Extraction equipment and preparation method of novel cistanche deserticola extract instant in drinking wine

Abstract

The invention relates to the technical field of production equipment and process of homology of medicine and food, and discloses extraction equipment of a novel cistanche deserticola extract instant in drinking wine and a preparation method of the cistanche deserticola extract. The device comprises a supporting base, a console is mounted on one side of the upper surface of the supporting base, a double-effect reflux extraction tank is mounted above the supporting base, the upper end of the double-effect reflux extraction tank is communicated with a feeding port, the lower end of the double-effect reflux extraction tank is communicated with a first conveying pipe, one side of the first conveying pipe is communicated with a filtering channel, and the other side of the first conveying pipe is communicated with a second conveying pipe. One side of the filtering channel is communicated with a waste residue collecting box, the lower end of the filtering channel is provided with a filtrate collecting box, a conveying pump is installed in the filtrate collecting box, one end of the conveying pump is communicated with a second conveying pipe, the other end of the second conveying pipe is communicated with a low-temperature alcohol precipitation tank, and under the mutual cooperation of all the devices, linkage of multiple processes such as water extraction, alcohol precipitation and freeze-drying is achieved; the production efficiency is improved, the product is easier to dissolve in drinking wine, and the instant solubility is improved.

Description

Technical Field

[0001] The present invention belongs to the technical field of production equipment and processes for medicated and edible substances, and specifically relates to an extraction device for a novel cistanche deserticola extract that is quickly soluble in drinking wine and a production method thereof. Background Art

[0002] Cistanche deserticola is a traditional Chinese medicine for tonifying the kidney and strengthening yang, which contains rich alkaloids, amino acids, vitamins and other nutrients. Soaking cistanche deserticola in wine can be used both as medicine and for consumption. Mixing cistanche deserticola with other medicinal materials to make wine can bring its efficacy and functions into full play. Long-term consumption can increase physical strength and endurance, and also has the effects of tonifying the kidney and strengthening yang, and replenishing essence and marrow.

[0003] The extraction equipment for cistanche deserticola extract mainly includes a multi-functional extraction tank, a vacuum concentrator, a homogenizer, etc. The multi-functional extraction tank supports various extraction processes such as normal pressure, micro-pressure, water decoction, warm soaking, and heat reflux, which can ensure high extraction efficiency, short time, and high liquid medicine content. The vacuum concentrator, with its high efficiency and energy-saving characteristics, has become the preferred equipment for the concentration link, which helps to maintain the activity of the effective components of cistanche deserticola. The homogenizer ensures the uniform distribution of beverage components, improving stability and taste.

[0004] However, traditional extraction equipment usually uses direct steaming to extract the liquid essence of cistanche deserticola. This method takes a long time to achieve the ideal extraction effect, and during the process, the raw materials are unevenly heated, often unable to extract the effective components to the greatest extent, ultimately resulting in a reduction in product quality. At the same time, traditional extraction equipment only has a simple decoction function and cannot realize the linkage of multiple processes such as water extraction, alcohol precipitation, and freeze-drying, resulting in low production efficiency. Summary of the Invention

[0005] The purpose of the present invention is to solve the problems mentioned above, that is, traditional extraction equipment usually uses direct steaming to extract the liquid essence of cistanche deserticola. This method takes a long time to achieve the ideal extraction effect, and during the process, the raw materials are unevenly heated, often unable to extract the effective components to the greatest extent, ultimately resulting in a reduction in product quality. At the same time, traditional extraction equipment only has a simple decoction function and cannot realize the linkage of multiple processes such as water extraction, alcohol precipitation, and freeze-drying, resulting in low production efficiency. The present invention provides an extraction device for a novel cistanche deserticola extract that is quickly soluble in drinking wine and a production method thereof.

