CN203754695U - Grape wine aging device - Google Patents

Grape wine aging device Download PDF

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Publication number
CN203754695U
CN203754695U CN201420136815.8U CN201420136815U CN203754695U CN 203754695 U CN203754695 U CN 203754695U CN 201420136815 U CN201420136815 U CN 201420136815U CN 203754695 U CN203754695 U CN 203754695U
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CN
China
Prior art keywords
storage tank
tank
refrigeration
connects
grape wine
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Withdrawn - After Issue
Application number
CN201420136815.8U
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Chinese (zh)
Inventor
金丽秋
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WENCHENG COUNTY DAOFENG TECHNOLOGY Co Ltd
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WENCHENG COUNTY DAOFENG TECHNOLOGY Co Ltd
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Priority to CN201420136815.8U priority Critical patent/CN203754695U/en
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Publication of CN203754695U publication Critical patent/CN203754695U/en
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Abstract

The utility model provides a grape wine aging device, belonging to the technical field of brewing equipment and solving the technical problems that grape wine in the prior art has long aging time, is high in cost, is not suitable for batch production and the like. The grape wine aging device comprises a first storage tank and an oxygen storage tank, wherein the first storage tank is connected with a first delivery pump; the first delivery pump is connected with a mixer; a first flow meter and a first valve are also arranged on a pipeline between the first delivery pump and the mixer; the oxygen storage tank is connected with the mixer; a second flow meter and a second valve are arranged on a pipeline between the oxygen storage tank and the mixer; the mixer is connected with a second delivery pump; the second delivery pump is connected with a feeding hole of an aging tank via a heat exchanger; a discharge hole of the aging tank is connected with a second storage tank via the first valve. The grape wine aging device can achieve aging of the grape wine in a short time and is suitable for the requirements of large-scale production, thus effectively reducing the production cost.

Description

A kind of refrigeration of must device
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, on the pipeline between the first transferpump and mixing tank, be also provided with first flow meter and the first valve, oxygen storage tank connects mixing tank, on the pipeline between oxygen storage tank and mixing tank, be provided with the second under meter and the second valve, described mixing tank connects the second transferpump, described the second transferpump connects the opening for feed of digestion tank by interchanger, the discharge port of described digestion tank connects the second storage tank by the first valve.
In above-mentioned a kind of refrigeration of must device, in described digestion tank, be provided with several separating pools separate and sealing, every two adjacent separating pools are communicated with by upflow tube.
In above-mentioned a kind of refrigeration of must device, described upflow tube one end is communicated with the top of a separating pool, and the other end passes another adjacent separating pool and extend into the bottom of this separating pool.
In above-mentioned a kind of refrigeration of must device, on the pipeline between oxygen storage tank and mixing tank, be also provided with a check valve.
In above-mentioned a kind of 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 a kind of refrigeration of must device, described mixing tank is tube mixer.
In above-mentioned a kind of refrigeration of must device, described first flow is counted mass flowmeter, and described the second flow is counted spinner-type flowmeter.
In above-mentioned a kind of refrigeration of must device, described interchanger is shell and tube heat exchanger or plate-type heat exchanger.
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, first flow meter 51, the second under meter 52, the first valve 61, the second valve 62, interchanger 7, digestion tank 8, separating pool 81, upflow tube 82, check valve 9, air boost pump 10.
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, on the pipeline between the first transferpump 31 and mixing tank 4, be also provided with first flow meter 51 and the first valve 61, oxygen storage tank 2 connects mixing tank 4, on the pipeline between oxygen storage tank 2 and mixing tank 4, be provided with the second under meter 52 and the second valve 62, described mixing tank 4 connects the second transferpump 32, described the second transferpump 32 connects the opening for feed of digestion tank 8 by interchanger 7, the discharge port of described digestion tank 8 connects the second storage tank 12 by the first valve 61.Mixing tank 4 can mix grape wine and oxygen fully, interchanger 7 can heat the mixture of grape wine and oxygen, digestion tank 8 has extended the time that grape wine contacts with oxygen, thereby control the time that aldehyde material is oxidized to carboxylic acid, further control the reaction times of carboxylic acid and ethanol, thereby improve level of response.By regulating the first valve 61 and the second valve 62, can control the flow of grape wine and oxygen, and from first flow meter 51 and the second under meter 52 reading.
In digestion tank 8, be provided with several separating pools 81 separate and sealing, every two adjacent separating pools 81 are communicated with by upflow tube 82.Upflow tube 82 one end are communicated with the top of a separating pool 81, and the other end passes another adjacent separating pool 81 and extend into the bottom of this separating pool 81.Several separating pools 81 flow to the mixture of grape wine and oxygen another adjacent separating pool 81 by upflow tube 82 from a separating pool 81, that is to say and played the time stopping in digestion tank 8, thereby extended the reaction times, promoted the carrying out of reaction.
On the pipeline between oxygen storage tank 2 and mixing tank 4, be also provided with a check valve 9, prevent that grape wine from refluxing as oxygen storage tank 2.On pipeline between oxygen storage tank 2 and mixing tank 4, be also provided with air boost pump 10, the inlet mouth of described air boost pump 10 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 raising oxygen flow, accelerates oxidizing reaction speed.Mixing tank 4 is tube mixer, and mixing efficiency is higher, is applicable to duct type reaction.
First flow meter 51 is mass flowmeter, and described the second under meter 52 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.Interchanger 7 is shell and tube heat exchanger or plate-type heat exchanger.
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 first valve 61, control flow vinous and pressure, grape wine flow is from first flow meter 51 readings, by regulating the second valve 62, control flow and the pressure of the oxygen flow process in oxygen storage tank 2, oxygen flow is read from the second under meter 52, when oxygen pressure is inadequate, can open air boost pump 10 superchargings, quality vinous is converted to the volumeter 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, pump into by being pumped in digestion tank 8 after interchanger 7 heating afterwards, interchanger 7 is heated to 80-160 ℃ by the mixture of grape wine and oxygen, be preferably 120-150 ℃, the volume of separating pool 81 can be adjusted as required, so that the residence time of grape wine in digestion tank 8 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, first flow meter 51, the second under meter 52, the first valve 61, the second valve 62, interchanger 7, digestion tank 8, separating pool 81, upflow tube 82, check valve 9, air boost pump 10 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 (8)

