CN219050399U - Extraction equipment - Google Patents
Extraction equipment Download PDFInfo
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- CN219050399U CN219050399U CN202223414482.4U CN202223414482U CN219050399U CN 219050399 U CN219050399 U CN 219050399U CN 202223414482 U CN202223414482 U CN 202223414482U CN 219050399 U CN219050399 U CN 219050399U
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- pressure distillation
- pipe
- barrel
- crushing
- layering
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- 238000000605 extraction Methods 0.000 title claims abstract description 25
- 238000004821 distillation Methods 0.000 claims abstract description 55
- 239000000463 material Substances 0.000 claims abstract description 14
- 238000010992 reflux Methods 0.000 claims abstract description 14
- 238000010438 heat treatment Methods 0.000 claims abstract description 12
- 238000006243 chemical reaction Methods 0.000 claims abstract description 4
- 238000001816 cooling Methods 0.000 claims description 17
- 230000006837 decompression Effects 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 238000009833 condensation Methods 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- 240000008397 Ganoderma lucidum Species 0.000 abstract description 14
- 235000001637 Ganoderma lucidum Nutrition 0.000 abstract description 14
- 238000009835 boiling Methods 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 description 6
- 230000009286 beneficial effect Effects 0.000 description 3
- 229920001231 Polysaccharide peptide Polymers 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 108010022457 polysaccharide peptide Proteins 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 201000006474 Brain Ischemia Diseases 0.000 description 1
- 206010008120 Cerebral ischaemia Diseases 0.000 description 1
- 229920002101 Chitin Polymers 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 206010008118 cerebral infarction Diseases 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 210000000936 intestine Anatomy 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 150000004671 saturated fatty acids Chemical class 0.000 description 1
- 230000002000 scavenging effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 210000002784 stomach Anatomy 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
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Abstract
The utility model discloses extraction equipment, which comprises a high-pressure distillation structure, wherein a crushing structure for crushing materials and accelerating reaction is arranged in the high-pressure distillation structure, a layering box is arranged on one side of a condensing mechanism, a reflux outlet is arranged at the bottom of the layering box, the reflux outlet is connected with the high-pressure distillation structure through a reflux pipe, and the overflow outlet is connected with a fine crushing box through an overflow pipe. According to the extraction equipment, the crushing structure is arranged in the high-pressure distillation barrel, so that materials can be crushed in the high-pressure distillation barrel, and the extractant at the bottom after layering can enter the high-pressure distillation structure again by arranging the reflux port at the bottom of the layering box. The fixed temperature heating plate is arranged in the fine-crushing box body, so that the internal temperature is higher than the boiling point of the extractant and lower than the boiling point of the ganoderma lucidum spore oil, and the purity of the extracted ganoderma lucidum spore oil is further improved.
Description
Technical Field
The utility model relates to the technical field of extraction, in particular to extraction equipment.
Background
The ganoderma lucidum spores contain rich beneficial components such as polysaccharide peptide, protein, enzyme, trace elements and the like, but the ganoderma lucidum spores are provided with a layer of chitin which cannot be dissolved in water, so that the beneficial components such as polysaccharide peptide and the like are difficult to be absorbed by human bodies after the spores enter intestines and stomach. Therefore, the ganoderma lucidum spore oil extracted after spore wall breaking can be used as an auxiliary choice for diet adjustment, the ganoderma lucidum spore oil is yellow transparent liquid, the main components are saturated fatty acid, unsaturated fatty acid and the like, and the ganoderma lucidum spore oil containing a small amount of ganoderma lucidum acid has the effects of resisting cerebral ischemia and resisting oxidation and scavenging free radicals, and most of the existing extraction equipment has the following problems: 1. the function is single, only the extraction procedure can be carried out, the materials are crushed and added manually, the second extraction separation is insufficient, the extracted spore oil still contains extractant components, and the third extraction agent cannot be recycled, so that the cost is increased.
Disclosure of Invention
The utility model aims to provide extraction equipment so as to solve the problems that the extraction equipment has single function, insufficient extraction separation and the extractant cannot be recycled in the prior art.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides an extraction equipment, includes high-pressure distillation structure, high-pressure distillation structure is inside to be equipped with and is used for smashing the broken structure that the material quickened the reaction, high-pressure distillation structure is connected with the decompression structure through the conveyer pipe, and the decompression structure other end and condensation mechanism interconnect, the layering case is installed to condensation mechanism one side, and layering case bottom is equipped with the backward flow export, and the top is equipped with the overflow export, and the backward flow export is connected with high-pressure distillation structure through the back flow, and the overflow export passes through the overflow pipe and is connected with the pure case of essence.
