Wine steam condensation tank

Abstract

The utility model discloses a wine steam condensation tank which comprises a tank body and further comprises a water inlet, a water outlet, a steam inlet and a wine outlet which are formed in the tank body, and a condensate water channel and a wine steam channel which are arranged in the tank body and used for heat exchange, and the two ends of the condensate water channel communicate with the water inlet and the water outlet correspondingly. And two ends of the wine steam channel are respectively communicated with the steam inlet and the wine outlet. According to the utility model, multi-stage condensation is adopted, and the temperature of wine steam can be condensed stage by stage, so that condensed wine can be recycled more uniformly, and the problem of subsequent wine steam blockage caused by condensed water adhesion due to concentrated condensation is avoided.

Description

Technical Field

[0001] The utility model relates to the technical field of condensation devices, in particular to the technical field of steam-water circulation condensation devices, and specifically to a wine steam condensation tank. Background Art

[0002] Baijiu, a popular distilled liquor produced in my country, is a representative example of distilled spirits. Its brewing process typically includes the preparation of raw ingredients, fermentation, distillation, condensation, and post-processing. Since the distillation process produces high-temperature liquor vapor, condensation is required to obtain liquid liquor. Various condensing devices are used in the vapor condensation process, but most typically utilize heat exchange, with water cooling being the more direct method. While the principles of condensation are generally the same, the specific cooling devices employed vary significantly.

[0003] Vapor condensing equipment is a crucial piece of equipment during the distillation stage of liquor production. Its function is to condense the vapors generated during distillation into liquid liquor. In recent years, significant advancements have been made in both the technology and materials used in these equipment. First, improvements have been made in the materials used for the condensers: modern condensing equipment often utilizes stainless steel, which offers excellent corrosion resistance and thermal conductivity, ensuring both liquor purity and equipment durability. Some high-end liquor breweries still use copper condensers because copper reacts with sulfides, enhancing the flavor and purity of the liquor. Second, structural optimization has been achieved. First, the use of coil condensers increases the condensing area and improves condensation efficiency. Second, the integrated steamer and condenser design optimizes the condensing structure. Finally, various structural designs are being employed to increase the condensing area and optimize condensation efficiency. Utility Model Content

[0004] In order to solve the technical problem of liquor distillation and condensation, the present application provides a liquor vapor condensation tank for replacing the existing liquor cooling equipment.

[0005] In order to achieve the above objectives, the technical solutions adopted in this application are:

[0006] A wine vapor condensation tank comprises a tank body, a water inlet, a water outlet, a steam inlet and a wine outlet arranged on the tank body, and a condensation water channel and a wine vapor channel arranged in the tank body for heat exchange, wherein the two ends of the condensation water channel are respectively connected to the water inlet and the water outlet, and the two ends of the wine vapor channel are respectively connected to the steam inlet and the wine outlet.

[0007] Preferably, the condensed water channel and the wine vapor channel include at least two stages of heat exchange structures in the tank body.

[0008] In the case of adopting a two-stage heat exchange structure for condensation, preferably, an outer tank cover and an upper inner tank cover are fixedly provided on the tank body, and an upper isolation plate is provided in the tank body, a first-level heat exchange chamber for accommodating condensed water is formed between the outer tank cover and the upper inner tank cover, the water outlet connected to the first-level heat exchange chamber is provided on the outer tank cover, a first-level cooling chamber for accommodating wine vapor is formed between the upper inner tank cover and the upper isolation plate, the steam inlet is connected to the first-level cooling chamber, a second-level heat exchange chamber for accommodating condensed water is formed between the upper isolation plate and the lower isolation plate installed at the bottom of the tank body, the second-level heat exchange chamber is connected to the first-level heat exchange chamber, the second-level heat exchange chamber is connected to the water inlet, and a plurality of condensing tubes are installed in the second-level heat exchange chamber, one end of any condensing tube passes through the upper isolation plate and is connected to the first-level cooling chamber, and the other end of the condensing tube passes through the lower isolation plate and is connected to the wine outlet.

[0009] Still further preferably, the primary heat exchange chamber and the secondary heat exchange chamber are connected through a first flow guiding mechanism arranged on the tank body, and the first flow guiding mechanism includes a first joint A arranged on the outer tank cover, a first joint B arranged on the tank body, and a first bend pipe for sealingly connecting the first joint A and the first joint B.

