CN207775182U - A kind of orange oil distillation processing concentrator - Google Patents
A kind of orange oil distillation processing concentrator Download PDFInfo
- Publication number
- CN207775182U CN207775182U CN201721770753.6U CN201721770753U CN207775182U CN 207775182 U CN207775182 U CN 207775182U CN 201721770753 U CN201721770753 U CN 201721770753U CN 207775182 U CN207775182 U CN 207775182U
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- China
- Prior art keywords
- tower body
- pipe
- tower
- orange oil
- collector
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model is related to distill manufacture field,More particularly to a kind of orange oil distillation processing concentrator,Including destilling tower and collector,Destilling tower includes tower body,Reaction bench,Heater and venthole,Heater is fixed in tower body,Reaction bench is fixed at tower body bottom,The lower end radii of reaction bench is equal with tower body radius,Annular diversion trench is formed between the upper end side wall and tower body madial wall of reaction bench,And depth is gradually increased by left side to the right side of tower body,Slot bottom side wall positioned at the diversion trench on right side offers flow-guiding mouth,Flow-guiding mouth is connected by second pipe with collector,When start-up operation,Liquid runs down tower body inner wall, which is taken advantage of a situation, to be slid into diversion trench,Since the depth of diversion trench gradually increases from left side to right side,Liquid is collected on the right side of being flowed into diversion trench,And it is sent into collector and is concentrated by flow-guiding mouth and second pipe,The utility model improves the oil yield of sweet orange oil,It avoids due to collecting the case where oil plant deficiency leads to waste.
Description
Technical field
The utility model is related to distill manufacture field more particularly to a kind of orange oil distillation processing concentrator.
Background technology
Orange oil is orange fruit through the obtained essential oil of steam distillation, is one of a small number of contrastimulant essential oils, has
Sweet tea sweet orange fragrance, the insomnia caused by intense strain and pressure, improvement anxiety, the diaphoretic effect of energy, people can be expelled
Very early can utilize orange fruit by steam distillation method processing produce orange oil, but traditional orange oil processing side
Method is there are long processing time, time cost is high and energy expenditure is big defect.
Invention content
The purpose of this utility model provides a kind of orange oil distillation processing concentration and sets mainly according to insufficient present on
It is standby.
To achieve the goals above, the technical solution of the utility model is：
A kind of orange oil distillation processing concentrator, including destilling tower and collector, the destilling tower include tower body, reaction
Platform, heater and the steam (vapor) outlet being opened at the top of the tower body, the venthole is by first pipe and is located at the collection
First charging aperture at the top of device is connected, and the heater is fixed in the tower body, and the reaction bench is fixed at described
Tower body bottom, the lower end radii of the reaction bench is equal with the tower body radius, and the lower end of the reaction bench and the tower body
It is tightly connected, forms annular diversion trench, and the diversion trench between the upper end side wall of the reaction bench and the tower body madial wall
Depth gradually increased by left side to the right side of the tower body, the slot bottom side wall positioned at the diversion trench on right side offers water conservancy diversion
Mouthful, the flow-guiding mouth is connected by second pipe with the second charging aperture positioned at the collector bottom sidewall.
Preferably, the reaction bench top offers the groove for placing converted products.
Preferably, blender is equipped in the groove.
Preferably, the destilling tower further includes the vacuum pump for being fixed at the tower body outer wall, and the side wall of the tower body is opened
Equipped with gas outlet, the gas outlet is connected by escape pipe with the vacuum pump, and the escape pipe is equipped with motor-driven valve.
Preferably, the destilling tower further includes pressure sensor, temperature sensor and controller, the pressure sensor,
The temperature sensor is set in the tower body, and the controller is fixed at outside the tower body, the pressure sensor and institute
Temperature sensor is stated to electrically connect with the controller.
