CN109628218A - It is a kind of to use uniformly heated camellia seed oil distillation technique - Google Patents
It is a kind of to use uniformly heated camellia seed oil distillation technique Download PDFInfo
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- CN109628218A CN109628218A CN201811401441.7A CN201811401441A CN109628218A CN 109628218 A CN109628218 A CN 109628218A CN 201811401441 A CN201811401441 A CN 201811401441A CN 109628218 A CN109628218 A CN 109628218A
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- seed oil
- steam
- camellia seed
- distillation
- chamber
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/12—Refining fats or fatty oils by distillation
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Microbiology (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
Abstract
It is a kind of to use uniformly heated camellia seed oil distillation technique, comprising the following steps: camellia seed oil to be poured into feed hopper, then camellia seed oil flows into distillation chamber along passage；Start reboiler, the steam in reboiler is imported into steam-distributing pipe by steam lead, steam-distributing pipe passes through steam again and is in charge of in the camellia seed oil that steam is uniformly introduced to distillation chamber.Structure of the invention 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 present invention relates to food processing technology fields, and in particular, to a kind of to be distilled using uniformly heated camellia seed oil
Technique.
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.
Uniformly heated camellia seed oil distillation technique is used therefore, it is necessary to a kind of.
Summary of the invention
The object of the invention is that the shortcomings that overcoming the above-mentioned prior art and deficiency, provide a kind of using uniformly heated
Camellia seed oil distillation technique, the inventive structure are biased to Simple automation, and process flow is very simple, are removed using distillation chamber and reflux
Miscellaneous chamber is used cooperatively, and is on the one hand provided with return channel in reflux removal of impurities chamber, is effectively collected condensed water and led back to reboiling
In device, 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 in camellia seed oil
The position of different depth, so that the distillation degree of camellia seed oil different location is uniform.
Technical solution used by the present invention solves the above problems is:
It is a kind of to use uniformly heated camellia seed oil distillation technique, camellia seed oil is poured into feed hopper, then camellia seed
Oil flows into distillation chamber along passage；
Start reboiler, the steam in reboiler is imported into steam-distributing pipe by steam lead, steam-distributing pipe leads to again
Steam is crossed to be in charge of in the camellia seed oil that steam is uniformly introduced to distillation chamber；
In distillation process, the impurity in camellia seed oil enters reflux removal of impurities chamber and is absorbed by removal of impurities plate after being evaporated, and steams
Vapour is then collected in return channel, is led back to the steam in return channel in reboiler by reflux separator tube and return-flow catheter；
After the completion of to be distilled, the camellia seed oil after the completion of distillation is imported in discharging distributor by discharge nozzle, if also needing
Camellia seed oil after the completion of distillation further distilled, be then conducted into feed hopper by return-flow catheter, if not
It needs further to distill the camellia seed oil after the completion of distillation, then camellia seed oil is conducted by fuel-displaced return-flow catheter and received
In header.
Wherein, distilling apparatus includes distillation chamber, and the distillation process of camellia seed oil is carried out in distillation chamber, the distillation
The upper end of chamber is removably connected with reflux removal of impurities chamber, and equipment can be disassembled by being detachably connected after the completion of being advantageous in that distillation
Clean and maintenance is carried out, the difficulty of clean and maintenance is reduced；The reflux removal of impurities top of chamber is provided with feed hopper, needs the mountain of deodorization
Tea-seed oil is added in distillation chamber by the feed hopper, and funnelform entrance can avoid spilling when camellia seed oil is added
It falls；It is provided with the first closed switch in the feed hopper, after camellia seed oil addition, which is closed
It closes, guarantees the air-tightness of equipment；The feed hopper bottom end is provided with passage, and the passage passes through reflux removal of impurities chamber
It extend into the top of the distillation chamber afterwards, the camellia seed oil of addition can be avoided reflux removal of impurities chamber by passage and be directly entered distillation
In chamber, avoidable camellia seed oil be attached to reflux removal of impurities it is intracavitary and/or touch removal of impurities plate on impurity；The reflux removal of impurities chamber
Middle part be detachably provided with removal of impurities plate, convenient for removal of impurities plate disassembly come under cleaned；It is provided with back above the removal of impurities plate
Device is flowed, which can effectively receive condensed water, and condensed water is avoided to be flowed back in distillation chamber again；The top of the return channel
Be provided with acceleration cooler, environment temperature is higher do not utilize cooling for reflux when, then open the acceleration cooler, help to cool down；
