graduation mark；It is also set inside inlet
It is equipped with baffle, one end of baffle is fixedly connected on the inner wall of inlet, and the other end of baffle is suspended on inside inlet；Separator
Inner wall be provided with coating, coating includes insulating layer, adherent layer, and insulating layer is mutually adhered with inner wall, and adherent layer is mutually sticked with insulating layer
Even.
Preferably, there are two baffle plate settings, and two baffles are juxtaposed on inlet inner wall.
Preferably, the shape of two baffles is L-type, and baffle is elastic baffle.
Preferably, separator body includes stainless steel separator ontology.
Preferably, the size of inlet opening and the size of inlet tube match.
Preferably, liquid outlet is provided with the first movable valve, and collector is provided with the second movable valve.
The utility model provides a kind of volatilization oil recovery apparatus, which includes separator, collector, extractor and cold
Condenser.Relationship between each component: separator includes inlet, liquid outlet and separator body, and the one of inlet and condenser
End is connected by inlet tube, and the other end of condenser and the gas outlet of extractor are connected by connecting tube, the refluxing opening of extractor
It is connect with liquid outlet by outlet tube.In use process, the oil mixing with water gas extracted from extractor is cold by condenser
Solidifying to become oil mixing with water liquid, oil mixing with water liquid enters separator through inlet tube.Due to the difference of oil and the physical characteristic of water,
After static separation after a period of time, volatile oil is separated from water into two layers, and volatile oil is on upper layer, and water is in lower layer.In order to divide
The volatile oil recycling separated out, is provided with collection port in the one side wall of separator, collecting pipe crosses collection port, and both ends are separately connected
Separator and collector.In use process, volatile oil is flowed out by collecting pipe by separator, is flowed into collector and is received
Collection.In order to keep separator more stable, inlet is fixedly connected with separator body, liquid outlet and separator body one at
Type.In order to prevent during water-oil separating, there is dust to fall into separator, is arranged with guarantor in inlet one end close to condenser
Protecting cover, protection cap bottom surface are provided with inlet opening.Since oil mixing with water gas becomes cold during oil mixing with water liquid by condensation
It is solidifying to be not thorough so that in oil mixing with water liquid mixing and doping oil mixing with water gas, mixing liquid enter separation by inlet
When device, the air pressure of separator is more than or less than ambient pressure, and in order to keep inside and outside air pressure balance, protection cap bottom surface is provided with row
Stomata.The case where in order to have a clear understanding of mixing liquid position in the separator and water-oil separating, inlet includes glass feed liquor
Mouthful, inlet is provided with graduation mark, and graduation mark includes the first graduation mark, the second graduation mark and third graduation mark, the first graduation mark
The both ends of inlet are respectively arranged at third graduation mark, the second graduation mark includes multiple graduation marks, and is set to the first scale
Between line and third graduation mark.First graduation mark is the upper limit of mixing liquid in the separator, when the liquid level of oil mixing with water liquid
When reaching the first graduation mark, stop feed liquor；Third graduation mark is that oil collects the lower limit stopped, when oil is lower than third graduation mark,
Stop collecting oil.The amount for learning the volatile oil of collection can be understood by multiple graduation marks of the second graduation mark.In order to make from into
The mixing liquid that fluid apertures enters inlet slowly enters separator, does not destroy the stability of existing separator liquid surface, into
Baffle is additionally provided with inside liquid mouth, one end of baffle is fixedly connected on the inner wall of inlet, and the other end of baffle is suspended on feed liquor
Mouth is internal.In order to make oil reduce adherency of the oil to separator during the feed liquor of separator, separation and collection, in separator
Inner wall be provided with coating, coating includes insulating layer and adherent layer, and insulating layer is mutually adhered with inner wall, and adherent layer is mutually sticked with insulating layer
Even.The setting of insulating layer is to reduce the probability that high-temperature electric conduction causes oily spontaneous combustion, and the setting of adherent layer is right in order to reduce oil
The adherency of separator reduces the collecting amount of oil.In the utility model, feed liquor is adjusted in time by the way that graduation mark is arranged in inlet
With the situation for collecting oil, separation in time and collection oil.Baffle is set further through in inlet, reduces oil mixing with water liquid to original
The destruction of page balance, so that oil is separated from water faster, also more thoroughly.Coating is set finally by separator inner wall, is subtracted
Few oily adherency in separator inner wall, oily collection are more thorough.In the utility model, by inlet be arranged graduation mark,
Baffle and coating is set in separator inner wall, is separated from water oil more thorough, reduces repeated isolation and collect oily.
