CN209412170U - It is a kind of for removing the distillation equipment of camellia seed oil stink - Google Patents
It is a kind of for removing the distillation equipment of camellia seed oil stink Download PDFInfo
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- CN209412170U CN209412170U CN201821932803.0U CN201821932803U CN209412170U CN 209412170 U CN209412170 U CN 209412170U CN 201821932803 U CN201821932803 U CN 201821932803U CN 209412170 U CN209412170 U CN 209412170U
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- chamber
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- removal
- impurities
- steam
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Abstract
It is a kind of for removing the distillation equipment of camellia seed oil stink, including distilling chamber (1), the upper end of distillation chamber (1) is removably connected with reflux removal of impurities chamber (2), it is provided with feed hopper (15) at the top of reflux removal of impurities chamber (2), the first closed switch (16) is provided on the feed hopper (15).The utility model structure is biased to Simple automation, process flow is very simple, it is used cooperatively using distillation chamber and reflux removal of impurities chamber, on the one hand return channel is provided in reflux removal of impurities chamber, it effectively collects condensed water and is led back in reboiler, can largely save steam, on the other hand be provided with steam-distributing pipe and steam is in charge of, the position that steam can be imported to different depth in camellia seed oil, so that the distillation degree of camellia seed oil different location is uniform.
Description
Technical field
The utility model relates to food processing technology fields, and in particular, to a kind of for removing camellia seed oil stink
Distillation equipment.
Background technique
Currently, China not only abounds with the healthy grain and oil such as peanut oil, sunflower oil, the camellia with special role is also abounded with
Oil, camellia oil not only eats deliciousness, and full of nutrition, and camellia oil can generate a small amount of low with peculiar smell during liquefaction
Object is boiled, mainly has aldehyde, ketone, unsaturated hydrocarbon etc., therefore needs the method deodorization by distillation, existing material filling type deodorization
Tower is all made of direct vaporizing extract process and heats to camellia oil, and such method needs to consume a large amount of steam, and not safe enough
Stablize, to the distillation degree of camellia seed oil also because of the position reason that steam imports in distillation process, so that distillation is uneven.
Therefore, it is necessary to a kind of for removing the distillation equipment of camellia seed oil stink.
Utility model content
The purpose of this utility model is that the shortcomings that overcoming the above-mentioned prior art and deficiency, provides a kind of for removing mountain
The distillation equipment of tea-seed oil stink, the utility model structure are biased to Simple automation, and process flow is very simple, using distillation chamber
Be used cooperatively with reflux removal of impurities chamber, be on the one hand provided with return channel in reflux removal of impurities chamber, effectively collect condensed water and by its
It leads back in reboiler, can largely save steam, be on the other hand provided with steam-distributing pipe and steam is in charge of, steam can be imported mountain
The position of different depth in tea-seed oil, so that the distillation degree of camellia seed oil different location is uniform.
