CN114183999A - Method and equipment for extracting superoxide dismutase-rich water - Google Patents
Method and equipment for extracting superoxide dismutase-rich water Download PDFInfo
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- CN114183999A CN114183999A CN202111539310.7A CN202111539310A CN114183999A CN 114183999 A CN114183999 A CN 114183999A CN 202111539310 A CN202111539310 A CN 202111539310A CN 114183999 A CN114183999 A CN 114183999A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 102000019197 Superoxide Dismutase Human genes 0.000 title claims abstract description 49
- 108010012715 Superoxide dismutase Proteins 0.000 title claims abstract description 49
- 238000000034 method Methods 0.000 title claims abstract description 20
- 238000001704 evaporation Methods 0.000 claims abstract description 83
- 230000008020 evaporation Effects 0.000 claims abstract description 79
- 238000001035 drying Methods 0.000 claims abstract description 67
- 238000009833 condensation Methods 0.000 claims abstract description 25
- 230000005494 condensation Effects 0.000 claims abstract description 25
- 238000003809 water extraction Methods 0.000 claims abstract description 11
- 230000008569 process Effects 0.000 claims abstract description 9
- 244000025254 Cannabis sativa Species 0.000 claims description 15
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 13
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 13
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 claims description 13
- 238000000605 extraction Methods 0.000 claims description 8
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- 238000004806 packaging method and process Methods 0.000 claims description 3
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- -1 superoxide anion free radical Chemical class 0.000 description 4
- 239000002516 radical scavenger Substances 0.000 description 3
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- 201000004624 Dermatitis Diseases 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 229940123457 Free radical scavenger Drugs 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000007791 dehumidification Methods 0.000 description 2
- 238000007323 disproportionation reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B1/00—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0078—Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
- B01D5/009—Collecting, removing and/or treatment of the condensate
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/0004—Oxidoreductases (1.)
- C12N9/0089—Oxidoreductases (1.) acting on superoxide as acceptor (1.15)
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12Y—ENZYMES
- C12Y115/00—Oxidoreductases acting on superoxide as acceptor (1.15)
- C12Y115/01—Oxidoreductases acting on superoxide as acceptor (1.15) with NAD or NADP as acceptor (1.15.1)
- C12Y115/01001—Superoxide dismutase (1.15.1.1)
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B1/00—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids
- F26B1/005—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids by means of disintegrating, e.g. crushing, shredding, milling the materials to be dried
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/005—Treatment of dryer exhaust gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B9/00—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
- F26B9/10—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in the open air; in pans or tables in rooms; Drying stacks of loose material on floors which may be covered, e.g. by a roof
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Abstract
A method and equipment for extracting superoxide dismutase-rich water relate to a method for extracting superoxide dismutase, in particular to improvement of the method and equipment for extracting superoxide dismutase-rich water. The device comprises a closed-loop air energy compressor unit, an evaporation drying chamber and a condensation collection chamber, wherein the closed-loop air energy compressor unit is arranged on the left side of the evaporation drying chamber; a plurality of layers of evaporation racks are arranged in the evaporation drying chamber, and each layer of the evaporation rack is provided with a plurality of trays; the upper part of the right side in the evaporation drying chamber is provided with a return fan unit, and the upper part of the left side in the evaporation drying chamber is provided with a return air inlet. The invention can extract the water rich in superoxide dismutase by simple equipment and simple process; the method can achieve the production purpose through common equipment and processes, greatly reduces the cost and the period of water extraction rich in superoxide dismutase, reduces the production cost and simplifies the production process.
Description
Technical Field
The invention relates to an extraction method of superoxide dismutase, in particular to improvement of extraction method equipment of water rich in superoxide dismutase.
Background
Superoxide dismutase (SOD) is also known as superoxide dismutase (SOD). Is a type of catalyst capable of catalyzing superoxide anion free radical (O)2-) disproportionation to H2O2And O2The enzyme of (1). The main function of superoxide dismutase is to catalyze the disproportionation of superoxide anion free radicals, which are normal metabolites in the body, into hydrogen peroxide and oxygen. But the accumulation of free radicals will cause membrane lipids to undergo peroxidation and cause membrane fission, resulting in cell damage and even death. Superoxide dismutase is the most important and optimal free radical scavenger in organisms, and maintains the metabolic balance of human bodies.
In addition, superoxide dismutase has significant therapeutic effect on myocardial infarction, vascular heart disease, collagen disease, neonatal dyspnea syndrome, edema, emphysema, oxygen poisoning, etc., and can be used for treating various dermatoses such as psoriasis, dermatitis, eczema, pruritus, etc. Superoxide dismutase as superoxide anion free radical scavenger has wide application in delaying human body aging, preventing diseases, improving human body immunity, and as food and cosmetic additive. Superoxide dismutase was found as the first enzyme to act on superoxide anions, and its effective action in preventing and treating diseases associated with superoxide radicals has been well demonstrated. When the superoxide anion is generated too much or the concentration of superoxide dismutase is low, the disease can be caused by the excessive superoxide anion, and the exogenous superoxide dismutase can be effectively used for preventing and treating the disease. Superoxide radicals in the human body can cause various diseases, and superoxide dismutase as its natural scavenger is normally in dynamic equilibrium therewith. The prior extraction process of the high-content superoxide dismutase water is complex and high in cost, and no simple, quick and low-cost method and equipment for extracting the high-content superoxide dismutase water exist in the market at present.
Disclosure of Invention
The invention aims to provide a method and equipment for extracting superoxide dismutase-rich water, aiming at overcoming the defects and shortcomings of the prior art, and the superoxide dismutase-rich water can be extracted by simple equipment and a simple process; the method can achieve the production purpose through common equipment and processes, greatly reduces the cost and the period of water extraction rich in superoxide dismutase, reduces the production cost and simplifies the production process.
In order to realize the purpose, the extraction equipment of the superoxide dismutase-rich water adopts the following technical scheme: the device comprises a closed-loop air energy compressor unit 1, an evaporation drying chamber 2 and a condensation collection chamber 3, wherein the closed-loop air energy compressor unit 1 is arranged on the left side of the evaporation drying chamber 2, a hot air outlet of the closed-loop air energy compressor unit 1 is connected to the bottom of the left side in the evaporation drying chamber 2, and the condensation collection chamber 3 is arranged on the upper part of the closed-loop air energy compressor unit 1 and is overlapped with the closed-loop air energy compressor unit 1; a plurality of layers of evaporation frames 21 are arranged in the evaporation drying chamber 2, and each layer of the plurality of layers of evaporation frames 21 is provided with a plurality of trays 22; the upper part of the right side in the evaporation drying chamber 2 is provided with a return fan unit 23, and the upper part of the left side in the evaporation drying chamber 2 is provided with a return air inlet 24.
The evaporation drying chamber 2 is of a box type structure. Select for use van-type structure can conveniently remove, assemble, dismantle, also can conveniently operate the comdenstion water in the collection room 3, and sealed square structure can guarantee inside seal, also can guarantee that inside air current circulates according to predetermined direction.
The air return unit 23 is composed of a plurality of air return fans arranged in the same direction, and the air outlet direction of each air return fan faces to the left side in the evaporation drying chamber 2.
The tray is 70-80cm long, 50-60cm wide and 12-18cm high. The proper length and width facilitate the operation of workers, the labor intensity of workers is not increased, the working efficiency can be ensured, and the height is to ensure that the materials in the tray can be dried and evaporated in a preset time, so that the drying and evaporating efficiency is ensured.
The closed-loop air energy compressor unit 1 comprises a compressor 11, an evaporator and a hot air outlet, and the hot air outlet is connected to the lower portion in the evaporation drying chamber 2. The closed-loop air energy heat pump heats copper pipes and fins of an evaporator by using a compressor 11 to do work, hot air is blown to materials by using a circulating fan, and moisture in the materials is evaporated into water vapor after contacting with the hot air. The temperature of the copper tube fin on the evaporator is balanced to the dew point temperature which corresponds to the current temperature and humidity and is the best temperature by a fan. The wet hot water vapor is sucked into the condenser of the main machine and condensed into water to flow out. Thereby achieving the effect of collecting condensed water. Because the compressor does work and heats, the heat in the air is not absorbed. Therefore, the influence of the temperature of the external environment on the energy efficiency of the machine is extremely small. And because the drying is realized by dehumidification, no dehumidification and no heat loss are realized, and the energy consumption is lower.
The condensation collection chamber 3 is internally provided with a condenser 31, the bottom of the condenser 31 is provided with a water collecting tank 32, the joint of the condensation collection chamber 3 and the evaporation drying chamber 2 is provided with an air return opening 24, and the air return opening 24 penetrates through the evaporation drying chamber 2 and the condensation collection chamber 3. The hot and humid air circulating through the evaporation drying chamber 2 passes through the air return opening 24 and then reaches the condensation collection chamber 3, and after being condensed by the condenser 31, the condensed water is collected by the condenser and then reaches the water collection tank 32.
An evaporator 25 is arranged at the connecting interface of the evaporation drying chamber 2 and the closed-loop air energy compressor unit 1, the evaporator 25 is designed in groups, and the evaporator 25 is composed of three to five groups of evaporation devices; a compressor 11 is arranged in the closed-loop air energy compressor unit 1. The compressor 11 can be used for providing hot air for the evaporator 25 and also providing a refrigerant for the condensation collection chamber 3, so that the condensation efficiency of the condensation collection chamber 3 is improved, the compressor 11 has two purposes, a large amount of energy can be saved, and the production cost is reduced.
And a return air partition plate 26 is arranged above the multi-layer evaporation rack 21 in the evaporation drying chamber 2. The return air partition plate 26 is used for partitioning the evaporation drying chamber 2, hot air at the lower part flows rightwards, and the hot air rises to the rightmost side and is blown leftwards through the upper part of the return air partition plate 26 by the return fan unit 23 and directly enters the collection chamber 3.
The extraction process of the superoxide dismutase-rich water comprises the following steps: firstly, selecting the rosin grass with standard length, bright color and stable growth vigor; grading, cleaning, cutting and crushing the selected rosin grass; thirdly, uniformly spreading the crushed materials in a tray 22, and placing the tray 22 on a multi-layer evaporation rack 21; fourthly, starting a closed loop air energy compressor unit 1 and a return fan unit 23 in the evaporation drying chamber 2; fifthly, evaporating and drying the materials in the tray 22; condensing the water vapor through a condenser 31 of the condensing and collecting chamber 3, condensing the water vapor and collecting the condensed water vapor in a water collecting tank 32; and seventhly, sterilizing and packaging the collected condensed water.
And the cutting and crushing in the second step is to crush the rosin grass into a grass crushing material with the length of 1-2 cm. The length is beneficial to uniform and stable drying and volatilization.
The working principle of the invention is as follows: the invention uses the evaporation and drying of the rosin grass to evaporate the superoxide dismutase in the rosin grass into the air, and then condenses and collects the air rich in the superoxide dismutase to obtain the condensed water rich in the superoxide dismutase.
The invention adopts a box structure, which is convenient to move, assemble and disassemble, and can also be convenient to operate the condensed water in the collection chamber 3, and the sealing square structure can ensure internal sealing and internal airflow to flow in a preset direction. The evaporation drying chamber 2 is convenient for workers to operate due to proper length and width, the labor intensity of workers is not increased, the working efficiency can be guaranteed, and the height is to guarantee that materials in the tray can be subjected to preset drying evaporation within preset time, so that the drying evaporation efficiency is guaranteed. The air circulated through the evaporation drying chamber 2 passes through the air return opening 24 and then reaches the condensation collection chamber 3, and after the air is condensed by the condenser 31, the condensed water is collected by the condenser and then reaches the water collection tank 32.
The invention is also provided with monitoring systems for temperature, humidity and other data, and the monitoring systems can remotely monitor through a network and can also remotely monitor and control through a mobile phone.
The compressor 11 of the invention can not only send hot air to the air outlet to ensure the evaporation effect in the evaporation drying chamber 2, but also ensure that the refrigerant in the condensation pipe in the condensation collection chamber 3 can be refrigerated through the reverse phase of heating, thereby not only maintaining the internal temperature and humidity, but also saving a large amount of energy.
By adopting the technical scheme, the water rich in superoxide dismutase can be extracted by simple equipment and a simple process; the method can achieve the production purpose through common equipment and processes, greatly reduces the cost and the period of water extraction rich in superoxide dismutase, reduces the production cost and simplifies the production process.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
Fig. 1 is a structural view of the present invention.
Description of reference numerals: the closed-loop air energy compressor unit 1, the evaporation drying chamber 2, the condensation collection chamber 3, the multi-layer evaporation frame 21, the tray 22, the air return fan unit 23, the air return opening 24, the condenser 31 and the water collecting tank 32.
Detailed Description
Referring to fig. 1, the technical solution adopted by the present embodiment is: the device consists of a closed-loop air energy compressor unit 1, an evaporation drying chamber 2 and a condensation collection chamber 3, wherein the closed-loop air energy compressor unit 1 is arranged on the left side of the evaporation drying chamber 2, a hot air outlet of the closed-loop air energy compressor unit 1 is connected to the bottom of the left side in the evaporation drying chamber 2, and the condensation collection chamber 3 is arranged on the upper part of the closed-loop air energy compressor unit 1 and is overlapped with the closed-loop air energy compressor unit 1; a plurality of layers of evaporation frames 21 are arranged in the evaporation drying chamber 2, and each layer of the plurality of layers of evaporation frames 21 is provided with a plurality of trays 22; the upper part of the right side in the evaporation drying chamber 2 is provided with a return fan unit 23, and the upper part of the left side in the evaporation drying chamber 2 is provided with a return air inlet 24. The evaporation drying chamber 2 is of a box type structure.
The air return unit 23 is composed of a plurality of air return fans arranged in the same direction, and the air outlet direction of each air return fan faces to the left side in the evaporation drying chamber 2. The tray is 80cm in length, 60cm in width and 15cm in height. The closed-loop air energy compressor unit 1 comprises a compressor 11, an evaporator and a hot air outlet, and the hot air outlet is connected to the lower left side in the evaporation drying chamber 2. The condensation collection chamber 3 is internally provided with a condenser 31, the bottom of the condenser 31 is provided with a water collecting tank 32, the joint of the condensation collection chamber 3 and the evaporation drying chamber 2 is provided with an air return opening 24, and the air return opening 24 penetrates through the evaporation drying chamber 2 and the condensation collection chamber 3. The connection interface of the evaporation drying chamber 2 and the closed-loop air energy compressor unit 1 is provided with an evaporator 25, the evaporator 25 is designed in groups, and the evaporator 25 is composed of three to five groups of evaporation devices. And a return air partition plate 26 is arranged above the multi-layer evaporation rack 21 in the evaporation drying chamber 2.
The extraction process of the superoxide dismutase-rich water in the specific embodiment comprises the following steps: firstly, selecting the rosin grass with standard length, bright color and stable growth vigor; grading, cleaning, cutting and crushing the selected rosin grass; thirdly, uniformly spreading the crushed materials in a tray 22, and placing the tray 22 on a multi-layer evaporation rack 21; fourthly, starting a closed loop air energy compressor unit 1 and a return fan unit 23 in the evaporation drying chamber 2; fifthly, evaporating and drying the materials in the tray 22; condensing air through a condenser 31 of the condensing and collecting chamber 3, condensing water vapor and collecting the condensed water vapor in a water collecting tank 32; and seventhly, sterilizing and packaging the collected condensed water.
And the cutting and crushing in the second step are to crush the rosin grass into a grass crushing material with the length of 2 cm.
The working principle of the specific embodiment is as follows: the specific embodiment utilizes the evaporation and drying of the rosin grass to evaporate the superoxide dismutase in the rosin grass into the air, and then condenses and collects the air rich in the superoxide dismutase to obtain the condensed water rich in the superoxide dismutase.
This embodiment selects for use van-type structure can conveniently remove, assemble, dismantle, also can conveniently operate the comdenstion water in the collection room 3, and inside seal can be guaranteed to sealed square structure, also can guarantee that inside air current circulates according to predetermined direction. The evaporation drying chamber 2 is convenient for workers to operate due to proper length and width, the labor intensity of workers is not increased, the working efficiency can be guaranteed, and the height is to guarantee that materials in the tray can be subjected to preset drying evaporation within preset time, so that the drying evaporation efficiency is guaranteed. The air circulated through the evaporation drying chamber 2 passes through the air return opening 24 and then reaches the condensation collection chamber 3, and after the air is condensed by the condenser 31, the condensed water is collected by the condenser and then reaches the water collection tank 32.
After the technical scheme is adopted, the specific implementation mode can extract the water rich in the superoxide dismutase by simple equipment and a simple process; the method can achieve the production purpose through common equipment and processes, greatly reduces the cost and the period of water extraction rich in superoxide dismutase, reduces the production cost and simplifies the production process.
The above description is only for the purpose of illustrating the technical solutions of the present invention and not for the purpose of limiting the same, and other modifications or equivalent substitutions made by those skilled in the art to the technical solutions of the present invention should be covered within the scope of the claims of the present invention without departing from the spirit and scope of the technical solutions of the present invention.
