CN203807453U - Wine aging device - Google Patents
Wine aging device Download PDFInfo
- Publication number
- CN203807453U CN203807453U CN201420136952.1U CN201420136952U CN203807453U CN 203807453 U CN203807453 U CN 203807453U CN 201420136952 U CN201420136952 U CN 201420136952U CN 203807453 U CN203807453 U CN 203807453U
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- storage tank
- tank
- connects
- transferpump
- valve
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Abstract
The utility model provides a wine aging device, belongs to the technical field of wine making equipment and solves the technical problems of long aging time, high cost, unsuitability for batch production and the like of wine in the prior art. The wine aging device comprises a first storage tank and an oxygen storage tank, wherein the first storage tank is connected with a first conveying pump; the first conveying pump is connected with a mixer; the oxygen storage tank is connected with the mixer; the mixer is connected with a second conveying pump; the second conveying pump is connected with the feed inlet of an aging tank; the discharge opening of the aging tank is connected with a second storage tank through a first valve. The wine aging device can realize the aging of wine in short time and meets the requirement for large-scale production, so that the production cost is effectively reduced.
Description
Technical field
The utility model belongs to Brewing equipment technical field, relates to a kind of Production of Wine device, especially relates to a kind of refrigeration of must device.
Background technology
At present, grape wine has sizable market in China, has higher nutritive value, has multiple health care, more and more welcomed by the people.But, in grape wine after the grape wine of new brew and allotment, aldehyde material is more, these aldehyde materials be not yet oxidized to carboxylic acid and with ethanol generation condensation reaction, therefore cause ethanol and fragrance vinous to depart from, people can feel pungent alcohol smell and the mouthfeel of stimulation when tasting this class wine, thereby lose the due glamour of grape wine.
For above-mentioned technical problem, people, conventionally by new wine is contained in oak barrel and is stored the several years, make grape wine that oxidation and condensation reaction occur, and the ethanol in the grape wine after ageing and essence can be good at merging, so aroma is strong, and mouthfeel is mellow.But the method needs the time of ageing longer, generally at least more than 1 year, and the time of ageing is longer, and expense is also higher, and floor space is also more.Therefore aforesaid method is not suitable for the Production requirement of extensive mass, has certain limitation.
Summary of the invention
The purpose of this utility model is for the deficiencies in the prior art, and a kind of refrigeration of must device is provided, and has solved that the prior art refrigeration of must time is long, cost is high, be not suitable for the technical problems such as batch production.
For achieving the above object, the utility model has adopted following technical proposal: a kind of refrigeration of must device, comprise the first storage tank and oxygen storage tank, described the first storage tank connects the first transferpump, the first transferpump connects mixing tank, and oxygen storage tank connects mixing tank, and described mixing tank connects the second transferpump, described the second transferpump connects the opening for feed of digestion tank, and the discharge port of described digestion tank connects the second storage tank by the first valve.
In above-mentioned refrigeration of must device, on the pipeline between the first transferpump and mixing tank, be also provided with first flow meter and the second valve, on the pipeline between oxygen storage tank and mixing tank, be provided with the second under meter and the 3rd valve.
In above-mentioned refrigeration of must device, on the pipeline between described oxygen storage tank and mixing tank, be also provided with air boost pump, the inlet mouth of described air boost pump directly connects oxygen storage tank.
In above-mentioned refrigeration of must device, described digestion tank is provided with steam-in and vapour outlet, is provided with drain valve on vapour outlet, is provided with coil pipe in digestion tank, the opening for feed of described coil pipe connects the discharge port of the second transferpump, and the discharge port of described coil pipe connects the first valve.
In above-mentioned refrigeration of must device, described the second transferpump is multistage turbine pump.
In above-mentioned refrigeration of must device, described mixing tank is tube mixer.
In above-mentioned refrigeration of must device, described first flow is counted mass flowmeter, and described the second flow is counted spinner-type flowmeter.
Compared with prior art, the utility model has the advantage of: by passing into oxygen, to make the aldehyde material accelerated oxidation in grape wine be carboxylic acid, and make carboxylic acid and ethanol synthesis, thereby accelerated refrigeration of must speed, after new wine is processed by this device, have strong aroma and mellow mouthfeel, fragrance vinous and alcohol merge, and no longer have pungent alcohol smell; By this device, process grape wine, can realize at short notice ageing vinous, be applicable to scale operation demand, thereby effectively reduce production cost; This apparatus structure is simple, is applicable to promoting.
