CN108102786A - A kind of essential oil method of purification and equipment - Google Patents

A kind of essential oil method of purification and equipment Download PDF

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Publication number
CN108102786A
CN108102786A CN201810022196.2A CN201810022196A CN108102786A CN 108102786 A CN108102786 A CN 108102786A CN 201810022196 A CN201810022196 A CN 201810022196A CN 108102786 A CN108102786 A CN 108102786A
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China
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essential oil
processing box
material processing
distillation still
tower
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CN201810022196.2A
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Chinese (zh)
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刘芬
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Individual
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Individual
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Priority to CN201810022196.2A priority Critical patent/CN108102786A/en
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    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B9/00Essential oils; Perfumes
    • C11B9/02Recovery or refining of essential oils from raw materials
    • C11B9/027Recovery of volatiles by distillation or stripping
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B9/00Essential oils; Perfumes
    • C11B9/02Recovery or refining of essential oils from raw materials
    • C11B9/022Refining

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (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)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The present invention relates to a kind of essential oil method of purification and equipment, the equipment includes a support platform, a material processing box is equipped in the upper surface of support platform, a stirring reducing mechanism is equipped in material processing box, a high pressure steam case is equipped in the one side of material processing box, a water inlet is equipped in the one side of material processing box, a feed inlet is equipped at the top of material processing box, a distillation still is additionally provided in the upper surface of support platform, a connecting pipe is equipped between material processing box and distillation still, the first destilling tower and after-fractionating tower are equipped at the top of distillation still, the first heating plate is equipped in distillation still, at least one heating condensation is additionally provided in distillation still, the first destilling tower and after-fractionating tower are equipped at the top of distillation still, it is interconnected between first destilling tower and after-fractionating tower, after-fractionating tower is equipped with an at least discharge port.Essential oil equipment for purifying proposed by the present invention can effectively purify out essential oil cost from herbaceous material, have a good application prospect.

Description

A kind of essential oil method of purification and equipment
Technical field
The present invention relates to essential oil purification technique field, more particularly to a kind of essential oil method of purification and equipment.
Background technology
Essential oil is a kind of very common and important life and chemical article, is played very in daily life Important role.In recent years, with the further promotion that people pursue itself quality of the life, the usage amount of essential oil is also year by year Rise, therefore the essential oil for producing high quality has become an industry to begin to take shape.
The essential oil of makeup and foodstuff is presently used for, generally uses steam distillation extraction method.Using distillation equipment, Steam is conveyed into steam boiler, the derived essential oil in herbaceous plant is refined.However, existing essential oil equipment for purifying is past It is past complicated, it is expensive, considerably increase the cost of manufacture of essential oil.
The content of the invention
It is complicated the purpose of the present invention is to solve existing essential oil equipment for purifying based on this, it is expensive, greatly Big the problem of adding the cost of manufacture of essential oil.
The present invention proposes a kind of essential oil equipment for purifying, including a support platform, wherein, in the upper surface of the support platform Equipped with a material processing box, a stirring reducing mechanism is equipped in the material processing box, in the one side of the material processing box Equipped with a high pressure steam case, a water inlet is equipped in the one side of the material processing box, is set at the top of the material processing box There is a feed inlet, a distillation still is additionally provided in the upper surface of the support platform, in the material processing box and the distillation still Between be equipped with a connecting pipe, the top of the distillation still be equipped with the first destilling tower and after-fractionating tower, in the distillation still The first heating plate is inside equipped with, at least one heating condensation is additionally provided in the distillation still, is set at the top of the distillation still There are the first destilling tower and after-fractionating tower, be interconnected between first destilling tower and the after-fractionating tower, described the Two destilling towers are equipped with an at least discharge port.
Essential oil equipment for purifying proposed by the present invention when carrying out essential oil purification, passes through the stirring in material processing box first Reducing mechanism crushes herbaceous material, and the high steam for passing through release in high pressure steam case is aged herbaceous material Processing, obtained initial slurry is passed by communicating pipe in distillation still, is then condensed by the heating being arranged in distillation still Component carries out initial slurry rectifying, and obtained essential oil product is sequentially discharged through the first destilling tower and after-fractionating tower, with most Essential oil product is obtained eventually.Essential oil equipment for purifying proposed by the present invention, structure is relatively simple, and production cost is relatively low, and price is relatively low, While ensureing that essential oil purification operation normally produces, the production cost of enterprise is reduced.
The essential oil equipment for purifying, wherein, the stirring reducing mechanism includes a stirring motor and stirs electricity with described The stirring mobile jib that machine is fixedly connected is equipped with multiple cutting blades, the two of the stirring motor in the periphery of the stirring mobile jib End is respectively equipped with a fixed link, and one end of the fixed link is fixedly connected on the material processing box.
The essential oil equipment for purifying, wherein, a hygrosensor is additionally provided in the material processing box, in the raw material The outside for the treatment of box is equipped with an information display screen, and the shape of the feed inlet is cone.
The essential oil equipment for purifying, wherein, a condensation casing is equipped in the periphery of the communicating pipe, the condensation casing One end is connected with an inlet water tank, and the other end is connected with a water tank, and the first filter screen is equipped in one end of the communicating pipe, another End is equipped with the second filter screen.
The essential oil equipment for purifying, wherein, a screen modules, the filter screen group are equipped in first destilling tower Part includes the stratum reticulare, carbon-coating and the film layer that set gradually from top to bottom.
The essential oil equipment for purifying, wherein, a guide is equipped between first destilling tower and the after-fractionating tower Pipe is equipped with an observation window, the top of first destilling tower and the top of the after-fractionating tower on the after-fractionating tower It is connected by a gas-guide tube.
The essential oil equipment for purifying, wherein, the heating condensation includes the second heating plate and arranged on described second Cold plate directly over heating plate is externally provided with a temperature adjustment knob in the distillation still.
The essential oil equipment for purifying, wherein, it is equipped with case supports bar, the babinet branch in the bottom of the material processing box Strut is arranged at four square positions of the material processing box.
The essential oil equipment for purifying, wherein, it is equipped with support column, the quantity of the support column in the bottom surface of the support platform For 4, the shape of the support platform is square, and the support column is arranged at four square positions of the support platform.
The present invention also proposes a kind of essential oil method of purification, wherein, described method includes following steps:
Herbaceous material is added in by a feed inlet into a material processing box, then by high pressure steam case to the original Material treatment box is passed through high steam, starts stirring reducing mechanism and crushes processing to the herbaceous material;
The slurries obtained after the herbaceous material is crushed are flowed by a connecting pipe in a distillation still, by being arranged on It states the first heating plate in distillation still and heating condensation and the slurries is subjected to rectification and purification to obtain intermediate product;
After the intermediate product is filtered by the first destilling tower being arranged at the top of the distillation still, then flow into after-fractionating It discharges to finally obtain finished product product in tower.
The additional aspect and advantage of the present invention will be set forth in part in the description, and will partly become from the following description It obtains substantially or is recognized by the practice of the present invention.
Description of the drawings
Fig. 1 is the overall structure diagram of essential oil equipment for purifying proposed by the present invention;
Fig. 2 is the schematic enlarged-scale view of material processing box in essential oil equipment for purifying shown in FIG. 1;
Fig. 3 is the schematic enlarged-scale view that reducing mechanism is stirred in essential oil equipment for purifying shown in FIG. 1;
Fig. 4 is the schematic enlarged-scale view of communicating pipe in essential oil equipment for purifying shown in FIG. 1;
Fig. 5 is the schematic enlarged-scale view of screen modules in essential oil equipment for purifying shown in FIG. 1.
Primary symbols explanation:
Specific embodiment
For the ease of understanding the present invention, the present invention is described more fully below with reference to relevant drawings.In attached drawing Give the preferred embodiment of the present invention.But the present invention can realize in many different forms, however it is not limited to this paper institutes The embodiment of description.On the contrary, the purpose for providing these embodiments is made to the disclosure more thorough and comprehensive.
Unless otherwise defined, all of technologies and scientific terms used here by the article is with belonging to technical field of the invention The normally understood meaning of technical staff is identical.Term used in the description of the invention herein is intended merely to description tool The purpose of the embodiment of body, it is not intended that in the limitation present invention.Term as used herein " and/or " include one or more phases The arbitrary and all combination of the Listed Items of pass.
The essential oil of makeup and foodstuff is presently used for, generally uses steam distillation extraction method.Using distillation equipment, Steam is conveyed into steam boiler, the derived essential oil in herbaceous plant is refined.However, existing essential oil equipment for purifying is past It is past complicated, it is expensive, considerably increase the cost of manufacture of essential oil.
In order to solve this technical problem, the present invention proposes a kind of essential oil equipment for purifying, please refers to Fig.1 to Fig. 5, for Essential oil equipment for purifying proposed by the present invention, including a support platform 10, wherein, it is equipped with a raw material in the upper surface of support platform 10 Treatment box 20 is equipped with a stirring reducing mechanism 30 in material processing box 20, a high pressure is equipped in the one side of material processing box 20 Steam chest 203, the wherein high pressure steam case 203 are mainly used for being passed through high-temperature steam to material processing box 20, so that draft Raw material carries out ripening.
A water inlet 201 is additionally provided in the left side of material processing box 20, a charging is equipped at the top of material processing box 20 Mouth 202, the wherein shape of the feed inlet 202 are taper, and the setting convenient for staff primarily to carry out charging operation.
It can further be seen from figure 1 that being equipped with a stirring reducing mechanism 30 in material processing box 20, the wherein stirring crushes Device 30 includes a stirring motor 301 and the stirring mobile jib 302 being fixedly connected with the stirring motor 301.In addition, in the stirring The periphery of mobile jib 302 is equipped with multiple cutting blades 3021, and in the present invention, the quantity of the cutting blade 3021 is six.It is stirred at this The both ends for mixing motor 301 further respectively have a fixed link 303, and one end of wherein fixed link 303 is fixedly connected on material processing box On 20.Two fixed links 303 are primarily to stirring motor 301 is firmly secured on material processing box 20.
At the same time, case supports bar 204, wherein case supports bar are additionally provided in the bottom of above-mentioned raw materials treatment box 20 204 are arranged at four square positions of material processing box 20.In addition, a hygrosensor is additionally provided in material processing box 20 205, it is equipped with an information display screen 206 in the outside of material processing box 20.Wherein the hygrosensor 205 is a thermometer, should Information display screen 206 is mainly used for showing every biological parameter in material processing box 20.
A distillation still 50 is additionally provided in the upper surface of support platform 10, wherein above-mentioned material processing box 20 and the distillation still 50 are connected by a connecting pipe 40, to carry out the conveying of material.For the communicating pipe 40, in the periphery of the communicating pipe 40 Equipped with a condensation casing 401, the right end of the condensation casing 401 is connected with an inlet water tank 4011, and left end is connected with a water tank 4012.The setting is primarily to so that condensed water stops the longer time in casing 401 is condensed, to reach better condensation Effect.In addition, communicating pipe 40 left end be equipped with the first filter screen 402, right end be equipped with the second filter screen 403.The setting is mainly The impurity in material processing box 20 is entered in distillation still 50 in order to prevent, is caused the blocking of impurity in distillation still 50 and is influenced just Normal rectifying operation.
Specifically, for distillation still 50, the first destilling tower 60 and after-fractionating are equipped at the top of the distillation still 50 Tower 70.Wherein, a passage 603 is equipped between first destilling tower 60 and after-fractionating tower 70, which mainly uses It is flowed by the material in the first destilling tower 60 in after-fractionating tower 70.In addition, the top of first destilling tower 60 and second The top of destilling tower 70 is connected by a gas-guide tube 602, and the gas-guide tube 602 is primarily to the first destilling tower 60 and second of balance Air pressure between destilling tower 70.
Heating condensation 502 is equipped in distillation still 50, the wherein heating condensation 502 is located at the first heating plate 501 top.Specifically, the heating condensation 502 include the second heating plate 5022 and arranged on the second heating plate 5022 just The cold plate 5021 of top is externally provided with a temperature adjustment knob in distillation still 50.
For the first above-mentioned destilling tower 60, a screen modules 601 are equipped in first destilling tower 60.Wherein should Screen modules 601 include the stratum reticulare 6013, carbon-coating 6012 and the film layer 6011 that set gradually from top to bottom.The screen modules 601 can further purify the essential oil that rectifying obtains, to remove the foreign objects in essential oil.
For above-mentioned after-fractionating tower 70, an observation window 701 is equipped on the after-fractionating tower 70.The observation window 701 primarily to essential oil amount in the personal observations easy to operation after-fractionating tower 70.In addition, the one of after-fractionating tower 70 Side is additionally provided with a discharge port 702, for collecting essential oil finished product.
In addition, being equipped with support column 101 in the bottom surface of support platform 10, in the present invention, the quantity of the support column 101 is 4. The shape of the support platform 10 is square, and each support column 101 is arranged at four square positions of support platform 10.
Essential oil equipment for purifying proposed by the present invention when carrying out essential oil purification, passes through the stirring in material processing box first Reducing mechanism crushes herbaceous material, and the high steam for passing through release in high pressure steam case is aged herbaceous material Processing, obtained initial slurry is passed by communicating pipe in distillation still, is then condensed by the heating being arranged in distillation still Component carries out initial slurry rectifying, and obtained essential oil product is sequentially discharged through the first destilling tower and after-fractionating tower, with most Essential oil product is obtained eventually.Essential oil equipment for purifying proposed by the present invention, structure is relatively simple, and production cost is relatively low, and price is relatively low, While ensureing that essential oil purification operation normally produces, the production cost of enterprise is reduced.
The present invention also proposes a kind of essential oil method of purification, wherein, described method includes following steps:
(1) herbaceous material is added in by a feed inlet 202 into a material processing box 20 first, is then steamed by high pressure Vapour case 203 is passed through high steam into material processing box 20, starts stirring reducing mechanism 30 and processing is crushed to herbaceous material.
(2) slurries obtained after herbaceous material is crushed are by flowing into a distillation still 50 communicating pipe 40, by being arranged on Slurries are carried out rectification and purification to obtain intermediate product by the first heating plate 501 and heating condensation 502 in distillation still 50.
(3) after and then intermediate product is filtered by the first destilling tower 60 being arranged at the top of the distillation still 50, then flow into It discharges to finally obtain finished product product in after-fractionating tower 70.
Embodiment described above only expresses the several embodiments of the present invention, and description is more specific and detailed, but simultaneously Cannot the limitation to the scope of the claims of the present invention therefore be interpreted as.It should be pointed out that for those of ordinary skill in the art For, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to the guarantor of the present invention Protect scope.Therefore, the protection domain of patent of the present invention should be determined by the appended claims.

Claims (10)

1. a kind of essential oil equipment for purifying, including a support platform, which is characterized in that be equipped with one in the upper surface of the support platform Material processing box is equipped with a stirring reducing mechanism in the material processing box, one is equipped in the one side of the material processing box High pressure steam case, the one side of the material processing box be equipped with a water inlet, the top of the material processing box be equipped with one into Material mouth, a distillation still is additionally provided in the upper surface of the support platform, is set between the material processing box and the distillation still There is a connecting pipe, be equipped with the first destilling tower and after-fractionating tower at the top of the distillation still, be equipped in the distillation still First heating plate is additionally provided at least one heating condensation in the distillation still, first is equipped at the top of the distillation still Destilling tower and after-fractionating tower are interconnected between first destilling tower and the after-fractionating tower, the after-fractionating Tower is equipped with an at least discharge port.
2. essential oil equipment for purifying according to claim 1, which is characterized in that the stirring reducing mechanism includes a stirring electricity Machine and the stirring mobile jib being fixedly connected with the stirring motor are equipped with multiple cutting blades in the periphery of the stirring mobile jib, A fixed link is respectively equipped at the both ends of the stirring motor, one end of the fixed link is fixedly connected on the material processing box On.
3. essential oil equipment for purifying according to claim 2 a, which is characterized in that temperature is additionally provided in the material processing box Detector is spent, an information display screen is equipped in the outside of the material processing box, the shape of the feed inlet is cone.
4. essential oil equipment for purifying according to claim 2 a, which is characterized in that condensation is equipped in the periphery of the communicating pipe Casing, one end of the condensation casing are connected with an inlet water tank, and the other end is connected with a water tank, in one end of the communicating pipe Equipped with the first filter screen, the other end is equipped with the second filter screen.
5. essential oil equipment for purifying according to claim 2 a, which is characterized in that filtering is equipped in first destilling tower Screen component, the screen modules include the stratum reticulare, carbon-coating and the film layer that set gradually from top to bottom.
6. essential oil equipment for purifying according to claim 2, which is characterized in that steamed in first destilling tower and described second It evaporates and a passage is equipped between tower, an observation window, the top of first destilling tower and institute are equipped on the after-fractionating tower The top for stating after-fractionating tower is connected by a gas-guide tube.
7. essential oil equipment for purifying according to claim 1, which is characterized in that the heating condensation includes the second heating Plate and the cold plate directly over second heating plate, a temperature adjustment knob is externally provided in the distillation still.
8. essential oil equipment for purifying according to claim 1, which is characterized in that be equipped with case in the bottom of the material processing box Body supporting rod, the case supports bar are arranged at four square positions of the material processing box.
9. essential oil equipment for purifying according to claim 1, which is characterized in that be equipped with support in the bottom surface of the support platform Column, the quantity of the support column is 4, and the shape of the support platform is square, and the support column is arranged on the support platform At four square positions.
10. a kind of essential oil method of purification, which is characterized in that described method includes following steps:
Herbaceous material is added in by a feed inlet into a material processing box, then by high pressure steam case at the raw material Reason case is passed through high steam, starts stirring reducing mechanism and crushes processing to the herbaceous material;
The slurries obtained after the herbaceous material is crushed are flowed by a connecting pipe in a distillation still, by being arranged on the steaming It evaporates the first heating plate in kettle and heating condensation and the slurries is subjected to rectification and purification to obtain intermediate product;
After the intermediate product is filtered by the first destilling tower being arranged at the top of the distillation still, then flow into after-fractionating tower It discharges to finally obtain finished product product.
CN201810022196.2A 2018-01-10 2018-01-10 A kind of essential oil method of purification and equipment Pending CN108102786A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108774584A (en) * 2018-06-07 2018-11-09 安徽清山艾草制品有限公司 A kind of wormwood extractive distillation device
CN108841446A (en) * 2018-06-07 2018-11-20 安徽清山艾草制品有限公司 A kind of wormwood volatile oil extractor
CN110194991A (en) * 2019-03-06 2019-09-03 上海市南洋模范中学 Extracting method, equipment and the application of Bergamot
CN114307218A (en) * 2022-01-05 2022-04-12 吉安市中香天然植物有限公司 Continuous rectification production control system for spices
CN115212832A (en) * 2022-07-21 2022-10-21 江西海瑞天然植物有限公司 Preparation method of butyrate essential oil compound feed additive

