Fragrance pulverizer with fragrance recovery function

Abstract

The utility model discloses a perfume pulverizer with a fragrance recovery function, and relates to the field of perfume pulverizers. The perfume pulverizer with the fragrance recovery function comprises a fragrance recovery unit installed at the upper end of an induced draft system of general pulverizing equipment and a steam-water separation unit installed at the lower end of the induced draft system. According to the spice pulverizer with the aroma recovery function, when volatile aroma components are volatilized due to heating of the spice pulverizer, volatilized gas enters the upper connecting column at the moment, circulating water and airflow are introduced through the tube nest in the main connecting column and the tube nest matched with the jacket for primary cooling, ice water is introduced through the coil matched with the jacket for further cooling, and aroma recovery is conducted; the airflow is discharged outwards through the connecting column body to be collected, the cyclone reversing pipe and the reversing plate are matched to separate the collected aroma part from the airflow, the airflow part is separated, and meanwhile cooled liquid falls down to be collected.

Description

Technical Field

[0001] This utility model relates to the technical field of spice pulverizers, specifically a spice pulverizer with aroma recovery. Background Technology

[0002] A spice grinder uses high-speed rotating cutting blades to process spices into fine particles, which are then sorted by a classifier to select the appropriate particle size.

[0003] During the spice pulverization process, the spice pulverizer heats up during the crushing process, which can easily lead to the loss of volatile aroma components, especially when the amount of pulverized material increases during production.

[0004] This application adds an aroma recovery device before the induced draft system of a general pulverizing equipment. The device is columnar, with tubes at the top and circulating water through a jacket for initial cooling of the airflow. The bottom is a coil, with ice water through a jacket for further cooling and aroma recovery. A gas-liquid separator is added at the bottom to separate the collected aroma from the airflow, facilitating collection, improving aroma recovery efficiency, and effectively preventing the loss of volatile aroma components. Utility Model Content

[0005] To address the shortcomings of existing technologies, this utility model provides a fragrance pulverizer with aroma recovery, which solves the problem that the loss of volatile aroma components is easily caused by the heat generated by the fragrance pulverizer during the crushing process, and the volatilization becomes more obvious as the amount of pulverized components increases during the production process.

[0006] To achieve the above objectives, this utility model provides the following technical solution: a fragrance pulverizer with aroma recovery, comprising an aroma recovery unit installed at the upper end of the induced draft system of a general pulverizing equipment and a gas-liquid separation unit at the lower end, wherein the aroma recovery unit includes:

[0007] The main connecting column has tubes arranged at equal intervals inside, which, together with the jacket, circulate water for initial cooling of the airflow.

[0008] The upper connecting column is installed above the main connecting column;

[0009] The lower connecting column is installed below the main connecting column. A coil is installed in the lower connecting column, which works with the jacket to circulate ice water for further cooling and aroma recovery.

[0010] Preferably, the steam-water separation unit includes:

[0011] The main body of the gas-liquid separator is installed under the induced draft system of a general-purpose pulverizing equipment;

[0012] Connecting column, fixedly installed inside the connecting column.

[0013] Preferably, the outer peripheral wall of the connecting column is provided with a vortex reversing pipe.

[0014] Preferably, a liquid separating plate is installed inside the main body of the gas-liquid separator, and the liquid separating plate is located below the connecting column.

[0015] Preferably, a liquid collection filter is installed below the main body of the gas-liquid separator, and the liquid collection filter is used for liquid collection.

[0016] Preferably, the gas-water separator body has ports on both sides, and the two ports are used for gas inlet and gas outlet respectively.

[0017] Preferably, a reversing plate is installed between the main body of the gas-water separator and the connecting column, and the reversing plate is used to guide the airflow.