[0010] The present invention also provides another two-stage heat exchange structure. Preferably, an upper isolation plate and a lower isolation plate are further provided inside the tank body. The lower isolation plate divides the inside of the tank body into a secondary heat exchange chamber and a tertiary heat exchange chamber. A lower tank cover is further fixedly provided between the lower isolation plate and the bottom of the tank body. A three-stage cooling chamber is formed between the lower tank cover and the lower isolation plate, and a three-stage heat exchange chamber is formed between the lower tank cover and the bottom of the tank body. The three-stage heat exchange chamber is connected to a water inlet, and the secondary heat exchange chamber is connected to a water outlet.

[0011] The secondary heat exchange chamber and the tertiary heat exchange chamber are connected to each other through internal or external channels. Multiple condensers are installed in the secondary heat exchange chamber. One end of any condenser passes through the upper isolation plate to be connected to the steam inlet, and the other end of the condenser passes through the lower isolation plate to be connected to the tertiary cooling chamber. The tertiary cooling chamber is connected to the wine outlet.

[0012] Further preferably, the secondary heat exchange chamber and the tertiary heat exchange chamber are connected through a second flow guiding mechanism arranged on the outer wall of the tank body, and the second flow guiding mechanism includes a second joint A and a second joint B arranged on the tank body for connecting the secondary heat exchange chamber and the tertiary heat exchange chamber respectively, and a second bend pipe for connecting the second joint A and the second joint B.

[0013] In order to further improve the condensation effect, preferably, the condensation channel and the wine vapor channel include a three-stage heat exchange structure in the tank body.

[0014] Still further preferably, the three-stage heat exchange structure is implemented by the following scheme: an outer tank cover and an upper inner tank cover are fixedly provided on the tank body, and an upper isolation plate is provided in the tank body; a primary heat exchange chamber for accommodating condensed water is formed between the outer tank cover and the upper inner tank cover; the outer tank cover is provided with the water outlet communicated with the primary heat exchange chamber; a primary cooling chamber for accommodating wine vapor is formed between the upper inner tank cover and the upper isolation plate; the steam inlet is communicated with the primary cooling chamber through a pipeline;

[0015] A secondary heat exchange chamber for accommodating condensed water is formed between the upper isolation plate and the lower isolation plate installed at the bottom of the tank body, and the secondary heat exchange chamber is communicated with the primary heat exchange chamber;

[0016] A lower tank cover is fixedly provided between the lower isolation plate and the bottom of the tank body, a three-stage cooling chamber is formed between the lower tank cover and the lower isolation plate, and a three-stage heat exchange chamber is formed between the lower tank cover and the bottom of the tank body. The three-stage heat exchange chamber is interconnected with the two-stage heat exchange chamber, and the three-stage heat exchange chamber is also connected to a water inlet;

[0017] A plurality of condensing tubes are installed in the secondary heat exchange chamber. One end of any condensing tube passes through the upper isolation plate and is connected to the first-stage cooling chamber, and the other end of the condensing tube passes through the lower isolation plate and is connected to the third-stage cooling chamber. The third-stage cooling chamber is connected to the wine outlet.

[0018] Preferably, the primary heat exchange chamber and the secondary heat exchange chamber are connected through a first flow guiding mechanism arranged on the tank body, and the first flow guiding mechanism includes a first joint A arranged on the outer tank cover, a first joint B arranged on the tank body, and a first bend pipe for sealingly connecting the first joint A and the first joint B.

[0019] Preferably, the secondary heat exchange chamber and the tertiary heat exchange chamber are connected through a second flow guiding mechanism arranged on the outer wall of the tank body, and the second flow guiding mechanism includes a second joint A and a second joint B arranged on the tank body for connecting the secondary heat exchange chamber and the tertiary heat exchange chamber respectively, and a second bend pipe for connecting the second joint A and the second joint B.

[0020] Beneficial effects:

[0021] 1. The utility model adopts multi-stage condensation, which can condense the temperature of the wine vapor step by step, making the recovery of the condensed wine more uniform and avoiding the problem of subsequent wine vapor blockage caused by the adhesion of condensed water due to concentrated condensation.

