CN203253191U - Novel multifunctional extraction pot - Google Patents

Novel multifunctional extraction pot Download PDF

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Publication number
CN203253191U
CN203253191U CN 201320073648 CN201320073648U CN203253191U CN 203253191 U CN203253191 U CN 203253191U CN 201320073648 CN201320073648 CN 201320073648 CN 201320073648 U CN201320073648 U CN 201320073648U CN 203253191 U CN203253191 U CN 203253191U
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CN
China
Prior art keywords
tank body
wiper seal
frame columns
seal lid
extractor
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Withdrawn - After Issue
Application number
CN 201320073648
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Chinese (zh)
Inventor
阴耕云
徐世涛
魏杰
刘劲芸
韩智强
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.)
Yunnan Academy of Tobacco Science
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Yunnan Academy of Tobacco Science
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Publication date
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Priority to CN 201320073648 priority Critical patent/CN203253191U/en
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Publication of CN203253191U publication Critical patent/CN203253191U/en
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Abstract

The utility model relates to a novel multifunctional extraction pot which is especially suitable for extracting crude products of essential oil, tincture, and extract paste. The utility model belongs to the technical field of plant extraction. The pot body of the pot is a straight cylinder. Pneumatic pressure sealing covers are provided on two ends of the pot body. Movable straight cylindrical multilayer porous frame columns are arranged in the straight cylinder pot body. The diameters of the outer periphery of the frame columns are consistent with the inner diameter of the cylinder body. The heights of the frame columns are 10-500cm. A height range of frame column separator layers is 5-50cm. Stopping nails are arranged on the end in the straight cylinder body, such that the positions of the frame columns can be fixed. The frame columns can be temporarily placed into the cylinder body according to needs. An interlayer heating jacket is arranged on the periphery of the pot body. A steam pipe and a material filtering net are arranged in the lower-end sealing cover. Steam can be delivered in from the cover, and material primary filtering can be realized. When the cover is opened, slag discharge can be carried out. A material filtering net is arranged in the upper-end sealing cover. A steam outlet is arranged at the center of the top end. The upper-end sealing cover is connected with a condenser and an oil-water separator on the back end through detachable pipes. When the cover is opened, the frame columns inside the cylinder can be fetched or placed.

Description

A kind of Multifunction extractor
Technical field
The utility model relates to a kind of Multifunction extractor, is specially adapted to extract the extractor of the head product of essential oil, tincture, medicinal extract.Belong to the herbal extraction equipment technical field.
Background technology
Derived essential oil in the fragrant plant adopts extraction by steam distillation mostly.Steam distillation means containing spice berry and the water condistillation of volatile ingredient, and volatile ingredient is distillated in the lump with steam, divides the leach extraction method of getting volatile ingredient through condensation.The method is applicable to have volatility, can be destroyed with steam distillation, the lixiviate of stable and indissoluble or water-fast medicinal ingredient in water.Steam distillation can be divided into common hydrodistillation, water flowing steam distillation method, water and steam distillation method.For improving the concentration of distillate, generally need distillate is carried out redistillation or salt adding redistillation.
Extraction means transfers to extracting method in the suitable solvent with the DDGS in the spices.Temperature can be divided into cold extraction and two kinds of conventional methods are extracted in hot reflux by extracting, and solvent can be selected according to dissolubility, the polarity of extracting target product.
Steam distillation and extraction are not only different aspect the principle, and the equipment that adopts in the leaching process also there are differences.Traditional extraction equipment can't satisfy the demand of above-mentioned two kinds of extracting methods simultaneously, if extract essential oil product and tincture, medicinal extract product, still needs to purchase two and overlaps process equipments.
Summary of the invention
The purpose of this utility model is to overcome the prior art deficiency, invents a kind of Multifunction extractor.This extractor equipment can be used for steam distillation, can be used for extraction again, for the user saves the procuring equipment expense, has improved simultaneously capacity utilization.
The structure of the utility model Multifunction extractor is: a kind of Multifunction extractor, the middle part that it is characterized in that extractor is the identical straight tube cylindrical tank of internal diameter, tank body (1) up and down two ends respectively is equipped with the wiper seal lid (2 that can open, 3), the inwall of tank base is equipped with several bails perpendicular to inwall (4), place several multilayer movable porous frame hurdles (5) in the tank body, be placed with the material filtering net in the upper end wiper seal lid (2), the center, top of upper end wiper seal lid (2) has outlet (6), and outlet (6) links to each other by the detachable pipeline in ring flange and outside; The built-in steam pipe of lower end seal cover (3) and material filtering net, whole tank body is peripherally equipped with the interlayer heating jacket.
Frame hurdle (5) outside diameter and tank body middle part internal diameter are complementary, tank body middle part inwall can be freely put into or be taken out on frame hurdle (5), each frame hurdle (5) altitude range exists: 10cm ~ 500cm, the interlayer altitude range between frame hurdle (5) and frame hurdle (5) exists: 5cm ~ 50cm.
Described bail perpendicular to inwall (4) length is 2-5cm.
Being placed with separately material filtering grid specification in upper end wiper seal lid (2) and the lower end wiper seal lid (3) is 14 * 13mm perforated plate.
Operation principle is: when adopting extraction to produce medicinal extract or tincture, the closed lower end seal cover, directly drop into extractor in by the loam cake of opening material, the pipeline of the airtight rear connection tank body top central outlet of loam cake and condenser, treat that solvent enters in the tank body in proportion, the indexs such as predetermined process conditions temperature (by the steam that passes into, the control of tank body heating jacket), time are carried out processing routinely again; In the leaching process, capture simultaneously by the steam of the tank body top central outlet volatile ingredient to condenser, oil water separator.After the completion of processing, liquid to be extracted tentatively filters, drained after, open the lower end seal cover, carry out deslagging, cleaning; In oil water separator, obtain the volatile oil that might obtain.
When adopting the way of distillation to produce essential oil, at first material is put into multilayer, porous frame hurdle, the laying method of every layer of material will note avoiding cloth blocked up, excessively loose.The closed lower end seal cover, extractor is vertically put into by the loam cake of opening in the frame hurdle of placing material, the pipeline of the airtight rear connection tank body top central outlet of loam cake and condenser, open steam, distill processing by indexs such as predetermined technique initialization temperature (by the steam that passes into, the control of tank body heating jacket), time, pressure, supplementary set is by the volatile oil component of tank body top central outlet to condenser, oil water separator.After the completion of processing, open loam cake, propose frame hurdle, deslagging; Opening lower cover cleans; The volatile oil that in oil water separator, acquires.
The utlity model has following advantage:
This extractor can satisfy the demand of conventional extraction, and can carry out simultaneously the supplementary set of volatile ingredient; By inserting of built-in frame hurdle, this equipment can also satisfy the demand that the way of distillation is extracted.Thereby realize that a tank is multiplex, effectively save the equipment investment cost, reduce process equipment space hold rate.
Description of drawings:
Below in conjunction with implementation column shown in the attached body, the present utility model structure is described further, but protection domain is not limited to this implementation column.
Structural representation when Fig. 1 uses the extraction essential oil as the way of distillation, its center hurdle parts are placed in the tank body.
Schematic internal view when Fig. 2 act as extraction use extraction medicinal extract, tincture
Number in the figure: 1-Tank body; 2 -Upper end wiper seal lid; 3-lower end wiper seal lid; 4-bail; 5-porous frame hurdle; 6-outlet, 7 -Be connected to the pipeline of cooler or oil water separator.
The specific embodiment
The utility model tank body is shaped as straight tube shape cylinder, each dress of two ends is hinged with a pneumatic type wiper seal lid 2,3, place several removable straight tube circular multilayers, porous frame hurdle 5 in the straight tube shape cylinder tank body, the external diameter on each porous frame hurdle 5 and tank body 1 internal diameter coupling can freely be put into or take out.Each porous frame hurdle 5 altitude range exists: 10cm ~ 500cm, and the interlayer altitude range between porous frame hurdle and the porous frame hurdle exists: 5cm ~ 50cm; End or the bottom of straight tube cylinder tank interior are provided with bail 4, put with fixed placement porous frame field within it, and porous frame hurdle can be put into inner barrel according to actual needs temporarily; This tank body is with the interlayer heating jacket outward.
Be equipped with or be placed with a steam pipe and material filtering net in the lower end wiper seal lid 3, by lower end wiper seal lid 3, may input steam and realize the preliminary filtration of material, open lower end wiper seal and cover 3, can be used for deslagging.
2 are equipped with or place the material filtering net in the seal cover of upper end, and center, seal cover top, upper end is provided with a steam (vapor) outlet, links to each other with the oil water separator of condenser and rear end by the detachable pipeline in steam (vapor) outlet and outside.
Embodiment 1:(extraction)
As shown in Figure 2, when adopting extraction to produce hawthorn extract, the closed lower end seal cover, directly drop into extractor in by the loam cake of opening haw raw material, the pipeline of airtight rear connection tank body top central outlet and condenser is built in loam cake wiper seal, ethanol is added in the tank body in proportion, carry out processing by indexs such as predetermined technique initialization temperature, times again; In the leaching process, supplementary set is by the volatile ingredient of tank body top central outlet to condenser, oil water separator simultaneously.After the completion of processing, liquid to be extracted tentatively filters, drained after, open lower end wiper seal lid, carry out deslagging, cleaning.With the haw thorn extract head product that gets access to, the separation by the back segment operation, purification, the operation such as concentrated are obtained hawthorn extract at last.
The embodiment 2:(way of distillation)
As shown in Figure 1, when adopting the way of distillation to produce geranium oil, at first material is put into 6 layers (floor height 30cm), porous frame hurdle, every layer of material wanted evenly, divided placement, prevents from running vapour.Closed lower end wiper seal lid is vertically put into the extractor tank body with the frame hurdle of placing material by the loam cake of opening, and by the bail 4 of inner bottom fixedly porous frame field put.The pipeline that connects tank body top central outlet and condenser behind the airtight loam cake wiper seal lid, open steam, distill processing by predetermined technique initialization temperature, time, pressure index, supplementary set is by the volatile oil component of tank body top central outlet to condenser, oil water separator.After the completion of processing, open loam cake wiper seal lid, propose porous frame hurdle, deslagging; Opening lower cover wiper seal lid cleans; The first oil of the geranium oil that acquires in oil water separator is in order to following process.

Claims (2)

1. Multifunction extractor, the middle part that it is characterized in that extractor is the identical straight tube cylindrical tank of internal diameter, tank body (1) up and down two ends respectively is equipped with the wiper seal lid (2,3) that can open, the inwall of tank base is equipped with several bails perpendicular to inwall (4), place several multilayer movable porous frame hurdles (5) in the tank body, be placed with the material filtering net in the upper end wiper seal lid (2), the center, top of upper end wiper seal lid (2) has outlet (6), and outlet (6) links to each other by the detachable pipeline in ring flange and outside; The built-in steam pipe of lower end seal cover (3) and material filtering net, whole tank body is peripherally equipped with the interlayer heating jacket.
2. according to wanting profit to require 1 described Multifunction extractor, it is characterized in that frame hurdle (5) outside diameter and tank body middle part internal diameter is complementary, tank body middle part inwall can be freely put into or be taken out on frame hurdle (5), each frame hurdle (5) altitude range exists: 10cm ~ 500cm, the interlayer altitude range between frame hurdle (5) and frame hurdle (5) exists: 5cm ~ 50cm.
3, according to wanting profit to require 1 described Multifunction extractor, it is characterized in that described bail perpendicular to inwall (4) length is 2-5cm.
4, according to wanting profit to require 1 described Multifunction extractor, it is characterized in that being placed with separately material filtering grid specification in upper end wiper seal lid (2) and the lower end wiper seal lid (3) is 14 * 13mm perforated plate.
CN 201320073648 2013-02-17 2013-02-17 Novel multifunctional extraction pot Withdrawn - After Issue CN203253191U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201320073648 CN203253191U (en) 2013-02-17 2013-02-17 Novel multifunctional extraction pot

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201320073648 CN203253191U (en) 2013-02-17 2013-02-17 Novel multifunctional extraction pot

Publications (1)

Publication Number Publication Date
CN203253191U true CN203253191U (en) 2013-10-30

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CN 201320073648 Withdrawn - After Issue CN203253191U (en) 2013-02-17 2013-02-17 Novel multifunctional extraction pot

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CN (1) CN203253191U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103087827A (en) * 2013-02-17 2013-05-08 云南烟草科学研究院 Comprehensive extraction method using novel multifunctional tank
CN105038992A (en) * 2015-09-01 2015-11-11 湖南时代阳光药业股份有限公司 Multifunctional volatile oil distilling and extracting tank
CN106730984A (en) * 2017-01-07 2017-05-31 云南中烟工业有限责任公司 It is a kind of with the steam extraction device of silicagel column separator and its application
CN113150873A (en) * 2021-05-25 2021-07-23 福建农林大学 Cinnamomum camphora essential oil direct steam distillation pot

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103087827A (en) * 2013-02-17 2013-05-08 云南烟草科学研究院 Comprehensive extraction method using novel multifunctional tank
CN105038992A (en) * 2015-09-01 2015-11-11 湖南时代阳光药业股份有限公司 Multifunctional volatile oil distilling and extracting tank
CN106730984A (en) * 2017-01-07 2017-05-31 云南中烟工业有限责任公司 It is a kind of with the steam extraction device of silicagel column separator and its application
CN113150873A (en) * 2021-05-25 2021-07-23 福建农林大学 Cinnamomum camphora essential oil direct steam distillation pot

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C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20131030

Effective date of abandoning: 20140806

RGAV Abandon patent right to avoid regrant