CN211946960U - Making wine distillation cooling water cyclic utilization system - Google Patents
Making wine distillation cooling water cyclic utilization system Download PDFInfo
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- CN211946960U CN211946960U CN202020099302.XU CN202020099302U CN211946960U CN 211946960 U CN211946960 U CN 211946960U CN 202020099302 U CN202020099302 U CN 202020099302U CN 211946960 U CN211946960 U CN 211946960U
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Abstract
The utility model relates to a white spirit distillation cooling water cyclic utilization technical field, concretely relates to making wine distillation cooling water cyclic utilization system, including the condenser, the condenser includes cooling water container, condensation core, condenser water inlet, condenser gap, the condensation core is located cooling water container's inside, the upper and lower end of cooling water container lateral wall is equipped with condenser gap and condenser water inlet respectively, the condenser gap of condenser is connected with the return water pipe, the other end of return water pipe lets in the buffering pond, the buffering pond links to each other with the inlet end of cooling tower through the cooling tower inlet channel, be equipped with water pump one on the cooling tower inlet channel, the outlet end of cooling tower is linked together with groundwater pool through the cooling tower outlet conduit; the utility model provides a cooling water circulation system of recycling is again can effective cyclic utilization water resource, energy saving and emission reduction, reduction enterprise manufacturing cost under the condition that satisfies production technology.
Description
Technical Field
The utility model relates to a white spirit distillation cooling water cyclic utilization technical field, concretely relates to making wine distillation cooling water cyclic utilization system.
Background
Water cooled condensers are often used for liquor distillation condensers. The condenser uses low-temperature water as a condensing medium, in order to ensure the wine outlet temperature, the low-temperature water needs to be continuously supplemented in the production, and the overflowed high-temperature water is often wasted and is limited to be used in water resource deficient areas. High-temperature water is also fed into a cooling tower for cooling treatment, but the temperature of the cooled water is basically close to the room temperature. The temperature for receiving the white spirit during brewing the white spirit is generally 20 ℃ to 25 ℃, and the temperature is usually higher than the temperature in summer, so the temperature of the water cooled by the cooling tower in summer cannot reach below 20 ℃. The cooling water can be forcibly cooled and utilized by large-scale refrigeration equipment, but the energy consumption is large, and the energy conservation is not facilitated.
SUMMERY OF THE UTILITY MODEL
The utility model provides a to above problem, provide a cooling water circulation system of recycling, under the condition that satisfies production technology, can effective cyclic utilization water resource again, energy saving and emission reduction reduces the manufacturing cost of enterprise.
The utility model discloses cross following technical scheme and realize:
the utility model provides a making wine distillation cooling water cyclic utilization system, includes the condenser, the condenser includes cooling water container, condensation core, condenser water inlet, condenser gap, the inside of cooling water container is located to the condensation core, the upper and lower end of cooling water container lateral wall is equipped with condenser gap and condenser water inlet respectively, the condenser gap of condenser is connected with the return water pipe, the other end of return water pipe lets in the buffering pond, the buffering pond links to each other through the end of intaking of cooling tower inlet channel and cooling tower, be equipped with water pump one on the cooling tower inlet channel, the play water end of cooling tower is linked together through cooling tower outlet conduit and groundwater pool group, groundwater pool group is linked together through pond outlet conduit and condenser water inlet, be equipped with water pump two on the outlet conduit of pond.
Furthermore, a temperature sensor is arranged at a wine outlet of the condensation core, a flow control valve is further arranged on the water outlet pipeline of the water pool, the flow control valve is positioned between the second water pump and the water inlet of the condenser, and the temperature sensors at the wine outlet of the flow control valve and the condensation core are respectively electrically connected with an external controller.
Furthermore, the cooling tower is a closed air cooling tower.
Further, groundwater pond group is established ties by a plurality of ponds and is constituteed, links to each other through the communicating pipe between the adjacent pond, the communicating pipe import is in the lower part in preface pond, exports on the upper portion in preface pond, and there is the pond overflow mouth top side in adjacent pond, pond outlet conduit and cooling tower outlet conduit link to each other with the pond that is in leftmost and rightmost end respectively.
The utility model has the advantages that:
1. the utility model provides a making wine distillation cooling water cyclic utilization system can abundant cyclic utilization cooling water, reduces water wasting of resources.
2. And the production energy consumption is reduced by utilizing underground low-temperature natural cooling.
3. The advantage of no noise of the water-cooled condenser is kept, and the range of the using area of the condenser is enlarged.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings that are required to be used in the embodiments will be briefly described below, it should be understood that the following drawings only illustrate some embodiments of the present invention, and therefore should not be considered as limiting the scope, and for those skilled in the art, other related drawings can be obtained according to the drawings without inventive efforts.