[0022] 2. The utility model can be connected in series according to the condensation flow demand, increase the number of condensation stages, make the temperature difference between adjacent stages smaller, and avoid the dispersion of wine aroma; at the same time, multiple condensation tanks can also be connected in parallel to achieve large-volume condensation and improve condensation efficiency. BRIEF DESCRIPTION OF THE DRAWINGS

[0023] In order to more clearly illustrate the embodiments of the present application or the technical solutions in the prior art, the following briefly introduces the drawings required for use in the embodiments or the description of the prior art. Obviously, the drawings described below are only some embodiments of the present application. For those skilled in the art, other drawings can be obtained based on these drawings without paying any creative labor.

[0024] Figure 1 It is a structural axonometric drawing of the present utility model.

[0025] Figure 2 yes Figure 1 Another visual axonometric view of the structure.

[0026] Figure 3 It is a top view of the present utility model.

[0027] Figure 4 It is a schematic diagram of the internal structure of the tank body of an embodiment of the two-stage condensation of the present utility model.

[0028] Figure 5 It is a schematic diagram of the principle of steam and condensed water circulation in the condenser.

[0029] Figure 6 It is a schematic diagram of the cross-sectional structure of the condenser.

[0030] Figure 7 This is the main view of the condensation tank.

[0031] In the figure: 1 - tank body; 2 - outer tank cover; 21 - primary heat exchange chamber; 22 - upper inner tank cover; 23 - primary cooling chamber; 3 - steam inlet; 4 - water return port; 5 - first flow guide mechanism; 51 - first joint A; 52 - first elbow; 53 - first joint B; 6 - water inlet; 7 - wine outlet; 8 - second flow guide mechanism; 81 - second joint A; 82 - second elbow; 83 - second joint B;

[0032] 101-upper isolation plate; 102-condenser tube; 1021-upper connecting section; 1022-condenser section; 1023-lower connecting section; 103-connecting rod; 104-lower isolation plate; 105-secondary heat exchange chamber; 106-lower tank cover; 107-third-stage cooling chamber; 108-third-stage heat exchange chamber; DETAILED DESCRIPTION

[0033] To make the objectives, technical solutions, and advantages of the embodiments of the present application more clear, the technical solutions in the embodiments of the present application will be clearly and completely described below in conjunction with the accompanying drawings of the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, not all of the embodiments. Generally, the components of the embodiments of the present application described and shown in the drawings herein can be arranged and designed in various different configurations.

[0034] Therefore, the following detailed description of the embodiments of the present application provided in the accompanying drawings is not intended to limit the scope of the present application for protection, but merely represents selected embodiments of the present application. All other embodiments obtained by persons of ordinary skill in the art based on the embodiments in the present application without making any creative efforts shall fall within the scope of protection of the present application.

[0035] It should be noted that similar reference numerals and letters denote similar items in the following drawings, and therefore, once an item is defined in one drawing, it does not need to be further defined or explained in subsequent drawings.

[0036] In the description of this application, it should be noted that if the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc. appear, the orientation or position relationship indicated is based on the orientation or position relationship shown in the accompanying drawings, or the orientation or position relationship in which the product of the application is usually placed when in use. It is only for the convenience of describing this application and simplifying the description, and does not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operate in a specific orientation. Therefore, it cannot be understood as a limitation on this application. In addition, if the terms "first", "second", etc. appear in the description of this application, they are only used to distinguish the description and cannot be understood as indicating or implying relative importance.

[0037] Furthermore, the use of terms such as "horizontal" and "vertical" in the description of this application does not necessarily imply that a component must be absolutely horizontal or suspended, but rather that it can be slightly tilted. For example, "horizontal" simply means that its direction is more horizontal than "vertical" and does not mean that the structure must be completely horizontal, but rather that it can be slightly tilted.

[0038] It should also be noted that, unless otherwise expressly specified or limited, the terms "disposed," "installed," "connected," and "connected" should be understood broadly. For example, they may refer to fixed connections, detachable connections, or integral connections; mechanical connections or electrical connections; direct connections or indirect connections through an intermediate medium; and internal connections between two components. A person of ordinary skill in the art will understand the specific meanings of the above terms in this application based on the specific circumstances.