Detailed description of the invention
It, below will be to attached drawing needed in the embodiment in order to illustrate more clearly of the technical solution of the utility model
It is briefly described, it should be apparent that, for those of ordinary skills, in the premise of not making the creative labor property
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is a kind of structural schematic diagram for volatilization oil recovery apparatus that utility model provides；
Fig. 2 is a kind of structural schematic diagram for coating that utility model provides；
Fig. 3 is a kind of structural schematic diagram for protection cap that utility model provides；
Detailed description of the invention: 1- separator, 2- collector, 3- extractor, 4- condenser, 11- inlet, 12- liquid outlet, 13-
Separator body, 14- collection port, 21- collecting pipe, the second movable valve of 22-, the gas outlet 31-, 32- refluxing opening, 41- inlet tube,
111- protection cap, 112- graduation mark, 113- baffle, 114- coating, 121- outlet tube, the first movable valve of 122-, 1111- exhaust
Hole, 1112- inlet opening, the first graduation mark of 1121-, the second graduation mark of 1122-, 1123- third graduation mark, 1141- insulating layer,
1142- adherent layer.
Specific embodiment
Referring to Fig. 1, for a kind of structural schematic diagram for the oil recovery apparatus that volatilizees provided by the utility model；It referring to fig. 2, is this
A kind of structural schematic diagram for coating that utility model provides；It is that a kind of structure for protection cap that utility model provides is shown referring to Fig. 3
It is intended to.In conjunction with Fig. 1, Fig. 2 and Fig. 3 it is found that the utility model provides a kind of volatilization oil recovery apparatus, which includes separator
1, collector 2, extractor 3 and condenser 4.Relationship between each component: separator 1 includes inlet 11, liquid outlet 12 and divides
From device ontology 13, inlet 11 is connect with one end of condenser 4 by inlet tube 41, the other end and the extractor 3 of condenser 4
Gas outlet 31 is connected by connecting tube, and the refluxing opening 32 of extractor 3 is connect with liquid outlet 12 by outlet tube 121.Use process
In, the oil mixing with water gas extracted from extractor 3 becomes oil mixing with water liquid, oil-water mixture by the condensation of condenser 4
Body enters separator 1 through inlet tube 41.Due to the difference of oil and the physical characteristic of water, after static separation after a period of time,
Volatile oil is separated from water into two layers, and volatile oil is on upper layer, and water is in lower layer.In order to recycle the volatile oil isolated, in separator 1
One side wall be provided with collection port 14, collecting pipe 21 crosses collection port 14, and both ends are separately connected separator 1 and collector 2.Make
With in the process, volatile oil is flowed out by collecting pipe 21 by separator 1, is flowed into collector 2 and is collected.In order to make separator
1 is more stable, and inlet 11 is fixedly connected with separator body 13, and liquid outlet 12 and separator body 13 are integrally formed.In order to
During preventing water-oil separating, there is dust to fall into separator 1, is arranged with protection in 11 one end of inlet close to condenser 4
Lid 111,111 bottom surface of protection cap are provided with inlet opening 1112.Since oil mixing with water gas becomes oil mixing with water liquid by condensation
In the process condensation be not thorough so that in oil mixing with water liquid mixing and doping oil mixing with water gas, mixing liquid pass through inlet
When 11 entrance separator 1, the air pressure of separator 1 is more than or less than ambient pressure, in order to keep inside and outside air pressure balance, protection cap
111 bottom surfaces are provided with gas vent 1111.In order to have a clear understanding of the feelings of position and water-oil separating of the mixing liquid in separator 1
Condition, inlet 11 include glass inlet, and inlet 11 is provided with graduation mark 112, and graduation mark 112 includes the first graduation mark
1121, the second graduation mark 1122 and third graduation mark 1123, the first graduation mark 1121 and third graduation mark 1123 are respectively arranged at
The both ends of inlet 11, the second graduation mark 1122 includes multiple graduation marks, and is set to the first graduation mark 1121 and third scale
Between line 1123.First graduation mark 1121 is the upper limit of the mixing liquid in separator 1, when the liquid level of oil mixing with water liquid reaches
When the first graduation mark 1121, stop feed liquor；Third graduation mark 1123 is that oil collects the lower limit stopped, when oil is lower than third graduation mark
When 1123, stop collecting oil.The amount for learning the volatile oil of collection can be understood by multiple graduation marks of the second graduation mark 1122.
