A system and method for removing impurities and purifying liquor

Abstract

This invention discloses a system and method for purifying and removing impurities from baijiu (Chinese liquor), belonging to the field of baijiu purification technology. It includes a first purification component, a second purification component, a third purification component, and a collection component. These components are arranged sequentially. The first purification component heats the baijiu to 65°C under the action of a first heating base for first purification. The purified liquid then enters the second purification component, where it is heated to a higher temperature for a second purification under the action of a second heating base. The purified liquid then enters the third purification component, where it is heated to 20°C for a third purification under the action of a third heating base. The purified liquid also enters the collection tank. This method allows for multiple purification processes based on the different boiling points of the components, achieving a better purification effect.

Description

Technical Field

[0001] The invention relates to the technical field of liquor purification, and in particular to a liquor impurity removal and purification system and method. Background Art

[0002] As a special beverage, wine has been integrated into people's spiritual and cultural life. In the thousands of years of Chinese civilization, wine has penetrated almost every field of politics, economy, culture and education, social life, literature and art. Although wine is not a necessity of life, it has some special functions of disinfection, disease prevention and treatment, and health care. It has been medically proven that drinking in moderation can dredge meridians, promote qi and blood circulation, relax muscles and bones, eliminate fatigue, lower cholesterol, enhance intelligence, stimulate inspiration, delay aging, and prevent cardiovascular and cerebrovascular diseases. However, wine also has an anesthetic effect. Excessive drinking can numb people's nerves and make them confused. In particular, excessive drinking of wine containing excessive impurities will have serious consequences that damage the physical and mental health of the human body.

[0003] There are more than 1,800 types of trace elements in liquor that can be detected by current technical means. Experimental analysis has found that the various trace elements contained in liquor have different boiling point temperatures. The so-called boiling point of a liquid refers to the temperature when its saturated vapor pressure is equal to the external pressure. For example, the boiling point of acetaldehyde is 20.8°C, the boiling point of hydrocyanic acid is 25.7°C, the boiling point of propanal is 48°C, the boiling point of ethyl formate is 53-54°C, the boiling point of isobutyraldehyde is 64°C, the boiling point of methanol is 64.7°C, the boiling point of ethyl acetate is 77°C, and the boiling point of ethanol is 78.7°C. These low-boiling-point elements below 65°C are substances with a strong pungent taste and a strong sense of stimulation. They are also substances that have a heavy effect on the human nervous system. Although the total content in liquor is less than 0.1%, it has a great impact on the quality of the liquor. If the content is too high, drinking it will cause adverse reactions such as headaches and dry mouth. These substances that are harmful to the human body need to be removed, while elements with a boiling point above 70°C are mostly beneficial substances that add fragrance and mellowness to the liquor and need to be retained. The way to remove these harmful substances is volatilization separation. The so-called longer the liquor is stored, the stronger the aroma of the liquor is, because as time goes on, the harmful substances in the liquor slowly evaporate in the natural environment, making the liquor mellow and mellow with a strong aroma. Usually, in order to speed up the volatilization of harmful substances, the liquor can be heated. How to remove harmful substances in the liquor while retaining beneficial substances is the key to improving the quality and grade of liquor, and it is also a problem that all liquor companies are very concerned about and need to solve. Summary of the invention

[0004] The object of the present invention is to provide a system and method for removing impurities from and purifying liquor, so as to solve the problems raised in the above-mentioned background technology.

[0005] In order to solve the above technical problems, the present invention provides the following technical solutions: a liquor impurity removal and purification system, comprising: a first purification component, a second purification component, a third purification component and a collection component;

[0006] The first purification component, the second purification component, the third purification component and the collection component are arranged in sequence;

[0007] The first purification component includes a first heating base and a storage tank, wherein the storage tank is disposed on the first heating base, the first heating base is used to heat the storage tank to raise its temperature to 65° C., and a first delivery pipe is disposed on the storage tank;