Preferably, the high-pressure distillation structure comprises a high-pressure distillation barrel, a heating plate is arranged inside the high-pressure distillation barrel, a feed inlet is formed in the top of the high-pressure distillation barrel and is communicated with the inside of the crushing structure, and pressurizing equipment communicated with the inside of the barrel and a pressure gauge and a temperature gauge for detecting the pressure and the temperature inside the high-pressure distillation barrel are arranged outside the high-pressure distillation barrel.
Preferably, the crushing structure comprises a crushing box, a rotating shaft is arranged in the crushing box and connected with the output end of a rotating motor positioned at the outer side of the high-pressure distillation barrel, a rotating blade is arranged at the outer side of the rotating shaft, and an electric valve is arranged at the bottom of the crushing box.
Preferably, the rotary blade is composed of blades with different lengths, and the blade at the bottom end of the rotary shaft is longest, and the lengths of the blades are sequentially shortened along the rotary shaft to ensure that all materials at the inner layer and the outer layer of the rotary blade are fully smashed.
Preferably, the condensing mechanism comprises a cooling sleeve, one side of the cooling sleeve is connected with a cooler through a cooling loop through pipe, a spiral condensing pipe is arranged inside the cooling sleeve, a water inlet of the spiral condensing pipe is connected with a decompression structure, and a water outlet of the spiral condensing pipe is connected with the layering box.
Preferably, the essence case comprises an essence case body, a constant temperature heating plate is arranged in the essence case body, a thermometer is arranged outside the essence case body, one side of the essence case body is connected with a high-pressure distillation structure through a steam pipe, and an oil outlet is arranged outside the essence case body.
Compared with the prior art, the utility model has the beneficial effects that: the extraction equipment comprises an extraction device, a liquid extraction device and a liquid extraction device,
(1) The crushing structure is arranged in the high-pressure distillation barrel and is communicated with the feed inlet, so that materials can be crushed in the high-pressure distillation barrel after entering the high-pressure distillation barrel from the feed inlet, manual crushing is not needed, and production efficiency is improved.
(2) Through setting up the reflux mouth in layering case bottom, through opening the reflux pipe top valve of reflux mouth connection, can make the extractant of layering back bottom get into the high pressure distillation structure inside again, make its extractant obtain cyclic utilization reduce cost.
(3) The fixed temperature heating plate is arranged in the fine box body, so that the internal temperature of the fixed temperature heating plate is higher than the boiling point of the extractant and lower than the boiling point of the ganoderma lucidum spore oil, the purity of the extracted ganoderma lucidum spore oil is further improved, and the evaporated extractant enters the high-pressure distillation barrel again for recycling.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
FIG. 2 is a schematic diagram of the high pressure distillation structure of the present utility model;
FIG. 3 is a schematic view of a condensing mechanism according to the present utility model;
FIG. 4 is a schematic cross-sectional view of a essence box according to the present utility model.
In the figure: 1. the high-pressure distillation device comprises a high-pressure distillation structure 101, a high-pressure distillation barrel 102, a heating plate 103, a feed inlet 104, a pressurizing device 2, a crushing structure 201, a crushing box 202, a rotating shaft 203, a rotating motor 204, a rotating blade 205, an electric valve 3, a conveying pipe 4, a decompression structure 5, a condensing mechanism 501, a cooling sleeve 502, a cooling loop through pipe 503, a cooler 504, a spiral condensing pipe 6, a layering box 601, a reflux outlet 602, an overflow outlet 603, a reflux pipe 604, an overflow pipe 7, a essence box 701, an essence box 702, a constant-temperature heating plate 703, a steam pipe 704 and an oil outlet.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Referring to fig. 1-4, the present utility model provides a technical solution: an extraction apparatus is shown in fig. 1 and 2, wherein a crushing structure 2 for crushing materials and accelerating reaction is arranged inside a high-pressure distillation structure 1.
