CN200955049Y - Device for brewing yellow-rice wine - Google Patents
Device for brewing yellow-rice wine Download PDFInfo
- Publication number
- CN200955049Y CN200955049Y CN 200620134409 CN200620134409U CN200955049Y CN 200955049 Y CN200955049 Y CN 200955049Y CN 200620134409 CN200620134409 CN 200620134409 CN 200620134409 U CN200620134409 U CN 200620134409U CN 200955049 Y CN200955049 Y CN 200955049Y
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- simple distillation
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- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
The utility models relates to a yellow rice wine brewing device and comprises a raw distillers grains, a screw transfer pump, a filter press, a crude distillation column, an intermediate storage, a transfer pump, a flowmeter, a distillation column and a product storage groove connected with a tube successively. The utility model provides a yellow rice wine brewing device that practices tower distillation continuously or in batch according to the special requirements of yellow rice wine distillation. Lower the temperature of the high vacuum by multiple towers distillation and separate harmful substance which is harmful to human beings such as methanol, formaldehyde, and moisture etc from the liquid according to the differences of the different molecular and boiling point, and thereby reduce alcohol content, do not decrease amino acid content, lipid and aromatic material, maintain the nutrient composition, taste and color of amino acid and etc., prolong the retention period of bottle yellow rice wine, reduce production link, shorten technology process, reduce cross secondary pollution of the atmosphere and people, meanwhile reduce the construction demand for shop building, and be free from the limitation of brewing wine.
Description
Technical field
The utility model relates to a kind of device of brewing yellow wine, is applicable to that also with corn, barley, fruit etc. be raw material, through the fermented distilled production equipment of brewing low-alcoholic wine into.
Background technology
Traditional operational path is continued to use in brewageing of yellow rice wine always, greatly to last scale enterprise, little of the family workshop, the mode of brew is: raw materials pretreatment (broken, get juice, soak rice, steamed rice, koji)-fermentation-squeezing-filtration-can-sterilization-operations such as packing, original wine after the fermentation is blent through squeeze and filter, decoction, and technological process is complicated, because of not carrying out in sterile workshop, secondary pollution can be caused to product in technology circulation zone, thus cause some people to drink yellow rice wine can dry mouth and tougue, reserve strength is very big.The bottled rice wine quality guaranteed period is very short, and the diabetic subject drinks less and is advisable etc.Form these ill symptomses and mainly be because the temperature Change when relating to fermentation in the production process of yellow rice wine, mix the share of distiller's yeast, primary fermentation time length or the like, uncertain factor is a lot, is difficult to how many methyl alcohol, formaldehyde, sugar part, alcoholic strength, total number of bacterial colony, intestinal bacteria, aminoacids contents are controlled in yellow rice wine brew process.
The utility model content
The utility model provides a kind of device of brewing yellow wine, utilizes less equipment, and the simplest technological process reduces cost, reduces pollution, improves the yellow rice wine quality.
In order to achieve the above object, the utility model provides a kind of device of processing brewing yellow wine, it is characterized in that comprising former vinasse, simple distillation tower and relay tank and the finished product storage tank of pipe connection, it is characterized in that going back pipe connection between described relay tank and finished product storage tank has rectifying tower;
Described rectifying tower is provided with plurality of sections, and every section all has a distribution part collector.