[0008] The second purification assembly includes a first gantry, a first supporting base, a second heating base, a first switching mechanism, a first main tank and a first auxiliary tank, the first gantry is provided with a first door panel, the first door panel is provided with a first condensing pipe and a second conveying pipe, the first supporting base is located below the first condensing pipe, the second heating base is located below the second conveying pipe, the first switching mechanism is located in the first gantry and is drivingly connected to the first main tank and the first auxiliary tank to drive the first main tank and the first auxiliary tank to switch on the first supporting base and the second heating base, when the first main tank or the first auxiliary tank is located on the first supporting base, the opening of the first main tank or the first auxiliary tank is in contact with the first condensing pipe, when the first main tank or the first auxiliary tank is located on the second heating base, the opening of the first main tank or the first auxiliary tank is in contact with the second conveying pipe, and the second heating base is used to heat the first main tank or the first auxiliary tank located above it to 30°C;

[0009] The third purification assembly includes a second gantry, a second supporting base, a third heating base, a second switching mechanism, a second main tank and a second auxiliary tank, the second gantry is provided with a second door panel, the second door panel is provided with a second condensing pipe and a third delivery pipe, the second supporting base is located below the second condensing pipe, the third heating base is located below the third delivery pipe, the second switching mechanism is located in the second gantry and is drivingly connected to the second main tank and the second auxiliary tank to drive the second main tank and the second auxiliary tank to switch on the second supporting base and the third heating base, when the second main tank or the second auxiliary tank is located on the second supporting base, the opening of the second main tank or the second auxiliary tank is fitted with the second condensing pipe, when the second main tank or the second auxiliary tank is located on the third heating base, the opening of the second main tank or the second auxiliary tank is fitted with the third delivery pipe, and the third heating base is used to heat the second main tank or the second auxiliary tank located above it to 20°C;

[0010] The collecting assembly comprises a collecting door frame, a collecting door plate is arranged on the collecting door frame, a third condensing tube is arranged on the collecting door plate, and a collecting tank is arranged below the third condensing tube;

[0011] The first delivery pipe is communicated with the first condensation pipe, the second delivery pipe is communicated with the second condensation pipe, and the third delivery pipe is communicated with the third condensation pipe.

[0012] In a further embodiment, a feed port and a discharge port are provided on the storage tank, the feed port is located at the top of the storage tank, and the discharge port is located at the bottom of the storage tank.

[0013] In a further embodiment, the first switching mechanism includes a first switching motor, the first switching motor is located in the first gantry, the output end of the first switching motor is connected to the first switching plate, one end of the first switching plate is connected to the first main tank, the other end of the first switching plate is connected to the first auxiliary tank, the first main tank is provided with a first main tank material changing port, and the first auxiliary tank is provided with a first auxiliary tank material changing port.

[0014] In a further embodiment, a first support column is disposed on the first switching plate, and a first support wheel is disposed at the bottom of the first support column.

[0015] In a further embodiment, a first condenser is disposed on the first condenser tube, a first valve motor is disposed at the bottom of the first door panel, an output end of the first valve motor is connected to a first condenser valve, and the first condenser valve is disposed on the first condenser tube.

[0016] In a further embodiment, the second switching mechanism includes a second switching motor, which is located in the second gantry, and the output end of the second switching motor is connected to a second switching plate, one end of the second switching plate is connected to a second main tank, and the other end of the second switching plate is connected to a second auxiliary tank, a second main tank is provided with a second main tank material changing port, and a second auxiliary tank is provided with a second auxiliary tank material changing port.

[0017] In a further embodiment, a second support column is disposed on the second switching plate, and a second support wheel is disposed at the bottom of the second support column.

[0018] In a further embodiment, a second condenser is disposed on the second condenser tube, a second valve motor is disposed at the bottom of the second door panel, an output end of the second valve motor is connected to a second condenser valve, and the second condenser valve is disposed on the second condenser tube.

[0019] In a further embodiment, a third condenser is provided on the third condenser tube, a third condenser valve is provided at the bottom of the third condenser tube, and a collecting tank material replacement port is provided on the collecting tank.

