CN216320010U - Multi-cavity essential oil distillation structure - Google Patents
Multi-cavity essential oil distillation structure Download PDFInfo
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- CN216320010U CN216320010U CN202121539389.9U CN202121539389U CN216320010U CN 216320010 U CN216320010 U CN 216320010U CN 202121539389 U CN202121539389 U CN 202121539389U CN 216320010 U CN216320010 U CN 216320010U
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Abstract
The utility model relates to a multi-cavity essential oil distillation structure. The frame body comprises a first processing part and a second processing part, a condensation layer is further arranged between the first processing part and the second processing part, the transmission mechanism and the filtering part are arranged on the condensation layer, the detection module is arranged on the first processing part, and the control mechanism is arranged on the frame body and is connected with the filtering part, the detection module and the transmission mechanism; and an exhaust gas discharge device is arranged above the second treatment part. The utility model has strong practicability, can preferentially discharge low-boiling-point gas so as to play a role of preventing a condensation pipeline from being polluted, and can separate gas in the same distillation equipment.
Description
Technical Field
The utility model relates to the field of distillation, in particular to a multi-cavity essential oil distillation structure.
Background
With the development of society, the demand of residents on the quality of life is gradually improved, people often use essential oil/essence prepared from plant extracts in daily life, so that the demand for preparing the essential oil is increased rapidly, people often need to use different essential oils in a matching manner to improve the effect of the essential oil, at the present stage, ninety-five percent of the essential oil is prepared by means of distillation and extraction, the distillation and extraction refers to controlling the temperature of plant raw material/mixed liquid, and aiming at the boiling points of different materials in the different plant raw material/mixed liquid, the required raw material is changed into gas after controlling the temperature, and is extracted and then condensed to liquid, so that the extraction process is completed.
The distillation equipment at the present stage can not deal with the mixed components with similar boiling points when the plant raw materials \ mixed liquid is extracted, and air impurities are easily led into the cooling condensate stage along with gas, so that the adaptability of the distillation equipment is low, and the processing of making different essential oils can not be dealt with, referring to the novel temperature-controlled distiller described in patent document CN201410369648.6, the distillation equipment can easily lead to the simultaneous leading-in of the gas with similar boiling points, thereby influencing the making of the essential oils.
Meanwhile, for part of plant raw materials/mixed liquid with lower boiling points, the low-boiling-point gas-liquid is not needed during extraction, the existing equipment often mixes the gas-liquid with a condensing channel for the gas-liquid, and the condensing channel is easy to pollute, so that normal gas-liquid essential oil output is influenced.
At present, the distillation equipment has no extra temperature control in the condensation process, and the final output quality is easily influenced by the temperature change in the condensation stage.
Partial distillation equipment adopts and installs gas separation device additional and carry out gas separation's equipment scheme, and this kind of equipment structure has increased equipment acquisition and purchase cost and needs professional operating personnel to carry out data regulation and control simultaneously, and this will increase certain artifical study cost simultaneously.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the defects and provides a multi-cavity essential oil distillation structure which is reasonable in design, can be used for preventing a condensing pipeline from being polluted by preferentially discharging low-boiling-point gas and can be used for gas separation in the same distillation equipment.
The above object of the present invention is achieved by the following technical means:
a multi-cavity essential oil distillation structure comprises a frame body, a filtering part, a detection module, a transmission mechanism and a control mechanism, wherein the frame body comprises a first processing part and a second processing part, a condensation layer is arranged between the first processing part and the second processing part, the transmission mechanism and the filtering part are arranged on the condensation layer, the detection module is arranged on the first processing part, and the control mechanism is arranged on the frame body and is connected with the filtering part, the detection module and the transmission mechanism; and an exhaust gas discharge device is arranged above the second treatment part.
Further, among the above-mentioned technical scheme, the below of first processing portion has still opened the ring channel, still be provided with the accuse temperature module on the ring channel, the one end of accuse temperature module with it connects to detect the module, one side of ring channel still is provided with the flowing back body, one side of support body still is provided with the feed liquor body.
Further, among the above-mentioned technical scheme, exhaust emission device includes two at least exhaust emission pieces, the top of support body still is provided with the piece that discharges and holds the chamber, exhaust emission piece with the size that the piece that discharges held the chamber agrees with each other.
Furthermore, in the foregoing technical solution, the filtering portion is in a thin film shape and is disposed below the condensation layer, the transmission mechanism includes a first condensation duct and a second condensation duct, the first condensation duct and the second condensation duct are in a semi-ring shape and are symmetrically disposed on the condensation layer, the second condensation duct is connected to the filtering portion and the frame body, and the first condensation duct is disposed between the filtering portion and the second processing portion.
