Device for improving quality of distilled liquor by magnetic field assisted tower type distillation equipment
By using a magnetic field-assisted tower distillation device, the movement trajectory of small molecule volatile substances is altered by the magnetic field, which solves the problems of low distillation efficiency and poor quality in existing equipment and improves the quality of fruit distilled wine.
Patent Information
- Application Number
- CN202520250804.0
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-02-18
- Publication Date
- 2025-11-28
- Estimated Expiration
- 2035-02-18
AI Technical Summary
Existing distillation equipment suffers from low distillation efficiency or poor product quality when preparing fruit distilled spirits. In particular, Charentais pot distillation equipment is inefficient, tower distillation equipment has limited aroma compounds, and pomace distillation equipment generally has poor quality and efficiency.
A magnetic field-assisted column distillation device is used. By installing a magnet with adjustable magnetic field strength on the outer wall of the column and combining it with a two-section column design, the magnetic field is used to affect the movement trajectory of small molecule volatile substances, thereby enriching beneficial aroma substances and reducing undesirable aroma substances.
It improves the taste and quality of fruit distilled spirits. By using a magnetic field to achieve gas-liquid phase balance and mass and heat transfer during the distillation process, it enhances distillation efficiency and product quality.
Smart Images
Figure CN223607247U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model belongs to wine brewing equipment technical field, especially related to a device of magnetic field auxiliary tower type distillation equipment promotes distillation wine quality. BACKGROUND
[0002] The prior art produces fruit distillation wine through distilling fruit fermentation wine, and the content of alcohol, acid, ester, ketone, aldehyde and other organic matters in the wine directly affects the taste and quality of the fruit wine. The existing equipment produces fruit distillation wine through Charentes pot type distillation equipment, tower type distillation equipment and skin residue distillation equipment, but these equipment has certain defects in preparing fruit distillation wine. For example, although the fruit distillation wine prepared by Charentes pot type distillation has good quality, the distillation efficiency is low. Although the tower type distillation equipment has high production efficiency, the prepared fruit distillation wine is not rich in aroma substances, and the product quality is poor. The fruit distillation wine prepared by the skin residue distillation equipment has general product quality, and the distillation efficiency is also general. It is found that in the distillation process of fruit fermentation wine, the small molecule volatile substances in the wine body are affected by the Lorentz force of the magnetic field. By adjusting the strength of the magnetic field, the motion trajectory of the small molecule volatile substances can be changed, the enrichment of beneficial aroma substances in the wine body and the reduction of distillation of undesirable aroma substances are realized, and the product quality of fruit distillation wine is improved. Therefore, it is urgent for the personnel in the field to propose an equipment combining the magnetic field and the tower type distillation equipment for improving the wine quality. CONTENT OF THE UTILITY MODEL
[0003] Therefore, the utility model provides a device of magnetic field auxiliary tower type distillation equipment promotes distillation wine quality for solving the above problems.
[0004] In order to realize the above purpose, the utility model adopts the following technical scheme:
[0005] A device of magnetic field auxiliary tower type distillation equipment promotes distillation wine quality, including: distillation kettle, tower body, magnet, condenser I, condenser II, vacuum pump and front fraction tank, the tower body communicates with the distillation kettle, the magnet is arranged on the outer wall of the tower body, and the magnetic field intensity can be adjusted, the gas phase output end of the tower body, the condenser I and the condenser II are sequentially communicated, the vacuum pump communicates with the condenser II, and the condenser II communicates with the front fraction tank.
[0006] Further, the distillation column is divided into two sections, a distillation column I section and a distillation column II section, the distillation column I section is integrally formed with the distillation kettle, the bottom of the distillation column I section is communicated with the distillation kettle, the top of the distillation column I section is communicated with the bottom of the distillation column II section, the top of the distillation column II section, the condenser I and the condenser II are sequentially communicated, the output end of each tray in the distillation column II section is communicated with the product tank, the bottom of the distillation column II section is communicated with the top of the distillation column I section through the intermediate pump, and the outer wall of the distillation column I section and the distillation column II section is provided with a magnet.