[0020] A method for removing impurities from liquor and purifying the liquor system comprises the following steps:

[0021] S1: adding the liquor to be purified into the storage tank through the feed port, and starting the first heating base to heat the storage tank to 65°C;

[0022] S2: Start the first switching motor to move the first main tank or the first auxiliary tank to the first supporting base, start the first condenser, and the condensate condensed in the first condensation tube enters the first main tank or the first auxiliary tank. After the first main tank or the first auxiliary tank collects the condensate condensed in the first condensation tube, start the first valve motor to close the first condensation valve, start the first switching motor to switch the first main tank and the first auxiliary tank, and move the first main tank or the first auxiliary tank carrying the condensate to the second heating base to heat it to 30°C;

[0023] S3: starting the first valve motor to open the first condensation valve, and the condensate condensed in the first condensation pipe enters the first auxiliary tank or the first main tank placed on the first support base to continue collecting the condensate;

[0024] S4: Start the second switching motor to move the second main tank or the second auxiliary tank to the second supporting base, start the second condenser, and the condensate condensed in the second condensation tube enters the second main tank or the second auxiliary tank. After the second main tank or the second auxiliary tank collects the condensate condensed in the second condensation tube, start the second valve motor to close the second condensation valve, start the second switching motor to switch the second main tank and the second auxiliary tank, and move the second main tank or the second auxiliary tank carrying the condensate to the third heating base to heat it to 20°C.

[0025] S5: starting the second valve motor to open the second condensation valve, and the condensed liquid condensed in the second condensation pipe enters the second auxiliary tank or the second main tank placed on the second support base to continue collecting the condensed liquid;

[0026] S6: Start the third condenser, and the condensate condensed in the third condenser tube enters the collection tank.

[0027] Compared with the prior art, the beneficial effects achieved by the present invention are as follows: the storage tank is used to carry the liquor to be purified, and the liquor in the storage tank is heated to 65°C under the action of the first heating base, so that all acetaldehyde, hydrocyanic acid, propionaldehyde, ethyl formate, isobutyraldehyde and methanol are completely purified, and part of ethyl acetate and ethanol are volatilized at the same time. Under the action of the first condenser, this part of the purified gas is condensed to form a purified liquid, and then enters the first main tank or the first auxiliary tank located on the first supporting base, and then the first main tank or the first auxiliary tank is switched under the action of the first switching mechanism. The first main tank or the first auxiliary tank that collects the condensed purified liquid is moved to the second heating base, and then heated to 30°C for further purification, so that most of the ethyl acetate and ethanol are retained, and the rest enters the second condenser. Similarly, further purification is carried out in the third purification component, so that the purified acetaldehyde, hydrocyanic acid, propionaldehyde, ethyl formate, isobutyraldehyde and methanol are collected in the collection tank. After a purification process, the remaining purified liquid in the second purification component and the third purification component is added back to the first purification component, and multiple purifications are carried out to achieve better purification effects. BRIEF DESCRIPTION OF THE DRAWINGS

[0028] Figure 1 It is a schematic diagram of the overall structure of the present invention;

[0029] Figure 2 is a schematic structural diagram of the second purification component of the present invention;

[0030] Figure 3 is a schematic structural diagram of the third purification component of the present invention;

[0031] Figure 4 It is a schematic structural diagram of the first door frame and other parts of the present invention;

[0032] Figure 5 It is a structural schematic diagram of the first switching mechanism and other parts of the present invention;

[0033] Figure 6 It is a structural schematic diagram of the second door frame and other parts of the present invention;

[0034] Figure 7 It is a structural schematic diagram of the second switching mechanism and other parts of the present invention.

[0035] The accompanying drawings are marked as follows: 1. first heating base; 2. storage tank; 3. feed port; 4. discharge port; 5. first conveying pipe; 6. first door frame; 7. first door panel; 8. first condensing pipe; 9. first condenser; 10. first valve motor; 11. first condensing valve; 12. first switching motor; 13. first switching plate; 14. first main tank; 15. first auxiliary tank; 16. first supporting base; 17. second heating base; 18. first supporting column; 19. first supporting wheel; 20. first main tank refueling port; 21. first auxiliary tank refueling port; 22. second conveying pipe; 23. second door frame; 24. first Second door panel; 25. Second condenser tube; 26. Second condenser; 27. Second valve motor; 28. Second condenser valve; 29. ​​Second switching motor; 30. Second switching plate; 31. Second main tank; 32. Second auxiliary tank; 33. Second supporting base; 34. Third heating base; 35. Second supporting column; 36. Second supporting wheel; 37. Second main tank refueling port; 38. Second auxiliary tank refueling port; 39. Third conveying pipe; 40. Collecting door frame; 41. Collecting door panel; 42. Third condenser tube; 43. Third condenser; 44. Third condensing valve; 45. Collecting tank; 46. Collecting tank refueling port. DETAILED DESCRIPTION

[0036] In the following description, a large number of specific details are provided to provide a more thorough understanding of the present invention. However, it is apparent to those skilled in the art that the present invention can be implemented without one or more of these details. In other examples, in order to avoid confusion with the present invention, some technical features well known in the art are not described.