[0039] Example 1:

[0040] This embodiment provides a wine vapor condensation tank, see the attached manual Figure 1-Figure 2 As shown, it includes a tank body 1, and also includes a water inlet 6, a water outlet 4, a steam inlet 3 and a wine outlet 7 provided on the tank body 1, as well as a condensed water channel and a wine vapor channel provided in the tank body 1 for heat exchange. The two ends of the condensed water channel are respectively connected to the water inlet 6 and the water outlet 4, and the two ends of the wine vapor channel are respectively connected to the steam inlet 3 and the wine outlet 7. During condensation, the wine vapor produced by distillation enters the wine vapor channel through the steam inlet 3. During the flow, the steam exchanges heat with the condensed water channel to reduce the temperature, resulting in liquefaction, achieving the purpose of condensation, and finally flows out through the wine outlet 7 in the form of liquid alcohol; the condensed water at low temperature or room temperature enters the condensed water channel through the water inlet 6, contacts with the high-temperature wine vapor channel to undergo heat exchange, and the temperature rises, and flows out from the water outlet 4. This is repeated, so that the low-temperature water in the condensed water channel takes away the heat of the high-temperature wine vapor in the wine vapor channel, thereby achieving the effect of condensation.

[0041] Example 2:

[0042] In order to provide a condensing tank with better effect, this embodiment further optimizes the internal structure of the condensing tank based on Example 1. Figure 3-Figure 4 As shown in the partial structure of the structure shown, the condensed water channel and the wine vapor channel include at least two-stage heat exchange structures in the tank body 1. In this embodiment, when the two-stage heat exchange structure is used for condensation, the tank body 1 is fixedly provided with an outer tank cover 2 and an upper inner tank cover 22, as well as an upper isolation plate 101 provided in the tank body 1. A first-stage heat exchange chamber 21 for accommodating condensed water is formed between the outer tank cover 2 and the upper inner tank cover 22. The outer tank cover 2 is provided with the water outlet 4 connected to the first-stage heat exchange chamber 21. A first-stage cooling chamber 23 for accommodating wine vapor is formed between the upper inner tank cover 22 and the upper isolation plate 101. The steam inlet 3 is connected to the first-stage cooling chamber 21. 3, a secondary heat exchange chamber 105 for accommodating condensed water is formed between the upper isolation plate 101 and the lower isolation plate 104 installed at the bottom of the tank body 1, the secondary heat exchange chamber 105 is communicated with the primary heat exchange chamber 21, the secondary heat exchange chamber 105 is communicated with the water inlet 6, a plurality of condensing tubes 102 are installed in the secondary heat exchange chamber 105, one end of any condensing tube 102 passes through the upper isolation plate 101 and is communicated with the primary cooling chamber 23, and the other end of the condensing tube 102 passes through the lower isolation plate 104 and is communicated with the wine outlet 7.

[0043] Working principle:

[0044] See also Figure 4As shown, the cavity formed by the outer tank cover 2 and the upper isolation plate 101 is divided by the upper inner tank cover 22 into a primary heat exchange chamber 21 for condensed water and a primary cooling chamber 23 for high-temperature wine vapor. The low-temperature condensed water and the high-temperature wine vapor exchange heat through the upper inner tank cover 22. After the heat exchange, the temperature of the wine vapor decreases and the temperature of the condensed water increases, completing the primary heat exchange. To improve the efficiency and effectiveness of heat exchange, the surface area for heat exchange needs to be increased. Therefore, during the secondary heat exchange, condenser tubes 102 are used. The tank body 1 has a secondary heat exchange chamber 105 inside, and multiple condenser tubes 102 are installed in the secondary heat exchange chamber 105. The wine vapor circulates in the condenser tubes 102 and exchanges heat with the condensed water in the secondary heat exchange chamber 105 through the condenser tubes 102. This stage of heat exchange is called secondary heat exchange. In contrast, the surface area of ​​the condenser tubes 102 for heat exchange is greatly increased, allowing for sufficient heat exchange with the condensed water in the secondary heat exchange chamber 105, thus completing the secondary heat exchange. In actual use, for condensed water, the condensed water enters the secondary heat exchange chamber 105 from the water inlet 6 to exchange heat with each condenser tube 102, and then enters the primary heat exchange chamber 21 to exchange heat with the wine vapor in the primary cooling chamber 23, and finally is discharged from the water outlet 4. After the circulation and cooling treatment, it re-enters the circulation or is directly discharged for other uses. It is worth noting that the condensed water can also enter through the water outlet 4, and after heat exchange, it is discharged through the water inlet 6 for reverse condensation. The effects of forward condensation and reverse condensation are different. The flow direction of the condensed water depends on the temperature difference between the wine vapor and the condensed water. The greater the temperature difference, the better the forward condensation. Conversely, reverse condensation can be used. For wine vapor, the high-temperature wine vapor enters the primary cooling chamber 23 from the steam inlet 3, undergoes heat exchange and cooling, and then enters the condensation tank 102 with a smaller space for secondary heat exchange condensation. Finally, the condensed liquid alcohol / wine is discharged through the wine outlet 7 to obtain liquid wine. In this embodiment, the primary heat exchange chamber 21 and the secondary heat exchange chamber 105 can be connected through internal openings, for example, through through holes provided on the upper isolation plate 101, or can be connected through external pipes. The specific structure of the external pipes is detailed in the following embodiment 3.