Also be disposed with first transferpump and first flow meter between described former vinasse and the simple distillation tower; Store altar in the former vinasse and dress up the liquid of sampling wine and send into the first flow meter through first transferpump and measure, the wine liquid after the metering is sent into the simple distillation tower;
Be provided with first agitator in the described simple distillation tower, simple distillation tower upper and lower is provided with filter screen, the simple distillation tower bottom is provided with plunger discharge bottom valve and vacuum pipeline switching valve, simple distillation top of tower exit is provided with first plate-type heat exchanger, and simple distillation tower bottom exit is provided with first electric heating heat exchanger;
Described simple distillation tower also is provided with several pressure-measuring devices and temperature measuring set, is separately positioned on the outlet position of different wine degree by boiling point substance and molecule difference principle;
Between described first plate-type heat exchanger and the relay tank also successively pipe connection first quickly cooling unit and first vacuum tank are arranged;
Described first quickly cooling unit adopts semi-closed compressor, the secondary refrigeration;
Wine liquid in the simple distillation tower carries out low-temperature distillation, behind the certain hour, water and alcohol in the simple distillation tower, methyl alcohol, formaldehyde from cat head through first plate-type heat exchanger, flow into first vacuum tank through the first quickly cooling unit condensation again, described first agitator stirs wine liquid in still-process, wine liquid is up stirred, behind setting-up time, described plunger discharge bottom valve is opened, and the first agitator backwards rotation cleans up the simple distillation inner wall of tower, waste material is discharged in the lump, described vacuum pipeline switch valve vacuumizes from the simple distillation tower bottom, makes on the filter screen to be sucked out with the interior residue of tower, guarantees that the cat head filter screen does not stop up;
Pipe connection has the second adjustable flow meter between described first vacuum tank and the topping still, and the first vacuum in-tank mixing wine liquid is metered into topping still by the second adjustable flow meter after low pressure is separated, or pipeline is input in the relay tank;
Between first vacuum tank and intermediate storage tank liquid control valve is set, regulates the flow of liquid;
Described first plate-type heat exchanger makes aminoacids content not because of evaporating by heat with the cooling fluid of fermenation raw liquid as interchanger;
Described relay tank top is provided with second agitator; Described relay tank stores the liquid of crossing through the simple distillation column distillation, and described second agitator stirs the liquid in the middle storage tank, makes to stir back content liquid unanimity up and down.
Between described relay tank and the rectifying tower also successively pipe connection second transferpump and the 3rd under meter are arranged; Described second transferpump is transported to the wine liquid after stirring in the relay tank in the rectifying tower after the metering of the 3rd under meter, and described the 3rd under meter has guaranteed that the flow weighing apparatus is fixed, adapts to the needs of continuous processing;
Described rectifying tower divides plurality of sections, segmentation is distributed with several distribution part collectors, materials such as different wine degree are separated in segmentation, and the bottom of described rectifying tower is provided with second electric heating heat exchanger that adopts automatic temperature regulation instrument, and the top is provided with second plate-type heat exchanger;
Described rectifying tower also is provided with some temperature measuring sets and pressure-measuring device, is separately positioned on the opening for feed of different positions by boiling point substance and molecule difference principle;
Between described second plate-type heat exchanger and the finished product storage tank also successively pipe connection second quickly cooling unit and second vacuum tank are arranged;
Described second quickly cooling unit is the gas-liquid quick cooler, adopts semiclosed fluoridize adjustable compression unit;
Described second interchanger carries out preheating to the material that enters rectifying tower; Heat in the rectifying tower after the distillation,, isolate methyl alcohol, formaldehyde, flow into second vacuum tank again through top gas-liquid pipeline to the second quickly cooling unit condensation;
Pipe connection has the 4th adjustable flow meter between described second vacuum tank and the rectifying tower; Pipe connection has the 5th under meter between described second vacuum tank and the finished product storage tank; The described second vacuum in-tank mixing wine liquid is metered into rectifying tower by the 4th adjustable flow meter after low pressure is separated, or pipeline is input in the finished product storage tank as finished wine liquid after the metering of the 5th under meter;
Be provided with liquid control valve between second vacuum tank and finished product storage tank, regulate the flow of liquid.
The device of a kind of brewing yellow wine that the utility model provides, continuously or batch carry out the low temperature molecular distillation, can isolate objectionable impuritiess such as harmful methyl alcohol, formaldehyde, acidity, reduce ethanol content, do not reduce aminoacids content, nutritions such as maintenance amino acid are constant, mouthfeel is constant, color and taste is constant.Can be by the market requirement, selectedly adjust material level and put.Prolong the quality guaranteed period of bottled rice wine, reduce production link, shortened process has reduced air, personage's intersection secondary pollution, can also reduce the construction requirement of workshop factory building simultaneously, and the restriction of not made wine season.
Description of drawings
Fig. 1 is the structural representation of the device of a kind of brewing yellow wine of providing of the utility model.