[0037] Combined with Figure 1-7 As shown, a liquor impurity removal and purification system and method comprises a first heating base 1, a storage tank 2, a feed port 3, a discharge port 4, a first conveying pipe 5, a first door frame 6, a first door plate 7, a first condenser pipe 8, a first condenser 9, a first valve motor 10, a first condensation valve 11, a first switching motor 12, a first switching plate 13, a first main tank 14, a first auxiliary tank 15, a first supporting base 16, a second heating base 17, a first supporting column 18, a first supporting wheel 19, a first main tank refueling port 20, a first auxiliary tank refueling port 21, a second conveying pipe 22, a second door frame 2 3. The second door panel 24, the second condenser 25, the second condenser 26, the second valve motor 27, the second condensation valve 28, the second switching motor 29, the second switching plate 30, the second main tank 31, the second auxiliary tank 32, the second support base 33, the third heating base 34, the second support column 35, the second support wheel 36, the second main tank refueling port 37, the second auxiliary tank refueling port 38, the third conveying pipe 39, the collecting door frame 40, the collecting door panel 41, the third condenser 42, the third condenser 43, the third condensation valve 44, the collecting tank 45 and the collecting tank refueling port 46.

[0038] See also Figure 1-7 , the present invention provides a technical solution: a liquor impurity removal and purification system, comprising: a first purification component, a second purification component, a third purification component and a collection component;

[0039] The first purification component, the second purification component, the third purification component and the collection component are arranged in sequence;

[0040] The first purification component includes a first heating base 1 and a storage tank 2. The storage tank 2 is disposed on the first heating base 1. The first heating base 1 is used to heat the storage tank 2 to raise its temperature to 60° C. The storage tank 2 is provided with a first delivery pipe 5.

[0041] The second purification assembly includes a first door frame 6, a first support base 16, a second heating base 17, a first switching mechanism, a first main tank 14 and a first auxiliary tank 15. The first door frame 6 is provided with a first door panel 7, and the first door panel 7 is provided with a first condensation pipe 8 and a second delivery pipe 22. The first support base 16 is located below the first condensation pipe 8, and the second heating base 17 is located below the second delivery pipe 22. The first switching mechanism is located in the first door frame 6 and is connected to the first main tank 14 and the first auxiliary tank 15 to drive the first main tank 14. Switching with the first auxiliary tank 15 on the first support base 16 and the second heating base 17, when the first main tank 14 or the first auxiliary tank 15 is located on the first support base 16, the opening of the first main tank 14 or the first auxiliary tank 15 is in contact with the first condensing pipe 8, when the first main tank 14 or the first auxiliary tank 15 is located on the second heating base 17, the opening of the first main tank 14 or the first auxiliary tank 15 is in contact with the second delivery pipe 22, and the second heating base 17 is used to heat the first main tank 14 or the first auxiliary tank 15 located thereon to 30°C;

[0042] The third purification component includes a second gantry 23, a second supporting base 33, a third heating base 34, a second switching mechanism, a second main tank 31 and a second auxiliary tank 32. The second gantry 23 is provided with a second door panel 24, and the second door panel 24 is provided with a second condensing pipe 25 and a third conveying pipe 39. The second supporting base 33 is located below the second condensing pipe 25, and the third heating base 34 is located below the third conveying pipe 39. The second switching mechanism is located in the second gantry 23 and is drivingly connected to the second main tank 31 and the second auxiliary tank 32 to drive the second main tank 31 and the second auxiliary tank 32. The tank 31 and the second auxiliary tank 32 are switched on the second support base 33 and the third heating base 34. When the second main tank 31 or the second auxiliary tank 32 is located on the second support base 33, the opening of the second main tank 31 or the second auxiliary tank 32 is in contact with the second condensing pipe 25. When the second main tank 31 or the second auxiliary tank 32 is located on the third heating base 34, the opening of the second main tank 31 or the second auxiliary tank 32 is in contact with the third delivery pipe 39. The third heating base 34 is used to heat the second main tank 31 or the second auxiliary tank 32 located thereon to a temperature of 20°C.

