CN205627169U - Extraction discharge tank and plant essential oil extraction system - Google Patents

Extraction discharge tank and plant essential oil extraction system Download PDF

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Publication number
CN205627169U
CN205627169U CN201620295740.7U CN201620295740U CN205627169U CN 205627169 U CN205627169 U CN 205627169U CN 201620295740 U CN201620295740 U CN 201620295740U CN 205627169 U CN205627169 U CN 205627169U
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coolant
water
extraction
outlet
pipe
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CN201620295740.7U
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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 an extraction discharge tank and plant essential oil extraction system should extract discharge tank and be equipped with refrigerant fourth inlet tube, extraction discharge tank one side of connecting refrigerant third outlet pipe and be equipped with refrigerant fourth outlet pipe, hot water import pipe and first hot water outlet pipe, the extraction discharge tank outside is surrounding the water tank, the water tank communicates with each other in hot water import pipe and first hot water outlet pipe, the oil -free vacuum pump is connected to refrigerant fourth outlet pipe. It is in advantages such as essential oil extraction process lossless, operating power consumption are 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, and the productivity is big, energy -conserving, the running cost is low, easily separates with the result, coolant separating is efficient, improves the work efficiency of system at double.

Description

Extract batch can and plants essential oil extracting system
[technical field]
This utility model relates to one and extracts batch can and plants essential oil extracting system.
[background technology]
Traditional quintessence oil stems from herbal flower, leaf, root, bark, fruit, seed, resin etc. and extract with distillation, squeezing mode.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 function in balanced body, play the effect of beauty and skin care.
Common quintessence oil extracting process has steam distillation, freezing compression method (milling process), chemical solvent extraction, oils and fats partition method (fat suction method), carbon dioxide extraction method, infusion method, currently also has multiple extraction equipment.There is the problems such as extraction yield is low, inefficiency, device structure complicated, oil-water separation is thorough, energy consumption cost is high in current extraction equipment.
nullSuch as Chinese utility model patent,The notification number of this patent is CN205133557U,Disclose a kind of cinnamon essential oil extraction equipment,Including distillating still、Condenser and oil water separator,Oil water separator includes that bottom is cone、Top is in cylindrical tank body,The taper large end face of tank body is upwards connected with cylindrical lower surface,Tank body cylinder-shaped top is provided with and the discharge nozzle of condenser inner space,The conical lower portion of tank body is provided with quintessence oil separation chamber,The bottom of quintessence oil separation chamber is communicated with flowline,It is provided with balance pipe on the tapered sidewalls of tank body,First flow control valve it is provided with on balance pipe,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,Balance pipe connects with drain pipe,Drain pipe connects with distillating still,Second flow control valve it is provided with on drain pipe,Second flow control valve is between balance pipe and the junction point of drain pipe and 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 the time that quintessence oil separates.
In order to overcome above-mentioned problem, we have developed one and extract batch can and plants essential oil extracting system, in the device systems of its mode being applicable to subcritical abstraction quintessence oil.
[utility model content]
The purpose of this utility model technical problem to be solved is intended to provide one to extract batch can and plants essential oil extracting system, it has simple and practical, low cost of manufacture, stable, application is wide, working service convenience, 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: one extracts batch can, this extracts batch can and is provided with and connects coolant the 4th inlet tube of coolant the 3rd outlet, extract batch can side and be provided with coolant the 4th outlet, the first hot water inlet pipe and the first hot water outlet pipe;Extracting and surround water tank outside batch can, described water tank is in communication with the first hot water inlet pipe and the first hot water outlet pipe;Coolant the 4th outlet connects oilless vacuum pump.
In the one or more embodiment of this utility model, it also includes that lid, described lid are provided with the first observation window, the first manometer and the first temperature sensor.
Under same design, this utility model also provides for a kind of plants essential oil extracting system, and 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 connects the second water intake end and the second water side by hot water pipeline;
Coolant circulating system it include the condenser being sequentially arranged from top to bottom, coolant storage tank, extraction hold material retort and claim 1-2 according to any one of extract batch can;Described condenser has coolant the first inlet tube, coolant the first outlet, the first water inlet pipe connecting water-cooling device and the first outlet pipe;Coolant the second outlet, the second water inlet pipe of connection water-cooling device and the second outlet pipe that described coolant storage tank has coolant the second inlet tube connecting coolant the first outlet, is formed at coolant storage tank bottom;Described extraction is held material retort and is located at the lower section of coolant storage tank, and described extraction is held material retort and had coolant the 3rd inlet tube of docking coolant the second outlet, and described 3rd inlet tube is connected at extraction and holds the gondola water faucet portion in material retort;Described gondola water faucet portion is laid with multiple mouth spray, is provided with appearance bin below described gondola water faucet portion, holds bin and is provided with multilamellar placement plate;Described extraction is held the periphery of material retort and is provided with water tank, and water tank has the tank entry and pipe outlet passed through for water route;Described extraction appearance material retort has the lower section of extraction appearance material retort described in lid and is provided with coolant the 3rd outlet;Described first water intake end connects extraction and holds the peripheral water tank of material retort;