Accompanying drawing explanation
Fig. 1 is the structural representation that the utility model provides.
In figure, the first storage tank 11, the second storage tank 12, oxygen storage tank 2, the first transferpump 31, the second transferpump 32, mixing tank 4, digestion tank 5, steam-in 51, vapour outlet 52, drain valve 53, coil pipe 54, the first valve 61, the second valve 62, the 3rd valve 63, first flow meter 71, the second under meter 72, air boost pump 8.
Embodiment
As shown in Figure 1, a kind of refrigeration of must device, comprise the first storage tank 11 and oxygen storage tank 2, described the first storage tank 11 connects the first transferpump 31, the first transferpump 31 connects mixing tank 4, and oxygen storage tank 2 connects mixing tank 4, and described mixing tank 4 connects the second transferpump 32, described the second transferpump 32 connects the opening for feed of digestion tank 5, and the discharge port of described digestion tank 5 connects the second storage tank 12 by the first valve 61.Mixing tank 4 can mix grape wine and oxygen fully, digestion tank 5 has extended the time that grape wine contacts with oxygen, thereby controls the time that aldehyde material is oxidized to carboxylic acid, further controls the reaction times of carboxylic acid and ethanol, digestion tank 5 can also heat, thus fast reaction speed.
As a kind of preferred scheme, on the pipeline between the first transferpump 31 and mixing tank 4, be also provided with first flow meter 71 and the second valve 62, on the pipeline between oxygen storage tank 2 and mixing tank 4, be provided with the second under meter 72 and the 3rd valve 63.By regulating the second valve 62 and the 3rd valve 63, can control the flow of grape wine and oxygen, and from first flow meter 71 and the second under meter 72 reading.
On pipeline between oxygen storage tank 2 and mixing tank 4, be also provided with air boost pump 8, the inlet mouth of described air boost pump 8 directly connects oxygen storage tank 2.When as inadequate in the oxygen pressure in oxygen storage tank 2, can pass through air boost pump 8 superchargings, thereby improve oxygen flow, accelerate oxidizing reaction speed.
Digestion tank 5 is provided with steam-in 51 and vapour outlet 52, is provided with drain valve 53 on vapour outlet 52, is provided with coil pipe 54 in digestion tank 5, and steam 51 enters from steam-in, and coil pipe 54 is carried out to heat exchange, discharges afterwards from the drain valve 53 of vapour outlet 52; The opening for feed of described coil pipe connects the discharge port of the second transferpump 32, and the discharge port of described coil pipe 54 connects the first valve 61.Steam can be passed into digestion tank 5 inside, the grape wine in coil pipe 54 and oxygen is heated to the carrying out of the carrying out of accelerating oxidation reaction and the condensation reaction of ethanol and carboxylic acid.The second transferpump 32 is multistage turbine pump.Multistage turbine pump can have higher lift, in conjunction with the pressure in the adjustable coil pipe 54 of the first valve 61, thereby reaction is carried out under high pressure conditions, further promotes the speed of reaction.
Mixing tank 4 is tube mixer.Mixing efficiency is higher, is applicable to duct type reaction.First flow meter 71 is mass flowmeter, and described the second under meter 72 is spinner-type flowmeter.Because color vinous is darker, therefore can easily reading with spinner-type flowmeter, with mass flowmeter, can accurately and intuitively carry out the reading of flow, oxygen does not have color, therefore use spinner-type flowmeter read-around ratio more convenient, thereby be convenient to control the ratio of grape wine and oxygen.
