Dry type heat recovery wine cooling system and method

A heat recovery and cooling system technology, applied in the field of winemaking, can solve the problems of low efficiency, large limitations and high energy consumption, and achieve the effects of simple structure, novel method and high efficiency

Pending Publication Date: 2021-06-29
广东一钛科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In the brewing industry, especially in the liquor distillation system, it is necessary to use cooling devices to take away the heat generated during the distillation and liquefaction of liquor. High performance, low efficiency, and low accuracy of wine temperature control, which is not conducive to improving market competitiveness
In particular, the traditional cooling device uses a cooling tower as a cold source, which is bulky and constantly needs water supply and drainage, which has great limitations on the design of the entire cooling device, and requires the use of a large amount of water, and the design of water supply and drainage, The system is complex and expensive

Method used

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  • Dry type heat recovery wine cooling system and method
  • Dry type heat recovery wine cooling system and method

Examples

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Effect test

Embodiment 1

[0023] See figure 1 As shown, it is a dry heat recovery wine cooling system, which includes: a heat exchange device 100, which includes a shell 1 and a primary heat exchange core 2, a secondary heat exchange core 2, and a secondary heat exchanger installed in the shell 1 from top to bottom. Heat core 3, a first shell-side flow channel 11 and a second shell-side flow channel 12 that communicate with each other are respectively formed between the inner wall of the shell 1 and the primary heat exchange core 2 and the secondary heat exchange core 3, and the upper end of the shell 1 is provided with a A wine steam inlet 14 communicated with the first shell-side flow channel 11; a sauce-flavored wine outlet 15 communicated with the second shell-side flow channel 12 is provided at the lower end of the shell 1; The first plate-side flow channel 20 and the second plate-side flow channel 30 isolated from the first shell-side flow channel 11 and the second shell-side flow channel 12 are ...

Embodiment 2

[0028] See figure 2 As shown, the present invention is a dry heat recovery wine cooling system, which includes: a heat exchange device 100, which includes a shell 1 and a first-stage heat exchange core 2, a second-stage heat exchange core installed in the shell 1 sequentially from top to bottom. First-stage heat exchange core 3 and third-stage heat exchange core 4, the inner wall of the shell 1 and the first-stage heat exchange core 2, the second-stage heat exchange core 3 and the third-stage heat exchange core 4 are respectively formed with interconnected first shell-side flow channels 11. The second shell-side flow channel 12 and the third shell-side flow channel 13, and the upper end of the shell 1 is provided with a wine steam inlet 14 communicating with the first shell-side flow channel 11; Outlet 15; the primary heat exchange core 2, the secondary heat exchange core 3 and the tertiary heat exchange core 4 respectively have a first shell-side flow channel 11, a second sh...

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Abstract

The invention discloses a dry type heat recovery wine cooling system and method. The wine cooling system comprises a heat exchange device, a heat recovery module and a circulating water cooling module, wherein the heat exchange device comprises a shell, a first-stage heat exchange core and a second-stage heat exchange core, a first shell pass flow channel and a second shell pass flow channel which communicate with each other are formed between the inner wall of the shell and the first-stage heat exchange core and between the inner wall of the shell and the second-stage heat exchange core respectively, and a wine steam inlet is formed in the upper end of the shell; a Maotai-flavor liquor outlet is formed in the lower end of the shell; a first plate pass flow channel and a second plate pass flow channel which are isolated from the first shell pass flow channel and the second shell pass flow channel are formed in the first-stage heat exchange core and the second-stage heat exchange core respectively, and a first inlet and a first outlet which communicate with the first plate pass flow channel and a second inlet and a second outlet which communicate with the second plate pass flow channel are formed in the side face of the shell; the heat recovery module is connected with the first inlet and the first outlet through a cold water pipe and a hot water pipe respectively; the circulating water cooling module comprises a surface air cooler or a dry air cooler, a first water pump, a first water supply pipe, a first control valve, a first water return pipe and a second control valve, and the first water supply pipe is connected with the second inlet; and the first water return pipe is connected with the second outlet, and the first water supply pipe is connected with a water compensation tank.

Description

Technical field: [0001] The invention relates to the technical field of wine making, in particular to a dry heat recovery wine cooling system and method. Background technique: [0002] Brewing is the process of using microbial fermentation to produce alcoholic beverages with a certain concentration. Brewing raw materials and brewing containers are two prerequisites for grain wine making. Liquor is a distilled wine made from grains and grains, using Daqu, Xiaoqu or bran koji, and distiller's yeast as saccharification starters, after cooking, saccharifying, fermenting, and distilling. [0003] In the brewing industry, especially in the liquor distillation system, it is necessary to use cooling devices to take away the heat generated during the distillation and liquefaction of liquor. The energy is high, the efficiency is not high, and the temperature control precision of the wine liquid is low, which is not conducive to improving the market competitiveness. In particular, t...

Claims

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Application Information

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IPC IPC(8): C12H6/02
CPCC12H6/02
Inventor 黄晓东黄华东李雄伟谭海龙
Owner 广东一钛科技有限公司
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