CN208933302U - A kind of high-efficient essential oil extraction system and essential oil production line - Google Patents

Abstract

A kind of high-efficient essential oil extraction system, is related to field of pharmaceutical equipment, including steam generator, extractor, condenser and the alternating temperature oil water separator being sequentially communicated；Alternating temperature oil water separator includes shell, mixed liquor feed pipe, water phase outlet tube and is located at the intracorporal separation chamber of shell, is provided with light oil separator at the top of shell, bottom is provided with heavy fuel separator；Separation chamber includes the second separation chamber positioned at the first separation chamber of upper part of the housing and positioned at lower part of the housing；One end of mixed liquor feed pipe is extend into the first separation chamber through shell, and the other end of mixed liquor feed pipe is connected to condenser, and water phase outlet tube is extend into the second separation chamber through shell；The position of corresponding second separation chamber of hull outside is arranged with condenser jacket, and the condensation chamber passed through for condensate liquid is formed between condenser jacket and shell.The high-efficient essential oil extraction system, separative efficiency are high.The utility model additionally provides a kind of essential oil production line including above-mentioned high-efficient essential oil extraction system, good in economic efficiency.

Description

A kind of high-efficient essential oil extraction system and essential oil production line

Technical field

The utility model relates to field of pharmaceutical equipment, raw in particular to a kind of high-efficient essential oil extraction system and essential oil Produce assembly line.

Background technique

Volatile oil is also referred to as essential oil, is that the one kind existed in plant has volatility, can be with steam distillation, not with water Miscible oily liquids.Volatile oil has fragrant odor mostly, and has various bioactivity.Volatile oil is in plant Boundary's distributed pole is wide, and the plant used as Chinese medicine just has hundreds of containing volatile oil.The composition of volatile oil is considerably complicated, basic Group becomes terpenoid, aromatic compound, aliphatic compound etc., and the ratio that wherein terpene accounts for is maximum and mainly single Terpene, sequiterpene and its containing oxygen derivative.The important substance that volatile oil is acted on as Chinese medicine generation, study its extract with separate for Developing new drug and promotion TCM Modernization are of great significance.For a long time, domestic and foreign scholars mention traditional medicine volatile oil It takes and has carried out a large amount of research and probe with separating, constantly improved although extracting with separation method, majority is still In the laboratory research stage, industrial application can not be carried out.

Volatile oil collection separator collection matched with extract equipment, separative efficiency are not high enough at present, to part medicinal material In mass production even can not be collected into volatile oil, cause medicinal material utilization rate low, energy consumption is high, it is at high cost the problems such as, volatile oil mentions It takes, separate the quality for equipping the production and product that have seriously affected Chinese materia medica preparation.

In consideration of it, special propose the application.

Utility model content

The utility model provides a kind of high-efficient essential oil extraction system, recovery rate height high to the extraction efficiency of volatile oil.

The utility model additionally provides a kind of essential oil production line, good in economic efficiency.

The embodiments of the present invention are achieved in that

A kind of high-efficient essential oil extraction system, including steam generator, extractor, condenser and alternating temperature oil water separator, Steam generator is connected to the bottom of extractor, and the top of extractor is connected to the top of condenser, the lower part of condenser and change Warm oil water separator connection；Alternating temperature oil water separator include shell, mixed liquor feed pipe, water phase outlet tube and be located at shell it is intracorporal Separation chamber is provided with light oil separator at the top of shell, and bottom is provided with heavy fuel separator；Separation chamber includes being located at upper part of the housing The first separation chamber, and the second separation chamber positioned at lower part of the housing；One end of mixed liquor feed pipe extend into the through shell In one separation chamber, the other end of mixed liquor feed pipe is connected to condenser, and water phase outlet tube extend into the second separation through shell It is indoor；The position of corresponding second separation chamber of hull outside is arranged with condenser jacket, is formed between condenser jacket and shell for condensate liquid By condensation chamber.

Further, in the other preferred embodiments of the utility model, the bottom of extractor is provided with for by steam Generator is passed through to the equally distributed steam uniform device of steam of extractor.

Further, in the other preferred embodiments of the utility model, high-efficient essential oil extraction system further includes surge tank, The top of surge tank is connected to water phase outlet tube, and the lower part of surge tank is connected to steam generator.

Further, in the other preferred embodiments of the utility model, the top of shell and surge tank are provided with and exhale Haustorium.

Further, in the other preferred embodiments of the utility model, condensation chamber is provided with condensate inlet and condensation Liquid outlet, condensate inlet are located at the bottom of condensation chamber, and condensate outlet is located at the top of condensation chamber.