[0006] The technical solution adopted by the present invention is as follows: An extraction device for a cistanche deserticola extract that is quickly soluble in drinking wine, comprising a support base, on one side of the upper surface of the support base, an operation console is installed, above the support base, a double-effect reflux extraction tank is installed, at the upper end of the double-effect reflux extraction tank, a feed inlet is communicated, at the lower end of the double-effect reflux extraction tank, a conveying pipe I is communicated, on one side of the conveying pipe I, a filtering channel is communicated, on one side of the filtering channel, a waste residue collection box is communicated, at the lower end of the filtering channel, a filtrate collection box is arranged, inside the filtrate collection box, a delivery pump is installed, at one end of the delivery pump, a conveying pipe II is communicated, at the other end of the conveying pipe II, a low-temperature alcohol precipitation tank is communicated, at the upper end of the low-temperature alcohol precipitation tank, an ethanol addition pipe is communicated, at the lower end of the low-temperature alcohol precipitation tank, a pulverizing-drying integrated machine is communicated, and on one side of the pulverizing-drying integrated machine, a low-humidity packaging production line is installed.

[0007] By adopting the above technical solution, with the mutual cooperation of each device, multi-process linkages such as water extraction, alcohol precipitation, and freeze-drying are realized, the production efficiency is improved, and the product is made more soluble in drinking wine, improving the quick solubility.

[0008] In a preferred embodiment, a filter screen is arranged between the filtering channel and the filtrate collection box, and a waste residue collection box corresponding to the filter screen is placed inside the waste residue collection box.

[0009] By adopting the above technical solution, under the action of the filter screen, the filtrate and the filter residue can be separated, so that the waste residue can fall into the waste residue collection box, facilitating collection and treatment and improving convenience.

[0010] In a preferred embodiment, a stirring motor is installed at the upper end inside the low-temperature alcohol precipitation tank, a stirring shaft is arranged at the lower end of the stirring motor, an electric sealing plate is installed inside the low-temperature alcohol precipitation tank, and a first filter screen, a second filter screen, and a third filter screen are sequentially arranged from top to bottom inside the low-temperature alcohol precipitation tank, and the pore sizes of the first filter screen, the second filter screen, and the third filter screen are different.

[0011] By adopting the above technical solution, under the action of the stirring shaft, the mixing of ethanol and the product is accelerated to form flocculent precipitation. After the reaction is completed, the electric sealing plate is opened, and the product passes through the first filter screen to intercept the medicinal residue debris, then passes through the second filter screen to remove the precipitation flocs, and finally intercepts microorganisms and colloidal particles to ensure that the clarity of the filtrate is ≥95%.

[0012] In a preferred embodiment, an ethanol concentration detector is installed on one inner wall of the low-temperature alcohol precipitation tank.

[0013] By adopting the above technical solution, under the action of the ethanol concentration detector, the concentration of ethanol is monitored in real time to keep it at an appropriate concentration to ensure the sugar precipitation effect.

[0014] In a preferred embodiment, a jacket is sleeved on the outer surface of the low-temperature alcohol precipitation tank, the jacket is connected to a low-temperature coolant circulation system, and a temperature monitor is installed on one inner wall of the low-temperature alcohol precipitation tank.

[0015] By adopting the above technical solution, ethylene glycol coolant is introduced into the jacket to reduce the molecular thermal motion rate, promote the slow aggregation of sugar into large particle precipitates, and at the same time avoid the concentration fluctuation caused by ethanol volatilization.

[0016] In a preferred embodiment, a plurality of pulverizing blowers are installed inside the upper end of the pulverizing-drying integrated machine.

[0017] By adopting the above technical solution, under the action of the pulverizing blower, compressed air forms a supersonic air flow, carrying material particles to collide at high speed inside the pulverizing-drying integrated machine, and the larger particle diameter particles are thrown towards the cavity wall for continuous pulverization.

[0018] In a preferred embodiment, a cold air delivery pipe is communicated with the inside of one end of the pulverizing-drying integrated machine, a cold air device is communicated with one side of the cold air delivery pipe, and a temperature detector is installed on one inner wall of the pulverizing-drying integrated machine.

[0019] By adopting the above technical solution, the temperature inside the pulverizing-drying integrated machine can be detected under the action of the temperature detector, and then adjusted through the cold air delivery pipe, which is convenient to adjust to a suitable temperature in a timely and accurate manner and improve work efficiency.

[0020] In a preferred embodiment, a third conveying pipe is communicated with one end of the pulverizing-drying integrated machine.

[0021] By adopting the above technical solution, under the action of the third conveying pipe, during the freeze-drying process, the volatile oil component can be recovered through the condensation chamber and can be used for subsequent flavoring.