The return channel be arranged in it is described reflux removal of impurities cavity outer wall on reflux separator tube be connected to, the reflux separator tube also with reflux
Conduit connection, passes sequentially through reflux separator tube and return-flow catheter, the collected condensed water of return channel is led back in reboiler；Institute
It states and is provided with the second closed switch on return-flow catheter, the second closed switch is closed when not needing to lead back to condensed water, guarantees to set
Standby air-tightness；The return-flow catheter is also connected to reboiler, and steam lead, the reboiler qigong are also communicated on the reboiler
Steam carried out in distillation chamber by steam lead；It is provided with the closed switch of third on the steam lead, is not needing to steaming
When evaporating addition steam in chamber, the closed switch of third is closed, guarantees the air-tightness of equipment；The steam lead passes through the distillation
The outer wall of chamber is connected to steam-distributing pipe, is in charge of if being provided with dry saturated steam on the steam-distributing pipe, steam-distributing pipe and steam
The steam mean allocation of distillation chamber can will be entered to the different location of distillation chamber by being in charge of, and the camellia seed oil that can avoid portion steams
Boiling range spends weight and/or kicks the beam；The bottom of the distillation chamber is communicated with discharge nozzle, after distillation, will be removed by discharge nozzle
Camellia seed oil after miscellaneous is released；It is provided with the 4th closed switch on the discharge nozzle, in distillation process, the 4th closed need to be opened
It closes, guarantees the air-tightness of equipment；The end of the discharge nozzle is provided with discharging distributor, described discharging distributor one end with
Oil out duct connection, the other end of the discharging distributor are connected to fuel-displaced return-flow catheter, are arranged on the fuel-displaced return-flow catheter
There is reflux pump, the end of the fuel-displaced return-flow catheter extends to the upper end of the feed hopper, if also needing the mountain completed to distillation
Tea-seed oil is further distilled, then camellia seed oil is oriented to fuel-displaced return-flow catheter by discharging distributor, in the work of reflux pump
It is back to feed hopper under, if the camellia seed oil no longer completed to distillation is further distilled, passes through discharging distributor
Camellia seed oil is oriented to oil out duct, is introduced directly into camellia seed oil collecting box.
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 present invention are:
Structure of the invention is biased to Simple automation, and process flow is very simple, is matched using distillation chamber and reflux removal of impurities chamber
It closes and uses, be on the one hand provided with return channel in reflux removal of impurities chamber, effectively collect condensed water and led back in reboiler, it can be big
Amount saves steam, is on the other hand provided with steam-distributing pipe and steam is in charge of, and steam can be imported different depth in camellia seed oil
Position so that the distillation degree of camellia seed oil different location is uniform.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention.
Fig. 2 is return channel structural schematic diagram of the invention.
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, structure of the invention is biased to Simple automation, and process flow is non-
It is often simple, using being used cooperatively for distillation chamber and reflux removal of impurities chamber, it on the one hand is provided with return channel in reflux removal of impurities chamber, effectively
It collects condensed water and is led back in reboiler, can largely save steam, be on the other hand provided with steam-distributing pipe and steam point
Steam can be imported the position of different depth in camellia seed oil, so that the distillation degree of camellia seed oil different location is uniform by pipe.Under
Detailed description further is made in conjunction with the embodiments and attached drawing, to the present invention in face, and embodiments of the present invention are not limited thereto, figure
In an only example applying of the present invention, there is no essential constraint to the principle of the present invention.
Embodiment:
As depicted in figs. 1 and 2, a kind of to use uniformly heated camellia seed oil distillation technique, camellia seed oil is poured into pan feeding
Funnel, then camellia seed oil flows into distillation chamber along passage；
Start reboiler, the steam in reboiler is imported into steam-distributing pipe by steam lead, steam-distributing pipe leads to again
Steam is crossed to be in charge of in the camellia seed oil that steam is uniformly introduced to distillation chamber；
In distillation process, the impurity in camellia seed oil enters reflux removal of impurities chamber and is absorbed by removal of impurities plate after being evaporated, and steams
Vapour is then collected in return channel, is led back to the steam in return channel in reboiler by reflux separator tube and return-flow catheter；
After the completion of to be distilled, the camellia seed oil after the completion of distillation is imported in discharging distributor by discharge nozzle, if also needing
Camellia seed oil after the completion of distillation further distilled, be then conducted into feed hopper by return-flow catheter, if not
It needs further to distill the camellia seed oil after the completion of distillation, then camellia seed oil is conducted by fuel-displaced return-flow catheter and received
In header.