[0045] Example 3:

[0046] This embodiment provides an external piping structure based on embodiment 2. Figure 4As shown, the primary heat exchange chamber 21 and the secondary heat exchange chamber 105 are connected via a first flow guiding mechanism 5 provided on the tank body 1. The first flow guiding mechanism 5 includes a first joint A51 provided on the outer tank cover 2, a first joint B53 provided on the tank body 1, and a first elbow 52 for sealingly connecting and conducting the first joint A51 and the first joint B53. The water inlet 6 can be provided on the inner wall of the tank body 1, preferably located near the bottom of the secondary heat exchange chamber 105.

[0047] Example 4:

[0048] The utility model also provides another two-stage heat exchange structure. Figure 4 As shown, the interior of the tank body 1 is further provided with an upper isolation plate 101 and a lower isolation plate 104. The lower isolation plate 104 divides the interior of the tank body 1 into a secondary heat exchange chamber 105 and a tertiary heat exchange chamber 108. A lower tank cover 106 is further fixedly provided between the lower isolation plate 104 and the bottom of the tank body 1. A tertiary cooling chamber 107 is formed between the lower tank cover 106 and the lower isolation plate 104. A tertiary heat exchange chamber 108 is formed between the lower tank cover 106 and the bottom of the tank body 1. The tertiary heat exchange chamber 108 is connected to the water inlet 6, and the secondary heat exchange chamber 105 is connected to the water outlet 4.

[0049] The secondary heat exchange chamber 105 and the tertiary heat exchange chamber 108 are connected to each other through internal or external channels. Multiple condensing tubes 102 are installed in the secondary heat exchange chamber 105. One end of any condensing tube 102 passes through the upper isolation plate 101 and is connected to the steam inlet 3, and the other end of the condensing tube 102 passes through the lower isolation plate 104 and is connected to the tertiary cooling chamber 107. The tertiary cooling chamber 107 is connected to the wine outlet 7.

[0050] Working principle: Condensed water enters the tertiary heat exchange chamber 108 through the water inlet 6, then enters the secondary heat exchange chamber 105 through the internal or external channel, and is finally discharged through the water outlet 4, so that the entire condensed water channel is filled with condensed water; high-temperature wine vapor enters the condenser tube 102 from the steam inlet 3, first undergoes a first heat exchange with the condensed water in the secondary heat exchange chamber 105, and then, after condensing through the condenser tube 102, enters the tertiary cooling chamber 107 for a second heat exchange, and after condensation, the liquid wine is discharged through the wine outlet 7. Among them, when the secondary heat exchange chamber 105 and the tertiary heat exchange chamber 108 are connected through the outside, they are connected through the second flow guiding mechanism 8 provided on the outer wall of the tank body 1, and the second flow guiding mechanism 8 includes a second joint A81 and a second joint B83 provided on the tank body 1 for connecting the secondary heat exchange chamber 105 and the tertiary heat exchange chamber 108, respectively, and a second bend pipe 82 for connecting the second joint A81 and the second joint B83. It should be noted that the purpose of using a detachable structure for both the first flow-guiding mechanism 5 in Example 3 and the second flow-guiding mechanism 8 in this embodiment is to facilitate cleaning, inspection, and maintenance of the internal structures of each flow chamber, thereby preventing scale buildup or other factors affecting condensation from being inspected and addressed. The detachable structure allows for visual inspection and maintenance.

[0051] Example 5:

[0052] In order to further improve the condensation effect, this embodiment also provides another condensation tank with a three-stage condensation structure. Figure 1-Figure 7 As shown, the condensation channel and the wine vapor channel include a three-stage heat exchange structure in the tank body 1.