Further, in the other preferred embodiments of the utility model, alternating temperature oil water separator is additionally provided with condenser pipe, Condenser pipe includes inlet tube, helix tube and outlet tube, and helix tube is located in the second separation chamber, and is arranged around water phase outlet tube, spiral shell The both ends of coil are connected to inlet tube and outlet tube respectively, and inlet tube and outlet tube run through shell.

Further, in the other preferred embodiments of the utility model, alternating temperature oil water separator further includes cyclonic separation Device, cyclone separator are located in the first separation chamber, and the head piece that enters of cyclone separator is connected to mixed liquor feed pipe, cyclone separator Top be provided with overflow port, bottom is provided with underflow opening.

Further, in the other preferred embodiments of the utility model, vortex chamber, eddy flow are provided in cyclone separator Chamber includes the cylindrical section vortex chamber being located above and underlying conical section vortex chamber, the opening's edge that becomes a mandarin of cyclone separator The tangential direction of cylindrical section vortex chamber is arranged.

Further, in the other preferred embodiments of the utility model, spoiler, flow-disturbing are provided with below underflow opening Plate is connect with shell, and is arranged with the underflow opening interval of cyclone separator；Liquid gap was provided between spoiler and shell.

A kind of essential oil production line, including above-mentioned high-efficient essential oil extraction system.

The beneficial effect of the utility model embodiment is:

The utility model embodiment provides a kind of high-efficient essential oil extraction system, due to the alternating temperature oil water separator of setting, During heavy oil decline, it can be cooled down again to oil water mixture after light oil separation, make the density of heavy oil and water Difference becomes larger, to be more easier to separate.The alternating temperature oil water separator is easy to operate, and separative efficiency is high, is particularly suitable for having light Oil has the volatile oil of heavy oil again.

The utility model is by the above-mentioned essential oil production line being related to, due to including provided by the utility model point From high-efficient high-efficient essential oil extraction system, therefore its is good in economic efficiency.

Detailed description of the invention

It, below will be to use required in embodiment in order to illustrate more clearly of the technical solution of the utility model embodiment Attached drawing be briefly described, it should be understood that the following drawings illustrates only some embodiments of the utility model, therefore should not be by Regard the restriction to range as, for those of ordinary skill in the art, without creative efforts, may be used also To obtain other relevant attached drawings according to these attached drawings.

Fig. 1 is the structural schematic diagram for the high-efficient essential oil extraction system that the utility model first embodiment provides；

Fig. 2 is the structural schematic diagram of the alternating temperature oil water separator in Fig. 1；

Fig. 3 is the knot of the alternating temperature oil water separator of high-efficient essential oil extraction system provided by the utility model second embodiment Structure schematic diagram；

Fig. 4 is the section view of the cyclone separator of high-efficient essential oil extraction system provided by the utility model second embodiment Figure；

Fig. 5 is the alternating temperature water-oil separating of high-efficient essential oil extraction system provided by the utility model embodiment second embodiment The schematic diagram of the spoiler of device.

Icon: 100- alternating temperature oil water separator；110- shell；111- light oil separator；112- heavy fuel separator；113- is mixed Close liquid feed pipe；114- water phase outlet tube；115- respirator；The separation chamber 120-；The first separation chamber 121-；122- second is separated Room；130- condenser jacket；131- condensation chamber；132- condensate inlet；133- condensate outlet；140- condenser pipe；141- inlet tube； 200- alternating temperature oil water separator；142- helix tube；143- outlet tube；150- cyclone separator；151- enters head piece；152- overflow Mouthful；153- underflow opening；154- vortex chamber；1541- cylindrical section vortex chamber；1542- conical section vortex chamber；160- spoiler；161- Cross liquid gap；10- high-efficient essential oil extraction system；11- steam generator；12- extractor；13- condenser；14- steam uniform device； 15- surge tank.

Specific embodiment

It is practical below in conjunction with this to keep the purposes, technical schemes and advantages of the utility model embodiment clearer The technical solution in the utility model embodiment is clearly and completely described in attached drawing in novel embodiment, shows So, described embodiment is a part of embodiment of the utility model, rather than whole embodiments.It is practical based on this Embodiment in novel, it is obtained by those of ordinary skill in the art without making creative efforts every other Embodiment is fallen within the protection scope of the utility model.Therefore, the implementation to the utility model provided in the accompanying drawings below The detailed description of mode is not intended to limit the range of claimed invention, but is merely representative of the utility model Selected embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not making creative labor Every other embodiment obtained under the premise of dynamic, fall within the protection scope of the utility model.