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), on the pipeline between the first transferpump (31) and mixing tank (4), be also provided with first flow meter (51) and the first valve (61), oxygen storage tank (2) connects mixing tank (4), on the pipeline between oxygen storage tank (2) and mixing tank (4), be provided with the second under meter (52) and the second valve (62), described mixing tank (4) connects the second transferpump (32), described the second transferpump (32) connects the opening for feed of digestion tank (8) by interchanger (7), the discharge port of described digestion tank (8) connects the second storage tank (12) by the first valve (61).
2. a kind of refrigeration of must device according to claim 1, is characterized in that, is provided with several separating pools (81) separate and sealing in described digestion tank (8), and every adjacent two separating pools (81) are communicated with by upflow tube (82).
3. a kind of refrigeration of must device according to claim 2, it is characterized in that, described upflow tube (82) one end is communicated with the top of a separating pool (81), and the other end passes adjacent another separating pool (81) and extend into the bottom of this separating pool (81).
4. according to a kind of refrigeration of must device described in claim 1 or 2 or 3, it is characterized in that, on the pipeline between oxygen storage tank (2) and mixing tank (4), be also provided with a check valve (9).
5. a kind of refrigeration of must device according to claim 4, it is characterized in that, on pipeline between described oxygen storage tank (2) and mixing tank (4), be also provided with air boost pump (10), the inlet mouth of described air boost pump (10) directly connects oxygen storage tank (2).
6. according to a kind of refrigeration of must device described in claim 1 or 2 or 3, it is characterized in that, described mixing tank (4) is tube mixer.
7. according to a kind of refrigeration of must device described in claim 1 or 2 or 3, it is characterized in that, described first flow meter (51) is mass flowmeter, and described the second under meter (52) is spinner-type flowmeter.
8. according to a kind of refrigeration of must device described in claim 1 or 2 or 3, it is characterized in that, described interchanger (7) is shell and tube heat exchanger or plate-type heat exchanger.
CN201420136815.8U 2014-03-25 2014-03-25 Grape wine aging device Withdrawn - After Issue CN203754695U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420136815.8U CN203754695U (en) 2014-03-25 2014-03-25 Grape wine aging device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420136815.8U CN203754695U (en) 2014-03-25 2014-03-25 Grape wine aging device

Publications (1)

Publication Number Publication Date
CN203754695U true CN203754695U (en) 2014-08-06

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CN201420136815.8U Withdrawn - After Issue CN203754695U (en) 2014-03-25 2014-03-25 Grape wine aging device

Country Status (1)

Country Link
CN (1) CN203754695U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111254037A (en) * 2020-03-31 2020-06-09 泸州职业技术学院 White spirit ageing equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111254037A (en) * 2020-03-31 2020-06-09 泸州职业技术学院 White spirit ageing equipment

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GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20140806

Effective date of abandoning: 20160420

C25 Abandonment of patent right or utility model to avoid double patenting