[0043] The collecting assembly comprises a collecting door frame 40, a collecting door plate 41 is arranged on the collecting door frame 40, a third condensing pipe 42 is arranged on the collecting door plate 41, and a collecting tank 45 is arranged below the third condensing pipe 42;

[0044] The first delivery pipe 5 is in communication with the first condensation pipe 8 , the second delivery pipe 22 is in communication with the second condensation pipe 25 , and the third delivery pipe 39 is in communication with the third condensation pipe 42 .

[0045] Through the above technical scheme, the storage tank 2 is used to carry the liquor to be purified. Under the action of the first heating base 1, the liquor in the storage tank 2 is heated to 65°C, so that all acetaldehyde, hydrocyanic acid, propionaldehyde, ethyl formate, isobutyraldehyde and methanol are completely purified, and part of ethyl acetate and ethanol will volatilize at the same time. Under the action of the first condenser 8, this part of the purified gas is condensed to form a purified liquid, and then enters the first main tank 14 or the first auxiliary tank 15 located on the first supporting base 16. Then, under the action of the first switching mechanism, the first main tank 14 or the first auxiliary tank 15 is switched to collect the purified liquid. The first main tank 14 or the first auxiliary tank 15 of the condensed purified liquid is moved to the second heating base 17, and then heated to 30°C for further purification, so that most of the ethyl acetate and ethanol are retained, and the rest enters the second condenser 25. Similarly, further purification is carried out in the third purification component, so that the purified acetaldehyde, hydrocyanic acid, propionaldehyde, ethyl formate, isobutyraldehyde and methanol are collected in the collection tank 45. After a purification process, the remaining purified liquid in the second purification component and the third purification component is added back to the first purification component, and multiple purifications are carried out to achieve better purification effects.

[0046] In a further embodiment, a feed port 3 and a discharge port 4 are provided on the storage tank 2 , wherein the feed port 3 is located at the top of the storage tank 2 , and the discharge port 4 is located at the bottom of the storage tank 2 .

[0047] Through the above technical solution, it is convenient to add materials to the storage tank 2 with the help of the feed port 3, and it is convenient to take out the purified liquor in the storage tank 2 with the help of the discharge port 4.

[0048] In a further embodiment, the first switching mechanism includes a first switching motor 12, the first switching motor 12 is located in the first gantry 6, the output end of the first switching motor 12 is connected to a first switching plate 13, one end of the first switching plate 13 is connected to a first main tank 14, the other end of the first switching plate 13 is connected to a first auxiliary tank 15, the first main tank 14 is provided with a first main tank refueling port 20, and the first auxiliary tank 15 is provided with a first auxiliary tank refueling port 21.

[0049] Through the above technical solution, with the help of the first switching motor 12, under the action of the first switching plate 13, the first main tank 14 and the first auxiliary tank 15 can be driven to rotate, so as to realize the switching of the first main tank 14 and the first auxiliary tank 15 on the first supporting base 16 or the second heating base 17, thereby ensuring the next step of purification while condensing, thereby ensuring the overall efficiency.

[0050] In a further embodiment, a first support column 18 is disposed on the first switching plate 13 , and a first support wheel 19 is disposed at the bottom of the first support column 18 .

[0051] Through the above technical solution, with the help of the first support wheel 19 and the first support column 18, the stability of the first main tank 14 and the first auxiliary tank 15 during rotation can be ensured.

[0052] In a further embodiment, a first condenser 9 is provided on the first condenser tube 8 , a first valve motor 10 is provided at the bottom of the first door panel 7 , an output end of the first valve motor 10 is connected to a first condensation valve 11 , and the first condensation valve 11 is provided on the first condenser tube 8 .

[0053] Through the above technical scheme, the condensation effect of the first condenser 8 is improved with the help of the first condenser 9, and the opening and closing of the first condensation valve 11 is conveniently controlled with the help of the first valve motor 10, thereby avoiding leakage of the first condenser 8 when switching between the first main tank 14 and the first auxiliary tank 15.