Embodiment
Followingly specify a kind of better embodiment of the present utility model according to Fig. 1:
As shown in Figure 1, the utility model provides a kind of device of processing brewing yellow wine, it is characterized in that comprising former vinasse 1, simple distillation tower 401 and relay tank 8 and the finished product storage tank 10 of pipe connection, it is characterized in that going back pipe connection between described relay tank 8 and finished product storage tank 10 has rectifying tower 402;
Described rectifying tower 402 is provided with plurality of sections, and every section all has a distribution part collector;
Also be disposed with first transferpump 201 and first flow meter 301 between described former vinasse 1 and the simple distillation tower 401; Store altar in the former vinasse 1 and dress up the liquid of sampling wine and send into first flow meter 301 through first transferpump 201 and measure, the wine liquid after the metering is sent into simple distillation tower 401;
Described simple distillation tower 401 also is provided with plurality of sections, and every section all has a distribution part collector;
Be provided with first agitator in the described simple distillation tower 401, simple distillation tower 401 upper and lowers are provided with filter screen 4011, simple distillation tower 401 bottoms are provided with plunger discharge bottom valve 4012 and vacuum pipeline switching valve 4013, simple distillation tower 401 top exit places are provided with first plate-type heat exchanger 501, simple distillation tower 401 outlet at bottom places are provided with first electric heating heat exchanger 901, and described simple distillation tower 401 is provided with the opening for feed of some different positionss and the discharge port of some different positionss;
Described simple distillation tower 401 also is provided with several pressure-measuring devices and temperature measuring set, is separately positioned on the discharge port position of different wine degree by boiling point substance and molecule difference principle;
Between described first plate-type heat exchanger 501 and the relay tank 8 also successively pipe connection first quickly cooling unit 601 and first vacuum tank 701 are arranged;
Described first quickly cooling unit 601 adopts semi-closed compressor, the secondary refrigeration;
Wine liquid in the simple distillation tower 401 carries out low-temperature distillation, behind the certain hour, water and alcohol in the simple distillation tower 401, methyl alcohol, formaldehyde from cat head through first plate-type heat exchanger 501,601 condensations flow into first vacuum tank 701 through first quickly cooling unit again, described first agitator stirs wine liquid in still-process, wine liquid is up stirred, behind setting-up time, described plunger discharge bottom valve 4012 is opened, the first agitator backwards rotation, the simple distillation inner wall of tower is cleaned up, waste material is discharged in the lump, described vacuum pipeline switch valve 4013 vacuumizes from the simple distillation tower bottom, makes on the filter screen 4011 to be sucked out with the interior residue of tower, guarantees that cat head filter screen 4011 does not stop up;
Pipe connection has the second adjustable flow meter, 302, the first vacuum tanks, the 701 interior wine liquid that mix to be metered into topping still 401 by the second adjustable flow meter 302 after low pressure is separated between described first vacuum tank 701 and the topping still 401, or pipeline is input in the relay tank 8;
8 of first vacuum tank 701 and intermediate storage tank are provided with liquid control valve, regulate the flow of liquid;
Described first plate-type heat exchanger, 501 usefulness fermenation raw liquids make aminoacids content not because of evaporating by heat as the cooling fluid of interchanger;
Described relay tank 8 tops are provided with second agitator; Described relay tank 8 stores through simple distillation tower 401 distilled liquid, and described second agitator stirs the liquid in the middle storage tank 8, makes to stir back content liquid unanimity up and down.