[0007] Further, the distillation column is divided into two sections, a distillation column I section and a distillation column II section, the distillation column I section is integrally formed with the distillation kettle, the bottom of the distillation column I section is communicated with the distillation kettle, the top of the distillation column I section is communicated with the bottom of the distillation column II section, the top of the distillation column II section, the condenser I and the condenser II are sequentially communicated, the output end of each tray in the distillation column II section is communicated with the product tank, the bottom of the distillation column II section is communicated with the top of the distillation column I section through the intermediate pump, and the outer wall of the distillation column I section and the distillation column II section is provided with a magnet.
[0008] Further, the distillation column I section and the distillation column II section are provided with a plurality of sampling ports.
[0009] Further, the inner coil is arranged in the inside of the fusel tank and the product tank, and the circulating water is used for cooling.
[0010] Further, the top of the fusel tank, the product tank and the fore fraction tank is provided with an exhaust valve, and the exhaust valve is used for freely switching between a vacuum environment and a normal pressure environment.
[0011] Further, the magnets are symmetrically arranged, and the magnets are provided with an opening for avoiding pipelines.
[0012] The utility model discloses the beneficial effect lies in:
[0013] The utility model discloses for guaranteeing the height limit of whole pry dress equipment, divides distillation column into 2 sections, distillation column I section and distillation column II section, and the gas phase on the top of distillation column I section enters the bottom of distillation column II section through the guide gas cylinder, and the liquid phase in the bottom of distillation column II section returns to the top tray of distillation column I section through the action of intermediate pump, thereby guaranteeing the gas-liquid phase balance and mass transfer and heat transfer of two section tower body, and the magnet is arranged on the outer wall of distillation column I section and distillation column II section, makes the small molecule volatile material in the distillation process be affected by the magnetic field, realizes the enrichment of beneficial aroma material and reduces the distillation of bad aroma material, improves the taste and quality of fruit distilled liquor. ACCURACY
[0014] In order to more clearly illustrate the technical scheme in the embodiments of the utility model or the prior art, the following will briefly introduce the drawings needed to be used in the embodiment or the prior art description, obviously, the drawings in the following description are only the embodiments of the utility model, and for the ordinary skilled person in the art, other drawings can also be obtained according to the provided drawings without creating the creative labor.
[0015] Figure 1 is a schematic view of a device for improving the quality of distilled liquor by a magnetic field assisted tower type distillation equipment.
[0016] Figure 2 is a schematic view of the structure of the distillation tower I section and the magnet.
[0017] Figure 3 is a schematic view of the structure of the distillation tower II section and the magnet.
[0018] Figure 4 is a schematic view of the structure of the magnet.
[0019] In the figure:
[0020] 10-distillation kettle, 21-distillation tower I section, 22-distillation tower II section, 30-magnet, 31-aperture, 40-condenser I, 50-condenser II, 60-vacuum pump, 70-finished product tank, 80-forefraction tank, 90-intermediate pump, 100-fusel oil tank, 110-emptying valve. DETAILED DESCRIPTION
[0021] The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments. Based on the embodiments in the present application, all other embodiments obtained by those skilled in the art without creative labor fall within the scope of protection of the present application.
[0022] Referring to the drawings shown in the accompanying drawings Figures 1-4 The present application provides a device for improving the quality of distilled liquor by a magnetic field assisted tower type distillation equipment, which comprises a distillation kettle 10, a tower body, a magnet 30, a condenser I 40, a condenser II 50, a vacuum pump 60 and a forefraction tank 80. The tower body is in communication with the distillation kettle 10. The magnet 30 is arranged on the outer wall of the tower body. The magnet 30 is a magnet generating device, which is internally provided with a magnetic induction coil. After being electrified, the magnet 30 can generate a magnetic field and adjust the strength of the magnetic field. The purpose of the magnet 30 is to generate a magnetic field for the tower body. The gas phase output end of the tower body, the condenser I 40 and the condenser II 50 are in sequence in communication. The vacuum pump 60 is in communication with the condenser II 50. The condenser II 50 is in communication with the forefraction tank 80. The output end of each tower plate in the tower body collects finished product ethanol. After the fruit fermented liquor is heated by saturated steam and enters the tower body, it continuously exchanges heat on the tower plate in the process of rising. Small molecular volatile substances are simultaneously affected by the magnetic field generated by the magnet 30, so that the enrichment of beneficial aroma substances and the reduction of the distillation of undesirable aroma substances are realized, and the quality of the fruit wine is improved. The finished product ethanol collected from the tower plate in the tower body is removed from the end of the condenser II 50 and temporarily stored in the forefraction tank 80, which is periodically discharged. After the distillation is completed, the distillation residue is stored in the distillation kettle 10 and is periodically discharged.