[0022] In a preferred embodiment, a cooling cavity is formed in the inner wall of the pulverizing-drying integrated machine, a water inlet pipe corresponding to the cooling cavity is communicated with one side of the pulverizing-drying integrated machine, and a water outlet pipe corresponding to the water inlet pipe is communicated with the other side of the pulverizing-drying integrated machine.

[0023] By adopting the above technical solution, under the action of the water inlet pipe and the water outlet pipe, the internal temperature of the pulverizing-drying integrated machine can be controlled at a suitable temperature to maintain the quality of the product.

[0024] In a preferred embodiment, the steps are as follows.

[0025] Step 1: Cut the cistanche deserticola, put it into the inside of the double-effect reflux extraction tank through the feed port, add water in the corresponding proportion, and then heat it. Control the heating temperature at 90±2°C, and control the stirring speed of the stirring device at 150 rpm. Extract for 2 hours each time, for a total of 2 times.

[0026] Step 2: After the extraction is completed, discharge through the first conveying pipe. When the filtrate passes through the filtration channel, it is filtered by the filter screen and collected into the inside of the filtrate collection tank. The waste residue flows into the inside of the waste residue collection tank and is collected in the waste residue collection box. Then, the filtrate in the filtrate collection tank is conveyed to the inside of the low-temperature alcohol precipitation tank through the second conveying pipe by the conveying pump.

[0027] Step 3: Slowly add absolute ethanol to the inside of the low-temperature alcohol precipitation tank through the ethanol addition pipe until the concentration reaches 80%. Adjust the pressure in the low-temperature alcohol precipitation tank ≤ -0.06 MPa, the temperature ≤ 60°C, and the stirring speed 50 rpm. Carry out sugar precipitation for 48 hours. After the sugar precipitation is completed, open the electric sealing plate, and the product is filtered through the first filter screen, the second filter screen, and the third filter screen with different pore sizes in turn.

[0028] Step 4: The filtered product falls into the inside of the crushing-drying integrated machine. Adjust the temperature inside it to -40°C through the cold air conveying pipe and maintain it for 2 hours. Then raise the temperature to -20°C and maintain it for 24 hours for the first drying. Continue to raise the temperature to 20°C and maintain it for 24 hours until the water content of the extract ≤ 5% for the second drying.

[0029] Step 5: After the drying is completed, control the temperature inside the crushing-drying integrated machine at below 10°C, start the crushing fan, and crush the product under the action of airflow crushing technology. After the crushing is completed, raise the temperature to 60°C and dry for 48 hours. After the drying is completed, the product is conveyed to the low-humidity packaging production line for packaging to complete the output of the finished product.

[0030] In summary, due to the adoption of the above technical solutions, the beneficial effects of the present invention are as follows:

[0031] 1. With the mutual cooperation of each device, multi-process linkages such as water extraction, alcohol precipitation, and freeze-drying are realized, improving production efficiency, and enabling the full retention of medicinal effects and improving product quality.

[0032] 2. Under this process, the product is more easily soluble in drinking wine, improving the instant solubility. BRIEF DESCRIPTION OF THE DRAWINGS

[0033] Figure 1 It is a front structural schematic diagram of the extraction device in the present invention;

[0034] Figure 2 Schematic diagram of the planar structure of the filtration device in the present invention;

[0035] Figure 3 Schematic diagram of the planar structure of the low-temperature alcohol precipitation tank in the present invention;

[0036] Figure 4 Schematic diagram of the planar structure of the pulverizing-drying integrated machine in the present invention;

[0037] Figure 5 Flow chart of extraction in the present invention.

[0038] Reference numerals in the figure: 1, support base; 2, filtrate collection box; 3, waste residue collection box; 4, control console; 5, filtration channel; 6, conveying pipe 1; 7, double-effect reflux extraction tank; 8, feed inlet; 9, conveying pipe 2; 10, ethanol addition pipe; 11, low-temperature alcohol precipitation tank; 12, conveying pipe 3; 13, low-humidity packaging production line; 14, water outlet pipe; 15, pulverizing-drying integrated machine; 16, water inlet pipe; 17, conveying pump; 18, filter screen; 19, waste residue collection box; 20, stirring motor; 21, ethanol concentration detector; 22, stirring shaft; 23, electric sealing plate; 24, first filter screen; 25, second filter screen; 26, third filter screen; 27, jacket; 28, temperature detector; 29, pulverizing fan; 30, cold air conveying pipe. Detailed implementation manners

[0039] To make the objectives, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention. Obviously, the described embodiments are some but not all of the embodiments of the present invention. All other embodiments obtained by those of ordinary skill in the art based on the embodiments of the present invention without creative efforts shall fall within the protection scope of the present invention.