The technical scheme in the invention for solving the above technical problem is:
It is a kind of for removing the distillation equipment of camellia seed oil stink, including distillation chamber, the distillation process of camellia seed oil are then
It is carried out in distillation chamber, the upper end of the distillation chamber is removably connected with reflux removal of impurities chamber, and being detachably connected is advantageous in that steaming
Equipment can be disassembled to carry out clean and maintenance after the completion of evaporating, reduce the difficulty of clean and maintenance；The reflux removal of impurities top of chamber is set
It is equipped with feed hopper, needs the camellia seed oil of deodorization to be added in distillation chamber by the feed hopper, and funnelform entrance
It can avoid trickling down when camellia seed oil is added；It is provided with the first closed switch in the feed hopper, adds and ties in camellia seed oil
The first closed switch is closed, guarantees the air-tightness of equipment by Shu Hou；The feed hopper bottom end is provided with passage, described
Passage extend into the top for distilling chamber after passing through the reflux removal of impurities chamber, and the camellia seed oil of addition can be kept away by passage
It opens reflux removal of impurities chamber to be directly entered in distillation chamber, it is intracavitary and/or touch removal of impurities that avoidable camellia seed oil is attached to reflux removal of impurities
Impurity on plate；The middle part of the reflux removal of impurities chamber is detachably provided with removal of impurities plate, is cleaned under coming convenient for removal of impurities plate disassembly；
It is provided with return channel above the removal of impurities plate, which can effectively receive condensed water, and condensed water is avoided to flow back to again
It distills in chamber；Acceleration cooler is provided with above the return channel, environment temperature is higher do not utilize cooling for reflux when, then open
The acceleration cooler is opened, helps to cool down；The return channel connects with the reflux separator tube being arranged on the reflux removal of impurities cavity outer wall
Logical, the reflux separator tube is also connected to return-flow catheter, passes sequentially through reflux separator tube and return-flow catheter, return channel is gathered up
The condensed water come is led back in reboiler；The second closed switch is provided on the return-flow catheter, when not needing to lead back to condensed water
Second closed switch is closed, guarantees the air-tightness of equipment；The return-flow catheter is also connected to reboiler, on the reboiler also
It is communicated with steam lead, the steam of the reboiler qigong is carried out in distillation chamber by steam lead；It is provided on the steam lead
The closed switch of third is closed when not needing that steam is added into distillation chamber, guarantees the airtight of equipment by the closed switch of third
Property；The outer wall that the steam lead passes through the distillation chamber is connected to steam-distributing pipe, if being provided on the steam-distributing pipe
Dry saturated steam is in charge of, and steam-distributing pipe and steam are in charge of the different positions that the steam mean allocation for entering distillation chamber can extremely be distilled to chamber
It sets, the camellia seed oil distillation degree of avoidable portion is overweight and/or kicks the beam；The bottom of the distillation chamber is communicated with discharging
Pipe is released the camellia seed oil after removal of impurities by discharge nozzle after distillation；The 4th is provided on the discharge nozzle closed to open
It closes, in distillation process, the 4th closed switch need to be closed, guarantee the air-tightness of equipment；The end of the discharge nozzle is provided with
Discharging distributor, described discharging distributor one end are connected to oil out duct, the other end of the discharging distributor and fuel-displaced reflux
Conduit is connected to, and is provided with reflux pump on the fuel-displaced return-flow catheter, the end of the fuel-displaced return-flow catheter extends to the pan feeding
The upper end of funnel passes through discharging distributor for camellia seed if the camellia seed oil completed to distillation is also needed further to be distilled
Oil is oriented to fuel-displaced return-flow catheter, is back to feed hopper under the action of reflux pump, if the camellia seed oil no longer completed to distillation
It is further distilled, then camellia seed oil is oriented to by oil out duct by discharging distributor, be introduced directly into camellia seed oil collecting box
In.
Further, the return channel bottom of the return channel is weldingly fixed on the inner wall of the reflux removal of impurities chamber, and institute
The reflux wall for stating return channel is horn shape.
Further, the removal of impurities plate is several, and removal of impurities filler is provided on the removal of impurities plate, and the removal of impurities is filled out
Material can effectively remove the stink impurity of camellia seed oil.
Further, the reflux removal of impurities chamber is also communicated with vacuum tube, and the end of the vacuum tube is provided with vacuum pump, can
Vacuumize process, temperature needed for can reducing stink impurity are carried out to distillation chamber and reflux removal of impurities chamber by vacuum pump.
Further, the steam, which is in charge of, is vertically arranged, vertical with the steam-distributing pipe.
Further, the length that the every steam is in charge of is different, so that the steam being passed through is in camellia seed oil
Depth is different, guarantees that camellia seed oil uniformly distills.
Further, the distillation bottom of chamber portion is additionally provided with several agitating devices, is further ensured that camellia seed oil is uniform
Distillation.
To sum up, the beneficial effects of the utility model are:
The utility model structure is biased to Simple automation, and process flow is very simple, using distillation chamber and reflux removal of impurities chamber
Be used cooperatively, on the one hand reflux removal of impurities chamber in be provided with return channel, effectively collect condensed water simultaneously led back in reboiler,
Steam can be largely saved, steam-distributing pipe is on the other hand provided with and steam is in charge of, steam can be imported different in camellia seed oil
The position of depth, so that the distillation degree of camellia seed oil different location is uniform.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the return channel structural schematic diagram of the utility model.