Described coolant circulating system also includes thermal jacket pipe;Coolant the 5th outlet, the second hot water inlet pipe of connection hot water apparatus and the second hot water outlet pipe that described jacket pipe has coolant the 5th inlet tube connecting coolant the 4th outlet, connects coolant the first inlet tube;
Described oilless vacuum pump is connected to extract between batch can and thermal jacket pipe, and the pipeline front end of oilless vacuum pump connects ball valve, and rear end connects vacuumizing and exhausting valve.
In the one or more embodiment of this utility model, described in extract batch can and be provided with manual ball valve;Described condenser, coolant storage tank, extraction hold material retort, extract the outer surface of batch can and thermal jacket pipe and be equipped with the water tank for water route circulation heat exchange.
This utility model is produced beneficial effect compared with background technology:
Owing to using above-mentioned technical scheme, the advantages such as it has simple and practical, low cost of manufacture, stable, application is wide, working service convenience, good heat insulating, long-lived feature, and extraction 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 of reservation extract do not destroy, 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 separation efficiency 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 uses bypass to connect balance pressure initiation without hindrance gravity flow work.Therefore, it is technical, practicality and the quintessence oil extraction equipment of the equal top grade of economy.
[accompanying drawing explanation]
Fig. 1 is the structural representation of plants essential oil extracting system in one embodiment of this utility model;
Fig. 2 is the structural representation that in one embodiment of this utility model, material retort is held in extraction;
Fig. 3 is the structural representation extracting batch can 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, and the most same or similar label represents same or similar element or has 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 ", " afterwards ", " left ", " right ", " vertically ", " level ", " push up ", " end ", " interior ", " outward ", " clockwise ", indicating positions such as " counterclockwise " and position relationship are based on orientation shown in the drawings or position relationship, it is for only for ease of narration this utility model and simplifies description, rather than indicate or imply that the device of indication or element must have specific orientation, with particular orientation structure and operation, it is not intended that limit concrete protection domain of the present utility model.
Additionally, be only used for describing purpose if any term " first ", " second ", and it is not intended that indicate or imply relative importance or the implicit quantity indicating technical characteristic.Thus, defining " first ", " second " feature can be expressed or implicit include one or more this feature, in this utility model describes, " at least " is meant that one or more, unless otherwise expressly limited specifically.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, connect for example, it may be fixing, it is also possible to be to removably connect, or be integrally connected;Can also be 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, above-mentioned term concrete meaning in this utility model can be understood as the case may be.
In this utility model, unless otherwise prescribed and limit, fisrt feature second feature it " on " or D score can include that the first and second features directly contact, it is also possible to include that fisrt feature and second feature are not directly contact but by the other characterisation contact between them.And, fisrt feature second feature " on ", " under " and " above " include that fisrt feature directly over second feature and oblique upper, or is only the height representing fisrt feature level height higher than second feature.Fisrt feature second feature " on ", " under " and " below " include that fisrt feature immediately below second feature or obliquely downward, or 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 clearer, clear and definite.It is exemplary for describing embodiment below with reference to accompanying drawing, 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 plants essential oil extracting system for this utility model, and it includes coolant circulating system and water passage circulation system;Described coolant circulating system includes that condenser 1, coolant storage tank 2, extraction are held material retort 3, extracted batch can 4 and thermal jacket pipe 5, and they are connected and form peripheral passage for coolant.Described water passage circulation system includes that source pump 10, source pump 10 have water-cooling device 101 and the hot water apparatus 102 of heat exchange of Cooling capacity exchanging;The condenser 1 that is sequentially connected with, coolant storage tank 2, extraction are held material retort 3, are extracted batch can 4 and thermal jacket pipe 5.Condenser 1 has coolant the first inlet tube 11 and coolant the first outlet 12, and the water tank of its periphery connects the first water inlet pipe 13 and the first outlet pipe 14 of water-cooling device 101;Coolant storage tank 2 has coolant the second inlet tube 21 connecting coolant the first outlet 12 and coolant the second outlet 22 being formed at coolant storage tank bottom, and the water tank of its periphery connects the second water inlet pipe 23 and the second outlet pipe 24 of water-cooling device 101;Extraction is held material retort 3 and is located at the lower section of coolant storage tank 2, and described extraction is held material retort 2 and had coolant the 3rd inlet tube 31 of docking coolant the second outlet 22, and described 3rd inlet tube 31 is connected at extraction and holds the gondola water faucet portion 32 in material retort;Described extraction is held the lower section of material retort 3 and is provided with coolant the 3rd outlet 33;Extract batch can 4 and be provided with coolant the 4th inlet tube 41 connecting coolant the 3rd outlet 33 pipes, extract batch can 4 side and be provided with coolant the 4th outlet 42, the water tank of its periphery connects the first hot water inlet pipe 44 and the first hot water outlet pipe 45 of hot water apparatus 102;Thermal jacket pipe 5 has coolant the 5th inlet tube 51 connecting coolant the 4th outlet 42 and coolant the 5th outlet 52 connecting coolant the first inlet tube 11, the second hot water inlet 53 pipe and the second hot water outlet pipe 54 of hot water apparatus 102 is connected on the water tank of its periphery, the clean degree of coolant separation and the efficiency of raising isolated movement, oilless vacuum pump 9 is used to be connected to extract between batch can 4 and thermal jacket pipe 5, the pipeline front end of oilless