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System and method for simultaneously producing alcohol-free wine and strong wine

A technology for alcoholic wine and high-quality wine, which is applied in the preparation of wine, chemical instruments and methods, biochemical equipment and methods, etc., can solve the problems of complex process and degraded wine quality, and achieves simple operation, high dealcoholization efficiency, The effect of low energy consumption

Pending Publication Date: 2019-04-09
JIANGSU JIUMO HIGH TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The former method mainly includes fermenting with specific yeast, changing the saccharification process and changing the fermentation process, etc. It does not require additional investment in equipment, but the process is complicated, and while limiting the production of ethanol, it also largely limits the production of alcohol in wine. The formation of other flavor substances, resulting in the decline of wine quality

Method used

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  • System and method for simultaneously producing alcohol-free wine and strong wine

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0075] Using the above system, the material of the base membrane that preferentially permeates organic matter pervaporation membranes is sulfonated polyetherketone (SPEK), the pore diameter of the base membrane is 80nm, the material of the separation layer is polydimethylsiloxane with terminal amino groups, and the The ammonia value of the amino polydimethylsiloxane is 0.2, and the mass ratio of the hydrophobic nano-titanium dioxide to the amino-terminated polydimethylsiloxane is 0.5:100. Inject 50kg of wine raw materials (alcohol content 12.5v / v%) into the raw material tank, heat it to 45°C and send it to the primary membrane separation system through the raw material pump. The raw material side is circulated, the permeate side is vacuumed, and the vacuum pressure is 5000Pa. The vapor on the permeate side is liquefied and collected in the first cooling device, the condensation temperature is maintained at -10°C, the alcohol content of the permeate is 36°, and the permeate flu...

Embodiment 2

[0077] Using the above system, the material of the base membrane that preferentially permeates the organic pervaporation membrane is sulfonated polyether ketone ether ketone ketone (SPEKEKK), the pore size of the base membrane is 20nm, and the material of the separation layer is amino-terminated polydimethyl Siloxane, the ammonia value of the amino-terminated polydimethylsiloxane is 0.4, and the mass ratio of the hydrophobic nano-titanium dioxide to the amino-terminated polydimethylsiloxane is 1:100. Inject 50kg of wine raw materials (alcohol content 12.5v / v%) into the raw material tank, heat it to 35°C and send it to the primary membrane separation system through the raw material pump. The raw material side is circulated, the permeate side is vacuumed, and the vacuum pressure is 10000Pa. The vapor on the permeate side is liquefied and collected in the first cooling device, the condensation temperature is maintained at -10°C, the alcohol content of the permeate is 30°, and the...

Embodiment 3

[0079] Using the above system, the material of the base membrane that preferentially permeates the organic matter pervaporation membrane is sulfonated polyether ketone ether ketone ketone (SPEKEKK), the pore diameter of the base membrane is 8nm, and the material of the separation layer is amino-terminated polydimethyl The siloxane, the ammonia value of the amino-terminated polydimethylsiloxane is 0.6, and the mass ratio of the hydrophobic nano-titanium dioxide to the amino-terminated polydimethylsiloxane is 1.5:100. Inject 50kg of wine raw materials (alcohol content 12.5v / v%) into the raw material tank, heat it to 35°C and send it to the primary membrane separation system through the raw material pump. The raw material side is circulated, the permeate side is vacuumed, and the vacuum pressure is 10000Pa. The vapor on the permeate side is liquefied and collected in the first cooling device, the condensation temperature is maintained at -5°C, the alcohol content of the permeate ...

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Abstract

The invention discloses a system and method for simultaneously producing alcohol-free wine and strong wine. The system comprises a primary membrane separation system and a secondary membrane separation system, wherein an inlet of the primary membrane separation system is connected with a raw material; the permeation side of the primary membrane separation system is connected with an inlet of the secondary membrane separation system; each of the primary membrane separation system and the secondary membrane separation system comprises a preferentially-permeable organic matter permeation vaporization membrane. The system and method can reduce the alcohol content without affecting the efficacy of the wine, and obtain the healthier alcohol-free wine with a wider application range; meanwhile, the strong wine can be also obtained to manufacture brandy to make resources configured optimally.

Description

technical field [0001] The invention belongs to the technical field of pervaporation membrane separation, and in particular relates to a system and method for simultaneously producing alcohol-free wine and high-alcohol wine. Background technique [0002] Wine is a kind of fruit wine made from grapes. Its alcohol content is higher than beer but lower than liquor. It is rich in nutrition and has obvious health care effects. Some people think that wine is one of the healthiest and most hygienic beverages. It can adjust the performance of metabolism, promote blood circulation and prevent the increase of cholesterol. It also has the effects of diuresis, stimulating liver function and preventing aging. It is also an auxiliary agent for the treatment of heart disease, and can prevent diseases such as scurvy, anemia, beriberi, indigestion and keratitis. Regular drinking of grape wine reduces the risk of heart disease, blood lipids and arteriosclerosis. [0003] In recent years...

Claims

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Application Information

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IPC IPC(8): C12G1/14C12H3/04C12H6/00
CPCC12G1/00C12H1/063B01D61/3621C12H3/04C12G1/14C12H6/00B01D2317/025B01D2311/04B01D2311/2688B01D2317/04B01D69/12B01D71/52B01D71/82B01D71/70B01D69/148B01D71/701
Inventor 丁晓斌赵祥强孙雪飞戴萍萍涂睿
Owner JIANGSU JIUMO HIGH TECH CO LTD
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