Further, in the above technical solution, the conveying mechanism further includes a first disc body in a disc shape, and an opening and closing device, the first disc body is disposed above the condensation layer, a hollow through hole is further disposed at a circumferential center of the first disc body, an embedded cavity is further disposed on a wall surface of the first disc body facing the hollow through hole, a driving central control portion is disposed on the first disc body, the opening and closing device is movably disposed on the embedded cavity and connected with the driving central control portion, and a predetermined distance exists between a circumferential edge of the first disc body and a circular center in a horizontal direction and a vertical direction.
Further, in the above technical solution, the diameter of the cross section of the shutter is the same as the diameter of the hollow through hole, the shutter includes at least two sealing sheets, and the sealing sheets are completely disposed inside the embedded cavity when the shutter is closed.
Further, in the above technical solution, the connecting edge of each closing sheet is further provided with a central sealing port for preventing gas from leaking out.
Furthermore, in the above technical solution, the condensation layer is cylindrical, and a predetermined distance exists between the circumferential edge of the condensation layer and the center of the circle in the horizontal direction and the vertical direction, the filtering portion completely isolates the first processing portion and the condensation layer, and a temperature control layer is further disposed between the condensation layer and the frame body.
Further, in the above technical solution, the filter part includes a filter layer and a regeneration device, the filter layer is disposed on a side surface of the condensation layer facing the first treatment part, and the regeneration device is wrapped on a circumferential edge of the filter layer.
The utility model has the beneficial effects that:
the method has the advantages that: by adopting a double-cavity mode of the first treatment part and the second treatment part, different cavities are subjected to sub-module regulation and control aiming at different boiling point gases, so that residual pollution caused by gas streaming is prevented, and the gas distillation purity is improved.
The method has the advantages that: the device is characterized in that a cylinder connecting structure is adopted, mixed gas after temperature control gasification passes through the filtering part, the most preferable molecular filter of the filtering part can also be a filtering module with a gas filtering function, one gas of the mixed gas is adsorbed and filtered in the filtering part, the filtered gas is guided out by the first guide structure and then liquefied and stored, the device effectively deals with the distillation guide of the mixed gas, and is also suitable for the guide conditions of single-class gas and multiple-class gas, the adaptability of distillation equipment is greatly improved, and the cost and the labor input are reduced.
Drawings
In order to more clearly illustrate the embodiments of the present invention, the drawings that need to be used in the description of the embodiments or the prior art will be briefly described below.
Fig. 1 is a schematic cross-sectional structure of the present invention.
Fig. 2 is a schematic structural diagram of the present invention.
Fig. 3 is a front view of the present invention.
Fig. 4 is a schematic structural diagram of the first tray, the opening and closing device, the central sealing port and the temperature control layer according to the present invention.
The names of the components corresponding to the numerical identifiers in fig. 1 to 4 are as follows:
a frame body-1; a first processing unit-11; a second processing unit-12; an exhaust gas discharge device-13; a discharge sheet accommodation chamber-131; an annular groove-14; a temperature control module-15; a drainage tube body-16; a liquid inlet pipe body-17;
a filter part-2; a filtering layer-21; a regeneration device-22;
a detection module-3;
a transmission mechanism-4; a first condensation duct-41; a second condensation duct-42; a first disc body-43; an opener-44; central seal port-45; a temperature control layer-46;
control means-5;
condensation layer-6.
Detailed Description
The technical solution of the present invention will be clearly and completely described below with reference to the accompanying drawings, and in the description of the present invention, it should be noted that:
the term "connected" is to be understood broadly, and may be mechanical or electrical; they may be connected directly or indirectly through intervening media, or may be interconnected between two elements.
The terms "front", "rear", "side", "upper", "lower" and the like are used as terms of orientation or positional relationship based on the drawings, and are only for convenience of description of the present invention.
For those skilled in the art, the technical solutions in the embodiments may be combined with each other, but must be based on the realization of the technical solutions by those skilled in the art, and when the technical solutions are contradictory or cannot be realized, the combination of the technical solutions should be considered to be absent and not be within the protection scope of the present invention.
The present invention is further described with reference to the following specific examples, but it should be noted that the present invention is implemented on the premise of the technical solution of the present invention, and the detailed embodiments and specific operation procedures are given, but the scope of the present invention is not limited to the following examples.