Preferably, back-shaped pipe distilling apparatus, the back-shaped pipe distillation dress are equipped between the destilling tower and the collector
It sets including back-shaped pipe and condenser, the back-shaped pipe is set in the condenser, one end of the back-shaped pipe and the pipeline phase
Connection, one end of the back-shaped pipe is connected with the first pipe, and the other end of the back-shaped pipe passes through pipeline and described the
One feed inlet is connected, and the condenser includes set on the coolant outlet of the condenser overhead and set on the condenser
The coolant inlet pipe of bottom.
Preferably, the collector bottom is equipped with discharge gate, and the discharge gate is equipped with valve.
As a result of above technical scheme, the utility model has the advantages that：The destilling tower of the utility model
Collected except distillate except through venthole, reaction bench be also provided in the tower body bottom of destilling tower, the side wall of reaction bench with
Diversion trench is formed between tower body inner wall, by setting, when destilling tower is started to work, the steam for evaporating formation encounters the interior of tower body
After wall formed liquid and adhere to in tower body inner wall, liquid runs down tower body inner wall take advantage of a situation slide and fall into diversion trench, due to water conservancy diversion
The depth of slot gradually increases from left side to right side, liquid flowed into diversion trench on the right side of be collected, and pass through flow-guiding mouth and
Two pipelines are sent into collector, by setting, are improved the oil yield efficiency of sweet orange oil, are only passed through venthole compared to traditional
To the method that oil plant carries out distillation collection, the utility model can effectively save the distillation process time of orange oil, to save
Time cost and the consumption for reducing energy.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
In figure：1, destilling tower；11, tower body；111, gas outlet；112, escape pipe；113, motor-driven valve；12, reaction bench；
121, groove；122, blender；13, heater；14, venthole；141, first pipe；151, flow-guiding mouth；152, second pipe；
16, vacuum pump；17, pressure sensor；18, temperature sensor；19, controller；2, collector；21, first charging aperture；22,
Two feed inlets；3, back-shaped pipe distilling apparatus；31, back-shaped pipe；32, condenser；321, coolant outlet；322, coolant inlet
Pipe.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
It removes, be fully described by, wherein the drawings are for illustrative purposes only and are merely schematic diagrams rather than pictorial diagram, Bu Nengli
Solution is the limitation to this patent；In order to better illustrate the utility model embodiment, the certain components of attached drawing have omission, amplification
Or reduce, do not represent the size of actual product；It will be understood by those skilled in the art that certain known features and its explanation in attached drawing
It may omit and will be understood by.
The described embodiments are only a part of the embodiments of the utility model for the utility model, rather than whole implementation
Example.Based on the embodiments of the present invention, those of ordinary skill in the art are obtained without making creative work
The every other embodiment obtained, shall fall within the protection scope of the present invention.
Embodiment is described in detail：
Such as Fig. 1, a kind of orange oil distillation processing concentrator, including destilling tower 1 and collector 2, the destilling tower 1 include
Tower body 11, reaction bench 12, heater 13 and the venthole 14 for being opened in the top of the tower body 11, the venthole 14 pass through the
One pipeline 141 is connected with the first charging aperture 21 positioned at 2 top of the collector, and the heater 13 is fixed at described
In tower body 11, the reaction bench 12 is fixed at 11 bottom of the tower body, the lower end radii of the reaction bench 12 and the tower body
11 radiuses are equal, and the lower end of the reaction bench 12 and the tower body 11 are tightly connected, the upper end side wall of the reaction bench 12 with
Annular diversion trench 15 is formed between 11 madial wall of the tower body, and the depth of the diversion trench 15 is by the left side of the tower body 11
Gradually increase to right side, flow-guiding mouth 151, the flow-guiding mouth 151 are offered positioned at the slot bottom side wall of the diversion trench 15 on right side
It is connected with the collector 2 by second pipe 152.