vacuum pump 9 connects ball valve 91, and rear end connects vacuumizing and exhausting valve 91.The effect playing forced-ventilated of oilless vacuum pump 9, accelerates coolant and separates and discharge, be greatly effectively improved the work efficiency of system.Plate-type heat-exchange is the water-cooling device 101 first water intake end 104 and the first water side 105 by cold water pipes connecting plate type heat exchanger 103, described hot water apparatus 102 connects the second water intake end 106 and the second water side 107 by hot water pipeline, and described first water intake end 103 connects extraction and holds the peripheral water tank of material retort 3;This plate-type heat-exchange is heated evenly reliably, extension device service life, to run the temperature difference little, it is beneficial to the stability contorting to temperature, condenser, coolant storage tank, extraction are held material retort and extract the top-down setting of batch can, the self gravitation utilizing coolant is formed from its streaming supply condition, the most energy-conservation, allow coolant without power consumption, loss-free work.
Further for making stable temperature control so that in tank temperature not with outside air heat exchange, hold material retort 3 in described coolant storage tank 2, extraction and extract the outer surface of batch can 4 and all wrap 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 quintessence oil recycling can 6 at the described batch can 4 that extracts.Described condenser 1, coolant storage tank 2, extraction hold material retort 3, extract the outer surface of batch can 4 and thermal jacket pipe 5 and be equipped with the water tank 8 for water route circulation heat exchange.The temperature utilizing water route regulates coolant phase transformation in water tank 8 flowing.
As shown in Figure 2, this concrete extraction is provided with in holding material retort 3 and includes that one end extends to the gondola water faucet portion 32 outside tank, described gondola water faucet portion 32 is laid with multiple mouth spray 321, is provided with appearance bin 35 below described gondola water faucet portion 32, holds bin and is provided with multilamellar placement plate 351;Extraction is held the periphery of material retort and is provided with water tank 8, and water tank 8 has the tank entry 81 and pipe outlet 82 passed through for water route;Described extraction is held material retort and is had lid 34.Described lid 34 is provided with observation window 341, manometer 342 and temperature sensor 343.
As illustrated in FIG. 3, concrete extracts batch can 4, and this extracts batch can and is provided with and connects coolant the 4th inlet tube 41 of coolant the 3rd outlet 33, extract batch can 4 side and be provided with coolant the 4th outlet the 42, first hot water inlet pipe 44 and the first hot water outlet pipe 45;Extracting and surround water tank 8 outside batch can, described water tank 8 is in communication with the first hot water inlet pipe 44 and the first hot water outlet pipe 45;Coolant the 4th outlet 42 connects oilless vacuum pump 9.It also includes that lid 46, lid 46 are provided with the first observation window the 461, first manometer 462 and the first temperature sensor 463.
When needing to put into the extraction materials such as the flower of plant, leaf, skin, extraction is held material retort 3 and is had the lid 34 that can be repeatedly opened or close.During use, material retort 3 built-in extraction material is held in extraction, coolant enters and flows downwardly into gondola water faucet portion 32 from coolant storage tank 2 and spill to be scattered to extract material enter into the quintessence oil in extraction plant and extract batch can 4, heats make coolant phase transformation of being heated be located away from quintessence oil and enter back into thermal jacket pipe 5 and be heated further and return to condenser 1 and enter back into coolant storage tank 2 and so circulate extracting batch can 4.Being provided with coolant by-pass line 25 between coolant storage tank 2 and extraction appearance material retort 3, when the extraction appearance material retort 3 under gravity flow state occurs that pressure is higher, open coolant by-pass line 25 UNICOM, such pressure will reach poised state, is formed without hindrance from stream mode.Therefore, it has simple and practical, low cost of manufacture, stable, application is wide, working service convenience, 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;And extraction process is nontoxic, harmless, environmental protection, pollution-free, non-thermal technology, the biologically active prod of reservation extract do not destroy, 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.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;Using air energy, effectively save power consumption, and can produce cold energy and heat energy exchanges, water-cooling device 101 connects condenser 1 and the water tank of coolant storage tank 2 periphery needing cold;Hot water apparatus 102 connect need heat make coolant separate and accelerate separate extract batch can 4 and the water tank of thermal jacket pipe 5 periphery.Supplement it is of course possible to add electric heating on hot water apparatus outlet pipe, suitably supply in the case of air source deficiency to make up;Also it is a preferably additional project.
The 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) be 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, by extraction material and extractant molecule diffusion process in immersion process, reach in the extractant that the liposoluble constituent in solid material transfers to liquid, extractant is separated by the process by being evaporated under reduced pressure with purpose product again, finally gives a kind of novel extraction and the isolation technics of purpose product.
In the description of description, the description of reference term " embodiment ", " preferably ", " example ", " concrete example " or " some examples " etc. means to combine this embodiment or specific features, structure, material or the feature of example description, being contained at least one embodiment of the present utility model or example, the schematic representation for above-mentioned term is not necessarily referring to identical embodiment or example in this manual.And, the specific features of description, structure, material or feature can combine in any one or more embodiments or example in a suitable manner.
By above-mentioned structure and the description of principle; person of ordinary skill in the field is to be understood that; this utility model is not limited to above-mentioned detailed description of the invention; the improvement and the replacement that use techniques well known on the basis of this utility model all fall within protection domain of the present utility model, should be limited it by each claim.