Specifically, the high-pressure distillation structure 1 comprises a high-pressure distillation barrel 101, a heating plate 102 is arranged inside the high-pressure distillation barrel 101, a feed inlet 103 is formed in the top of the high-pressure distillation barrel 101, the feed inlet 103 is communicated with the inside of the crushing structure 2, and a pressurizing device 104 communicated with the inside of the barrel body of the high-pressure distillation barrel 101, a pressure gauge and a temperature gauge for detecting the pressure and the temperature inside the high-pressure distillation barrel 101 are arranged outside the high-pressure distillation barrel 101.
Specifically, the crushing structure 2 comprises a crushing box 201, a rotating shaft 202 is arranged inside the crushing box 201, the rotating shaft 202 is connected with the output end of a rotating motor 203 positioned on the outer side of the high-pressure distillation barrel 101, a rotating blade 204 is arranged on the outer side of the rotating shaft 202, and an electric valve 205 is arranged at the bottom of the crushing box 201.
In a further embodiment, the rotary blade 203 is composed of blades of different lengths, and the blade at the bottom end of the rotary shaft 202 is longest, and the lengths of the blades along the rotary shaft 202 are sequentially reduced, so that all materials in the inner and outer layers of the rotary blade are fully broken.
In a further embodiment, a discharge hole for deslagging and discharging is formed in the outer side of the high-pressure distillation barrel 101, a control switch of the electric valve 205 is located in the outer side of the high-pressure distillation barrel 101, and a connection port of the feed inlet 103 and the crushing structure 2 is located in the upper half part of the crushing box 201, so that more materials can be added into the crushing box 201 through the feed inlet 103 to be crushed.
When the crushing device is used, the sealing cover above the feed inlet 103 is opened to enable materials to enter the crushing box 201 through the feed inlet 103, at the moment, the rotating motor 203 is opened to drive the rotating blade 204 on the outer side of the rotating shaft 202 to rotate to crush the materials, and after crushing, the electric valve 205 at the bottom of the crushing box 201 is opened through the switch to enable the materials to be mixed with the extractant.
According to fig. 1 and 3, the high-pressure distillation structure 1 is connected with a pressure reducing structure 4 through a delivery pipe 3, and the other end of the pressure reducing structure 4 is connected with a condensing mechanism 5.
Specifically, the condensing mechanism 5 includes cooling jacket 501, and cooling jacket 501 one side is connected with cooler 503 through cooling circuit siphunculus 502, cooling jacket 501 inside is provided with spiral condenser pipe 504, and spiral condenser pipe 504 water inlet is connected with pressure reducing structure 4, and the delivery port is connected with layering case 6.
In a further embodiment, the pressure reducing structure 4 consists of an inflow opening, a pressure reducing chamber and an outflow opening, the inflow opening being connected to the conveying pipe 3, the outflow opening being connected to the water inlet of the spiral condensing duct 504 by means of a fixing bolt.
When the device is used, when the conveying pipe 3 conveys mixed gas to enter the decompression chamber through the inflow port for decompression, the decompressed mixed gas enters the spiral condensing pipe 504 through the outflow port, a cooling circulation is formed between the cooling machine 503 and the cooling loop through pipe 502, and the mixed gas in the spiral condensing pipe 504 is cooled into liquid to flow into the layering box 6 for layering.
According to fig. 1 and 4, a layering tank 6 is installed on one side of the condensing mechanism 5, a reflux outlet 601 is arranged at the bottom of the layering tank 6, an overflow outlet 602 is arranged at the top of the layering tank 6, the reflux outlet 601 is connected with the high-pressure distillation structure 1 through a reflux pipe 603, and the overflow outlet 602 is connected with the fine crushing tank 7 through an overflow pipe 604.
Specifically, the essence box 7 includes an essence box 701, a constant temperature heating plate 702 is disposed inside the essence box 701, a thermometer and an oil outlet are installed at the outer side of the essence box 701, one side of the essence box 701 is connected to the high pressure distillation structure 1 through a steam pipe 703, and an oil outlet 704 is disposed at the outer side of the essence box 701.
In a further embodiment, the temperature inside the crushing box 701 is higher than the boiling point of the extractant and lower than the boiling point of the ganoderma lucidum spore oil by the constant temperature heating plate 702, and the return pipe 603 and the steam pipe 703 are provided with one-way valves above and connected with the high pressure distillation barrel 101 through the same connection port.