[0053] In this embodiment, the three-stage heat exchange structure is implemented by the following scheme: the outer tank cover 2 and the upper inner tank cover 22 are fixedly provided on the tank body 1, and the upper isolation plate 101 is provided in the tank body 1. A primary heat exchange chamber 21 for accommodating condensed water is formed between the outer tank cover 2 and the upper inner tank cover 22. The outer tank cover 2 is provided with the water outlet 4 connected to the primary heat exchange chamber 21. A primary cooling chamber 23 for accommodating wine vapor is formed between the upper inner tank cover 22 and the upper isolation plate 101. The steam inlet 3 is connected to the primary cooling chamber 23 through a pipeline.

[0054] A secondary heat exchange chamber 105 for accommodating condensed water is formed between the upper isolation plate 101 and the lower isolation plate 104 installed at the bottom of the tank body 1. The secondary heat exchange chamber 105 is connected to the primary heat exchange chamber 21.

[0055] A lower tank cover 106 is fixedly provided between the lower isolation plate 104 and the inner bottom of the tank body 1. A three-stage cooling chamber 107 is formed between the lower tank cover 106 and the lower isolation plate 104. A three-stage heat exchange chamber 108 is formed between the lower tank cover 106 and the bottom of the tank body 1. The three-stage heat exchange chamber 108 is interconnected with the two-stage heat exchange chamber 105. The three-stage heat exchange chamber 108 is also connected to the water inlet 6.

[0056] A plurality of condensing tubes 102 are installed in the secondary heat exchange chamber 105. One end of any condensing tube 102 passes through the upper isolation plate 101 and is connected to the primary cooling chamber 23. The other end of the condensing tube 102 passes through the lower isolation plate 104 and is connected to the tertiary cooling chamber 107. The tertiary cooling chamber 107 is connected to the wine outlet 7.

[0057] In this embodiment, the primary heat exchange chamber 21 and the secondary heat exchange chamber 105 are connected through a first flow guiding mechanism 5 provided on the tank body 1. The first flow guiding mechanism 5 includes a first joint A51 provided on the outer tank cover 2, a first joint B53 provided on the tank body 1, and a first bend pipe 52 for sealingly connecting the first joint A51 and the first joint B53.

[0058] In this embodiment, the secondary heat exchange chamber 105 and the tertiary heat exchange chamber 108 are connected through a second flow guiding mechanism 8 arranged on the outer wall of the tank body 1. The second flow guiding mechanism 8 includes a second joint A81 and a second joint B83 arranged on the tank body 1 for connecting the secondary heat exchange chamber 105 and the tertiary heat exchange chamber 108 respectively, and a second bend pipe 82 for connecting the second joint A81 and the second joint B83.

[0059] This embodiment integrates the two two-stage heat exchange structures of the above-mentioned embodiments 2 to 4 to realize three-stage heat exchange, and its condensation principle is as shown in the principle of the corresponding structures shown in the above-mentioned embodiments 2 to 4.

[0060] The condenser provided in this embodiment, when used alone or in parallel, employs three-stage condensation. The condensate channel, in the order of condensate flow, comprises the water inlet 6, the third-stage heat exchange chamber 108, then enters the secondary heat exchange chamber 105 through the internal or external channel, then enters the primary heat exchange chamber 21 through the internal or external channel, and finally is discharged through the return port 4. At this point, the condensate has completed its flow through the condensate channel, and continuous condensation is achieved through the continuous input of condensate. Of course, the direction of condensate flow can also be reversed when necessary. Wine vapor enters the primary cooling chamber 23 through the steam inlet 3 for the first cooling. Since the condensate in the primary heat exchange chamber 21 has already undergone two heat exchanges from the bottom, it has been heated twice and is significantly higher than when it first enters the condenser. This reduces the temperature difference between the wine vapor and the condensate upon entering the primary cooling chamber 23, preventing the wine vapor from rapidly and directly condensing into liquid. This prevents clogging of the condenser tube 102 used for the subsequent secondary condensation. After cooling, the wine vapor enters the condenser 102. This stage of condensation is the main condensation. Since the internal space of the condensation tank 102 is relatively small, the vapor can fully contact the inner wall of the condenser 102 and condense into liquid. It then flows into the three-stage cooling chamber 107 of the next stage for cooling and condensation. At the same time, the liquid wine is collected and finally discharged through the wine outlet 7. In this embodiment, three-stage condensation is adopted. The temperature of the condensed water decreases step by step along the flow direction of the wine vapor. The temperature of the last stage is the lowest. This can avoid the blockage of the condenser tube 102 caused by the premature condensation of the wine vapor, resulting in the accumulation of wine vapor and even the problem of steam spraying from the wine outlet, thereby wasting wine vapor. Gradient step-by-step condensation can not only condense step by step to ensure the effect of wine vapor condensation, but also make the wine vapor condense and fall step by step, always keeping the steam on top and the liquid wine on the bottom, so that the recovery of the original wine is continuous. Among them, see Figure 4-Figure 5 As shown, the condenser 102 includes an upper connecting section 1021 connected to the upper isolation plate 101, a lower connecting section connected to the lower isolation plate 104, and a condensation section 1022 which is mainly used as a condenser in a spiral or S-shaped bend or other curved form to extend the condensation length as the condensation tank 102 is mainly used. The longer the condensation section 1022, the better the condensation effect. However, when the condensation section 1022 is in use, the height along the steam flow direction should be set lower and lower, so as to avoid the problem of accumulation of liquid wine after condensation.