The destilling tower of the utility model is collected except through venthole 14 except distillate, in the tower body bottom of destilling tower 1
It is also provided with reaction bench 12, diversion trench 15 is formed between 1 inner wall of side wall and tower body of reaction bench 12, by setting, when destilling tower 1
When start-up operation, evaporate formation steam encounter the inner wall of tower body 11 after form liquid and adhere to on 11 inner wall of tower body, liquid
It takes advantage of a situation along 11 inner wall of tower body and slides and fall into diversion trench 15, since the depth of diversion trench 15 gradually increases from left side to right side,
Liquid is collected on the right side of being flowed into diversion trench 15, and is sent into collector 2 by flow-guiding mouth 151 and second pipe 152, is led to
Setting is crossed, the oil yield efficiency of sweet orange oil is improved, distillation collection is only carried out to oil plant by venthole compared to traditional
Method, the utility model can effectively save the distillation process time of orange oil, to save time cost and reduce energy
Consumption.
In the present embodiment, 12 top of the reaction bench offers the groove 121 for placing converted products, the groove
Blender 122 is equipped in 121, it would be desirable to which the sweet orange of processing is first passed through to be crushed in advance and is put into groove 121 later, and sweet orange is distilling
Start, by thermal distillation, by the way that blender 122 is arranged, sweet orange can be directed at while distilling and carries out flange stirring, makes sweet orange in tower 1
It is heated evenly in destilling tower 1, improves the effect of distillation.
In the present embodiment, the destilling tower 1 further includes the vacuum pump 16 for being fixed at 11 outer wall of the tower body, the tower
The side wall of body 11 offers gas outlet 111, and the gas outlet 111 is connected by escape pipe 112 with the vacuum pump 16, described
Escape pipe 112 is equipped with motor-driven valve 113.Vacuum pump 16 carries out vacuumize process to destilling tower 1 and collector 2 in advance, reduces production
While the boiling point of product is to reduce energy expenditure but also the discharge of extra air avoid generating in distillation process it is extra
Impurity, to improve the purity of distillation.
In the present embodiment, the destilling tower 1 further includes pressure sensor 17, temperature sensor 18 and controller 19, institute
Pressure sensor 17, the temperature sensor 18 are stated in the tower body 11, the controller 19 is fixed at the tower body
Outside 11, the pressure sensor 17, the temperature sensor 18, the vacuum pump 16, the heater 13 with the control
Device 19 electrically connects.Tower body internal pressure and temperature, pressure sensing are monitored in real time by pressure sensor 17 and temperature sensor 18
Device 17 and temperature sensor 18 transmit a signal to controller 19, and controller 19 controls vacuum pump 16 and heater 13 is opened and closed
It closes, makes the more flexible convenience of operating process.
In the present embodiment, it is additionally provided with back-shaped pipe distilling apparatus 3 between the destilling tower 1 and the collector 2, described time
Shape pipe distilling apparatus 3 includes back-shaped pipe 31 and condenser 32, and the back-shaped pipe 31 is set in the condenser 32, the back-shaped pipe
31 one end is connected with the first pipe 141, and one end of the back-shaped pipe 31 is connected with the first pipe 141, institute
The other end for stating back-shaped pipe 31 is connected by pipeline with the first charging aperture 21, and the condenser 32 includes set on described cold
The coolant outlet 321 at 32 top of condenser and the coolant inlet pipe 322 set on 32 bottom of the condenser, the collector
2 bottoms are equipped with discharge gate 23, and the discharge gate 23 is equipped with valve 24；The sweet orange oil gas for distilling and generating by destilling tower 1
Body enters back-shaped pipe distilling apparatus by first pipe 141 and is condensed, and sweet orange oil gas is condensed into essential oil liquid, stream
Enter in collector, completes the collection work of the whole steams generated in 1 process of destilling tower.
Obviously, above-described embodiment of the utility model patent is only intended to clearly illustrate made by the utility model patent
Citing, and it is not the restriction to the embodiment of the utility model patent.For those of ordinary skill in the art,
Other different forms of changes or modifications may be made based on the above description.There is no need and unable to all realities
The mode of applying is exhaustive.It is all within the spirit and principle of the utility model patent made by any modification, equivalent replacement and change
Into etc., it should be included within the utility model scope of the claims.