[0023] Preferably, in one embodiment, the device for improving the quality of distilled liquor by magnetic field assisted column distillation equipment further comprises a product tank 70 and an intermediate pump 90, in order to ensure the height limit of the whole skid-mounted equipment, the column body is divided into two sections, a distillation column I section 21 and a distillation column II section 22. The distillation column I section 21 is arranged on the distillation kettle 10 and is integrally formed with the distillation kettle 10. The bottom of the distillation column I section 21 is in communication with the distillation kettle 10. The top end of the distillation column I section 21 is in communication with the bottom of the distillation column II section 22. The gas phase output end of the distillation column II section 22, the condenser I 40 and the condenser II 50 are sequentially communicated. The output end of the tray in the distillation column II section 22 is in communication with the product tank 70. The bottom of the distillation column II section 22 is in communication with the top end of the distillation column I section 21 through the intermediate pump 90. The outer side walls of the distillation column I section 21 and the distillation column II section 22 are both provided with magnets 30. The volatile substances in the fruit fermented liquor are heated and enter the distillation column I section 21 for step-by-step heat exchange. In the process, the magnetic field generated by the magnets 30 acts on the volatile substances, so as to realize the enrichment of beneficial aroma substances and the reduction of the distillation of undesirable aroma substances. The gas phase at the top of the distillation column I section 21 enters the bottom of the distillation column II section 22 through the gas guide cylinder. The gas phase in the distillation column II section 22 continues to rise. In the process, the magnetic field generated by the magnets 30 acts on the gas phase, so as to further enrich the beneficial aroma substances and reduce the distillation of undesirable aroma substances. The distilled fruit distilled liquor is collected in the product tank 70 through the output end of the tray in the distillation column II section 22 and is temporarily stored in the product tank 70 and is regularly discharged. The liquid phase at the bottom of the distillation column II section 22 is returned to the top tray of the distillation column I section 21 through the action of the intermediate pump 90, so as to ensure the gas-liquid phase balance and mass transfer and heat transfer of the two column bodies.
[0024] Preferably, in one embodiment, the device for improving the quality of distilled liquor by magnetic field assisted column distillation equipment further comprises a fusel oil tank 100. The output end of each layer of tray in the distillation column I section 21 is in communication with the fusel oil tank 100, which is used for collecting fusel oil.
[0025] Preferably, in one embodiment, a plurality of sampling ports are arranged on the distillation column I section 21 and the distillation column II section 22, so as to select the optimal sampling port according to the running condition of the device.
[0026] Preferably, in one embodiment, inner coils are arranged in the fusel oil tank 100 and the product tank 70, which are used for cooling by circulating water.
[0027] Preferably, in one embodiment, an emptying valve 110 is arranged at the top of the fusel oil tank 100, the product tank 70 and the forefraction tank 80, which is used for freely switching between the vacuum environment and the normal pressure environment.
[0028] Preferably, in one embodiment, the magnets 30 are symmetrically arranged. A plurality of openings 31 are arranged on the magnets 30. The openings 31 avoid the pipelines on the distillation column I section 21 and the distillation column II section 22.