[0061] The above description is merely a preferred embodiment of the present application and is not intended to limit the present application. Various modifications and variations are possible for those skilled in the art. Any modifications, equivalent substitutions, or improvements made within the spirit and principles of the present application shall be included within the scope of protection of the present application.

Claims

1. A wine vapor condensation tank, comprising a tank body (1), characterized in that: The invention also includes a water inlet (6), a water outlet (4), a steam inlet (3) and a wine outlet (7) provided on the tank body (1), and a condensed water channel and a wine steam channel provided in the tank body (1) for heat exchange, wherein the two ends of the condensed water channel are respectively communicated with the water inlet (6) and the water outlet (4), and the two ends of the wine steam channel are respectively communicated with the steam inlet (3) and the wine outlet (7).

2. The wine vapor condensation tank according to claim 1, characterized in that: The condensed water channel and the wine vapor channel include at least two stages of heat exchange structures in the tank body (1).

3. The wine vapor condensation tank according to claim 2, characterized in that: The tank body (1) is fixedly provided with an outer tank cover (2) and an upper inner tank cover (22), and an upper isolation plate (101) provided in the tank body (1); a first-stage heat exchange chamber (21) for accommodating condensed water is formed between the outer tank cover (2) and the upper inner tank cover (22); the outer tank cover (2) is provided with the water outlet (4) communicating with the first-stage heat exchange chamber (21); a first-stage cooling chamber (23) for accommodating wine vapor is formed between the upper inner tank cover (22) and the upper isolation plate (101); the steam inlet (3) is communicated with the first-stage cooling chamber (23); the upper isolation plate ( A secondary heat exchange chamber (105) for accommodating condensed water is formed between the upper isolation plate (101) and the lower isolation plate (104) installed at the bottom of the tank body (1), the secondary heat exchange chamber (105) is communicated with the primary heat exchange chamber (21), the secondary heat exchange chamber (105) is communicated with the water inlet (6), and a plurality of condensing tubes (102) are installed in the secondary heat exchange chamber (105), one end of any condensing tube (102) passes through the upper isolation plate (101) and is communicated with the primary cooling chamber (23), and the other end of the condensing tube (102) passes through the lower isolation plate (104) and is communicated with the wine outlet (7).

4. The wine vapor condensation tank according to claim 3, characterized in that: The primary heat exchange chamber (21) and the secondary heat exchange chamber (105) are communicated with each other via a first flow guiding mechanism (5) provided on the tank body (1), wherein the first flow guiding mechanism (5) comprises a first joint A (51) provided on the outer tank cover (2), a first joint B (53) provided on the tank body (1), and a first elbow (52) for sealingly connecting and conducting the first joint A (51) and the first joint B (53).