[0040] Refer to Figures 1-5, An extraction device for a new type of cistanche deserticola extract that is quickly soluble in drinking wine, including a support base 1. On one side of the upper surface of the support base 1, an operation console 4 is installed. Above the support base 1, a double-effect reflux extraction tank 7 is installed. The upper end of the double-effect reflux extraction tank 7 is connected to a feed inlet 8. The lower end of the double-effect reflux extraction tank 7 is connected to a first conveying pipe 6. On one side of the first conveying pipe 6, a filtering channel 5 is connected. On one side of the filtering channel 5, a waste residue collection box 3 is connected. At the lower end of the filtering channel 5, a filtrate collection box 2 is provided. Inside the filtrate collection box 2, a delivery pump 17 is installed. One end of the delivery pump 17 is connected to a second conveying pipe 9. The other end of the second conveying pipe 9 is connected to a low-temperature alcohol precipitation tank 11. The upper end of the low-temperature alcohol precipitation tank 11 is connected to an ethanol addition pipe 10. The lower end of the low-temperature alcohol precipitation tank 11 is connected to a crushing-drying integrated machine 15. On one side of the crushing-drying integrated machine 15, a low-humidity packaging production line 13 is installed. With the mutual cooperation of each device, multi-process linkages such as water extraction, alcohol precipitation, and freeze-drying are achieved, improving production efficiency and making the product more easily soluble in drinking wine, thereby improving the quick solubility.

[0041] Refer to Figure 2 , A filter screen 18 is provided between the filtering channel 5 and the filtrate collection box 2. Inside the waste residue collection box 3, a waste residue collection box 19 corresponding to the filter screen 18 is placed. Under the action of the filter screen 18, the filtrate and filter residue can be separated, enabling the waste residue to fall into the inside of the waste residue collection box 19, facilitating collection and treatment and improving convenience.

[0042] Refer to Figure 3 , Inside the upper end of the low-temperature alcohol precipitation tank 11, a stirring motor 20 is installed. At the lower end of the stirring motor 20, a stirring shaft 22 is provided. Inside the low-temperature alcohol precipitation tank 11, an electric sealing plate 23 is installed. Inside the low-temperature alcohol precipitation tank 11, a first filter screen 24, a second filter screen 25, and a third filter screen 26 are arranged from top to bottom in sequence. The pore sizes of the first filter screen 24, the second filter screen 25, and the third filter screen 26 are different. Under the action of the stirring shaft 22, the mixing of ethanol and the product is accelerated to form flocculent precipitation. After the reaction is completed, the electric sealing plate 23 is opened, and the product passes through the first filter screen 24 to intercept medicinal residue debris, then passes through the second filter screen 25 to remove precipitation flocs, and finally intercepts microorganisms and colloidal particles to ensure that the clarity of the filtrate is ≥95%.

[0043] Refer to Figure 3 , On one side inner wall of the low-temperature alcohol precipitation tank 11, an ethanol concentration detector 21 is installed. Under the action of the ethanol concentration detector 21, the concentration of ethanol is monitored in real time to keep it at an appropriate concentration and ensure the sugar precipitation effect.

[0044] Refer to Figure 3, a jacket 27 is sleeved on the outer surface of the low-temperature alcohol precipitation tank 11. The jacket 27 is connected to the low-temperature coolant circulation system. A temperature monitor is installed on one inner wall of the low-temperature alcohol precipitation tank 11. Ethylene glycol coolant is introduced into the jacket 27 to reduce the molecular thermal motion rate, promote the slow aggregation of sugar into large particle precipitates, and at the same time avoid the concentration fluctuation caused by ethanol volatilization.