Referring to fig. 1 to 4, the preferred embodiment is:
a multi-cavity essential oil distillation structure comprises a frame body 1, a filtering part 2, a detection module 3, a transmission mechanism 4 and a control mechanism 5, wherein the frame body 1 comprises a first processing part 11 and a second processing part 12, a condensation layer 6 is further arranged between the first processing part 11 and the second processing part 12, the transmission mechanism 4 and the filtering part 2 are arranged on the condensation layer 6, the detection module 3 is arranged on the first processing part 11, and the control mechanism 5 is arranged on the frame body 1 and is connected with the filtering part 2, the detection module 3 and the transmission mechanism 4; an exhaust gas discharge device 13 is further provided above the second treatment section 12.
In this embodiment, a dual-cavity mode of the first processing portion and the second processing portion is adopted, and different cavities are subjected to sub-module regulation and control aiming at different boiling point gases, so that residual pollution caused by gas series flow is prevented, and the gas distillation purity is improved.
As shown in fig. 1 to 2, an annular groove 14 is further formed below the first processing portion 11, a temperature control module 15 is further disposed on the annular groove 14, one end of the temperature control module 15 is connected with the detection module 3, a liquid discharge pipe 16 is further disposed on one side of the annular groove 14, and a liquid inlet pipe 17 is further disposed on one side of the frame body 1.
As shown in fig. 1 to 2, the exhaust emission device 13 includes at least two exhaust emission sheets, and a discharge sheet accommodating cavity 131 is further disposed at the top of the frame body 1, and the size of the exhaust emission sheet and the size of the discharge sheet accommodating cavity 131 are matched with each other.
As shown in fig. 3 to 4, the filter unit 2 is formed in a thin film shape and disposed below the condensation layer 6, the transfer mechanism 4 includes a first condensation duct 41 and a second condensation duct 42, the first condensation duct 41 and the second condensation duct 42 are formed in a semi-ring shape, the first condensation duct 41 and the second condensation duct 42 are symmetrically disposed on the condensation layer 6, the second condensation duct 42 is connected to the filter unit 2 and the frame body 1, and the first condensation duct 41 is disposed between the filter unit 2 and the second treatment unit 12.
In this embodiment, condensation layer and filter house adopt cylinder connection structure, and the mixed gas after the gasification of accuse temperature passes through the filter house, the most preferred molecular filter that is of filter house also can be the filter module that has gas filtering capability, one of them gaseous of mixed gas is adsorbed and filtered in the filter house, and the gaseous of filtration is derived by transmission device and is carried out the liquefaction and remain again, and the device effectively deals with mixed gas's distillation direction, also is applicable to single type gas, the direction condition of multiclass gas simultaneously, very big improvement distillation plant's suitability, simultaneously reduce cost and artifical input.
As shown in fig. 1 to 4, the conveying mechanism 4 further includes a first disc 43 in a disc shape, and an opener 44, the first disc 43 is disposed above the condensation layer 6, a hollow through hole is further disposed at a circumferential center of the first disc 43, an embedded cavity is further disposed on a wall surface of the first disc 43 facing the hollow through hole, the driving central control portion is disposed on the first disc 43, the opener 44 is movably disposed on the embedded cavity and connected to the driving central control portion, and a circumferential edge of the first disc 43 and the circumferential center have a predetermined distance in a horizontal direction and a vertical direction.
As shown in fig. 1 to 4, the diameter of the cross section of the shutter 44 is the same as the diameter of the hollow through hole, and the shutter 44 includes at least two closing sheets, and when the shutter 44 is closed, the closing sheets are completely placed inside the embedded cavity. The interconnecting edges of each closure flap are also provided with a central sealing port 45 for preventing gas leakage.
In the embodiment, the central sealing port is arranged, so that gas leakage is effectively prevented.
As shown in fig. 1 to 4, the condensing layer 6 is cylindrical and has a predetermined distance between the circumferential edge and the center of the circle in the horizontal direction and the vertical direction, the filtering portion 2 completely isolates the first treating portion 11 and the condensing layer 6, and a temperature control layer 46 is further disposed between the condensing layer 6 and the frame body 1. The filtering part 2 comprises a filtering layer 21 and a regenerating device 22, wherein the filtering layer 21 is arranged on one side surface of the condensing layer 6 facing the first treatment part 11, and the regenerating device 22 is wrapped on the circumferential edge of the filtering layer 21.