5. The wine vapor condensation tank according to claim 2, characterized in that: An upper isolation plate (101) and a lower isolation plate (104) are further provided inside the tank body (1), and the lower isolation plate (104) divides the inside of the tank body (1) into a secondary heat exchange chamber (105) and a tertiary heat exchange chamber (108). A lower tank cover (106) is further fixedly provided between the lower isolation plate (104) and the bottom of the tank body (1), and a tertiary cooling chamber (107) is formed between the lower tank cover (106) and the lower isolation plate (104). A tertiary heat exchange chamber (108) is formed between the lower tank cover (106) and the bottom of the tank body (1). The tertiary heat exchange chamber (108) is connected to a water inlet (6), and the secondary heat exchange chamber (105) is connected to a water outlet (4). The secondary heat exchange chamber (105) and the tertiary heat exchange chamber (108) are connected to each other through internal or external channels. A plurality of condensing tubes (102) are installed in the secondary heat exchange chamber (105). One end of any condensing tube (102) passes through the upper isolation plate (101) and is connected to the steam inlet (3). The other end of the condensing tube (102) passes through the lower isolation plate (104) and is connected to the tertiary cooling chamber (107). The tertiary cooling chamber (107) is connected to the wine outlet (7).

6. The wine vapor condensation tank according to claim 5, characterized in that: The secondary heat exchange chamber (105) and the tertiary heat exchange chamber (108) are connected via a second flow guiding mechanism (8) provided on the outer wall of the tank body (1), the second flow guiding mechanism (8) comprising a second joint A (81) and a second joint B (83) provided on the tank body (1) for connecting the secondary heat exchange chamber (105) and the tertiary heat exchange chamber (108), respectively, and a second elbow (82) for connecting the second joint A (81) and the second joint B (83).

7. The wine vapor condensation tank according to claim 1, characterized in that: The condensed water channel and the wine vapor channel comprise a three-stage heat exchange structure in the tank body (1).

8. The wine vapor condensation tank according to claim 7, characterized in that: The tank body (1) is fixedly provided with an outer tank cover (2) and an upper inner tank cover (22), and an upper isolation plate (101) provided in the tank body (1); a primary heat exchange chamber (21) for accommodating condensed water is formed between the outer tank cover (2) and the upper inner tank cover (22); the outer tank cover (2) is provided with the water outlet (4) communicating with the primary heat exchange chamber (21); a primary cooling chamber (23) for accommodating wine vapor is formed between the upper inner tank cover (22) and the upper isolation plate (101); the steam inlet (3) is communicated with the primary cooling chamber (23) through a pipeline; A secondary heat exchange chamber (105) for accommodating condensed water is formed between the upper isolation plate (101) and the lower isolation plate (104) installed at the bottom of the tank body (1), and the secondary heat exchange chamber (105) is communicated with the primary heat exchange chamber (21); A lower tank cover (106) is fixedly provided between the lower isolation plate (104) and the inner bottom of the tank body (1), a three-stage cooling chamber (107) is formed between the lower tank cover (106) and the lower isolation plate (104), and a three-stage heat exchange chamber (108) is formed between the lower tank cover (106) and the bottom of the tank body (1), the three-stage heat exchange chamber (108) and the two-stage heat exchange chamber (105) are interconnected, and the three-stage heat exchange chamber (108) is also connected to a water inlet (6); A plurality of condensing tubes (102) are installed in the secondary heat exchange chamber (105), one end of any condensing tube (102) passes through the upper isolation plate (101) and is connected to the primary cooling chamber (23), and the other end of the condensing tube (102) passes through the lower isolation plate (104) and is connected to the tertiary cooling chamber (107), and the tertiary cooling chamber (107) is connected to the wine outlet (7).

9. The wine vapor condensation tank according to claim 8, characterized in that: The primary heat exchange chamber (21) and the secondary heat exchange chamber (105) are communicated with each other via a first flow guiding mechanism (5) provided on the tank body (1), wherein the first flow guiding mechanism (5) comprises a first joint A (51) provided on the outer tank cover (2), a first joint B (53) provided on the tank body (1), and a first elbow (52) for sealingly connecting and conducting the first joint A (51) and the first joint B (53).

10. The wine vapor condensation tank according to claim 8, characterized in that: The secondary heat exchange chamber (105) and the tertiary heat exchange chamber (108) are connected via a second flow guiding mechanism (8) provided on the outer wall of the tank body (1), the second flow guiding mechanism (8) comprising a second joint A (81) and a second joint B (83) provided on the tank body (1) for connecting the secondary heat exchange chamber (105) and the tertiary heat exchange chamber (108), respectively, and a second elbow (82) for connecting the second joint A (81) and the second joint B (83).

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