Claims (10)
1. The extraction equipment of the superoxide dismutase-rich water is characterized in that: the device comprises a closed-loop air energy compressor set (1), an evaporation drying chamber (2) and a condensation collection chamber (3), wherein the closed-loop air energy compressor set (1) is arranged on the left side of the evaporation drying chamber (2), a hot air outlet of the closed-loop air energy compressor set (1) is connected to the bottom of the left side in the evaporation drying chamber (2), and the condensation collection chamber (3) is arranged on the upper part of the closed-loop air energy compressor set (1) and is stacked with the closed-loop air energy compressor set (1); a plurality of layers of evaporation racks (21) are arranged in the evaporation drying chamber (2), and each layer of the plurality of layers of evaporation racks (21) is provided with a plurality of trays (22); a fan return unit (23) is arranged on the upper part of the right side in the evaporation drying chamber (2), and an air return opening (24) is arranged on the upper part of the left side in the evaporation drying chamber (2).
2. The superoxide dismutase rich water extraction apparatus as claimed in claim 1, wherein: the evaporation drying chamber (2) is of a box type structure.
3. The superoxide dismutase rich water extraction apparatus as claimed in claim 1, wherein: the air return unit (23) is composed of a plurality of air return machines arranged in the same direction, and the air outlet direction of the air return machines faces to the left side in the evaporation drying chamber (2).
4. The superoxide dismutase rich water extraction apparatus as claimed in claim 1, wherein: the tray is 70-80cm long, 50-60cm wide and 12-18cm high.
5. The superoxide dismutase rich water extraction apparatus as claimed in claim 1, wherein: the closed-loop air energy compressor unit (1) comprises a compressor (11), an evaporator and a hot air outlet, wherein the hot air outlet is connected to the lower left side in the evaporation drying chamber (2).
6. The superoxide dismutase rich water extraction apparatus as claimed in claim 1, wherein: the condensation collection chamber (3) is internally provided with a condenser (31), the bottom of the condenser (31) is provided with a water collecting tank (32), the joint of the condensation collection chamber (3) and the evaporation drying chamber (2) is provided with an air return opening (24), and the air return opening (24) penetrates through the evaporation drying chamber (2) and the condensation collection chamber (3).
7. The superoxide dismutase rich water extraction apparatus as claimed in claim 1, wherein: the evaporator drying chamber (2) is provided with evaporimeter (25) with the connection interface department of closed loop air energy compressor unit (1), evaporimeter (25) are for designing in groups, evaporimeter (25) comprise three to five groups of evaporation devices.
8. The superoxide dismutase rich water extraction apparatus as claimed in claim 1, wherein: and a return air partition plate (26) is arranged above the multi-layer evaporation rack (21) in the evaporation drying chamber (2).
9. The extraction process of the superoxide dismutase-rich water is characterized by comprising the following steps: firstly, selecting the rosin grass with standard length, bright color and stable growth vigor; grading, cleaning, cutting and crushing the selected rosin grass; thirdly, uniformly spreading the crushed materials in a tray (22), and placing the tray (22) on a multi-layer evaporation rack (21); fourthly, a fan return unit (23) in the closed-loop air energy compressor unit (1) and the evaporation drying chamber (2) is started; fifthly, evaporating and drying the materials in the tray (22); condensing air through a condenser (31) of the condensing and collecting chamber (3), condensing water vapor and collecting the condensed water vapor in a water collecting tank (32); and seventhly, sterilizing and packaging the collected condensed water.
10. The superoxide dismutase rich water extracting process as claimed in claim 9, wherein the cutting pulverization in the second step is a pulverization of the rosin grass to a length of 1-2 cm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111539310.7A CN114183999A (en) | 2021-12-16 | 2021-12-16 | Method and equipment for extracting superoxide dismutase-rich water |
Applications Claiming Priority (1)
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| CN202111539310.7A CN114183999A (en) | 2021-12-16 | 2021-12-16 | Method and equipment for extracting superoxide dismutase-rich water |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104087562A (en) * | 2014-07-24 | 2014-10-08 | 北京翰若生物科技有限公司 | Extraction method of superoxide dismutase |
| CN211953489U (en) * | 2020-04-21 | 2020-11-17 | 连云港市桑辉新能源科技有限公司 | Closed drying equipment for honeysuckle liquid extraction |
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Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104087562A (en) * | 2014-07-24 | 2014-10-08 | 北京翰若生物科技有限公司 | Extraction method of superoxide dismutase |
| CN211953489U (en) * | 2020-04-21 | 2020-11-17 | 连云港市桑辉新能源科技有限公司 | Closed drying equipment for honeysuckle liquid extraction |
Non-Patent Citations (1)
| Title |
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| 冯霄等编著: "《化工节能原理与技术》", 31 January 1998 * |
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