The above description is intended to illustrate the preferred embodiments of the present invention, and not to limit the scope of the present invention, and all modifications and equivalents of the structures described in the specification and drawings, or any other technical fields related thereto, which are directly or indirectly applicable to the present invention, are intended to be included within the scope of the present invention.
Claims (9)
1. The utility model provides a multicavity essential oil distillation structure, includes support body (1), filter house (2), detects module (3), transmission device (4) and control mechanism (5), its characterized in that: the frame body (1) comprises a first processing part (11) and a second processing part (12), a condensation layer (6) is further arranged between the first processing part (11) and the second processing part (12), the transmission mechanism (4) and the filtering part (2) are arranged on the condensation layer (6), the detection module (3) is arranged on the first processing part (11), and the control mechanism (5) is arranged on the frame body (1) and is connected with the filtering part (2), the detection module (3) and the transmission mechanism (4); an exhaust gas discharge device (13) is arranged above the second treatment part (12).
2. A multi-cavity essential oil distillation structure according to claim 1, wherein: annular groove (14) have still been opened to the below of first processing portion (11), still be provided with on annular groove (14) and control temperature module (15), the one end of controlling temperature module (15) with it connects to detect module (3), one side of annular groove (14) still is provided with flowing back body (16), one side of support body (1) still is provided with feed liquor body (17).
3. A multi-cavity essential oil distillation structure according to claim 1, wherein: exhaust emission device (13) include two at least exhaust emission pieces, the top of support body (1) still is provided with the piece of discharging and holds chamber (131), exhaust emission piece with the size that the piece of discharging held chamber (131) agrees with each other.
4. A multi-cavity essential oil distillation structure according to claim 1, wherein: the filtering part (2) is in a film shape and is arranged below the condensation layer (6), the transmission mechanism (4) comprises a first condensation pipeline (41) and a second condensation pipeline (42), the first condensation pipeline (41) and the second condensation pipeline (42) are in a semi-ring shape, the first condensation pipeline (41) and the second condensation pipeline (42) are symmetrically arranged on the condensation layer (6), the second condensation pipeline (42) is connected with the filtering part (2) and the frame body (1), and the first condensation pipeline (41) is arranged between the filtering part (2) and the second processing part (12).
5. A multi-cavity essential oil distillation structure according to claim 4, wherein: transport mechanism (4) are still including being discoid first disk body (43), switching device (44), first disk body (43) set up the top of condensation layer (6), the circumference center department of first disk body (43) still is provided with the cavity through-hole, first disk body (43) orientation still be provided with embedded cavity on the wall of cavity through-hole, be provided with the accuse portion in the drive on first disk body (43), switching device (44) activity sets up on the embedded cavity and its with the accuse portion is connected in the drive, there is the set distance in horizontal direction and vertical direction at the circumferential edge of first disk body (43) and center.
6. A multi-cavity essential oil distillation structure according to claim 5, wherein: the diameter of the cross section of the opener (44) is the same as that of the hollow through hole, the opener (44) comprises at least two sealing sheets, and the sealing sheets are completely arranged inside the embedded cavity when the opener (44) is closed.
7. A multi-cavity essential oil distillation structure according to claim 6, wherein: the interconnecting edges of each closure flap are also provided with a central sealing port (45) for preventing gas leakage.
8. A multi-cavity essential oil distillation structure according to claim 1, wherein: condensation layer (6) are cylindricly and its circumferential edge and circle center have the given distance in horizontal direction and vertical direction, filter portion (2) completely isolated first processing portion (11) and condensation layer (6), condensation layer (6) with still be provided with between support body (1) accuse temperature layer (46).
9. A multi-cavity essential oil distillation structure according to claim 1, wherein: the filtering part (2) comprises a filtering layer (21) and a regenerating device (22), the filtering layer (21) is arranged on one side face, facing the first treatment part (11), of the condensing layer (6), and the regenerating device (22) is wrapped and arranged on the circumferential edge of the filtering layer (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121539389.9U CN216320010U (en) | 2021-07-07 | 2021-07-07 | Multi-cavity essential oil distillation structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121539389.9U CN216320010U (en) | 2021-07-07 | 2021-07-07 | Multi-cavity essential oil distillation structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216320010U true CN216320010U (en) | 2022-04-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121539389.9U Active CN216320010U (en) | 2021-07-07 | 2021-07-07 | Multi-cavity essential oil distillation structure |
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| CN (1) | CN216320010U (en) |
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2021
- 2021-07-07 CN CN202121539389.9U patent/CN216320010U/en active Active
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