Wherein, distilling apparatus includes distillation chamber 1, and the distillation process of camellia seed oil is carried out in distillation chamber, the steaming
The upper end for evaporating chamber 1 is removably connected with reflux removal of impurities chamber 2, and equipment can be torn open by being detachably connected after the completion of being advantageous in that distillation
Carry out clean and maintenance is dismantled, the difficulty of clean and maintenance is reduced；It is provided with feed hopper 15 at the top of the reflux removal of impurities chamber 2, is needed
The camellia seed oil of deodorization is added in distillation chamber by the feed hopper, and funnelform entrance can avoid that camellia seed is being added
It is trickled down when oily；The first closed switch 16 is provided in the feed hopper 15, it is after camellia seed oil addition, this is first close
Make and break is closed, and guarantees the air-tightness of equipment；15 bottom end of feed hopper is provided with passage 17, and the passage 17 passes through
The top of the distillation chamber 1 is extend into after the reflux removal of impurities chamber 2, the camellia seed oil of addition can be avoided reflux by passage and be removed
Miscellaneous chamber is directly entered in distillation chamber, and avoidable camellia seed oil is attached to reflux and cleans intracavitary and/or touch miscellaneous on removal of impurities plate
Matter；The middle part of the reflux removal of impurities chamber 2 is detachably provided with removal of impurities plate 25, is cleaned under coming convenient for removal of impurities plate disassembly；It is described
The top of removal of impurities plate 25 is provided with return channel 19, which can effectively receive condensed water, and condensed water is avoided to flow back to again
It distills in chamber；The top of the return channel 19 be provided with accelerate cooler 18, environment temperature is higher do not utilize cooling for reflux when,
The acceleration cooler is then opened, helps to cool down；The return channel 19 and the reflux being arranged on reflux removal of impurities 2 outer wall of chamber are slow
Washing pipe 20 is connected to, and the reflux separator tube 20 is also connected to return-flow catheter 21, passes sequentially through reflux separator tube and return-flow catheter, will
The collected condensed water of return channel is led back in reboiler；The second closed switch 22 is provided on the return-flow catheter 21, not
The second closed switch is closed when needing to lead back to condensed water, guarantees the air-tightness of equipment；The return-flow catheter 21 also with reboiler 3
It is connected to, is also communicated with steam lead 4 on the reboiler 3, the steam of the reboiler qigong is carried out in distillation chamber by steam lead；
It is provided with the closed switch 5 of third on the steam lead 4, when not needing that steam is added into distillation chamber, opens third is closed
It closes, guarantees the air-tightness of equipment；The outer wall that the steam lead 4 passes through the distillation chamber 1 is connected to steam-distributing pipe 6,
If being provided with dry saturated steam on the steam-distributing pipe 6 is in charge of 7, steam-distributing pipe and steam are in charge of the steam that can will enter distillation chamber
For mean allocation to the different location for distilling chamber, the camellia seed oil distillation degree of avoidable portion is overweight and/or kicks the beam；It is described
The bottom of distillation chamber 1 is communicated with discharge nozzle 10, after distillation, is released the camellia seed oil after removal of impurities by discharge nozzle；Institute
It states and is provided with the 4th closed switch 9 on discharge nozzle 10, in distillation process, the 4th closed switch need to be closed, guarantee equipment
Air-tightness；The end of the discharge nozzle 10 is provided with discharging distributor 11, described 11 one end of discharging distributor and oil out duct 26
Connection, the other end of the discharging distributor 11 are connected to fuel-displaced return-flow catheter 13, are provided on the fuel-displaced return-flow catheter 13
The end of reflux pump 14, the fuel-displaced return-flow catheter 13 extends to the upper end of the feed hopper 15, if also needing to complete distillation
Camellia seed oil further distilled, then camellia seed oil is oriented to by fuel-displaced return-flow catheter by discharging distributor, in reflux pump
Under the action of be back to feed hopper, if no longer to distillation complete camellia seed oil further distilled, by discharging divide
Camellia seed oil is oriented to oil out duct by orchestration, is introduced directly into 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.