Fig. 1 is a schematic structural diagram of the present invention;
fig. 2 is a schematic structural diagram of the condenser of the present invention.
The corresponding part names for the various reference numbers in the figures are:
a condenser-10; a cooling water container-11; -12 a condensation core; a water inlet-13 of the condenser; condenser overflow-14; a water return pipeline-20; a buffer pool-30; a cooling tower water inlet pipeline-40; a first water pump-50; cooling tower-60; a cooling tower outlet conduit-70; underground water pond group-80; a communication pipe-81; a pool overflow port-82; pool-83; pool outlet conduit-90; a second water pump 100; a flow control valve-110.
Detailed Description
To make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the drawings of the embodiments of the present invention are combined to clearly and completely describe the technical solutions of the embodiments of the present invention, and obviously, the described embodiments are some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention. Thus, the following detailed description of the embodiments of the present invention, presented in the accompanying drawings, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
In the description of the present invention, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implying any number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of the present invention, "a plurality" means two or more unless specifically limited otherwise.
The present invention will be described in further detail with reference to the accompanying drawings.
Referring to fig. 1-2, a system for recycling cooling water in wine brewing distillation comprises a condenser 10, wherein the condenser 10 comprises a cooling water container 11, a condensation core 12, a condenser water inlet 13 and a condenser overflow port 14, the condensation core 12 is arranged in the cooling water container 11, the upper end and the lower end of the side wall of the cooling water container 11 are respectively provided with the condenser overflow port 14 and the condenser water inlet 13, and the condenser overflow port and the condenser water inlet 13 are the structures of the existing condensers;
the condenser overflow port 14 of the condenser 10 is connected with a return water pipe 20, the other end of the return water pipe 20 is connected into a buffer water tank 30, wherein the buffer water tank 30 can adopt a closed container or an open container to play roles of temporarily storing hot water and primarily dissipating heat, the buffer water tank 30 is connected with the water inlet end of a cooling tower 60 through a cooling tower water inlet pipe 40, a first water pump 50 is arranged on the cooling tower water inlet pipe 40, the output end of the first water pump 50 is communicated with the cooling tower 60, the input end of the first water pump is communicated with the buffer water tank 30, the water outlet end of the cooling tower 60 is communicated with an underground water tank group 80 through a cooling tower water outlet pipe 70,
in cold winter, the water is cooled to 10-15 ℃, wherein the underground water tank group 80 is located underground, the underground temperature is generally warm in winter and cool in summer, and the method is more suitable for preparing cooling water with stable temperature.
The underground water tank group 80 is communicated with the water inlet 13 of the condenser through a water tank outlet pipeline 90, a second water pump 100 is arranged on the water tank outlet pipeline 90, the output end of the second water pump 100 is communicated with the water inlet 13 of the condenser, and the input end of the second water pump 100 is communicated with the underground water tank group 80.
Furthermore, a temperature sensor is arranged at the wine outlet of the condensation core 12, a flow control valve 110 is also arranged on the water outlet pipeline 90 of the water pool, the flow control valve 110 is positioned between the second water pump 100 and the water inlet 13 of the condenser, and the temperature sensors at the wine outlet of the condensation core 12 and the flow control valve 110 are respectively electrically connected with an external controller; when the temperature sensor at the wine outlet of the condensation core 12 detects that the wine outlet temperature is higher than the set temperature (for example, 20 ℃), the external controller controls the opening of the flow control valve 110 to be increased, and the water inlet flow is increased, so that the cooling effect of the wine vapor is improved.
Further, the cooling tower 60 is a closed air cooling tower; the hot water is forced to be cooled in the closed cooling tower, the evaporation and concentration of water quantity can be reduced by adopting the closed cooling tower, and simultaneously the generation of scale is avoided as much as possible.
Furthermore, the underground water pool group 80 is composed of a plurality of water pools 83 which are connected in series, adjacent water pools 83 are connected through a communication pipeline 81, the inlet of the communication pipeline 81 is arranged at the lower part of the front-sequence water pool 83, the outlet of the communication pipeline is arranged at the upper part of the rear-sequence water pool 83, the side surface of the top of the adjacent water pool 83 is provided with a water pool overflow port 82, and the water pool water outlet pipeline 90 and the cooling tower water outlet pipeline 70 are respectively connected with the water pools 83 at the leftmost end and the rightmost end; the side surface of the top of the adjacent water tank is provided with a water tank overflow port, so that the water tank overflow port has the function of communicating air and also has the function of overflowing when the water amount is too large. The water entering the water pool is firstly cooled primarily in a first water pool, then the water with lower temperature in the bottom layer preferentially flows into a second water pool (the hot water with lower density is positioned in the upper layer, the cold water with higher temperature density is positioned in the lower layer), the water is further naturally cooled in the second water pool, the water with lower temperature in the bottom layer preferentially flows into a third water pool, and the like until the water is cooled to the underground temperature.