Claims (7)
1. a kind of orange oil distillation processing concentrator, it is characterised in that:Including destilling tower (1) and collector (2), the distillation
Tower (1) includes tower body (11), reaction bench (12), heater (13) and the venthole (14) being opened at the top of the tower body (11),
The venthole (14) is connected by first pipe (141) with the first charging aperture (21) at the top of the collector (2),
The heater (13) is fixed in the tower body (11), and the reaction bench (12) is fixed at the tower body (11) bottom,
The lower end radii of the reaction bench (12) is equal with the tower body (11) radius, and the lower end of the reaction bench (12) and the tower
Body (11) is tightly connected, and annular diversion trench is formed between the upper end side wall and the tower body (11) madial wall of the reaction bench (12)
(15), and the depth of the diversion trench (15) is gradually increased by left side to the right side of the tower body (11), is located at the described of right side
The slot bottom side wall of diversion trench (15) offers flow-guiding mouth (151), the flow-guiding mouth (151) by second pipe (152) be located at
The second charging aperture (22) of collector (2) bottom sidewall is connected.
2. a kind of orange oil distillation processing concentrator according to claim 1, it is characterised in that:The reaction bench (12)
Top offers the groove (121) for placing converted products.
3. a kind of orange oil distillation processing concentrator according to claim 2, it is characterised in that：The groove (121)
It is interior to be equipped with blender (122).
4. a kind of orange oil distillation processing concentrator according to claim 1, it is characterised in that:The destilling tower (1)
Further include the vacuum pump (16) for being fixed at the tower body (11) outer wall, the side wall of the tower body (11) offers gas outlet
(111), the gas outlet (111) is connected by escape pipe (112) with the vacuum pump (16), on the escape pipe (112)
Equipped with motor-driven valve (113).
5. a kind of orange oil distillation processing concentrator according to claim 1, it is characterised in that:The destilling tower (1)
Further include pressure sensor (17), temperature sensor (18) and controller (19), the pressure sensor (17), the temperature pass
Sensor (18) is set in the tower body (11), and the controller (19) is fixed at the tower body (11) outside, the pressure sensing
Device (17) and the temperature sensor (18) are electrically connected with the controller (19).
6. a kind of orange oil distillation processing concentrator according to claim 1, it is characterised in that:The destilling tower (1)
Back-shaped pipe distilling apparatus (3) is additionally provided between the collector (2), the back-shaped pipe distilling apparatus (3) includes back-shaped pipe
(31) and condenser (32), the back-shaped pipe (31) are set in the condenser (32), one end of the back-shaped pipe (31) and institute
It states first pipe (141) to be connected, the other end of the back-shaped pipe (31) is connected by pipeline with the first charging aperture (21)
Logical, the condenser (32) includes being set to coolant outlet (321) at the top of the condenser (32) and set on the condensation
The coolant inlet pipe (322) of device (32) bottom.
7. a kind of orange oil distillation processing concentrator according to claim 1, it is characterised in that：The collector (2)
Bottom is equipped with discharge gate (23), and the discharge gate (23) is equipped with valve (24).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721770753.6U CN207775182U (en) | 2017-12-18 | 2017-12-18 | A kind of orange oil distillation processing concentrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721770753.6U CN207775182U (en) | 2017-12-18 | 2017-12-18 | A kind of orange oil distillation processing concentrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207775182U true CN207775182U (en) | 2018-08-28 |
Family
ID=63226438
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721770753.6U Expired - Fee Related CN207775182U (en) | 2017-12-18 | 2017-12-18 | A kind of orange oil distillation processing concentrator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207775182U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115200772A (en) * | 2022-07-19 | 2022-10-18 | 上海捷氢科技股份有限公司 | Pressure sensor and proton exchange membrane fuel cell system |
-
2017
- 2017-12-18 CN CN201721770753.6U patent/CN207775182U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115200772A (en) * | 2022-07-19 | 2022-10-18 | 上海捷氢科技股份有限公司 | Pressure sensor and proton exchange membrane fuel cell system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180828 Termination date: 20201218 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |