CN205627167U - Gravity flow plant essential oil extraction system - Google Patents

Gravity flow plant essential oil extraction system Download PDF

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Publication number
CN205627167U
CN205627167U CN201620294699.1U CN201620294699U CN205627167U CN 205627167 U CN205627167 U CN 205627167U CN 201620294699 U CN201620294699 U CN 201620294699U CN 205627167 U CN205627167 U CN 205627167U
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water
coolant
tank
pipe
outlet
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许林兴
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Guangdong Yaohe Biotechnology Co ltd
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Zhongshan City Yao Wo Biotechnology Co Ltd
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Abstract

The utility model discloses a gravity flow plant essential oil extraction system, it includes condenser, refrigerant storage tank, retort and the discharge tank that top -down set gradually, their messenger of mutual UNICOM refrigerant fluids form gravity flow according to its gravity and supply with the state. Be equipped with the refrigerant by pass line between refrigerant storage tank and the retort, supply with state in the internal pressure of refrigerant storage tank and retort in order to form without hindrance gravity flow with the aid of refrigerant by pass line balance. It has advantages such as the extraction is efficient, the essential oil extracts the process lossless, operating power consumption is little, and the extraction process is nontoxic, harmless, and environmental protection, pollution -free, non -thermal processing, the active product that remains the extract product do not destroy, not oxidation, but the big industrialization large -scale production of productivity is energy -conserving, the running cost is low, easily separates with the result, coolant separating is efficient, improves the work efficiency of system at double. It forms through setting up of co -altitude position not flows automatically further energy -conservingly, adopts the bypass to connect the equilibrium pressure in addition and forms the without hindrance work of flowing automatically.

Description

Gravity flow plants essential oil extracting system
[technical field]
This utility model relates to a kind of gravity flow plants essential oil extracting system.
[background technology]
Traditional quintessence oil stems from herbal flower, leaf, root, bark, fruit, seed, resin etc. with distillation, squeezing side Formula extract.Owing to aromatic essential oil volatility is high, it is easy to be absorbed by the body, and people's intracorporeal organ can be permeated rapidly, can put down Weigh internal function, plays the effect of beauty and skin care.Common quintessence oil extracting process has steam distillation, freezing compression method (pressure Squeezing method), chemical solvent extraction, oils and fats partition method (fat suction method), carbon dioxide extraction method, infusion method, currently also have multiple extraction Fetching is put.Current extraction equipment exists that extraction yield is low, inefficiency, device structure complicated, oil-water separation not thoroughly, energy consumption High in cost of production problem.
Such as Chinese utility model patent, the notification number of this patent is CN205133557U, discloses a kind of cinnamon essential oil extraction Fetching is put, and including distillating still, condenser and oil water separator, oil water separator includes that bottom is cylinder in cone, top Tank body, the taper large end face of tank body is upwards connected with cylindrical lower surface, and tank body cylinder-shaped top is provided with and condenser The discharge nozzle of inner space, the conical lower portion of tank body is provided with quintessence oil separation chamber, and the bottom of quintessence oil separation chamber is communicated with flowline, Being provided with balance pipe on the tapered sidewalls of tank body, balance pipe is provided with first flow control valve, the lowest part of balance pipe is higher than The highest point of quintessence oil separation chamber, tank body conical lower section is provided with drain pipe, and balance pipe connects with drain pipe, drain pipe and distillation Still connects, and drain pipe is provided with second flow control valve, and second flow control valve is between the junction point of balance pipe Yu drain pipe And between oil water separator and the junction point of drain pipe.Cinnamon essential oil is layered rapidly by the quintessence oil separation chamber that cross section is less, shortens Time that quintessence oil separates.
In order to overcome above-mentioned problem, we have developed a kind of gravity flow plants essential oil extracting system, and it is applicable to Asia In the device systems of the mode of critical extraction quintessence oil.
[utility model content]
The purpose of this utility model technical problem to be solved is intended to provide a kind of plate to change formula water supply installation and gravity flow Plants essential oil extracting system, its have simple and practical, low cost of manufacture, stable, application is wide, working service is convenient, Good heat insulating, long-lived feature, and the advantage such as extraction efficiency is high, quintessence oil extraction process free of losses, operation energy consumption are little. Therefore, it is technical, practicality and the equipment of the equal top grade of economy.
To achieve these goals, the technical solution adopted in the utility model: a kind of gravity flow plants essential oil extracting system, It includes:
Source pump, described source pump has water-cooling device and the hot water apparatus of heat exchange of Cooling capacity exchanging;Described Water-cooling device passes through the first water intake end and first water side of cold water pipes connecting plate type heat exchanger, and described hot water apparatus is by warm Waterpipe connects the second water intake end and the second water side;
Condenser, coolant storage tank, retort and the discharge tank being sequentially arranged from top to bottom;
Described condenser has coolant the first inlet tube, coolant the first outlet, the first water inlet pipe of connection water-cooling device With the first outlet pipe;
Described coolant storage tank has coolant second inlet tube of connection coolant the first outlet, is formed at coolant storage tank bottom Coolant the second outlet, connect the second water inlet pipe of water-cooling device and the second outlet pipe;
Described retort is located at the lower section of coolant storage tank, and described retort has the coolant the of docking coolant the second outlet Three inlet tubes, the gondola water faucet portion that described 3rd inlet tube is connected in retort;The lower section of described retort is provided with coolant the 3rd Outlet;The peripheral water tank of described first water intake end coupled reaction tank;
Described discharge tank is provided with connection coolant the 4th inlet tube of coolant the 3rd outlet, discharge tank side and is provided with coolant the Four outlets, the first hot water inlet pipe connecting hot water apparatus and the first hot water outlet pipe;
Thermal jacket pipe;It has coolant the 5th inlet tube of connection coolant the 4th outlet, connects coolant the first inlet tube Coolant the 5th outlet, connect the second hot water inlet pipe of hot water apparatus and the second hot water outlet pipe;
Oilless vacuum pump;It is connected between discharge tank and thermal jacket pipe;Described oilless vacuum pump be connected to discharge tank and Between thermal jacket pipe, the pipeline front end of oilless vacuum pump connects ball valve, and rear end connects vacuumizing and exhausting valve.
In one or more embodiments of the present utility model, coolant storage is located at by described second water inlet pipe and the second outlet pipe On the water tank of tank.
In one or more embodiments of the present utility model, described discharge tank is provided with manual ball valve;Described retort has There is the lid that can be repeatedly opened or close;Described condenser, coolant storage tank, retort, discharge tank and the outer surface of thermal jacket pipe It is equipped with the water tank for water route circulation heat exchange.
In one or more embodiments of the present utility model, the water of condenser is located at by described water inlet pipe and the first outlet pipe On casing;Described first hot water inlet pipe and the first hot water outlet pipe set out on the water tank of batch can;Described second hot water inlet Pipe and the second hot water outlet pipe set on the water tank of thermal jacket pipe.
In one or more embodiments of the present utility model, the outer surface of described coolant storage tank, retort and discharge tank All wrap up insulation material.
This utility model is produced beneficial effect compared with background technology:
Owing to using above-mentioned technical scheme, its have simple and practical, low cost of manufacture, stable, application is wide, Working service convenience, good heat insulating, long-lived feature, extraction efficiency height, quintessence oil extraction process free of losses, operation energy consumption The advantage such as little;And extraction process is nontoxic, harmless, environmental protection, pollution-free, non-thermal technology, the biologically active prod of reservation extract do not break Bad, do not aoxidize, production capacity is big, can industrialization large-scale production, energy-conservation, operating cost is low, it is easy to separate with product;Coolant separates effect Rate is high, significantly improves the work efficiency of system;It flows automatically the most energy-conservation by the formation that arranges in differing heights orientation, and Bypass is used to connect balance pressure initiation without hindrance gravity flow work.Therefore, it is technical, practicality and the essence of the equal top grade of economy Oil extraction equipment.
[accompanying drawing explanation]
Fig. 1 is the structural representation of gravity flow plants essential oil extracting system in one embodiment of this utility model.
[detailed description of the invention]
Of the present utility model embodiment is described below in detail, and described embodiment example is shown in the drawings, the most ad initio Represent same or similar element to same or similar label eventually or there is the element of same or like function.
In description of the present utility model, it should be noted that for the noun of locality, if any term " " center ", " laterally ", " longitudinally ", " length ", " width ", " thickness ", " on ", D score, "front", "rear", "left", "right", " vertically ", " level ", " top ", The indicating position such as " end ", " interior ", " outward ", " clockwise ", " counterclockwise " and position relationship are based on orientation shown in the drawings or position Put relation, be for only for ease of narration this utility model and simplify description rather than instruction or the device of hint indication or element Must have specific orientation, with particular orientation structure and operation, it is impossible to be interpreted as limiting concrete protection model of the present utility model Enclose.
Additionally, be only used for describing purpose if any term " first ", " second ", and it is not intended that indicate or imply relatively heavy The property wanted or the implicit quantity indicating technical characteristic.Thus, define " first ", " second " feature can be expressed or imply and include One or more this feature, in this utility model describes, " at least " is meant that one or more, unless otherwise bright The most concrete restriction.In this utility model, except as otherwise clear stipulaties and restriction, " assemble " if any term, " being connected ", " connection " Term should go to understand as broad sense, connects for example, it may be fixing, it is also possible to be to removably connect, or be integrally connected;Can also It is to be mechanically connected;Can be to be joined directly together, it is also possible to be to be connected by intermediary, can be that two element internals are connected. For those of ordinary skills, concrete in this utility model of above-mentioned term can be understood as the case may be Implication.
In this utility model, unless otherwise prescribed and limit, fisrt feature second feature it " on " or D score can To include that the first and second features directly contact, it is also possible to include that fisrt feature is not directly to contact with second feature but passes through Other characterisation contact between them.And, fisrt feature second feature " on ", " under " and " above " include that first is special Levy directly over second feature and oblique upper, or be only the height representing fisrt feature level height higher than second feature.The One feature second feature " on ", " under " and " below " include fisrt feature immediately below second feature or obliquely downward, or It is merely representative of fisrt feature level height less than second feature.
Below in conjunction with the accompanying drawing of description, by detailed description of the invention of the present utility model is further described, make The technical solution of the utility model and beneficial effect thereof are clearer, clear and definite.Describing embodiment below with reference to accompanying drawing is to show Example, it is intended to explain this utility model, and it is not intended that to restriction of the present utility model.
Refer to illustrated in fig. 1, it provides preferably embodiment to be a kind of gravity flow plants essential oil for this utility model Extracting system, it includes source pump 10, its water-cooling device 101 with Cooling capacity exchanging and the hot water apparatus 102 of heat exchange; Condenser 1, coolant storage tank 2, retort 3, discharge tank 4 and the thermal jacket pipe 5 being sequentially connected with.Condenser 1 has coolant first and enters Mouth pipe 11 and coolant the first outlet 12, the water tank of its periphery connects the first water inlet pipe 13 and the first water outlet of water-cooling device 101 Pipe 14;Coolant storage tank 2 has coolant the second inlet tube 21 connecting coolant the first outlet 12 and is formed at coolant storage tank bottom Coolant the second outlet 22, the water tank of its periphery connects the second water inlet pipe 23 and the second outlet pipe 24 of water-cooling device 101; Retort 3 is located at the lower section of coolant storage tank 2, and described retort 2 has coolant the 3rd entrance of docking coolant the second outlet 22 Pipe 31, the gondola water faucet portion 32 that described 3rd inlet tube 31 is connected in retort;The lower section of described retort 3 is provided with coolant the 3rd Outlet 33;Discharge tank 4 is provided with coolant the 4th inlet tube 41 connecting coolant the 3rd outlet 33 pipes, and discharge tank 4 side is provided with cold Matchmaker the 4th outlet 42, the water tank of its periphery connects the first hot water inlet pipe 44 and the first hot water effluent of hot water apparatus 102 Pipe 45;Thermal jacket pipe 5 has coolant the 5th inlet tube 51 and connection coolant the first inlet tube connecting coolant the 4th outlet 42 Coolant the 5th outlet 52 of 11, the water tank of its periphery connects the second hot water inlet 53 pipe and second heat of hot water apparatus 102 Water outlet pipe 54, the clean degree of coolant separation and the efficiency of raising isolated movement, use oilless vacuum pump 9 to be connected to discharge tank 4 With between thermal jacket pipe 5, the pipeline front end of oilless vacuum pump 9 connects ball valve 91, rear end connects vacuumizing and exhausting valve 91.Oil-free is true The effect playing forced-ventilated of empty pump 9, accelerates coolant and separates and discharge, be greatly effectively improved the work efficiency of system.Board-like change Heat is the water-cooling device 101 first water intake end 104 and the first water side 105, the institute by cold water pipes connecting plate type heat exchanger 103 Stating hot water apparatus 102 and connect the second water intake end 106 and the second water side 107 by hot water pipeline, described first water intake end 103 is even Connect the peripheral water tank of retort 3;This plate-type heat-exchange is heated evenly reliably, and extension device service life, to run the temperature difference little, is beneficial to Stability contorting to temperature, the top-down setting of condenser, coolant storage tank, retort and discharge tank, utilize self of coolant Gravity is formed from its streaming supply condition, the most energy-conservation, allows coolant without power consumption, loss-free work.
Further for making stable temperature control so that in tank temperature not with outside air heat exchange, described coolant storage tank 2, The outer surface of retort 3 and discharge tank 4 all wraps up insulation material.
For ease of the collection of quintessence oil, when needing quintessence oil, it is provided with manual ball valve 43, lower section docking essence at described discharge tank 4 Oil recovery tank 6.The outer surface of described condenser 1, coolant storage tank 2, retort 3, discharge tank 4 and thermal jacket pipe 5 is equipped with water supply The water tank 8 of road circulation heat exchange.The temperature utilizing water route regulates coolant phase transformation in water tank 8 flowing.
When needing to put into the extraction materials such as the flower of plant, leaf, skin, retort 3 has the lid that can be repeatedly opened or close Body 34.During use, retort 3 built-in extraction material, coolant enter from coolant storage tank 2 flow downwardly into gondola water faucet portion 32 spill be scattered to extraction Taking and enter into discharge tank 4 with the quintessence oil in extraction plant on material, heating at discharge tank 4 makes coolant phase transformation of being heated be located away from quintessence oil Enter back into thermal jacket pipe 5 to be heated further and return to condenser 1 and enter back into coolant storage tank 2 and so circulate.Coolant storage tank 2 is with anti- Answer and between tank 3, be provided with coolant by-pass line 25, when the retort 3 under gravity flow state occurs that pressure is higher, open by coolant Thread a pipe 25 UNICOMs, and such pressure will reach poised state, is formed without hindrance from stream mode.Therefore, it has simple in construction in fact By, low cost of manufacture, stable, application is wide, working service convenience, good heat insulating, long-lived feature, and extracts The advantage such as efficiency height, quintessence oil extraction process free of losses, operation energy consumption are little;And extraction process is nontoxic, harmless, environmental protection, pollution-free, Non-thermal technology, the biologically active prod retaining extract do not destroy, do not aoxidize, production capacity is big, can industrialization large-scale production, energy-conservation, fortune Row low cost, it is easy to separate with product.Therefore, it is technical, practicality and the quintessence oil extraction equipment of the equal top grade of economy.
The water-cooling device 101 of source pump 10 and hot water apparatus 102;Use air energy, effectively save power consumption, Er Qieke Exchanging with generation cold energy and heat energy, water-cooling device 101 connects condenser 1 and the water tank of coolant storage tank 2 periphery needing cold; Hot water apparatus 102 connects to be needed heat to make coolant separate and accelerates discharge tank 4 and the water tank of thermal jacket pipe 5 periphery separated.When So can add electric heating on hot water apparatus outlet pipe to supplement, suitably supply in the case of air source deficiency to make up; Also it is a preferably additional project.
The gravity flow plants essential oil extracting system of the present embodiment can be applicable to the equipment of subcritical plant extraction method.
Subcritical abstraction (Sub-critical fluid extraction technology) is to utilize subcritical fluids (coolant) as extractant, in airtight, anaerobic.In the pressure vessel of low pressure, according to the similar principle mixed of Organic substance, pass through Extraction material and extractant molecule diffusion process in immersion process, the liposoluble constituent reached in solid material transfers to liquid In the extractant of state, then by the process being evaporated under reduced pressure, extractant is separated with purpose product, finally give the one of purpose product Plant novel extraction and isolation technics.
In the description of description, reference term " embodiment ", " preferably ", " example ", " concrete example " or " one A little examples " etc. description means to combine this embodiment or example describes specific features, structure, material or feature, be contained in In at least one embodiment of the present utility model or example, in this manual for above-mentioned term schematic representation not necessarily Refer to identical embodiment or example.And, the specific features of description, structure, material or feature can be any one Individual or multiple embodiment or example combine in a suitable manner.
By above-mentioned structure and the description of principle, person of ordinary skill in the field should be appreciated that this utility model It is not limited to above-mentioned detailed description of the invention, on the basis of this utility model, uses the improvement of techniques well known and substitute all Fall at protection domain of the present utility model, should be limited it by each claim.