Between described relay tank 8 and the rectifying tower 402 also successively pipe connection second transferpump 202 and the 3rd under meter 303 are arranged; Described second transferpump 202 is transported to the wine liquid after stirring in the relay tank 8 in the rectifying tower 402 after 303 meterings of the 3rd under meter, and described the 3rd under meter 303 has guaranteed that the flow weighing apparatus is fixed, adapts to the needs of continuous processing;
402 fens plurality of sections of described rectifying tower, segmentation is distributed with several distribution part collectors, materials such as different wine degree are separated in segmentation, the bottom of described rectifying tower 402 is provided with second electric heating heat exchanger 902 that adopts automatic temperature regulation instrument, the top is provided with second plate-type heat exchanger 502, and described rectifying tower 402 is provided with the opening for feed of some different positionss and the discharge port of some different positionss;
Described rectifying tower 402 also is provided with some temperature measuring sets and pressure-measuring device, is separately positioned on the opening for feed of different positions by boiling point substance and molecule difference principle;
Between described second plate-type heat exchanger 502 and the finished product storage tank 10 also successively pipe connection second quickly cooling unit 602 and second vacuum tank 702 are arranged;
Described second quickly cooling unit 602 is the gas-liquid quick cooler, adopts semiclosed fluoridize adjustable compression unit;
502 pairs of materials that enter rectifying tower 402 of described second interchanger carry out preheating; Heat in the rectifying tower 402 after the distillation,, isolate methyl alcohol, formaldehyde, flow into second vacuum tank 702 again through top gas-liquid pipeline to the second quickly cooling unit 602 condensations;
Pipe connection has the 4th adjustable flow meter 304 between described second vacuum tank 702 and the rectifying tower 402; Pipe connection has the 5th under meter 305 between described second vacuum tank 702 and the finished product storage tank 10; Mix wine liquid in described second vacuum tank 702 and after low pressure is separated, be metered into rectifying tower 402, or pipeline is input in the finished product storage tank 10 as finished wine liquid after 305 meterings of the 5th under meter by the 4th adjustable flow meter 304;
10 of second vacuum tank 702 and finished product storage tanks are provided with liquid control valve, regulate the flow of liquid.
The device of a kind of brewing yellow wine that the utility model provides, can be continuously or carry out column distillation in batches, can isolate harmful methyl alcohol, formaldehyde, Icing Sugar, acidity, objectionable impuritiess such as moisture content, reduce ethanol content, do not reduce aminoacids content, nutritions such as maintenance amino acid are constant, mouthfeel is constant, color and taste is constant, the quality guaranteed period of prolongation bottled rice wine, reduce production link, shortened process has reduced air, personage's intersection secondary pollution, simultaneously can also reduce the construction requirement of workshop factory building, and do not processed the seasonal restriction of yellow rice wine.
Claims (10)
1. the device of a brewing yellow wine, former vinasse (1), simple distillation tower (401) and the relay tank (8) and the finished product storage tank (10) that comprise pipe connection, it is characterized in that going back pipe connection between described relay tank (8) and finished product storage tank (10) has rectifying tower (402);
Described rectifying tower (8) is provided with plurality of sections, and every section all has a distribution part collector.
2. the device of brewing yellow wine as claimed in claim 1 is characterized in that, also is disposed with first transferpump (201) and first flow meter (301) between described former vinasse (1) and the simple distillation tower (401).
3. the device of brewing yellow wine as claimed in claim 1 is characterized in that,
Described simple distillation tower (401) also is provided with plurality of sections, and every section all has a distribution part collector;
Be provided with first agitator in the described simple distillation tower (401),
Simple distillation tower (401) upper and lower is provided with filter screen (4011),
Simple distillation tower (401) bottom is provided with plunger discharge bottom valve (4012) and vacuum pipeline switching valve (4013),
Simple distillation tower (401) top exit place is provided with first plate-type heat exchanger (501),
The outlet at bottom place is provided with first electric heating heat exchanger (901),
Described simple distillation tower (401) is provided with the opening for feed of some different positionss and the discharge port of some different positionss
Described simple distillation tower (401) also is provided with several pressure-measuring devices and temperature measuring set in the outlet position of different wine degree.
4. the device of brewing yellow wine as claimed in claim 3 is characterized in that, between described first plate-type heat exchanger (501) and the relay tank (8) also successively pipe connection first quickly cooling unit (601) and first vacuum tank (701) are arranged.
5. the device of brewing yellow wine as claimed in claim 4, it is characterized in that, pipe connection has the second adjustable flow meter (302) between described first vacuum tank (701) and the topping still (401), mix wine liquid in described first vacuum tank (701) and after low pressure is separated, be metered into topping still (401) by the second adjustable flow meter (302), or pipeline is input in the relay tank (8), is provided with liquid control valve between described first vacuum tank (701) and the relay tank (8).
6. the device of brewing yellow wine as claimed in claim 1 is characterized in that, described relay tank (8) top is provided with second agitator.
