CN201250221Y - Sub beer deaeration tower - Google Patents
Sub beer deaeration tower Download PDFInfo
- Publication number
- CN201250221Y CN201250221Y CNU200820071066XU CN200820071066U CN201250221Y CN 201250221 Y CN201250221 Y CN 201250221Y CN U200820071066X U CNU200820071066X U CN U200820071066XU CN 200820071066 U CN200820071066 U CN 200820071066U CN 201250221 Y CN201250221 Y CN 201250221Y
- Authority
- CN
- China
- Prior art keywords
- tower body
- beer
- pipe
- liquid
- wine
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
- Devices For Dispensing Beverages (AREA)
Abstract
The utility model relates to a processor for beer, in particular to a sub beer deaeration tower, which comprises a tower body, wherein the top of the tower body is connected with a liquid inlet tube which lower end is connected with a washing ball, the top of the tower body is provided with a gas exhaust tube, the bottom of the tower body is provided with a gas inlet tube connected with a carbon dioxide disperse, and the bottom of the tower body is provided with a liquid outlet tube. When recycles and rebottles sub beer, the processor can reduce the content of dissolved oxygen in beer.
Description
Technical field
The utility model relates to the treatment unit of a kind of beer time wine, relates in particular to the device for deoxidizing of beer time wine.
Background technology
At present in the production of beer, wrapping process and since equipment successively, large-scale production inevitably can produce the inferior wine of situations such as a certain amount of filling wine deficiency, gland be not tight.The general now above-mentioned inferior wine of dual mode processing that adopts: one, directly the inferior wine of output is outwelled; Two, concentrate recovery time wine, again its can is handled.First method is directly discharged the pollution that a large amount of inferior wine will inevitably cause environment, and in order to reduce the pollution to environment, the producer certainly will drop into the ability that more funds enlarge sewage disposal, has increased the cost of beer production again greatly.Second method concentrate reclaiming time wine again in the process of can, tends to cause wine liquid directly contact with air, the wearing out of acceleration beer, and then the quality of reduction beer.
The utility model content
The purpose of this utility model provides a kind of beer time free and easy oxygen column, reduces dissolved oxygen content in the wine liquid again in the pouring process reclaiming time wine.
For solving the problems of the technologies described above, the utility model comprises: tower body, and the tower body top connects liquid-in pipe, the liquid-in pipe lower end connects ball syringe, and gas discharge pipe is established at the tower body top, and inlet pipe is established in the tower body bottom, inlet pipe connects the carbonic acid gas decollator, and drain pipe is established in the tower body bottom.
The carbonic acid gas decollator is the pipeline of a sealing, and is porose on the duct wall.
Drain pipe connects volume pump.
The utility model adopts in the tower body bottom carbonic acid gas decollator is set, utilize the principle that the equilibrium partial pressure of this gas is directly proportional on the saturation concentration of gas in liquid and liquid level under the certain temperature, constantly to the tower body carbon dioxide gas, the replacement of oxygen that will dissolve in the wine liquid comes out, thereby reduce the dissolved oxygen in the wine liquid, guarantee to concentrate and reclaim can quality of beer again.Dissolved oxygen in the wine liquid can be reduced in the 50ppb from 1000-5000ppb after adopting this device, as follows wine wine liquid add-on be controlled at into the pure mellow wine amount 1% in, the dissolved oxygen in the wine liquid can be reduced to 1ppb.
Description of drawings
Fig. 1 is the structural representation of the utility model beer time a kind of embodiment of free and easy oxygen column.
Embodiment
The utility model adopts stainless steel sheet welding rounding cylindricality tower body 1 as shown in Figure 1.Tower body welded top liquid-in pipe 7, the liquid-in pipe lower end connects ball syringe 2, and ball syringe is spherical in shape, and the through hole that is evenly distributed above, through-hole diameter are 2mm.Gas discharge outlet is opened at the tower body top, gas discharge outlet place welding gas delivery pipe 3.The tower body bottom connects inlet pipe 8, and the end in inlet pipe connects carbonic acid gas decollator 5, and the carbonic acid gas decollator is the polyethylene pipe of a sealing, and is porose on the duct wall, carbonic acid gas is dispersed into small bubbles one by one by above-mentioned hole, fully contacts with wine liquid.The tower body bottom connects drain pipe 4, and connects volume pump 6 on the drain pipe.
During the utility model work, the inferior wine of the beer of centralized collection is passed through N
2/ CO
2Pressurization or pump are pressed in the tower body 1 from ball syringe 2 through liquid-in pipe, meanwhile open carbonic acid gas decollator 5, slowly spread CO in tower body uniformly
2Gas is to replace the oxygen in time wine wine liquid.And the carbonic acid gas of overflowing is discharged by the gas outlet pipe of tank deck.As the utility model running hours, out while advancing for keeping wine liquid, need be according to the flow quantity that goes out of volume pump reflection, the inferior wine wine liquid measure that control adds makes into and out of the liquid measure balance, thereby keeps handling the quality of back wine liquid.
Claims (3)
1. a beer time free and easy oxygen column, comprise tower body (1), the tower body top connects liquid-in pipe (7), the liquid-in pipe lower end connects ball syringe (2), gas discharge pipe (3) is established at the tower body top, it is characterized in that establishing inlet pipe (8) bottom the described tower body, inlet pipe connects carbonic acid gas decollator (5), and drain pipe (4) is established in the tower body bottom.
2. beer according to claim 1 time free and easy oxygen column is characterized in that described carbonic acid gas decollator is the pipeline of a sealing, and is porose on the duct wall.
3. beer according to claim 1 and 2 time free and easy oxygen column is characterized in that described drain pipe connects volume pump (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200820071066XU CN201250221Y (en) | 2008-06-18 | 2008-06-18 | Sub beer deaeration tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200820071066XU CN201250221Y (en) | 2008-06-18 | 2008-06-18 | Sub beer deaeration tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201250221Y true CN201250221Y (en) | 2009-06-03 |
Family
ID=40745893
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU200820071066XU Expired - Fee Related CN201250221Y (en) | 2008-06-18 | 2008-06-18 | Sub beer deaeration tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201250221Y (en) |
-
2008
- 2008-06-18 CN CNU200820071066XU patent/CN201250221Y/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090603 Termination date: 20110618 |