Working process of the present utility model is as follows: with the first transferpump 31, grape wine is pumped from the first storage tank 11, by regulating the second valve 62, control flow vinous and pressure, grape wine flow is from first flow meter 71 readings, by regulating the 3rd valve 63, control flow and the pressure of the oxygen flow process in oxygen storage tank 2, oxygen flow is read from the second under meter 72, when oxygen pressure is inadequate, can open air boost pump 8 superchargings, quality vinous is converted to the volume of 1L with 1kg, the conversion volume ratio of grape wine and oxygen is 1:0.01-0.5, preferably be controlled at 1:0.05-0.2, grape wine and oxygen mix in mixing tank 4, with the second transferpump 32, be pumped in digestion tank 5 afterwards, the Heating temperature of digestion tank 5 is 80-160 ℃, be preferably 120-150 ℃, the pressure that the first valve 61 is controlled in coil pipe 54, pressure is 0.1-1.0MPa, be preferably 0.3-0.5MPa, the length of coil pipe 54 can be adjusted as required, so that the residence time of grape wine in coil pipe 54 is 1-4hr, be preferably 2-3hr, afterwards, grape wine flow in the second storage tank 12 and preserves.
The advantage the utlity model has is: by passing into oxygen, to make the aldehyde material accelerated oxidation in grape wine be carboxylic acid, and make carboxylic acid and ethanol synthesis, thereby accelerated refrigeration of must speed, after new wine is processed by this device, there is strong aroma and mellow mouthfeel, fragrance vinous and alcohol merge, and no longer have pungent alcohol smell.
Specific embodiment described herein is only to the explanation for example of the utility model spirit.The utility model person of ordinary skill in the field can make various modifications or supplements or adopt similar mode to substitute described specific embodiment, but can't depart from spirit of the present utility model or surmount the defined scope of appended claims.
Although more used the terms such as the first storage tank 11, the second storage tank 12, oxygen storage tank 2, the first transferpump 31, the second transferpump 32, mixing tank 4, digestion tank 5, steam-in 51, vapour outlet 52, drain valve 53, coil pipe 54, the first valve 61, the second valve 62, the 3rd valve 63, first flow meter 71, the second under meter 72, air boost pump 8 herein, do not got rid of the possibility of using other term.Use these terms to be only used to describe more easily and explain essence of the present utility model, they are construed to any additional restriction is all contrary with the utility model spirit.
Claims (7)
1. a refrigeration of must device, comprise the first storage tank (11) and oxygen storage tank (2), it is characterized in that, described the first storage tank (11) connects the first transferpump (31), the first transferpump (31) connects mixing tank (4), oxygen storage tank (2) connects mixing tank (4), described mixing tank (4) connects the second transferpump (32), described the second transferpump (32) connects the opening for feed of digestion tank (5), and the discharge port of described digestion tank (5) connects the second storage tank (12) by the first valve (61).
2. refrigeration of must device according to claim 1, it is characterized in that, on the pipeline between the first transferpump (31) and mixing tank (4), be also provided with first flow meter (71) and the second valve (62), on the pipeline between oxygen storage tank (2) and mixing tank (4), be provided with the second under meter (72) and the 3rd valve (63).
3. refrigeration of must device according to claim 2, it is characterized in that, on pipeline between described oxygen storage tank (2) and mixing tank (4), be also provided with air boost pump (8), the inlet mouth of described air boost pump (8) directly connects oxygen storage tank (2).
4. according to the refrigeration of must device described in claim 1 or 2 or 3, it is characterized in that, described digestion tank (5) is provided with steam-in (51) and vapour outlet (52), on vapour outlet (52), be provided with drain valve (53), in digestion tank (5), be provided with coil pipe (54), the opening for feed of described coil pipe connects the discharge port of the second transferpump (32), and the discharge port of described coil pipe (54) connects the first valve (61).
5. refrigeration of must device according to claim 1, is characterized in that, described the second transferpump (32) is multistage turbine pump.
6. refrigeration of must device according to claim 1, is characterized in that, described mixing tank (4) is tube mixer.
7. refrigeration of must device according to claim 1, is characterized in that, described first flow meter (71) is mass flowmeter, and described the second under meter (72) is spinner-type flowmeter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420136952.1U CN203807453U (en) | 2014-03-25 | 2014-03-25 | Wine aging device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420136952.1U CN203807453U (en) | 2014-03-25 | 2014-03-25 | Wine aging device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203807453U true CN203807453U (en) | 2014-09-03 |
Family
ID=51446236
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420136952.1U Withdrawn - After Issue CN203807453U (en) | 2014-03-25 | 2014-03-25 | Wine aging device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203807453U (en) |
-
2014
- 2014-03-25 CN CN201420136952.1U patent/CN203807453U/en not_active Withdrawn - After Issue
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20140903 Effective date of abandoning: 20151223 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |