CN208218803U - One plant volatile oil extractor - Google Patents

One plant volatile oil extractor Download PDF

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Publication number
CN208218803U
CN208218803U CN201820552623.3U CN201820552623U CN208218803U CN 208218803 U CN208218803 U CN 208218803U CN 201820552623 U CN201820552623 U CN 201820552623U CN 208218803 U CN208218803 U CN 208218803U
Authority
CN
China
Prior art keywords
pipe
distillation still
squeezing
feed opening
volatile oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201820552623.3U
Other languages
Chinese (zh)
Inventor
徐卫红
郭连金
杜佳朋
李玲
徐芬芬
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shangrao Normal University
Original Assignee
Shangrao Normal University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shangrao Normal University filed Critical Shangrao Normal University
Priority to CN201820552623.3U priority Critical patent/CN208218803U/en
Application granted granted Critical
Publication of CN208218803U publication Critical patent/CN208218803U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model relates to a plant volatile oil extractors, including squeezing tank, squeezing tank side is provided with feed opening, destroyer is provided in feed opening, squeezing tank inner top is provided with hydraulic telescopic rod, hydraulic telescopic rod bottom is provided with pressing plate, lower platen is provided with below pressing plate, squeezing pot bottom is connected by outlet tube with distillation still bottom, distillation still inner top is provided with jet pipe, spray head is provided on jet pipe, jet pipe is connected by circulation pipe with distillation still bottom, circulating pump is provided on circulation pipe, middle part is provided with filter cloth in distillation still, bottom is provided with steam pipe in distillation still, pipe bundle condenser is connected with by condensing connecting tube at the top of distillation still, pipe bundle condenser is connected with oil water separator;The utility model integrates broken plant material, squeezing, distillation and abstraction function, has and occupies little space, production cost is low, and volatile oil extracting is high-efficient, good in economic efficiency feature.

Description

One plant volatile oil extractor
Technical field
The utility model relates to a kind of extraction element, specifically a kind of plant essential oil extracting device.
Background technique
With the raising of social scientific and technological level, according to the needs of people, the extraction element technology of various oil is always continuous It improves, wherein volatile oil is also known as essential oil, is a kind of moisture condensation can volatilize at normal temperature, condensable, the oily with water not phase mixing Liquid is the common important component of one of synthetic drug, has a variety of physiological activity, has larger value, content is in Chinese medicine Compared with horn of plenty in material.But existing extract equipment there are areas occupied big, with high costs, the low disadvantage of extraction efficiency.
Utility model content
In view of the above deficiencies, the purpose of the utility model is to provide one kind to occupy little space, and production cost is low, volatilization Oil extract is high-efficient, the plant essential oil extracting device of good in economic efficiency feature.
To achieve the above object, the utility model is the following technical schemes are provided: a plant volatile oil extractor, including Tank, distillation still, pipe bundle condenser and oil water separator are squeezed, squeezing tank side is provided with feed opening, is provided with brokenly in feed opening Millstone, squeezing tank inner top are provided with hydraulic telescopic rod, and hydraulic telescopic rod bottom is provided with pressing plate, is provided with pushing below pressing plate Plate, lower platen activity are threaded through on squeezing tank and are evenly equipped with several liquid-leadage holes, and squeezing pot bottom passes through outlet tube and distillation still bottom Portion is connected, and distillation still inner top is provided with jet pipe, and spray head is provided on jet pipe, and jet pipe passes through circulation pipe and distillation still bottom phase Even, circulating pump is provided on circulation pipe, middle part is provided with filter cloth in distillation still, and bottom is provided with steam pipe in distillation still, steams It evaporates kettle top portion and is connected with pipe bundle condenser by condensing connecting tube, pipe bundle condenser is connected with oil water separator.
The scheme advanced optimized, the steam pipe are screw type steam pipe, uniformly distributed several ventholes on steam pipe.
The scheme further optimized, the lower platen outboard end are provided with push-pull handle, squeeze on tank with push-pull handle The opposite other side is provided with feed opening, is hinged with lid on feed opening.
The utility model has the beneficial effect that the utility model collection plant material is broken, presses compared with prior art Squeezing, distillation and abstraction function have with occupying little space, production cost is low, and volatile oil extracting is high-efficient, good in economic efficiency in one The characteristics of.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model;
Fig. 2 is the structural schematic diagram of steam pipe.
Figure label are as follows: it is broken that 1- squeezes tank, 2- distillation still, 3- pipe bundle condenser, 4- oil water separator, 5- feed opening, 6- Millstone, 7- hydraulic telescopic rod, 8- pressing plate, 9- lower platen, 10- outlet tube, 11- jet pipe, 12- spray head, 13- circulation pipe, 14- circulation Pump, 15- filter cloth, 16- steam pipe, 17- condense connecting tube, 18- push-pull handle, 19- lid.
Specific embodiment
In order to make the purpose of the utility model, technical solutions and advantages more clearly understood, below in conjunction with attached drawing and implementation Example, the present invention will be further described in detail.It should be appreciated that specific embodiment described herein is only used to explain The utility model is not used to limit the utility model.
In the description of the present invention, it should be understood that term " longitudinal direction ", " transverse direction ", "upper", "lower", " preceding ", The orientation or positional relationship of the instructions such as " rear ", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside" be based on Orientation or positional relationship shown in the drawings is merely for convenience of description the utility model, rather than the dress of indication or suggestion meaning It sets or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as to the utility model Limitation.
Referring to attached drawing 1-2 it is found that a plant volatile oil extractor, including squeezing tank 1, distillation still 2, pipe bundle condenser 3 and oil water separator 4, squeezing 1 side of tank is provided with feed opening 5, and destroyer 6 is provided in feed opening 5, squeezes 1 inner top of tank It is provided with hydraulic telescopic rod 7,7 bottom of hydraulic telescopic rod is provided with pressing plate 8, and lower platen 9 is provided with below pressing plate 8, and lower platen 9 is living Dynamic to be threaded through on squeezing tank 1 and be evenly equipped with several liquid-leadage holes, squeezing 1 bottom of tank is connected by outlet tube 10 with 2 bottom of distillation still, 2 inner top of distillation still is provided with jet pipe 11, and spray head 12 is provided on jet pipe 11, and jet pipe 11 passes through circulation pipe 13 and 2 bottom of distillation still Portion is connected, and circulating pump 14 is provided on circulation pipe 13, and middle part is provided with filter cloth 15 in distillation still 2, and bottom is arranged in distillation still 2 There is steam pipe 16, passes through condensation connecting tube 17 at the top of distillation still 2 and be connected with pipe bundle condenser 3, pipe bundle condenser 3 is connected with grease Separator 4.
Further, the steam pipe 16 is screw type steam pipe, and uniformly distributed several ventholes on steam pipe 16 are improved and steamed The contact surface of vapour and pressed liquor, and then improve the volatilization efficiency of volatile oil.
Further, 9 outboard end of lower platen is provided with push-pull handle 18, squeezes opposite with push-pull handle 18 on tank 1 The other side be provided with feed opening, lid 19 is hinged on feed opening, after the completion of squeezing, pass through push-pull handle 18 push lower platen 9 It is stretched out outside squeezing tank 1 from feed opening, facilitates the discharge of squeezing waste material.
Utility model works principle: will be added from feed opening 5 originally, and the destroyer 6 in feed opening 5 be crushed laggard Enter to squeeze in tank 1, hydraulic telescopic rod 7 squeezes broken raw material with dynamic pressure plate 8, and squeezing liquid is through the sepage on lower platen 9 Hole flows to squeezing 1 bottom of tank, enters in distillation still 2 through outlet tube 10, and steam pipe 16 connects steam generation facility into distillation still 2 It is passed through steam, steam distills pressed liquor, and the volatile oil in pressed liquor generates volatilization, while circulating pump 14 and spray head 12 will Pressed liquor carries out continuous spray cycle, and filter cloth 15 is filtered the solid impurity in pressed liquor, by continuous spray cycle, The evaporation rate for substantially increasing volatile oil, the volatile oil for being mingled with vapor enter in pipe bundle condenser 3 through condensation connecting tube 17 Condensation liquefaction is carried out, oil water separator 4 carries out water-oil separating to oil-water mixture, realizes the extraction to plant volatile oil.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this Made any modifications, equivalent replacements, and improvements etc., should be included in the utility model within the spirit and principle of utility model Protection scope within.

Claims (3)

1. a plant volatile oil extractor, including squeezing tank, distillation still, pipe bundle condenser and oil water separator, feature Be: squeezing tank side is provided with feed opening, and destroyer is provided in feed opening, and squeezing tank inner top is provided with hydraulically extensible Bar, hydraulic telescopic rod bottom are provided with pressing plate, and lower platen is provided with below pressing plate, and lower platen activity is threaded through on squeezing tank and equal Several liquid-leadage holes are furnished with, squeezing pot bottom is connected by outlet tube with distillation still bottom, and distillation still inner top is provided with jet pipe, spray It is provided with spray head on pipe, jet pipe is connected by circulation pipe with distillation still bottom, and circulating pump is provided on circulation pipe, during distillation still is interior Portion is provided with filter cloth, and bottom is provided with steam pipe in distillation still, and it is cold by condensation connecting tube to be connected with tubulation at the top of distillation still Condenser, pipe bundle condenser are connected with oil water separator.
2. a plant volatile oil extractor according to claim 1, it is characterised in that: the steam pipe is spiral Type steam pipe, uniformly distributed several ventholes on steam pipe.
3. a plant volatile oil extractor according to claim 1, it is characterised in that: the lower platen outboard end Portion is provided with push-pull handle, squeezes the other side opposite with push-pull handle on tank and is provided with feed opening, is hinged with lid on feed opening.
CN201820552623.3U 2018-04-18 2018-04-18 One plant volatile oil extractor Expired - Fee Related CN208218803U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820552623.3U CN208218803U (en) 2018-04-18 2018-04-18 One plant volatile oil extractor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820552623.3U CN208218803U (en) 2018-04-18 2018-04-18 One plant volatile oil extractor

Publications (1)

Publication Number Publication Date
CN208218803U true CN208218803U (en) 2018-12-11

Family

ID=64529711

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820552623.3U Expired - Fee Related CN208218803U (en) 2018-04-18 2018-04-18 One plant volatile oil extractor

Country Status (1)

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CN (1) CN208218803U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110025017A (en) * 2019-04-22 2019-07-19 长沙理工大学 A kind of production system and method improving cranberry juice yield
CN111744229A (en) * 2020-07-03 2020-10-09 陈广建 Plant active ingredient extraction device and application thereof in cosmetics
CN112870750A (en) * 2021-01-21 2021-06-01 广西六万山生物科技有限公司 Distillation retort for leaching effective components of plants and application method thereof
CN113430054A (en) * 2021-07-26 2021-09-24 宋桂林 Cosmetic plant extraction of essential oil device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110025017A (en) * 2019-04-22 2019-07-19 长沙理工大学 A kind of production system and method improving cranberry juice yield
WO2020216045A1 (en) * 2019-04-22 2020-10-29 长沙理工大学 Production system and method for improving yield of waxberry juice
US11178888B2 (en) 2019-04-22 2021-11-23 Changsha University Of Science And Technology Production system and method for improving yield of bayberry juice
CN111744229A (en) * 2020-07-03 2020-10-09 陈广建 Plant active ingredient extraction device and application thereof in cosmetics
CN112870750A (en) * 2021-01-21 2021-06-01 广西六万山生物科技有限公司 Distillation retort for leaching effective components of plants and application method thereof
CN113430054A (en) * 2021-07-26 2021-09-24 宋桂林 Cosmetic plant extraction of essential oil 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: 20181211

Termination date: 20190418