The working principle is as follows: when the condenser 10 starts to operate, wine vapor passes through the condensation core 12 from top to bottom, so that cooling water in the cooling water container 11 is heated from top to bottom, meanwhile, because the density of hot water is smaller than that of cold water, the temperature of the upper layer cooling water is higher, the hot water at the upper layer in the cooling water container 11 is discharged out of the condenser 10 through the overflow port 14, the hot water discharged out of the condenser 10 flows to the buffer water pool 30 through the water return pipeline 20 for temporary storage and natural heat dissipation, then the water in the buffer water pool 30 is conveyed into the closed cooling tower 60 through the cooling tower water inlet pipeline 40 and the water pump 50 for forced air cooling, then the water which is forcibly cooled to room temperature (summer) or set temperature (winter) is discharged into the underground water pool group 80 through the cooling tower water outlet pipeline 70, the water entering the water pool 83 is primarily cooled in the first water pool 83, then the water with lower bottom layer temperature preferentially flows into the second, after the second water tank 83 is further cooled naturally, the water communication pipe 81 with the same lower temperature at the bottom layer preferentially flows into the third water tank 83, and so on until the water is cooled to the underground temperature, and then the cooling water is conveyed to the condenser 10 for reuse through the water outlet pipe 90 of the water tank and the second water pump 100.
The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention, and various modifications and changes may be made by those skilled in the art. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (4)
1. The utility model provides a making wine distillation cooling water cyclic utilization system, includes condenser (10), condenser (10) includes cooling water container (11), condensation core (12), condenser water inlet (13), condenser gap (14), the inside of cooling water container (11) is located in condensation core (12), the upper and lower end of cooling water container (11) lateral wall is equipped with condenser gap (14) and condenser water inlet (13) respectively, its characterized in that, condenser gap (14) of condenser (10) are connected with return water pipeline (20), the other end of return water pipeline (20) lets in buffer pool (30), buffer pool (30) link to each other through the inlet end of cooling tower inlet channel (40) with cooling tower (60), be equipped with water pump (50) on cooling tower inlet channel (40), the play water end of cooling tower (60) is linked together through cooling tower outlet conduit (70) and groundwater pond group (80), the underground water tank group (80) is communicated with the water inlet (13) of the condenser through a water tank water outlet pipeline (90), and a water pump II (100) is arranged on the water tank water outlet pipeline (90).
2. The system for recycling the distilled cooling water for brewing wine as claimed in claim 1, wherein a temperature sensor is disposed at the wine outlet of the condensation core (12), a flow control valve (110) is further disposed on the water outlet pipeline (90) of the water tank, the flow control valve (110) is located between the second water pump (100) and the water inlet (13) of the condenser, and the temperature sensors at the wine outlet of the flow control valve (110) and the condensation core (12) are respectively electrically connected to an external controller.
3. The system of claim 1, wherein the cooling tower is a closed air cooling tower.
4. The system for recycling the distilled cooling water for wine brewing according to claim 1, wherein the underground water pool (80) is composed of a plurality of water pools (83) which are connected in series, adjacent water pools (83) are connected through a communication pipeline (81), the inlet of the communication pipeline (81) is arranged at the lower part of the front-sequence water pool (83), the outlet of the communication pipeline is arranged at the upper part of the rear-sequence water pool (83), the side surface of the top of each adjacent water pool (83) is provided with a water pool overflow port (82), and the water pool water outlet pipeline (90) and the cooling tower water outlet pipeline (70) are respectively connected with the water pools (83) at the leftmost end and the rightmost end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020099302.XU CN211946960U (en) | 2020-01-16 | 2020-01-16 | Making wine distillation cooling water cyclic utilization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020099302.XU CN211946960U (en) | 2020-01-16 | 2020-01-16 | Making wine distillation cooling water cyclic utilization system |
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| Publication Number | Publication Date |
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| CN211946960U true CN211946960U (en) | 2020-11-17 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202020099302.XU Active CN211946960U (en) | 2020-01-16 | 2020-01-16 | Making wine distillation cooling water cyclic utilization system |
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| CN (1) | CN211946960U (en) |
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2020
- 2020-01-16 CN CN202020099302.XU patent/CN211946960U/en active Active
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210702 Address after: 644007 No. 150 Minjiang West Road, Yibin, Sichuan Patentee after: WULIANGYE GROUP Co.,Ltd. Address before: 350000 Building 1, 6 Xincheng Avenue, Xiaojiao Industrial Park, Meilie District, Sanming City, Fujian Province Patentee before: BAITE (FUJIAN) INTELLIGENT EQUIPMENT TECHNOLOGY Co.,Ltd. |
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| TR01 | Transfer of patent right |