Citations (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201610426U (en) * 2009-12-29 2010-10-20 李尧 Distilling still used for extracting natural essential oil
CN201930567U (en) * 2011-01-12 2011-08-17 王庆才 Double-tower aroma essential oil distillation device
CN102284188A (en) * 2011-05-26 2011-12-21 王庆才 Twin-tower type aromatic essential oil distillation equipment
CN204352580U (en) * 2014-12-31 2015-05-27 潍坊蓝海环境保护有限公司 A kind of decompression distillation still with agitating function
CN204529806U (en) * 2015-03-26 2015-08-05 江西思派思香料化工有限公司 A kind of device preparing plants essential oil
CN204752656U (en) * 2015-06-22 2015-11-11 临泉县华丰农植物炼油有限公司 Garlic oil refines device
CN105249527A (en) * 2015-10-31 2016-01-20 武汉纽威制药机械有限公司 Method for extracting tobacco aroma component through water jet comminution and centrifugal membrane vacuum low-temperature distillation
CN205241637U (en) * 2015-11-17 2016-05-18 欧芳生物科技(上海)有限公司 Rose essential oil extraction device
CN205241633U (en) * 2015-11-17 2016-05-18 欧芳生物科技(上海)有限公司 Have purification rose essential oil of mechanism extraction element
CN105733814A (en) * 2016-04-07 2016-07-06 广西贵港市宏利生物能源科技有限公司 Distilling production method for sandalwood essential oil and equipment
CN205740948U (en) * 2016-06-12 2016-11-30 黑龙江省科学院自然与生态研究所 A kind of plants essential oil extraction equipment
CN205850303U (en) * 2016-08-12 2017-01-04 黄山学院 A kind of tea tree planting essential oil extracting device
CN205893201U (en) * 2016-06-16 2017-01-18 重庆陆龟科技有限公司 Tea tree essential oil apparatus for producing
CN106350230A (en) * 2016-12-05 2017-01-25 永州山香香料有限公司 Litsea cubeba oil distillation separation equipment and technology
CN206127245U (en) * 2016-09-07 2017-04-26 中粮德信行健康产业有限公司 Distillation edulcoration device of raw oil
CN206266500U (en) * 2016-12-15 2017-06-20 西京学院 A kind of crude oil multilayer distilling apparatus
CN206308326U (en) * 2016-12-27 2017-07-07 宫紫怡 A kind of preparation facilities of Rosa Damascana
CN206476960U (en) * 2017-02-20 2017-09-08 吴广洲 A kind of energy-saving distilling equipment of oil
CN206580793U (en) * 2017-02-21 2017-10-24 吕东华 A kind of ginger oil extraction element
CN206607212U (en) * 2017-03-10 2017-11-03 钟苏 A kind of essential oil extracting device
CN206799569U (en) * 2017-05-31 2017-12-26 威海职业学院 A kind of essential oil extracting device
CN107513469A (en) * 2016-06-16 2017-12-26 重庆陆龟科技有限公司 A kind of device for producing tea tree ethereal oil
CN206858521U (en) * 2017-06-07 2018-01-09 翁诗瑾 A kind of distillation equipment for jasmine essential oil