In order to make the mixing liquid for entering inlet 11 from inlet opening 1112 slowly enter separator 1, existing 1 liquid of separator is not destroyed
The stability on surface, is additionally provided with baffle 113 inside inlet 11, and one end of baffle 113 is fixedly connected on inlet 11
Inner wall, the other end of baffle 113 are suspended on inside inlet 11.In order to make oil in the feed liquor of separator 1, separation and the mistake of collection
Adherency of the oil to separator 1 is reduced in journey, the inner wall of separator 1 is provided with coating 114, coating 114 includes insulating layer 1141
With adherent layer 1142, insulating layer 1141 is mutually adhered with inner wall, and adherent layer 1142 is adhered with 1141 phase of insulating layer.Insulating layer 1141
Setting is to reduce the probability that high-temperature electric conduction causes oily spontaneous combustion, and the setting of adherent layer 1142 is to reduce oil to separator 1
Adherency, improve oil collecting amount.In the utility model, by inlet 11 be arranged graduation mark 112 in time adjustment feed liquor and
The situation of oil is collected, separation in time and collection oil.Baffle 113 is set further through in inlet 11, reduces oil mixing with water liquid pair
The destruction of original level balance, so that oil is separated from water faster, also more thoroughly.It is applied finally by being arranged in 1 inner wall of separator
Layer 114 reduces oil in the adherency of 1 inner wall of separator, keeps the collection of oil more thorough.In the utility model, by inlet
11 are arranged graduation marks 112, baffle 113 and coating 114 are arranged in 1 inner wall of separator, are separated from water oil more thorough, reduce
Repeated isolation and collect oil.
In order to reduce destruction of the oil mixing with water liquid to existing liquid level for entering separator 1, in the present embodiment, in inlet
11 are internally provided with two baffles 113, and the shape of two baffles 113 is L-type, and baffle 113 is elastic baffle.Elasticity
The baffle 113 of L-type makes oil mixing with water liquid, slowly close to existing liquid level, it is flat to reduce existing liquid level along one side of baffle 113
The destruction of weighing apparatus property, improves the stability of liquid level, so that water-oil separating is more thorough in same time, so that the returning of volatile oil
It receives more thorough.
In order to make the liquid in separator 1 not receive extraneous erosion, and protect the stability of separator 1, the present embodiment
In in, separator body 13 include stainless steel separator ontology.Stainless steel separator ontology can provide the steady of structure for separator 1
It is qualitative, and stainless steel separator ontology has the characteristic of insulation and thermal insulation, reduces what the liquid in separator 1 was corroded by the external world
Chance improves the rate of recovery of volatile oil.
Enter in separator 1 to reduce extraneous dust, in the present embodiment, be provided with protection cap 111, in protection cap 111
It is provided with inlet opening 1112, and the size of inlet opening 1112 and the size of inlet tube 41 match.When the size of inlet opening 1112
Greater than inlet tube 41 size when, dust be easy by inlet opening 1112 enter separator 1 in；When inlet tube 41 and inlet opening
When 1112 size matches, reduces external dust and enter in separator 1 and pollute volatile oil, reduce the recycling of volatile oil.
In order to keep the recycling of oil more thorough, in the present embodiment, liquid outlet 12 is provided with the first movable valve 122, collector 2
It is provided with the second movable valve 22.Since the static separation of grease needs the time, when liquid level of the oil mixing with water liquid in separator 1
When reaching the first graduation mark 1121, oil mixing with water liquid stops entering in separator 1, and after static a period of time, water-oil separating is opened,
At this point, opening the second movable valve 22 in collector 2, volatile oil reaches in collector 2 by collecting pipe 21, when liquid level reaches
When third graduation mark 1123, the second movable valve 22 in collector 2 is closed, stops collecting volatile oil.At this point, opening liquid outlet
12 the first movable valve 122, so that water is transported in extractor 3 by outlet tube 121.By the way that the first movable valve is arranged
122 and second movable valve 22, so that the recycling of oil is more thorough.