In the description of the present invention, it should be understood that term " center ", " longitudinal direction ", " transverse direction ", " length ", " width Degree ", " thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside", The orientation or positional relationship of the instructions such as " clockwise ", " counterclockwise " be based on the orientation or positional relationship shown in the drawings, be only for Convenient for description the utility model and simplify description, rather than the equipment of indication or suggestion meaning or element must have specifically Orientation is constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.

In addition, term " first ", " second " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance Or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or Implicitly include one or more of the features.The meaning of " plurality " is two or two in the description of the present invention, More than, unless otherwise specifically defined.

In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " Gu It is fixed " etc. terms shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral；It can be Mechanical connection, is also possible to be electrically connected；It can be directly connected, two can also be can be indirectly connected through an intermediary The interaction relationship of connection or two elements inside element.It for the ordinary skill in the art, can basis Concrete condition understands the concrete meaning of above-mentioned term in the present invention.

In the present invention unless specifically defined or limited otherwise, fisrt feature the "upper" of second feature or it "lower" may include that the first and second features directly contact, and also may include that the first and second features are not direct contacts but lead to Cross the other characterisation contact between them.Moreover, fisrt feature includes above the second feature " above ", " above " and " above " One feature is right above second feature and oblique upper, or is merely representative of first feature horizontal height higher than second feature.First is special Sign is directly below and diagonally below the second feature including fisrt feature under the second feature " below ", " below " and " below ", or only Indicate that first feature horizontal height is less than second feature.

First embodiment

As shown in Figure 1, the utility model embodiment provides a kind of high-efficient essential oil extraction system 10 comprising steam generation Device 11, extractor 12, condenser 13 and alternating temperature oil water separator 100, steam generator 11 are connected to the bottom of extractor 12, The top of extractor 12 is connected to the top of condenser 13, and the lower part of condenser 13 is connected to alternating temperature oil water separator 100.

As shown in Fig. 2, alternating temperature oil water separator 100 includes shell 110, mixed liquor feed pipe 113, water phase outlet tube 114 With the separation chamber 120 being located in shell 110.In the present embodiment, the generally cylindrical type of shell 110, the top setting of shell 110 There is light oil separator 111, bottom is provided with heavy fuel separator 112.Separation chamber 120 includes first point for being located at 110 top of shell From room 121, and positioned at the second separation chamber 122 of 110 lower part of shell.It is stretched through shell 110 one end of mixed liquor feed pipe 113 Enter into the first separation chamber 121, the other end of mixed liquor feed pipe 113 is connected to condenser 13, and water phase outlet tube 114 runs through shell Body 110 is extend into the second separation chamber 122.The position of corresponding second separation chamber 122 is arranged with condenser jacket 130 on the outside of shell 110, The condensation chamber 131 passed through for condensate liquid is formed between condenser jacket 130 and shell 110.

The medicinal material handled well is fitted into extractor 12, after soaking in water by technique, starts steam generator 11, steam hair Raw device 11 is passed through high-temperature steam into extractor 12, and high-temperature steam acts on medicinal material and takes volatile oil contained therein out of, from extraction The top of tank 12, which enters in condenser 13, is condensed into liquid, and the condensed water containing volatile oil enters through mixed liquor feed pipe 113 to be become In the first separation chamber 121 in warm oil water separator 100, the light oil in oil water mixture rises, and by being located at the first separation chamber The light oil separator 111 at 121 tops is collected.And heavy oil and water then sink to entering the second separation chamber 122 together, and under Further separation during heavy, the heavy oil after separation is collected by the heavy fuel separator 112 of 122 bottom of the second separation chamber, cold Condensate is then discharged from water phase outlet tube 114.But the density of heavy oil and water is close, to realize that separation takes a long time.This Embodiment is by again cooling down to it, to increase the density contrast of heavy oil and water, making during heavy oil is with underwater sink It is easier to separate.It is worth noting that, in the present embodiment, between the first separation chamber 121 and the second separation chamber 122 not It is really separated, the first separation chamber 121 and the second separation chamber 122 are actually still one complete whole, second point It is only the differentiation functionally for having the effect to cool down again according to it, and carrying out from room 122.

Further, the bottom of extractor 12 is provided with equal for steam generator 11 to be passed through to steam to extractor 12 The steam uniform device 14 of even distribution.

Further, high-efficient essential oil extraction system 10 further includes surge tank 15, the top of surge tank 15 and water phase outlet tube 114 connections, the lower part of surge tank 15 is connected to steam generator 11.