The above is only the preferred embodiment of the present invention, protection scope of the present invention is not limited merely to above-described embodiment,
All technical solutions belonged under thinking of the present invention all belong to the scope of protection of the present invention.It should be pointed out that for the art
For those of ordinary skill, several improvements and modifications without departing from the principles of the present invention should be regarded as protection of the invention
Range.
Claims (7)
1. a kind of use uniformly heated camellia seed oil distillation technique, which comprises the following steps:
Camellia seed oil is poured into feed hopper, then camellia seed oil flows into distillation chamber along passage；
Start reboiler, the steam in reboiler is imported into steam-distributing pipe by steam lead, steam-distributing pipe passes through steaming again
Vapour is in charge of in the camellia seed oil that steam is uniformly introduced to distillation chamber；
In distillation process, the impurity in camellia seed oil enters reflux removal of impurities chamber and is absorbed by removal of impurities plate after being evaporated, steam is then
It is collected in return channel, is led back to the steam in return channel in reboiler by reflux separator tube and return-flow catheter；
After the completion of to be distilled, the camellia seed oil after the completion of distillation is imported in discharging distributor by discharge nozzle, if also needing pair
Camellia seed oil after the completion of distillation is further distilled, then is conducted into feed hopper by return-flow catheter, if not needing
Camellia seed oil after the completion of distillation is further distilled, then camellia seed oil collecting box is conducted by fuel-displaced return-flow catheter
In.
2. according to claim 1 a kind of using uniformly heated camellia seed oil distillation technique, which is characterized in that described time
The return channel bottom of stream device is weldingly fixed on the inner wall of the reflux removal of impurities chamber, and the reflux wall of the return channel is loudspeaker
Shape.
3. according to claim 1 a kind of using uniformly heated camellia seed oil distillation technique, which is characterized in that described to remove
Miscellaneous plate is several, and is provided with removal of impurities filler on the removal of impurities plate.
4. according to claim 1 a kind of using uniformly heated camellia seed oil distillation technique, which is characterized in that described time
Stream removal of impurities chamber is also communicated with vacuum tube, and the end of the vacuum tube is provided with vacuum pump.
5. according to claim 1 a kind of using uniformly heated camellia seed oil distillation technique, which is characterized in that the steaming
Vapour, which is in charge of, to be vertically arranged, vertical with the steam-distributing pipe.
6. according to claim 5 a kind of using uniformly heated camellia seed oil distillation technique, which is characterized in that every institute
It is different to state the length that steam is in charge of.
7. according to claim 1 a kind of using uniformly heated camellia seed oil distillation technique, which is characterized in that the steaming
It evaporates bottom of chamber portion and is additionally provided with several agitating devices.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811401441.7A CN109628218A (en) | 2018-11-22 | 2018-11-22 | It is a kind of to use uniformly heated camellia seed oil distillation technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811401441.7A CN109628218A (en) | 2018-11-22 | 2018-11-22 | It is a kind of to use uniformly heated camellia seed oil distillation technique |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109628218A true CN109628218A (en) | 2019-04-16 |
Family
ID=66069000
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811401441.7A Withdrawn CN109628218A (en) | 2018-11-22 | 2018-11-22 | It is a kind of to use uniformly heated camellia seed oil distillation technique |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109628218A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114181775A (en) * | 2021-12-21 | 2022-03-15 | 湖南博邦农林科技股份有限公司 | Distillation plant is used in camellia oil extraction with waste heat recycle function |
-
2018
- 2018-11-22 CN CN201811401441.7A patent/CN109628218A/en not_active Withdrawn
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114181775A (en) * | 2021-12-21 | 2022-03-15 | 湖南博邦农林科技股份有限公司 | Distillation plant is used in camellia oil extraction with waste heat recycle function |
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| Date | Code | Title | Description |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20190416 |
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| WW01 | Invention patent application withdrawn after publication |