[0018] This utility model discloses a fragrance pulverizer with aroma recovery, which has the following beneficial effects:

[0019] This fragrance pulverizer with aroma recovery function works as follows: When the pulverizer heats up, causing volatile aroma components to evaporate, the evaporated gas enters the upper connecting column. It then passes through the tubes in the main connecting column, which, in conjunction with the jacket, are circulated with water for initial cooling. The gas is then further cooled by passing through the coils and the jacket with ice water, thus recovering the aroma. The gas is discharged outward through the connecting column and collected. The collected aroma portion is separated from the gas flow by the swirl reversing pipe and the reversing plate. The cooled liquid falls and is collected. Attached Figure Description

[0020] To more clearly illustrate the technical solutions in the embodiments of this utility model or the prior art, the drawings used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings described below are only some embodiments of this utility model. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0021] Figure 1 This is a schematic diagram of the overall structure of this utility model;

[0022] Figure 2 This is a schematic diagram of the aroma recovery unit of this utility model;

[0023] Figure 3 This is a schematic diagram of the steam-water separation unit of this utility model.

[0024] In the diagram: 1. Aroma recovery unit; 11. Main connecting column; 111. Tube; 12. Upper connecting column; 13. Lower connecting column; 131. Coil; 2. Gas-liquid separation unit; 21. Gas-liquid separator body; 22. Connecting column; 23. Swirl reversing tube; 24. Liquid separator plate; 25. Pipe inlet; 26. Liquid collection filter; 27. Reversing plate. Detailed Implementation

[0025] To make the objectives, technical solutions, and advantages of the embodiments of this utility model clearer, the technical solutions in the embodiments of this utility model are described clearly and completely. Obviously, the described embodiments are only some embodiments of this utility model, not all embodiments. Based on the embodiments of this utility model, all other embodiments obtained by those skilled in the art without creative effort are within the protection scope of this utility model.

[0026] This application provides a fragrance pulverizer with aroma recovery, which solves the problem that the loss of volatile aroma components is easily caused by the heat generated by the fragrance pulverizer during the crushing process. The loss of volatile aroma components is more obvious as the amount of pulverized products increases during the production process. When the volatile aroma components evaporate due to the heat generated by the fragrance pulverizer, the evaporated gas enters the upper connecting column 12, passes through the tubes 111 in the main connecting column 11, and is initially cooled by circulating water through the tubes 111 and the jacket. Then, it is further cooled by ice water through the coil 131 and the jacket, thus recovering the aroma.

[0027] The airflow is discharged outward through the connecting column 22 and collected. With the help of the swirl reversing tube 23 and the reversing plate 27, the collected aroma part and the airflow are separated. The airflow part is separated, and the cooled liquid falls and is collected.

[0028] To better understand the above technical solutions, the following will provide a detailed explanation of the technical solutions in conjunction with the accompanying drawings and specific implementation methods.

[0029] This utility model discloses a fragrance pulverizer with aroma recovery function.

[0030] Example 1:

[0031] According to the appendix Figure 1-3 As shown, the device includes an aroma recovery unit 1 installed at the upper end of the induced draft system of a general-purpose pulverizing equipment and a vapor-liquid separation unit 2 installed at the lower end. The aroma recovery unit 1 includes:

[0032] The main connecting column 11 has tubes 111 arranged at equal intervals inside, which, together with the jacket, circulate water for initial cooling of the airflow.

[0033] The upper connecting post 12 is installed above the main connecting post 11;

[0034] The lower connecting column 13 is installed below the main connecting column 11. A coil 131 is installed in the lower connecting column 13, which works with the jacket to circulate ice water for further cooling and aroma recovery.

[0035] When the volatile aroma components evaporate due to the heat generated by the fragrance pulverizer, the evaporated gas enters the upper connecting column 12, passes through the tubes 111 in the main connecting column 11, and is circulated with water through the tubes 111 and the jacket. The gas is initially cooled, and then further cooled by ice water through the coil 131 and the jacket, thus recovering the aroma.

[0036] The steam-water separation unit 2 includes:

[0037] The main body 21 of the gas-liquid separator is installed under the induced draft system of a general-purpose pulverizing equipment;

[0038] The connecting column 22 is fixedly installed inside the connecting column 22. The airflow enters the air-water separator body 21 and is discharged outward through the connecting column 22 and collected.

[0039] A vortex reversing pipe 23 is provided on the outer peripheral wall of the connecting column 22. The vortex reversing pipe 23 guides the fluid to form a spiral flow state and increases the rotation speed of the fluid in the main body 21 of the gas-water separator by utilizing the vortex effect, thereby reducing the friction inside the pipe and improving the flow efficiency of the fluid.