Patent Citations (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201610426U (en) * 2009-12-29 2010-10-20 李尧 Distilling still used for extracting natural essential oil
CN201930567U (en) * 2011-01-12 2011-08-17 王庆才 Double-tower aroma essential oil distillation device
CN102284188A (en) * 2011-05-26 2011-12-21 王庆才 Twin-tower type aromatic essential oil distillation equipment
CN204352580U (en) * 2014-12-31 2015-05-27 潍坊蓝海环境保护有限公司 A kind of decompression distillation still with agitating function
CN204529806U (en) * 2015-03-26 2015-08-05 江西思派思香料化工有限公司 A kind of device preparing plants essential oil
CN204752656U (en) * 2015-06-22 2015-11-11 临泉县华丰农植物炼油有限公司 Garlic oil refines device
CN105249527A (en) * 2015-10-31 2016-01-20 武汉纽威制药机械有限公司 Method for extracting tobacco aroma component through water jet comminution and centrifugal membrane vacuum low-temperature distillation
CN205241637U (en) * 2015-11-17 2016-05-18 欧芳生物科技(上海)有限公司 Rose essential oil extraction device
CN205241633U (en) * 2015-11-17 2016-05-18 欧芳生物科技(上海)有限公司 Have purification rose essential oil of mechanism extraction element
CN105733814A (en) * 2016-04-07 2016-07-06 广西贵港市宏利生物能源科技有限公司 Distilling production method for sandalwood essential oil and equipment
CN205740948U (en) * 2016-06-12 2016-11-30 黑龙江省科学院自然与生态研究所 A kind of plants essential oil extraction equipment
CN205893201U (en) * 2016-06-16 2017-01-18 重庆陆龟科技有限公司 Tea tree essential oil apparatus for producing
CN107513469A (en) * 2016-06-16 2017-12-26 重庆陆龟科技有限公司 A kind of device for producing tea tree ethereal oil
CN205850303U (en) * 2016-08-12 2017-01-04 黄山学院 A kind of tea tree planting essential oil extracting device
CN206127245U (en) * 2016-09-07 2017-04-26 中粮德信行健康产业有限公司 Distillation edulcoration device of raw oil
CN106350230A (en) * 2016-12-05 2017-01-25 永州山香香料有限公司 Litsea cubeba oil distillation separation equipment and technology
CN206266500U (en) * 2016-12-15 2017-06-20 西京学院 A kind of crude oil multilayer distilling apparatus
CN206308326U (en) * 2016-12-27 2017-07-07 宫紫怡 A kind of preparation facilities of Rosa Damascana
CN206476960U (en) * 2017-02-20 2017-09-08 吴广洲 A kind of energy-saving distilling equipment of oil
CN206580793U (en) * 2017-02-21 2017-10-24 吕东华 A kind of ginger oil extraction element
CN206607212U (en) * 2017-03-10 2017-11-03 钟苏 A kind of essential oil extracting device
CN206799569U (en) * 2017-05-31 2017-12-26 威海职业学院 A kind of essential oil extracting device
CN206858521U (en) * 2017-06-07 2018-01-09 翁诗瑾 A kind of distillation equipment for jasmine essential oil

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CN108774584A (en) * 2018-06-07 2018-11-09 安徽清山艾草制品有限公司 A kind of wormwood extractive distillation device
CN108841446A (en) * 2018-06-07 2018-11-20 安徽清山艾草制品有限公司 A kind of wormwood volatile oil extractor
CN110194991A (en) * 2019-03-06 2019-09-03 上海市南洋模范中学 Extracting method, equipment and the application of Bergamot
CN114307218A (en) * 2022-01-05 2022-04-12 吉安市中香天然植物有限公司 Continuous rectification production control system for spices
CN115212832A (en) * 2022-07-21 2022-10-21 江西海瑞天然植物有限公司 Preparation method of butyrate essential oil compound feed additive

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