7. the device of brewing yellow wine as claimed in claim 1 is characterized in that, between described relay tank (8) and the rectifying tower (402) also successively pipe connection second transferpump (202) and the 3rd under meter (303) are arranged.
8. the device of brewing yellow wine as claimed in claim 1 is characterized in that,
The bottom of described rectifying tower (402) is provided with second electric heating heat exchanger (902),
The top is provided with second plate-type heat exchanger (502),
Described rectifying tower (402) is provided with the opening for feed of some different positionss and the discharge port of some different positionss
Described rectifying tower (402) also is provided with some temperature measuring sets and pressure-measuring device at the opening for feed of different positions.
9. the device of brewing yellow wine as claimed in claim 8 is characterized in that, between described second plate-type heat exchanger (502) and the finished product storage tank (10) also successively pipe connection second quickly cooling unit (602) and second vacuum tank (702) are arranged.
10. the device of brewing yellow wine as claimed in claim 9 is characterized in that, pipe connection has the 4th adjustable flow meter (304) between described second vacuum tank (702) and the rectifying tower (402); Pipe connection has the 5th under meter (305) between described second vacuum tank (702) and the finished product storage tank (10); Be provided with liquid control valve between described second vacuum tank (702) and finished product storage tank (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620134409 CN200955049Y (en) | 2006-06-01 | 2006-08-10 | Device for brewing yellow-rice wine |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200620042342 | 2006-06-01 | ||
| CN200620042342.0 | 2006-06-01 | ||
| CN 200620134409 CN200955049Y (en) | 2006-06-01 | 2006-08-10 | Device for brewing yellow-rice wine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200955049Y true CN200955049Y (en) | 2007-10-03 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620134409 Expired - Fee Related CN200955049Y (en) | 2006-06-01 | 2006-08-10 | Device for brewing yellow-rice wine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200955049Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103865741A (en) * | 2014-03-06 | 2014-06-18 | 江南大学 | Method for preparing high-degree liquid state white spirit by using yellow rice wine |
| CN104293636A (en) * | 2014-11-06 | 2015-01-21 | 乌毡帽酒业有限公司 | Novel device for manufacturing yellow rice wine |
| CN104312838A (en) * | 2014-11-06 | 2015-01-28 | 乌毡帽酒业有限公司 | Rice wine making equipment |
| CN110280036A (en) * | 2019-08-07 | 2019-09-27 | 安徽口子酒业股份有限公司 | The automatic continuous extraction element of liquor seasoning material is obtained from brewing spirit by-product yellow water |
| CN114606090A (en) * | 2021-04-21 | 2022-06-10 | 滦南建国科技有限公司 | Device for forcibly removing formaldehyde and methanol for liquor making by distillation |
-
2006
- 2006-08-10 CN CN 200620134409 patent/CN200955049Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103865741A (en) * | 2014-03-06 | 2014-06-18 | 江南大学 | Method for preparing high-degree liquid state white spirit by using yellow rice wine |
| CN103865741B (en) * | 2014-03-06 | 2015-05-13 | 江南大学 | Method for preparing high-degree liquid state white spirit by using yellow rice wine |
| CN104293636A (en) * | 2014-11-06 | 2015-01-21 | 乌毡帽酒业有限公司 | Novel device for manufacturing yellow rice wine |
| CN104312838A (en) * | 2014-11-06 | 2015-01-28 | 乌毡帽酒业有限公司 | Rice wine making equipment |
| CN104312838B (en) * | 2014-11-06 | 2016-03-23 | 乌毡帽酒业有限公司 | Yellow rice wine making equipment |
| CN104293636B (en) * | 2014-11-06 | 2016-05-25 | 乌毡帽酒业有限公司 | A kind of device of novel making yellow rice wine |
| CN110280036A (en) * | 2019-08-07 | 2019-09-27 | 安徽口子酒业股份有限公司 | The automatic continuous extraction element of liquor seasoning material is obtained from brewing spirit by-product yellow water |
| CN114606090A (en) * | 2021-04-21 | 2022-06-10 | 滦南建国科技有限公司 | Device for forcibly removing formaldehyde and methanol for liquor making by distillation |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071003 Termination date: 20150810 |
|
| EXPY | Termination of patent right or utility model |