[0054] In a further embodiment, the second switching mechanism includes a second switching motor 29, which is located in the second gantry 23, and the output end of the second switching motor 29 is connected to a second switching plate 30, one end of the second switching plate 30 is connected to a second main tank 31, and the other end of the second switching plate 30 is connected to a second auxiliary tank 32, the second main tank 31 is provided with a second main tank refueling port 37, and the second auxiliary tank 32 is provided with a second auxiliary tank refueling port 38.

[0055] Through the above technical solution, with the help of the second switching motor 29, under the action of the second switching plate 30, the second main tank 31 and the second auxiliary tank 32 can be driven to rotate, so as to realize the switching of the second main tank 31 and the second auxiliary tank 32 on the second support base 33 or the third heating base 34, thereby ensuring the next step of purification while condensing, thereby ensuring the overall efficiency.

[0056] In a further embodiment, a second support column 35 is disposed on the second switching plate 30 , and a second support wheel 36 is disposed at the bottom of the second support column 35 .

[0057] Through the above technical solution, with the help of the second support wheel 36 and the second support column 35, the stability of the second main tank 31 and the second auxiliary tank 32 during rotation can be ensured.

[0058] In a further embodiment, a second condenser 26 is provided on the second condenser tube 25 , a second valve motor 27 is provided at the bottom of the second door panel 24 , an output end of the second valve motor 27 is connected to a second condensation valve 28 , and the second condensation valve 28 is provided on the second condenser tube 25 .

[0059] Through the above technical solution, the condensation effect of the second condenser 25 is improved by means of the second condenser 26, and the opening and closing of the second condensation valve 28 is conveniently controlled by means of the second valve motor 27, so as to avoid leakage of the second condenser 25 when switching between the second main tank 31 and the second auxiliary tank 32.

[0060] In a further embodiment, a third condenser 43 is provided on the third condenser pipe 42 , a third condenser valve 44 is provided at the bottom of the third condenser pipe 42 , and a collecting tank refueling port 46 is provided on the collecting tank 45 .

[0061] Through the above technical solution, the condensation effect of the third condenser tube 42 is improved by means of the third condenser 43 , and the opening and closing of the third condensation valve 44 is controlled.

[0062] A method for removing impurities from liquor and purifying the liquor system comprises the following steps:

[0063] S1: adding the liquor to be purified into the storage tank 2 through the feed port 3, and starting the first heating base 1 to heat the storage tank 2 to 65° C.;

[0064] S2: Start the first switching motor 12 to move the first main tank 14 or the first auxiliary tank 15 to the first supporting base 16, start the first condenser 9, and the condensate condensed in the first condensation tube 8 enters the first main tank 14 or the first auxiliary tank 15. After the first main tank 14 or the first auxiliary tank 15 collects the condensate condensed in the first condensation tube 8, start the first valve motor 10 to close the first condensation valve 11, start the first switching motor 12 to switch the first main tank 14 and the first auxiliary tank 15, and move the first main tank 14 or the first auxiliary tank 15 carrying the condensate to the second heating base 17 to heat it to 30°C;

[0065] S3: starting the first valve motor 10 to open the first condensation valve 11, and the condensed liquid condensed in the first condensation pipe 8 enters the first auxiliary tank 15 or the first main tank 14 placed on the first support base 16 to continue collecting the condensed liquid;

[0066] S4: Start the second switching motor 29 to move the second main tank 31 or the second auxiliary tank 32 to the second supporting base 33, start the second condenser 26, and the condensed liquid in the second condensation tube 25 enters the second main tank 31 or the second auxiliary tank 32. After the second main tank 31 or the second auxiliary tank 32 collects the condensed liquid in the second condensation tube 25, start the second valve motor 27 to close the second condensation valve 28, start the second switching motor 29 to switch the second main tank 31 and the second auxiliary tank 32, and move the second main tank 31 or the second auxiliary tank 32 carrying the condensed liquid to the third heating base 34 to heat it to 20°C.