Claims (4)

1. one kind extracts batch can, it is characterised in that this extracts batch can and is provided with and connects coolant the 4th inlet tube of coolant the 3rd outlet, extract batch can side and be provided with coolant the 4th outlet, the first hot water inlet pipe and the first hot water outlet pipe;Extracting and surround water tank outside batch can, described water tank is in communication with the first hot water inlet pipe and the first hot water outlet pipe;Coolant the 4th outlet connects oilless vacuum pump.
The most according to claim 1 extract batch can, it is characterised in that: it also includes that lid, described lid are provided with the first observation window, the first manometer and the first temperature sensor.
3. a 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 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 connects the second water intake end and the second water side by hot water pipeline;
Coolant circulating system it include the condenser being sequentially arranged from top to bottom, coolant storage tank, extraction hold material retort and claim 1-2 according to any one of extract batch can;Described condenser has coolant the first inlet tube, coolant the first outlet, the first water inlet pipe connecting water-cooling device and the first outlet pipe;Coolant the second outlet, the second water inlet pipe of connection water-cooling device and the second outlet pipe that described coolant storage tank has coolant the second inlet tube connecting coolant the first outlet, is formed at coolant storage tank bottom;Described extraction is held material retort and is located at the lower section of coolant storage tank, and described extraction is held material retort and had coolant the 3rd inlet tube of docking coolant the second outlet, and described 3rd inlet tube is connected at extraction and holds the gondola water faucet portion in material retort;Described gondola water faucet portion is laid with multiple mouth spray, is provided with appearance bin below described gondola water faucet portion, holds bin and is provided with multilamellar placement plate;Described extraction is held the periphery of material retort and is provided with water tank, and water tank has the tank entry and pipe outlet passed through for water route;Described extraction appearance material retort has the lower section of extraction appearance material retort described in lid and is provided with coolant the 3rd outlet;Described first water intake end connects extraction and holds the peripheral water tank of material retort;
Described coolant circulating system also includes thermal jacket pipe;Coolant the 5th outlet, the second hot water inlet pipe of connection hot water apparatus and the second hot water outlet pipe that described jacket pipe has coolant the 5th inlet tube connecting coolant the 4th outlet, connects coolant the first inlet tube;
Described oilless vacuum pump is connected to extract between batch can and thermal jacket pipe, and the pipeline front end of oilless vacuum pump connects ball valve, and rear end connects vacuumizing and exhausting valve.
Plants essential oil extracting system the most according to claim 3, it is characterised in that extract batch can described in: and be provided with manual ball valve;Described condenser, coolant storage tank, extraction hold material retort, extract the outer surface of batch can and thermal jacket pipe and be equipped with the water tank for water route circulation heat exchange.
CN201620295740.7U 2016-04-11 2016-04-11 Extraction discharge tank and plant essential oil extraction system Active CN205627169U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

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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.