[0029] Working principle: the fruit fermented wine is stored in the distillation kettle 10, saturated steam is introduced to heat the fruit fermented wine; first, distillation is carried out under normal pressure or slightly negative pressure, the gas phase of the fruit fermented wine successively passes through the distillation column I section 21, the distillation column II section 22, the condenser I 40 and the condenser II 50, and low-boiling impurities in the raw material are removed and stored in the forefraction tank 80. Then the vacuum pump 60 is opened, the distillation kettle 10, the distillation column I section 21, the distillation column II section 22, the condenser I 40 and the condenser II 50 are vacuumized, the fruit fermented wine is heated and distilled by saturated steam, under the action of the magnetic field generated by the magnet 30 in the distillation column I section 21, the enrichment of beneficial aroma substances and the reduction of the distillation of undesirable aroma substances are realized, the gas phase at the top of the distillation column I section 21 enters the bottom of the distillation column II section 22 through the gas guide cylinder, the gas phase in the distillation column II section 22 continues to rise and distill, under the action of the magnetic field generated by the magnet 30 in the distillation column II section 22, the beneficial aroma substances are further enriched and the distillation of undesirable aroma substances is reduced, the distilled fruit distilled wine is collected in the finished product tank 70 through the output ends of each layer of tray in the distillation column II section 22. During the distillation process, part of the fusel alcohol is collected from the distillation column I section 21 and temporarily stored in the fusel alcohol tank 100.
[0030] The various embodiments in the specification are described in a progressive manner, and each embodiment focuses on the difference from other embodiments. The same or similar parts between the various embodiments can be referred to each other. For the device disclosed in the embodiments, since it corresponds to the method disclosed in the embodiments, the description is relatively simple, and the related parts can be referred to the method part.
[0031] The above description of the disclosed embodiments enables a person skilled in the art to implement or use the present application. Various modifications to these embodiments will be apparent to those skilled in the art, and the general principles defined herein can be implemented in other embodiments without departing from the spirit or scope of the present application. Therefore, the present application should not be limited to the embodiments shown herein, but should be consistent with the widest scope of principles and novel features disclosed herein.
Claims
1. A device for improving the quality of distilled spirits in a magnetic field assisted column distillation apparatus, comprising: It comprises: A distillation kettle (10), a tower body, a magnet (30), a condenser I (40), a condenser II (50), a vacuum pump (60) and a forefraction tank (80), the tower body is in communication with the distillation kettle (10), the magnet (30) is arranged on the outer wall of the tower body and can adjust the magnetic field intensity; the gas phase output end of the tower body, the condenser I (40) and the condenser II (50) are in communication in sequence, the vacuum pump (60) is in communication with the condenser II (50), and the condenser II (50) is in communication with the forefraction tank (80).
2. The device for improving the quality of distilled liquor by magnetic field assisted column distillation apparatus according to claim 1, characterized in that, It also comprises a finished product tank (70) and an intermediate pump (90), the tower body comprises a distillation column I section (21) and a distillation column II section (22), the distillation column I section (21) is arranged on the distillation kettle (10) and is integrally formed with the distillation kettle (10), the bottom of the distillation column I section (21) is in communication with the distillation kettle (10), the top end of the distillation column I section (21) is in communication with the bottom of the distillation column II section (22), the top end of the distillation column II section (22), the condenser I (40) and the condenser II (50) are in communication in sequence, the output end of each tray in the distillation column II section (22) is in communication with the finished product tank (70), the bottom of the distillation column II section (22) is in communication with the top end of the distillation column I section (21) through the intermediate pump (90), and the outer side walls of the distillation column I section (21) and the distillation column II section (22) are both provided with magnets (30).
3. The device for improving the quality of distilled liquor by magnetic field assisted column distillation apparatus according to claim 2, characterized in that, It also comprises a fusel oil tank (100), the tray output end in the distillation column I section (21) is in communication with the fusel oil tank (100) for collecting fusel oil.
4. The device for improving the quality of distilled liquor by magnetic field assisted column distillation apparatus according to claim 2, characterized in that, A plurality of sampling ports are arranged on the distillation column I section (21) and the distillation column II section (22).
5. The device for improving the quality of distilled liquor by magnetic field assisted column distillation apparatus according to claim 3, characterized in that, Inner coils are arranged in the fusel oil tank (100) and the finished product tank (70) for cooling by circulating water.
6. The device for improving the quality of distilled liquor by magnetic field assisted column distillation apparatus according to claim 3, characterized in that, Emptying valves (110) are arranged at the top of the fusel oil tank (100), the finished product tank (70) and the forefraction tank (80) for freely switching between vacuum environment and normal pressure environment.
7. The device for improving the quality of distilled liquor by magnetic field assisted column distillation apparatus according to claim 2, characterized in that, The magnets (30) are symmetrically arranged, and the magnets (30) are provided with notches (31) for avoiding pipelines.