[0045] Refer to Figure 4 , several crushing blowers 29 are installed inside the upper end of the crushing-drying integrated machine 15. Under the action of the crushing blowers 29, compressed air forms a supersonic airflow, carrying material particles to collide at high speed inside the crushing-drying integrated machine 15, and the larger particle sizes are thrown towards the cavity wall for continuous crushing.

[0046] Refer to Figure 1 and Figure 4 , one end inside the crushing-drying integrated machine 15 is connected to a cold air delivery pipe 30. One side of the cold air delivery pipe 30 is connected to a cold air device. A temperature detector 28 is installed on one inner wall of the crushing-drying integrated machine 15. Under the action of the temperature detector 28, the temperature inside the crushing-drying integrated machine 15 can be detected, and then adjusted through the cold air delivery pipe 30, which is convenient to adjust to the appropriate temperature in a timely and accurate manner, improving work efficiency.

[0047] Refer to Figure 1 and Figure 4 , one end of the crushing-drying integrated machine 15 is connected to a third conveying pipe 12. Under the action of the third conveying pipe 12, during the freeze-drying process, the volatile oil components can be recovered through the condensation chamber and can be used for subsequent flavoring.

[0048] Refer to Figure 4 , a cooling cavity is provided on the inner wall of the crushing-drying integrated machine 15. One side of the crushing-drying integrated machine 15 is connected to a water inlet pipe 16 corresponding to the cooling cavity, and the other side is connected to a water outlet pipe 14 corresponding to the water inlet pipe 16. Under the action of the water inlet pipe 16 and the water outlet pipe 14, the temperature inside the crushing-drying integrated machine 15 can be controlled at an appropriate temperature to maintain the quality of the product.

[0049] Refer to Figures 1-5 , the steps are as follows.

[0050] Step 1: Cut the cistanche deserticola into pieces, put them into the double-effect reflux extraction tank 7 through the feed inlet 8, add water in the corresponding proportion, and then heat. Control the heating temperature at 90 ± 2 °C, and control the stirring speed of the stirring device at 150 rpm. Extract for 2 hours each time, for a total of 2 times.

[0051] Step 2: After the extraction is completed, it is discharged through the first conveying pipe 6. When the filtrate passes through the filtration channel 5, it is filtered by the filter screen 18 and collected inside the filtrate collection tank 2. The waste residue flows into the waste residue collection tank 3 and is collected in the waste residue collection box 19. Then, the filtrate in the filtrate collection tank 2 is conveyed to the inside of the low-temperature ethanol precipitation tank 11 through the second conveying pipe 9 by the conveying pump 17.

[0052] Step 3: Slowly add anhydrous ethanol to the inside of the low-temperature ethanol precipitation tank 11 through the ethanol addition pipe 10 until the concentration reaches 80%. Adjust the pressure in the low-temperature ethanol precipitation tank 11 to ≤ -0.06 MPa, the temperature to ≤ 60 °C, and the stirring speed to 50 rpm, and carry out sugar precipitation for 48 hours. After the sugar precipitation is completed, open the electric sealing plate 23, and the product is filtered through the first filter screen 24, the second filter screen 25, and the third filter screen 26 with different pore sizes in sequence.

[0053] Step 4: The filtered product falls into the inside of the pulverization-drying integrated machine 15. The temperature inside it is adjusted to -40 °C through the cold air conveying pipe 30 and maintained for 2 hours. Then, it is heated to -20 °C and maintained for 24 hours for the first drying. It is continuously heated to 20 °C and maintained for 24 hours until the water content of the extract is ≤ 5%, and the second drying is carried out.

[0054] Step 5: After the drying is completed, control the temperature inside the pulverization-drying integrated machine 15 at 10 °C or below, start the pulverization fan 29, and under the action of the airflow pulverization technology, pulverize the product. After the pulverization is completed, raise the temperature to 60 °C and dry for 48 hours. After the drying is completed, the product is conveyed to the low-humidity packaging production line 13 for packaging to complete the output of the finished product.