The first purpose by the condensate return being discharged in alternating temperature oil water separator 100 to steam generator 11 is so that water It recycles, plays resource-effective effect, another object is that due in the condensed water after the separation of alternating temperature oil water separator 100 It may be also entrained with volatile oil, and reuse condensed water enables to volatile oil contained therein to be again introduced into system is separated, mentioned The high yield of volatile oil.

Condensation chamber 131 is provided with condensate inlet 132 and condensate outlet 133, and condensate inlet 132 is located at condensation chamber 131 bottom, condensate outlet 133 are located at the top of condensation chamber 131.Condensate liquid moves from the bottom to top, mixed with heavy oil and water It closes and forms adverse current between object, achieve the purpose that improve cooling effect.

Condensation chamber 131 allows condensate liquid from shell and around shell 110 1 weeks along the circumferential direction setting of shell 110 110 all directions uniformly cool down to the mixing liquid in the second separation chamber 122, increase the effect of separation.

Condenser jacket 130 is made of heat-barrier material.Condenser jacket 130 made of heat-barrier material can prevent the excessive of cold air, make Heat transmitting can preferably occur between shell 110 for condensate liquid, improve the cooling to mixing liquid in the second separation chamber 122 and imitate Rate.

The top of shell 110 and surge tank 15 are provided with respirator 115.Respirator 115 can be used for equilibrium separation room Air pressure in 120 is avoided the occurrence of since separation caused by negative pressure is unsmooth, flows backwards, or by the spray of the excessive initiation of pressure Situations such as liquid, leakage.

Second embodiment

The technical effect of high-efficient essential oil extraction system provided by the utility model embodiment, realization principle and generation and First embodiment is identical, and to briefly describe, the present embodiment does not refer to place, can refer to corresponding contents in first embodiment.

In order to further promote cooling efficiency, as shown in figure 3, the change of high-efficient essential oil extraction system provided in this embodiment Warm oil water separator 200 is additionally provided with condenser pipe 140, and condenser pipe 140 includes inlet tube 141, helix tube 142 and outlet tube 143, Helix tube 142 is located in the second separation chamber 122, and around water phase outlet tube 114 be arranged, the both ends of helix tube 142 respectively with feed liquor Pipe 141 is connected to outlet tube 143, and inlet tube 141 and outlet tube 143 run through shell 110.Condenser pipe 140 can extend into second In separation chamber 122, cools down to the mixing liquid inside the second separation chamber 122, be used cooperatively with condensation chamber 131, Ke Yiji The earth increases cooling efficiency.

Further, as shown in Figure 3 and Figure 4, in the present embodiment, alternating temperature oil water separator 200 further includes cyclonic separation Device 150, cyclone separator 150 are located in the first separation chamber 121, and cyclone separator 150 enters head piece 151 and mixed liquor feed pipe 113 connections, the top of cyclone separator 150 are provided with overflow port 152, and bottom is provided with underflow opening 153.Cyclone separator 150 Preliminary separation can be carried out to oil water mixture, under the effect of centrifugation, light oil is by the overflow port at the top of cyclone separator 150 152 outflows, and heavy oil and water are then flowed out by the underflow opening 153 of 150 bottom of cyclone separator.

Vortex chamber 154 is provided in cyclone separator 150, vortex chamber 154 includes the cylindrical section vortex chamber being located above 1541 and underlying conical section vortex chamber 1542, cyclone separator 150 enter head piece 151 along cylindrical section vortex chamber 1541 tangential direction setting.The oil water mixture tangentially entered helically gestalt movement is entering conical section vortex chamber After 1542, with being gradually reduced for internal diameter, liquid in rotation speed is gradually accelerated.Since the bore of underflow opening 153 is smaller, so that liquid Body can not all be discharged from underflow opening 153.Under such circumstances, heavy oil and water are flowed along the cavity wall of vortex chamber 154 by underflow opening 153 Out, and light oil is squeezed to upward at the lower center of pressure, flowed out by overflow port 152, realize the initial gross separation of light oil.

Further, as Fig. 3 and Fig. 5 show, the lower section of underflow opening 153 is provided with spoiler 160, spoiler 160 and shell 110 connections, and be spaced and be arranged with the underflow opening of cyclone separator 150 153；Liquid was provided between spoiler 160 and shell 110 Gap 161.The movement velocity of the heavy oil and water that flowed out by underflow opening 153 is very fast, after flowing into the second separation chamber 122, cannot accomplish Adequately stop cooling.The setting of spoiler 160 can then play preferable buffer function, heavy oil and water slug to spoiler On 160, after being blocked deceleration, then by cross liquid gap 161 be flowed into the second separation chamber 122, adequately cooled down, Jin Erti High score from effect.