Wherein, distill chamber 1, reflux removal of impurities chamber 2, reboiler 3, steam lead 4, the closed switch 5 of third, steam-distributing pipe 6,
Steam is in charge of 7, agitating device 8, the 4th closed switch 9, discharge nozzle 10, discharging distributor 11, camellia seed oil collecting box 12, fuel-displaced
Return-flow catheter 13, reflux pump 14, feed hopper 15, the first closed switch 16, passage 17, accelerate cooler 18, return channel 19,
Flow back separator tube 20, return-flow catheter 21, the second closed switch 22, vacuum tube 23, vacuum pump 24, removal of impurities plate 25, oil out duct 26.
Specific embodiment
Direct vaporizing extract process is all made of in order to solve material filling type deodorizing tower in the prior art to heat camellia oil, it is such
Method needs to consume a large amount of steam, and inadequate safety and stability, in distillation process to the distillation degree of camellia seed oil also because
For the position reason that steam imports, so that distilling non-uniform situation, the utility model structure is biased to Simple automation, technique stream
Cheng Feichang is simple, is used cooperatively using distillation chamber and reflux removal of impurities chamber, is on the one hand provided with return channel in reflux removal of impurities chamber,
It effectively collects condensed water and is led back in reboiler, can largely save steam, on the other hand be provided with steam-distributing pipe and steaming
Vapour is in charge of, and steam can be imported to the position of different depth in camellia seed oil, so that the distillation degree of camellia seed oil different location is equal
It is even.Below with reference to examples and drawings, detailed description further, but the embodiment party of the utility model are made to the utility model
Formula is without being limited thereto, and an example of only the utility model application in figure does not have the principles of the present invention essential
Constraint.
Embodiment:
As depicted in figs. 1 and 2, a kind of for removing the distillation equipment of camellia seed oil stink, including distillation chamber 1, camellia seed
The distillation process of oil is carried out in distillation chamber, and the upper end of the distillation chamber 1 is removably connected with reflux removal of impurities chamber 2, removable
Unload connection be advantageous in that distillation after the completion of equipment can be disassembled to carry out clean and maintenance, reduce the difficulty of clean and maintenance；Institute
It states and is provided with feed hopper 15 at the top of reflux removal of impurities chamber 2, the camellia seed oil of deodorization is needed to be added to distillation by the feed hopper
In chamber, and funnelform entrance can avoid trickling down when camellia seed oil is added；It is close that first is provided in the feed hopper 15
Make and break closes 16, after camellia seed oil addition, which is closed, guarantees the air-tightness of equipment；The pan feeding
15 bottom end of funnel is provided with passage 17, and the passage 17 extend into the distillation chamber 1 after passing through the reflux removal of impurities chamber 2
Top, the camellia seed oil of addition can be avoided reflux removal of impurities chamber by passage and be directly entered in distillation chamber, can avoid camellia seed oil
Be attached to reflux removal of impurities it is intracavitary and/or touch removal of impurities plate on impurity；The middle part of the reflux removal of impurities chamber 2 is detachably provided with
Clean plate 25, is cleaned under coming convenient for removal of impurities plate disassembly；The top of the removal of impurities plate 25 is provided with return channel 19, the return channel
Effectively condensed water can be received, condensed water is avoided to be flowed back in distillation chamber again；The top of the return channel 19 is provided with acceleration
Cooler 18, environment temperature is higher do not utilize cooling for reflux when, then open the acceleration cooler, help to cool down；The reflux
Device 19 be arranged in it is described reflux removal of impurities 2 outer wall of chamber on reflux separator tube 20 be connected to, the reflux separator tube 20 also with reflux
Conduit 21 is connected to, and passes sequentially through reflux separator tube and return-flow catheter, the collected condensed water of return channel is led back in reboiler；