[0055] The implementation principle of the embodiment of the extraction equipment and its manufacturing method of a novel cistanche deserticola extract that is quickly soluble in drinking wine of the present invention is as follows:

[0056] When carrying out the extraction work, cut the cistanche deserticola into pieces, put it into the inside of the double-effect reflux extraction tank 7 through the feed inlet 8, add water in the corresponding proportion, and then heat it. Control the heating temperature at 90±2°C, and control the stirring speed of the stirring device at 150 rpm. Extract for 2 hours each time, for a total of 2 times. After the extraction is completed, discharge it through the first conveying pipe 6. When the filtrate passes through the filtration channel 5, it is filtered by the filter screen 18, collected inside the filtrate collection tank 2, and the waste residue flows into the inside of the waste residue collection tank 3 and is collected in the waste residue collection box 19. Then, pump the filtrate in the filtrate collection tank 2 through the second conveying pipe 9 to the inside of the low-temperature alcohol precipitation tank 11 by the conveying pump 17. Slowly add anhydrous ethanol to the inside of the low-temperature alcohol precipitation tank 11 through the ethanol addition pipe 10 until the concentration reaches 80%. Adjust the pressure in the low-temperature alcohol precipitation tank 11 ≤ -0.06 MPa, the temperature ≤ 60°C, and the stirring speed 50 rpm, and carry out sugar precipitation for 48 hours. After the sugar precipitation is completed, open the electric sealing plate 23, and the product is filtered through the first filter screen 24, the second filter screen 25, and the third filter screen 26 with different mesh sizes in sequence. The filtered product falls into the inside of the pulverization-drying integrated machine 15. Adjust the temperature inside it to -40°C through the cold air conveying pipe 30 and maintain it for 2 hours. Then raise the temperature to -20°C and maintain it for 24 hours for the first drying. Continue to raise the temperature to 20°C and maintain it for 24 hours until the water content of the extract ≤ 5%, and carry out the second drying. After the drying is completed, control the temperature inside the pulverization-drying integrated machine 15 at 10°C or below, start the pulverization fan 29, and pulverize the product under the action of the airflow pulverization technology. After the pulverization is completed, raise the temperature to 60°C and dry for 48 hours. After the drying is completed, convey the product to the low-humidity packaging production line 13 for packaging to complete the output of the finished product.

[0057] The above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit it; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: they can still modify the technical solutions recorded in the foregoing embodiments, or perform equivalent replacements for some of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the spirit and scope of the technical solutions of the embodiments of the present invention.

Claims

1. An extraction device for a novel cistanche deserticola extract that is quickly soluble in drinking wine, comprising a support base (1), characterized in that: On one side of the upper surface of the support base (1), an operation console (4) is installed. Above the support base (1), a double-effect reflux extraction tank (7) is installed. The upper end of the double-effect reflux extraction tank (7) is connected to a feed inlet (8). The lower end of the double-effect reflux extraction tank (7) is connected to a first conveying pipe (6). One side of the first conveying pipe (6) is connected to a filtering channel (5). One side of the filtering channel (5) is connected to a waste residue collection box (3). The lower end of the filtering channel (5) is provided with a filtrate collection box (2). Inside the filtrate collection box (2), a delivery pump (17) is installed. One end of the delivery pump (17) is connected to a second conveying pipe (9). The other end of the second conveying pipe (9) is connected to a low-temperature alcohol precipitation tank (11). The upper end of the low-temperature alcohol precipitation tank (11) is connected to an ethanol addition pipe (10). The lower end of the low-temperature alcohol precipitation tank (11) is connected to a crushing-drying integrated machine (15). On one side of the crushing-drying integrated machine (15), a low-humidity packaging production line (13) is installed.

2. The extraction device for the cistanche deserticola extract that is rapidly soluble in drinking wine according to claim 1, characterized in that: A filter screen (18) is arranged between the filtering channel (5) and the filtrate collection box (2). Inside the waste residue collection box (3), a waste residue collection box (19) corresponding to the filter screen (18) is placed.

3. The extraction device for the cistanche deserticola extract that is quickly soluble in drinking wine according to claim 1, wherein: Inside the upper end of the low-temperature alcohol precipitation tank (11), a stirring motor (20) is installed. Below the stirring motor (20), a stirring shaft (22) is provided. Inside the low-temperature alcohol precipitation tank (11), an electric sealing plate (23) is installed. Inside the low-temperature alcohol precipitation tank (11), a first filter screen (24), a second filter screen (25), and a third filter screen (26) are arranged from top to bottom in sequence. The pore sizes of the first filter screen (24), the second filter screen (25), and the third filter screen (26) are different.