Claims (5)

1. a gravity flow plants essential oil extracting system, it is characterised in that it includes:
Source pump, described source pump has water-cooling device and the hot water apparatus of heat exchange of Cooling capacity exchanging;Described cold water Device passes through the first water intake end and first water side of cold water pipes connecting plate type heat exchanger, and described hot water apparatus passes through hot-water line Road connects the second water intake end and the second water side;
Condenser, coolant storage tank, retort and the discharge tank being sequentially arranged from top to bottom;
Described condenser has coolant the first inlet tube, coolant the first outlet, connects first water inlet pipe and the of water-cooling device One outlet pipe;
Described coolant storage tank has coolant second inlet tube of connection coolant the first outlet, is formed at the cold of coolant storage tank bottom Matchmaker's the second outlet, the second water inlet pipe connecting water-cooling device and the second outlet pipe;
Described retort is located at the lower section of coolant storage tank, and described retort has the coolant the 3rd of docking coolant the second outlet and enters Mouth pipe, the gondola water faucet portion that described 3rd inlet tube is connected in retort;The lower section of described retort is provided with coolant the 3rd outlet Pipe;The peripheral water tank of described first water intake end coupled reaction tank;
Described discharge tank is provided with connection coolant the 4th inlet tube of coolant the 3rd outlet, discharge tank side is provided with coolant the 4th and goes out Mouth pipe, the first hot water inlet pipe connecting hot water apparatus and the first hot water outlet pipe;
Thermal jacket pipe;It has coolant the 5th inlet tube of connection coolant the 4th outlet, connects the cold of coolant the first inlet tube Matchmaker the 5th outlet, the second hot water inlet pipe connecting hot water apparatus and the second hot water outlet pipe;
Oilless vacuum pump;It is connected between discharge tank and thermal jacket pipe;Described oilless vacuum pump is connected to discharge tank and heat folder Between sleeve pipe, the pipeline front end of oilless vacuum pump connects ball valve, and rear end connects vacuumizing and exhausting valve.
Gravity flow plants essential oil extracting system the most according to claim 1, it is characterised in that: described second water inlet pipe and Two outlet pipes are located on the water tank of coolant storage tank.
Gravity flow plants essential oil extracting system the most according to claim 1, it is characterised in that: described discharge tank is provided with manually Ball valve;Described retort has the lid that can be repeatedly opened or close;Described condenser, coolant storage tank, retort, discharge tank and The outer surface of thermal jacket pipe is equipped with the water tank for water route circulation heat exchange.
Gravity flow plants essential oil extracting system the most according to claim 3, it is characterised in that: described first water inlet pipe and One outlet pipe is located on the water tank of condenser;Described first hot water inlet pipe and the first hot water outlet pipe set out the water tank of batch can On body;Described second hot water inlet pipe and the second hot water outlet pipe set on the water tank of thermal jacket pipe.
Gravity flow plants essential oil extracting system the most according to claim 4, it is characterised in that: described coolant storage tank, reaction The outer surface of tank and discharge tank all wraps up insulation material.
CN201620294699.1U 2016-04-11 2016-04-11 Gravity flow plant essential oil extraction system Active CN205627167U (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106635422A (en) * 2016-12-13 2017-05-10 郑存义 Flowering plant essential oil vacuum extraction process and device
CN109628229A (en) * 2019-02-18 2019-04-16 中山市曜禾生物技术有限公司 Superconduction soaking type essential oil extracting system
CN111763572A (en) * 2020-07-08 2020-10-13 湖北瑞晟生物有限责任公司 Freezing compressor arrangement is used in essential oil secondary extraction

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106635422A (en) * 2016-12-13 2017-05-10 郑存义 Flowering plant essential oil vacuum extraction process and device
CN109628229A (en) * 2019-02-18 2019-04-16 中山市曜禾生物技术有限公司 Superconduction soaking type essential oil extracting system
CN111763572A (en) * 2020-07-08 2020-10-13 湖北瑞晟生物有限责任公司 Freezing compressor arrangement is used in essential oil secondary extraction
CN111763572B (en) * 2020-07-08 2022-05-20 湖北瑞晟生物有限责任公司 Freezing compressor arrangement is used in essential oil secondary extraction

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C14 Grant of patent or utility model
GR01 Patent grant
CP01 Change in the name or title of a patent holder

Address after: 528400 Office No. 2, No. 2 Shing Shi Road, Jin Tao commercial building, Zhongshan, Guangdong.

Patentee after: Guangdong Yaohe Biotechnology Co.,Ltd.

Address before: 528400 Office No. 2, No. 2 Shing Shi Road, Jin Tao commercial building, Zhongshan, Guangdong.

Patentee before: ZHONGSHAN YAOHE BIOTECHNOLOGY CO.,LTD.

CP01 Change in the name or title of a patent holder