It is provided with the second closed switch 22 on the return-flow catheter 21, closes the second closed switch when not needing to lead back to condensed water,
Guarantee the air-tightness of equipment；The return-flow catheter 21 is also connected to reboiler 3, is also communicated with steam lead on the reboiler 3
4, the steam of the reboiler qigong is carried out in distillation chamber by steam lead；The closed switch of third is provided on the steam lead 4
5, when not needing that steam is added into distillation chamber, the closed switch of third is closed, guarantees the air-tightness of equipment；The steam is led
The outer wall that pipe 4 passes through the distillation chamber 1 is connected to steam-distributing pipe 6, is in charge of if being provided with dry saturated steam on the steam-distributing pipe 6
7, steam-distributing pipe and steam are in charge of and can avoid portion by the steam mean allocation for entering distillation chamber to the different location for distilling chamber
The camellia seed oil distillation degree that quartile is set is overweight and/or kicks the beam；The bottom of the distillation chamber 1 is communicated with discharge nozzle 10, is distilling
After, the camellia seed oil after removal of impurities is released by discharge nozzle；The 4th closed switch 9 is provided on the discharge nozzle 10,
In distillation process, the 4th closed switch need to be closed, guarantee the air-tightness of equipment；The end of the discharge nozzle 10 is provided with discharging
Distributor 11, described 11 one end of discharging distributor are connected to oil out duct 26, the other end of the discharging distributor 11 with it is fuel-displaced
Return-flow catheter 13 is connected to, and is provided with reflux pump 14 on the fuel-displaced return-flow catheter 13, the end of the fuel-displaced return-flow catheter 13 is prolonged
The upper end of the feed hopper 15 is extended to, if the camellia seed oil completed to distillation is also needed further to be distilled, passes through discharging
Camellia seed oil is oriented to fuel-displaced return-flow catheter by distributor, is back to feed hopper under the action of reflux pump, if no longer to distillation
The camellia seed oil of completion is further distilled, then camellia seed oil is oriented to oil out duct by discharging distributor, be introduced directly into
In camellia seed oil collecting box 12.
Further in the present embodiment, the return channel bottom 191 of the return channel 19 is weldingly fixed on the reflux and removes
On the inner wall of miscellaneous chamber 2, and the reflux wall 192 of the return channel 19 is horn shape.
Further in the present embodiment, the removal of impurities plate 25 is several, and is provided with and removes on the removal of impurities plate 25
Miscellaneous filler, the removal of impurities filler can effectively remove the stink impurity of camellia seed oil.
Further in the present embodiment, the reflux removal of impurities chamber 2 is also communicated with vacuum tube 23, the end of the vacuum tube 23
End is provided with vacuum pump 24, can carry out vacuumize process to distillation chamber and reflux removal of impurities chamber by vacuum pump, it is miscellaneous can to reduce stink
Temperature needed for matter.
Further in the present embodiment, the steam is in charge of 7 and is vertically arranged, vertical with the steam-distributing pipe 6.
Further in the present embodiment, the length that the every steam is in charge of 7 is different, so that the steam being passed through exists
Depth in camellia seed oil is different, guarantees that camellia seed oil uniformly distills.
Further in the present embodiment, 1 bottom of distillation chamber is additionally provided with several agitating devices 8, further protects
Card camellia seed oil uniformly distills.
Above are merely preferred embodiments of the utility model, the protection scope of the utility model is not limited merely to above-mentioned
Embodiment, technical solution belonging to the idea of the present invention belong to the protection scope of the utility model.It should be pointed out that pair
For those skilled in the art, several improvements and modifications without departing from the principle of the utility model,
It should be regarded as the protection scope of the utility model.