4. The extraction device for the cistanche deserticola extract that is quickly soluble in drinking wine as described in claim 1, wherein: On one inner wall of the low-temperature alcohol precipitation tank (11), an ethanol concentration detector (21) is installed.

5. The extraction equipment for the cistanche deserticola extract that is rapidly soluble in drinking wine as described in claim 1, characterized in that: The outer surface of the low-temperature alcohol precipitation tank (11) is sleeved with a jacket (27). The jacket (27) is connected to a low-temperature coolant circulation system. On one inner wall of the low-temperature alcohol precipitation tank (11), a temperature monitor is installed.

6. The extraction device of the cistanche deserticola extract that is quickly soluble in drinking wine as described in claim 1, characterized in that: Inside the upper end of the crushing-drying integrated machine (15), a number of crushing blowers (29) are installed.

7. The extraction equipment for the cistanche deserticola extract that is quickly soluble in drinking wine according to claim 1, wherein: One end inside the crushing-drying integrated machine (15) is connected to a cold air conveying pipe (30). One side of the cold air conveying pipe (30) is connected to a cold air device. On one inner wall of the crushing-drying integrated machine (15), a temperature detector (28) is installed.

8. The extraction device for the cistanche deserticola extract that is quickly soluble in drinking wine as described in claim 1, characterized in that: One end of the crushing-drying integrated machine (15) is connected to a third conveying pipe (12).

9. The extraction device for the cistanche deserticola extract that is quickly soluble in drinking wine as claimed in claim 1, wherein: Inside the wall of the crushing-drying integrated machine (15), a cooling cavity is formed. One side of the crushing-drying integrated machine (15) is connected to a water inlet pipe (16) corresponding to the cooling cavity. The other side of the crushing-drying integrated machine (15) is connected to a water outlet pipe (14) corresponding to the water inlet pipe (16).

10. The manufacturing method of an extraction device for a novel cistanche deserticola extract that is rapidly soluble in drinking wine as claimed in claims 1 - 9, characterized in that: The steps are as follows. Step 1: Cut the cistanche deserticola into pieces, put them into the double-effect reflux extraction tank (7) through the feed inlet (8), add water in the corresponding proportion, and then heat it. Control the heating temperature at 90±2°C, and control the stirring speed of the stirring device at 150 rpm. Extract for 2 hours each time, for a total of 2 times; Step 2: After the extraction is completed, discharge through the first conveying pipe (6). When the filtrate passes through the filtration channel (5), it is filtered by the filter screen (18), collected into the filtrate collection tank (2), and the waste residue flows into the waste residue collection tank (3) and is collected in the waste residue collection box (19). Then, pump the filtrate in the filtrate collection tank (2) through the second conveying pipe (9) to the internal of the low-temperature alcohol precipitation tank (11) by the conveying pump (17); Step 3: Slowly add anhydrous ethanol to the internal of the low-temperature alcohol precipitation tank (11) through the ethanol addition pipe (10) until the concentration reaches 80%. Adjust the pressure in the low-temperature alcohol precipitation tank (11) ≤ -0.06 MPa, the temperature ≤ 60°C, and the stirring speed 50 rpm, and carry out sugar precipitation for 48 hours. After the sugar precipitation is completed, open the electric sealing plate (23), and the product is filtered through the first filter screen (24), the second filter screen (25), and the third filter screen (26) with different mesh sizes in sequence; Step 4: The filtered product falls into the internal of the crushing-drying integrated machine (15). Adjust the temperature inside it to -40°C through the cold air conveying pipe (30) and maintain it for 2 hours. Then, raise the temperature to -20°C and maintain it for 24 hours for the first drying. Continue to raise the temperature to 20°C and maintain it for 24 hours until the moisture content of the extract ≤ 5%, and carry out the second drying; Step 5: After the drying is completed, control the internal temperature of the crushing-drying integrated machine (15) below 10°C, start the crushing fan (29), and under the action of the airflow crushing technology, crush the product. After the crushing is completed, raise the temperature to 60°C and dry for 48 hours. After the drying is completed, convey the product to the low-humidity packaging production line (13) for packaging to complete the output of the finished product.

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