[0040] The centrifugal force generated by the rotational motion causes water droplets to be thrown against the inner wall of the equipment, while the gas continues to flow along the central axis, thus achieving gas-liquid separation.

[0041] A liquid separator plate 24 is installed inside the main body 21 of the gas-liquid separator, and the liquid separator plate 24 is located below the connecting column 22.

[0042] The airflow is discharged outward through the connecting column 22 and collected. With the help of the swirl reversing tube 23 and the reversing plate 27, the collected aroma part and the airflow are separated. The airflow part is separated, and the cooled liquid falls and is collected.

[0043] Example 2:

[0044] A liquid collection filter 26 is installed below the main body 21 of the gas-liquid separator. The liquid collection filter 26 is used to collect liquid, and the liquid distribution plate 24 is used to receive liquid, separate liquid, and transport liquid to the liquid collection filter 26. After the liquid is collected by the liquid collection filter 26, the liquid is transported.

[0045] Both sides of the gas-water separator body 21 are provided with pipe openings 25. The two pipe openings 25 are used for air intake and air exhaust respectively. Water vapor from the general pulverizing equipment induced draft system enters the gas-water separator body 21 through the pipe openings 25.

[0046] At this point, the density difference between gas and water is used to cause the heavier liquid water droplets to settle due to gravity during the flow, thereby achieving gas-liquid separation. The gas is transported upward through the connecting column 22 and discharged outward through the pipe 25.

[0047] A reversing plate 27 is installed between the main body 21 of the gas-liquid separator and the connecting column 22. The reversing plate 27 is used to guide the airflow. When the airflow suddenly changes direction, the water droplets will continue to maintain their original direction of motion due to their large mass and inertia, while the gas will change direction due to its smaller inertia, thereby achieving gas-liquid separation.

[0048] The foregoing has shown and described the basic principles, main features, and advantages of this utility model. Those skilled in the art should understand that this utility model is not limited to the above embodiments. The embodiments and descriptions in the specification are merely illustrative of the principles of this utility model. Various changes and modifications can be made to this utility model without departing from its spirit and scope, and all such changes and modifications fall within the scope of the claims. The scope of protection of this utility model is defined by the appended claims and their equivalents.

Claims

1. A flavor mill with aroma recovery, comprising an aroma recovery unit (1) installed at the upper end of the air induction system of a general-purpose pulverizing device and a vapor-liquid separation unit (2) installed at the lower end, characterized in that, The fragrance recovery unit (1) comprises: The main connecting column (11) is provided with column tubes (111) equidistantly inside, circulating water is passed through the jacket to preliminarily cool the airflow; The upper connecting column (12) is installed above the main connecting column (11); The lower connecting column (13) is installed below the main connecting column (11), the lower connecting column (13) is provided with a coil pipe (131) inside, ice water is passed through the jacket to further cool and recover the fragrance.

2. A flavour mill with aroma recovery according to claim 1, characterized in that The steam-water separation unit (2) comprises: The gas-water separator body (21) is installed below the general pulverizing device induced draft system; The connecting column body (22) is fixedly installed inside the connecting column body (22).

3. A flavour mill with aroma recovery according to claim 2, characterized in that The outer peripheral wall of the connecting column body (22) is provided with a cyclone reversing pipe (23).

4. A spice grinder with aroma recovery according to claim 2, characterized in that The gas-water separator body (21) is provided with a liquid distribution plate (24) inside, the liquid distribution plate (24) is below the connecting column body (22).

5. A flavour mill with aroma recovery according to claim 4, characterized in that The gas-water separator body (21) is provided with a liquid accumulation filter (26) below, the liquid accumulation filter (26) is used for collecting liquid.

6. A flavour mill with aroma recovery according to claim 5, characterized in that Both sides of the gas-water separator body (21) are provided with pipe mouths (25), the two pipe mouths (25) are respectively used for air inlet and air outlet.

7. A spice grinder with aroma recovery according to claim 2, characterized in that The gas-water separator body (21) and the connecting column body (22) are provided with a reversing plate (27) therebetween, the reversing plate (27) is used for guiding the airflow.

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