In conclusion high-efficient essential oil extraction system provided by the embodiment of the utility model, due to the alternating temperature grease point of setting From device, during heavy oil decline, it can be cooled down again to oil water mixture after light oil separation, make heavy oil and water Density contrast become larger, to be more easier to separate.The alternating temperature oil water separator is easy to operate, and separative efficiency is high, is particularly suitable for Having light oil again has the volatile oil of heavy oil.

The utility model embodiment additionally provides a kind of essential oil production line, including high-efficiency precision provided by the utility model Oil extract system, due to including the high high-efficient essential oil extraction system of separative efficiency provided by the utility model, therefore its economic benefit It is good.

The above descriptions are merely preferred embodiments of the present invention, is not intended to limit the utility model, for this For the technical staff in field, various modifications and changes may be made to the present invention.It is all in the spirit and principles of the utility model Within, any modification, equivalent replacement, improvement and so on should be included within the scope of protection of this utility model.

Claims (10)

1. a kind of high-efficient essential oil extraction system, which is characterized in that including steam generator, extractor, condenser and alternating temperature oil Separator, the steam generator are connected to the bottom of the extractor, the top of the extractor and the condenser Top connection, the lower part of the condenser is connected to the alternating temperature oil water separator；

The alternating temperature oil water separator includes shell, mixed liquor feed pipe, water phase outlet tube and is located at the intracorporal separation of the shell Room is provided with light oil separator at the top of the shell, and bottom is provided with heavy fuel separator；The separation chamber includes positioned at described First separation chamber of upper part of the housing, and the second separation chamber positioned at the lower part of the housing；One end of the mixed liquor feed pipe It being extend into first separation chamber through the shell, the other end of the mixed liquor feed pipe is connected to the condenser, The water phase outlet tube is extend into second separation chamber through the shell；The hull outside corresponds to second separation The position of room is arranged with condenser jacket, and the condensation chamber passed through for condensate liquid is formed between the condenser jacket and the shell.

2. high-efficient essential oil extraction system according to claim 1, which is characterized in that the bottom setting of the extractor is useful It is passed through in by the steam generator to the equally distributed steam uniform device of steam of the extractor.

3. high-efficient essential oil extraction system according to claim 1, which is characterized in that the high-efficient essential oil extraction system is also wrapped Surge tank is included, the top of the surge tank is connected to the water phase outlet tube, the lower part of the surge tank and the steam generation Device connection.

4. high-efficient essential oil extraction system according to claim 3, which is characterized in that the top of the shell and the buffering Tank is provided with respirator.

5. high-efficient essential oil extraction system according to claim 1, which is characterized in that the condensation chamber is provided with condensate liquid and enters Mouth and condensate outlet, the condensate inlet are located at the bottom of the condensation chamber, and the condensate outlet is located at the condensation The top of chamber.

6. high-efficient essential oil extraction system according to claim 1, which is characterized in that the alternating temperature oil water separator is also set up There is condenser pipe, the condenser pipe includes inlet tube, helix tube and outlet tube, and the helix tube is located in second separation chamber, And be arranged around the water phase outlet tube, the both ends of the helix tube are connected to the inlet tube and the outlet tube respectively, described Inlet tube and the outlet tube run through the shell.

7. high-efficient essential oil extraction system according to claim 1, which is characterized in that the alternating temperature oil water separator further includes Cyclone separator, the cyclone separator are located in first separation chamber, and the head piece that enters of the cyclone separator is mixed with described The connection of liquid feed pipe is closed, is provided with overflow port at the top of the cyclone separator, bottom is provided with underflow opening.

8. high-efficient essential oil extraction system according to claim 7, which is characterized in that be provided with rotation in the cyclone separator Chamber is flowed, the vortex chamber includes the cylindrical section vortex chamber being located above and underlying conical section vortex chamber, the eddy flow The tangential direction of the cylindrical section vortex chamber described in opening's edge that becomes a mandarin of separator is arranged.

9. high-efficient essential oil extraction system according to claim 8, which is characterized in that the lower section setting of the underflow opening is thanksed for your hospitality Flowing plate, the spoiler are connect with the shell, and are arranged with the underflow opening interval of the cyclone separator；The spoiler with Liquid gap was provided between the shell.

10. a kind of essential oil production line, which is characterized in that mentioned including high-efficient essential oil as described in any one of claims 1 to 9 Take system.