Those skilled in the art will readily occur to the utility model after considering the embodiment of specification and practice here
Other embodiments.The utility model is intended to cover any variations, uses, or adaptations of the utility model, these
Variations, uses, or adaptations follow the general principle of the utility model and including not used skills of the utility model
Common knowledge or conventional techniques in art field.The description and examples are only to be considered as illustrative, the utility model
True scope and spirit are indicated by the following claims.
It should be understood that the utility model is not limited to the accurate knot for being described above and being shown in the accompanying drawings
Structure, and various modifications and changes may be made without departing from the scope thereof.The scope of the utility model is only wanted by appended right
It asks to limit.
Claims (6)
1. a kind of volatilization oil recovery apparatus, which is characterized in that including separator (1), collector (2), extractor (3) and condenser
(4), in which:
The separator (1) includes inlet (11), liquid outlet (12) and separator body (13), the inlet (11) and institute
The one end for stating condenser (4) is connected by inlet tube (41), the other end of the condenser (4) and going out for the extractor (3)
Port (31) is connected by connecting tube, and the refluxing opening (32) of the extractor (3) and the liquid outlet (12) pass through outlet tube
(121) it connecting, the one side wall of the separator (1) is provided with collection port (14), and collecting pipe (21) crosses the collection port (14),
And both ends are separately connected the separator (1) and the collector (2)；
The inlet (11) is fixedly connected with the separator body (13), the liquid outlet (12) and the separator body
(13) it is integrally formed, the inlet (11) one end close to the condenser (4) is arranged with protection cap (111), the protection
Lid (111) bottom surface is provided with gas vent (1111) and inlet opening (1112)；
The inlet (11) includes glass inlet, and the inlet (11) is provided with graduation mark (112), the graduation mark
It (112) include the first graduation mark (1121), the second graduation mark (1122) and third graduation mark (1123), first graduation mark
(1121) and the third graduation mark (1123) is respectively arranged at the both ends of the inlet (11), second graduation mark
(1122) include multiple graduation marks, and be set between first graduation mark (1121) and the third graduation mark (1123)；
It is additionally provided with baffle (113) inside the inlet (11), one end of the baffle (113) is fixedly connected on the feed liquor
The inner wall of mouth (11), it is internal that the other end of the baffle (113) is suspended on the inlet (11)；
The inner wall of the separator (1) is provided with coating (114), and the coating (114) includes insulating layer (1141), adherent layer
(1142), the insulating layer (1141) is mutually adhered with the inner wall, the adherent layer (1142) and the insulating layer (1141) phase
It is adhered.
2. recyclable device according to claim 1, which is characterized in that there are two baffle (113) settings, and two institutes
It states baffle (113) and is juxtaposed on the inlet (11) inner wall.
3. recyclable device according to claim 2, which is characterized in that the shape of two baffles (113) is L-type, and
The baffle (113) is elastic baffle.
4. recyclable device according to claim 1, which is characterized in that the separator body (13) includes stainless steel separation
Device ontology.
5. recyclable device according to claim 1, which is characterized in that the size of the inlet opening (1112) and the feed liquor
The size of pipe (41) matches.
6. recyclable device according to claim 1, which is characterized in that the liquid outlet (12) is provided with the first movable valve
(122), the collector (2) is provided with the second movable valve (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821212373.5U CN208660428U (en) | 2018-07-30 | 2018-07-30 | A kind of volatilization oil recovery apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821212373.5U CN208660428U (en) | 2018-07-30 | 2018-07-30 | A kind of volatilization oil recovery apparatus |
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| Publication Number | Publication Date |
|---|---|
| CN208660428U true CN208660428U (en) | 2019-03-29 |
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ID=65832006
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| Application Number | Title | Priority Date | Filing Date |
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| CN201821212373.5U Active CN208660428U (en) | 2018-07-30 | 2018-07-30 | A kind of volatilization oil recovery apparatus |
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| CN (1) | CN208660428U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110835584A (en) * | 2019-11-29 | 2020-02-25 | 浙江大学 | Simultaneous nitrogen-blowing extraction device and essential oil fidelity extraction method |
-
2018
- 2018-07-30 CN CN201821212373.5U patent/CN208660428U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110835584A (en) * | 2019-11-29 | 2020-02-25 | 浙江大学 | Simultaneous nitrogen-blowing extraction device and essential oil fidelity extraction method |
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