Claims (7)
1. a kind of for removing the distillation equipment of camellia seed oil stink, which is characterized in that including distilling chamber (1), the distillation chamber
(1) upper end is removably connected with reflux removal of impurities chamber (2), is provided with feed hopper (15), institute at the top of reflux removal of impurities chamber (2)
It states and is provided with the first closed switch (16) on feed hopper (15), feed hopper (15) bottom end is provided with passage (17),
The passage (17) extend into the top for distilling chamber (1), the reflux removal of impurities chamber after passing through reflux removal of impurities chamber (2)
(2) middle part is detachably provided with removal of impurities plate (25), is provided with return channel (19), the reflux above the removal of impurities plate (25)
It is provided with above device (19) and accelerates cooler (18), the return channel (19) and setting are in reflux removal of impurities chamber (2) outer wall
On reflux separator tube (20) connection, the reflux separator tube (20) is also connected to return-flow catheter (21), the return-flow catheter
(21) the second closed switch (22) is provided on, the return-flow catheter (21) is also connected to reboiler (3), the reboiler (3)
On be also communicated with steam lead (4), the closed switch (5) of third, the steam lead (4) are provided on the steam lead (4)
Across it is described distillation chamber (1) outer wall be connected to steam-distributing pipe (6), the steam-distributing pipe (6) if on be provided with dry saturated steam
It is in charge of (7), the bottom of distillation chamber (1) is communicated with discharge nozzle (10), and the 4th is provided on the discharge nozzle (10) and closed is opened
It closes (9), the end of the discharge nozzle (10) is provided with discharging distributor (11), and described discharging distributor (11) one end is led with fuel-displaced
(26) connection is managed, the other end of the discharging distributor (11) is connected to fuel-displaced return-flow catheter (13), the fuel-displaced return-flow catheter
(13) it is provided on reflux pump (14), the end of the fuel-displaced return-flow catheter (13) extends to the upper of the feed hopper (15)
End.
2. according to claim 1 a kind of for removing the distillation equipment of camellia seed oil stink, which is characterized in that described time
The return channel bottom (191) of stream device (19) is weldingly fixed on the inner wall of reflux removal of impurities chamber (2), and the return channel (19)
Reflux wall (192) be horn shape.
3. according to claim 1 a kind of for removing the distillation equipment of camellia seed oil stink, which is characterized in that described to remove
Miscellaneous plate (25) is several, and is provided with removal of impurities filler on the removal of impurities plate (25).
4. according to claim 1 a kind of for removing the distillation equipment of camellia seed oil stink, which is characterized in that described time
Stream removal of impurities chamber (2) is also communicated with vacuum tube (23), and the end of the vacuum tube (23) is provided with vacuum pump (24).
5. according to claim 1 a kind of for removing the distillation equipment of camellia seed oil stink, which is characterized in that the steaming
Vapour is in charge of (7) and is vertically arranged, vertical with the steam-distributing pipe (6).
6. according to claim 5 a kind of for removing the distillation equipment of camellia seed oil stink, which is characterized in that every institute
State steam be in charge of (7) length it is different.
7. according to claim 1 a kind of for removing the distillation equipment of camellia seed oil stink, which is characterized in that the steaming
It evaporates chamber (1) bottom and is additionally provided with several agitating devices (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821932803.0U CN209412170U (en) | 2018-11-22 | 2018-11-22 | It is a kind of for removing the distillation equipment of camellia seed oil stink |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821932803.0U CN209412170U (en) | 2018-11-22 | 2018-11-22 | It is a kind of for removing the distillation equipment of camellia seed oil stink |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209412170U true CN209412170U (en) | 2019-09-20 |
Family
ID=67934806
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821932803.0U Expired - Fee Related CN209412170U (en) | 2018-11-22 | 2018-11-22 | It is a kind of for removing the distillation equipment of camellia seed oil stink |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209412170U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110898592A (en) * | 2019-12-10 | 2020-03-24 | 山西省农业科学院棉花研究所 | Smoke removing device |
-
2018
- 2018-11-22 CN CN201821932803.0U patent/CN209412170U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110898592A (en) * | 2019-12-10 | 2020-03-24 | 山西省农业科学院棉花研究所 | Smoke removing device |
| CN110898592B (en) * | 2019-12-10 | 2022-03-08 | 山西省农业科学院棉花研究所 | Smoke removing device |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190920 Termination date: 20201122 |