[0067] S5: starting the second valve motor 27 to open the second condensation valve 28, and the condensed liquid condensed in the second condensation pipe 25 enters the second auxiliary tank 32 or the second main tank 31 placed on the second support base 33 to continue collecting the condensed liquid;

[0068] S6: Start the third condenser 43 , and the condensed liquid in the third condensation pipe 42 enters the collection tank 45 .

[0069] The preferred embodiments of the present invention are described in detail above in conjunction with the accompanying drawings. However, the present invention is not limited to the specific details in the above embodiments. Within the technical concept of the present invention, various equivalent transformations can be made to the technical scheme of the present invention, and these equivalent transformations all belong to the protection scope of the present invention.

Claims

1. A liquor impurity removal and purification system, comprising: The first purification component, the second purification component, the third purification component and the collection component are characterized by: The first purification component, the second purification component, the third purification component and the collection component are arranged in sequence; The first purification component comprises a first heating base (1) and a storage tank (2), wherein the storage tank (2) is arranged on the first heating base (1), the first heating base (1) is used to heat the storage tank (2) to raise its temperature to 65° C., and the storage tank (2) is provided with a first delivery pipe (5); The second purification assembly comprises a first door frame (6), a first supporting base (16), a second heating base (17), a first switching mechanism, a first main tank (14) and a first auxiliary tank (15); the first door frame (6) is provided with a first door panel (7); the first door panel (7) is provided with a first condensing pipe (8) and a second conveying pipe (22); the first supporting base (16) is located below the first condensing pipe (8); the second heating base (17) is located below the second conveying pipe (22); the first switching mechanism is located in the first door frame (6) and is drivingly connected to the first main tank (14) and the first auxiliary tank (15) for driving the first main tank (14). Switching with the first auxiliary tank (15) on the first supporting base (16) and the second heating base (17), when the first main tank (14) or the first auxiliary tank (15) is located on the first supporting base (16), the opening of the first main tank (14) or the first auxiliary tank (15) is in contact with the first condensing pipe (8), and when the first main tank (14) or the first auxiliary tank (15) is located on the second heating base (17), the opening of the first main tank (14) or the first auxiliary tank (15) is in contact with the second conveying pipe (22), and the second heating base (17) is used to heat the first main tank (14) or the first auxiliary tank (15) located thereon to a temperature of 30°C; The third purification component comprises a second door frame (23), a second supporting base (33), a third heating base (34), a second switching mechanism, a second main tank (31) and a second auxiliary tank (32); the second door frame (23) is provided with a second door plate (24); the second door plate (24) is provided with a second condensing pipe (25) and a third conveying pipe (39); the second supporting base (33) is located below the second condensing pipe (25); the third heating base (34) is located below the third conveying pipe (39); the second switching mechanism is located in the second door frame (23) and is drivingly connected to the second main tank (31) and the second auxiliary tank (32) for driving the second main tank ( 31) and the second auxiliary tank (32) are switched on the second supporting base (33) and the third heating base (34); when the second main tank (31) or the second auxiliary tank (32) is located on the second supporting base (33), the opening of the second main tank (31) or the second auxiliary tank (32) is in contact with the second condensing pipe (25); when the second main tank (31) or the second auxiliary tank (32) is located on the third heating base (34), the opening of the second main tank (31) or the second auxiliary tank (32) is in contact with the third conveying pipe (39); the third heating base (34) is used to heat the second main tank (31) or the second auxiliary tank (32) located thereon to a temperature of 20°C; The collecting assembly comprises a collecting door frame (40), a collecting door plate (41) is arranged on the collecting door frame (40), a third condensing tube (42) is arranged on the collecting door plate (41), and a collecting tank (45) is arranged below the third condensing tube (42); The first delivery pipe (5) is connected to the first condensation pipe (8), the second delivery pipe (22) is connected to the second condensation pipe (25), and the third delivery pipe (39) is connected to the third condensation pipe (42).

2. A liquor impurity removal and purification system according to claim 1, characterized in that: The storage tank (2) is provided with a feed port (3) and a discharge port (4), wherein the feed port (3) is located at the top of the storage tank (2), and the discharge port (4) is located at the bottom of the storage tank (2).