When the mixed liquid flows into the layering box 6 for layering, the density of the selected extractant is far greater than that of the ganoderma lucidum spore oil and the two are not compatible, the extractant is positioned below the ganoderma lucidum spore oil, and when the layering box 6 is in a full box state, the mixed liquid is continuously conveyed from the water outlet of the spiral condensing tube 504, and the ganoderma lucidum spore oil flows into the fine crushing box 7 from the overflow outlet 602 through the overflow pipe 604.
What is not described in detail in this specification is prior art known to those skilled in the art.
The terms "center," "longitudinal," "transverse," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," and the like are used for descriptive simplicity and convenience only and not as an indication or implying that the apparatus or element being referred to must have a particular orientation, be constructed and operated for a particular orientation, based on the orientation or positional relationship illustrated in the drawings, and thus should not be construed as limiting the scope of the present utility model.
Although the present utility model has been described with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described, or equivalents may be substituted for elements thereof, and any modifications, equivalents, improvements and changes may be made without departing from the spirit and principles of the present utility model.
Claims (6)
1. Extraction apparatus comprising a high pressure distillation structure (1), characterized in that: the utility model discloses a high-pressure distillation structure (1) is inside to be equipped with crushing structure (2) that are used for smashing the material and accelerate the reaction, high-pressure distillation structure (1) is connected with decompression structure (4) through conveyer pipe (3), and decompression structure (4) other end and condensation mechanism (5) interconnect, layering case (6) are installed to condensation mechanism (5) one side, and layering case (6) bottom is equipped with reflux outlet (601), and the top is equipped with overflow export (602), and reflux outlet (601) are connected with high-pressure distillation structure (1) through back flow (603), and overflow export (602) are connected with the pure case (7) of essence through overflow pipe (604).
2. An extraction apparatus according to claim 1, characterized in that: the high-pressure distillation structure (1) comprises a high-pressure distillation barrel (101), a heating plate (102) is arranged inside the high-pressure distillation barrel (101), a feed inlet (103) is formed in the top of the high-pressure distillation barrel (101), the feed inlet (103) is communicated with the inside of the crushing structure (2), and a pressurizing device (104) communicated with the inside of the barrel body of the high-pressure distillation barrel (101) and a pressure gauge and a thermometer for detecting the pressure and the temperature inside the high-pressure distillation barrel (101) are arranged outside the high-pressure distillation barrel.
3. An extraction apparatus according to claim 1, characterized in that: crushing structure (2) are including broken case (201), and the inside axis of rotation (202) that is equipped with of broken case (201), axis of rotation (202) are connected with rotation motor (203) output that is located the high-pressure distillation barrel (101) outside, and rotary blade (204) are installed in axis of rotation (202) outside, broken case (201) bottom is equipped with electric valve (205).
4. An extraction apparatus according to claim 3, characterized in that: the rotary blade (204) is composed of blades with different lengths, and the blade at the bottom end of the rotary shaft (202) is longest, and the lengths of the blades upwards along the rotary shaft (202) are sequentially shortened, so that all materials at the inner layer and the outer layer of the rotary blade are fully smashed.
5. An extraction apparatus according to claim 1, characterized in that: the condensing mechanism (5) comprises a cooling sleeve (501), one side of the cooling sleeve (501) is connected with a cooler (503) through a cooling loop through pipe (502), a spiral condensing pipe (504) is arranged inside the cooling sleeve (501), a water inlet of the spiral condensing pipe (504) is connected with a decompression structure (4), and a water outlet of the spiral condensing pipe is connected with a layering box (6).
6. An extraction apparatus according to claim 1, characterized in that: the fine box (7) comprises a fine box body (701), a constant temperature heating plate (702) is arranged inside the fine box body (701), a thermometer is arranged outside the fine box body (701), one side of the fine box body (701) is connected with the high-pressure distillation structure (1) through a steam pipe (703), and an oil outlet (704) is arranged outside the fine box body (701).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223414482.4U CN219050399U (en) | 2022-12-20 | 2022-12-20 | Extraction equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223414482.4U CN219050399U (en) | 2022-12-20 | 2022-12-20 | Extraction equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219050399U true CN219050399U (en) | 2023-05-23 |
Family
ID=86342130
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202223414482.4U Active CN219050399U (en) | 2022-12-20 | 2022-12-20 | Extraction equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219050399U (en) |
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2022
- 2022-12-20 CN CN202223414482.4U patent/CN219050399U/en active Active
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