3. A liquor impurity removal and purification system according to claim 1, characterized in that: The first switching mechanism comprises a first switching motor (12), the first switching motor (12) is located in a first gantry (6), an output end of the first switching motor (12) is connected to a first switching plate (13), one end of the first switching plate (13) is connected to a first main tank (14), the other end of the first switching plate (13) is connected to a first auxiliary tank (15), a first main tank refueling port (20) is provided on the first main tank (14), and a first auxiliary tank refueling port (21) is provided on the first auxiliary tank (15).

4. A liquor impurity removal and purification system according to claim 3, characterized in that: A first support column (18) is arranged on the first switching plate (13), and a first support wheel (19) is arranged at the bottom of the first support column (18).

5. A liquor impurity removal and purification system according to claim 4, characterized in that: A first condenser (9) is arranged on the first condensation tube (8), a first valve motor (10) is arranged at the bottom of the first door panel (7), an output end of the first valve motor (10) is connected to a first condensation valve (11), and the first condensation valve (11) is arranged on the first condensation tube (8).

6. A liquor impurity removal and purification system according to claim 1, characterized in that: The second switching mechanism comprises a second switching motor (29), the second switching motor (29) is located in the second gantry (23), the output end of the second switching motor (29) is connected to a second switching plate (30), one end of the second switching plate (30) is connected to a second main tank (31), the other end of the second switching plate (30) is connected to a second auxiliary tank (32), the second main tank (31) is provided with a second main tank refueling port (37), and the second auxiliary tank (32) is provided with a second auxiliary tank refueling port (38).

7. A liquor impurity removal and purification system according to claim 6, characterized in that: A second support column (35) is provided on the second switching plate (30), and a second support wheel (36) is provided at the bottom of the second support column (35).

8. A liquor impurity removal and purification system according to claim 7, characterized in that: A second condenser (26) is arranged on the second condensation tube (25), a second valve motor (27) is arranged at the bottom of the second door panel (24), an output end of the second valve motor (27) is connected to a second condensation valve (28), and the second condensation valve (28) is arranged on the second condensation tube (25).

9. According to the white wine impurity removal and purification system according to claim 1, a third condenser (43) is provided on the third condenser tube (42), a third condensation valve (44) is provided at the bottom of the third condenser tube (42), and a collecting tank material replacement port (46) is provided on the collecting tank (45).

10. A method for removing impurities from liquor and purifying the system, characterized in that: The steps include: S1: adding liquor to be purified into the storage tank (2) through the feed port (3), and starting the first heating base (1) to heat the storage tank (2) to 65° C.; S2: Start the first switching motor (12) to move the first main tank (14) or the first auxiliary tank (15) onto the first supporting base (16), start the first condenser (9), and the condensate condensed in the first condensation tube (8) enters the first main tank (14) or the first auxiliary tank (15). After the first main tank (14) or the first auxiliary tank (15) collects the condensate condensed in the first condensation tube (8), start the first valve motor (10) to close the first condensation valve (11), start the first switching motor (12) to switch the first main tank (14) and the first auxiliary tank (15), so that the first main tank (14) or the first auxiliary tank (15) carrying the condensate moves to the second heating base (17) and is heated to 30°C; S3: starting the first valve motor (10) so that the first condensation valve (11) is opened, and the condensed liquid condensed in the first condensation pipe (8) enters the first auxiliary tank (15) or the first main tank (14) placed on the first support base (16) to continue collecting the condensed liquid; S4: Start the second switching motor (29) to move the second main tank (31) or the second auxiliary tank (32) onto the second supporting base (33), start the second condenser (26), and the condensate condensed in the second condensation tube (25) enters the second main tank (31) or the second auxiliary tank (32). After the second main tank (31) or the second auxiliary tank (32) collects the condensate condensed in the second condensation tube (25), start the second valve motor (27) to close the second condensation valve (28), start the second switching motor (29) to switch the second main tank (31) and the second auxiliary tank (32), and move the second main tank (31) or the second auxiliary tank (32) carrying the condensate onto the third heating base (34) to heat it to 20°C; S5: starting the second valve motor (27) so that the second condensation valve (28) is opened, and the condensed liquid condensed in the second condensation pipe (25) enters the second auxiliary tank (32) or the second main tank (31) placed on the second support base (33) to continue collecting the condensed liquid; S6: Start the third condenser (43), and the condensate condensed in the third condensation tube (42) enters the collection tank (45).

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