CN105586231A - Two-time-distillation and two-time-cooling brewing extraction device - Google Patents
Two-time-distillation and two-time-cooling brewing extraction device Download PDFInfo
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- CN105586231A CN105586231A CN201610170542.2A CN201610170542A CN105586231A CN 105586231 A CN105586231 A CN 105586231A CN 201610170542 A CN201610170542 A CN 201610170542A CN 105586231 A CN105586231 A CN 105586231A
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- tower
- distillation
- wine
- steam
- cooling
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- 238000004821 distillation Methods 0.000 title claims abstract description 55
- 238000001816 cooling Methods 0.000 title claims abstract description 42
- 238000000605 extraction Methods 0.000 title claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 238000009434 installation Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 abstract description 10
- 239000000463 material Substances 0.000 abstract description 4
- 238000010438 heat treatment Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
- C12H6/00—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages
- C12H6/02—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages by distillation
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Food Science & Technology (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention relates to a two-time-distillation and two-time-cooling brewing extraction device which is formed by connecting a boiler, a first-time distillation tower, a second-time distillation tower, a first-time cooling pipe and a second-time cooling tower. Liquor steam generated in the first-time distillation tower and auxiliary material liquor or liquid distillers' grains in the second-time distillation tower are mixed and extracted through steam heating and then cooled into liquor through the first-time cooling pipe and the second-time cooling tower, a spiral steam pipe in the first-time distillation tower can effectively prevent expansion during distillation of the distillers' grains, and therefore extraction is more complete, and the aims of increasing the concentration, purity and quality of liquor are achieved.
Description
Technical field
The present invention relates to a kind of wine brewing extraction element, relate in particular to the cooling extraction element of a kind of second distillation secondary, be suitable for liquid vinasse and extract application.
Background technology
Brewing technology can be divided into solid brewing and liquid brewing according to technique difference, it is few that solid brewing method has water consumption, easy to operate, investment is little, be fermented into that power is high, vinasse are easily processed, the features such as quality better of making wine, consumption energy consumption grain is high, liquor ratio of raw material is low, labour intensity is large, and therefore production cost is high; And that liquid brewing method has compared with solid brewing method is with short production cycle, mechanization degree is high, labour intensity is little, production cost is low, liquor ratio of raw material advantages of higher.
The basic technological process of liquid brewing is exactly three roads, raw material-fermentation-distillation; In brewing industry, distillation and the cooling step that is absolutely necessary, and in prior art, by distilling apparatus, the liquor-making raw material after fermenting is carried out to boiling and form wine steam, and then wine steam is imported to and in condensing unit, carries out condensation and form liquid wine, ubiquity incomplete, the cooling problem such as not in place of wine steam extraction, occurs vinasse swelling in still-process, directly affects the extraction efficiency of wine and the concentration of wine, purity and quality.
Summary of the invention
The object of the invention is to overcome above-mentioned defect, the cooling wine brewing extraction element of a kind of second distillation secondary providing, carry the vinasse in single flash tower are distilled by two-way steam, prevent that vinasse from expanding, extract operation via cooling wine brewing of second distillation secondary.
For achieving the above object, the present invention carries out in the following way.
The wine brewing extraction element that second distillation secondary is cooling, is characterized in that it comprises boiler, single flash tower, after-fractionating tower, cooling tube, recooling tower, ring-like distillation cascade; Described boiler top is provided with steam pipe, and steam pipe is carried by steam cock control, and a point two-way leads in single flash tower, and a road is to connect spiral steam pipe to lead to below in single flash tower, and another a-road-through is in single flash tower bottom; Described single flash tower and boiler are adjacent, and top is provided with pressure cooker charge door, Pressure gauge and wine steam (vapor) outlet, and wine steam (vapor) outlet coordinates installation with distillation cascade by snap joint; Described after-fractionating tower is adjacent with single flash tower, be connected by distillation cascade, second distillation tower bottom is provided with blow-off valve, and top is provided with pressure cooker charge door, Pressure gauge and wine steam (vapor) outlet equally, and wine steam (vapor) outlet coordinates installation with distillation cascade by snap joint; A described cooling tube is positioned on the distillation cascade between after-fractionating tower and recooling tower, and right-hand member top is provided with cooling tube cold water inlet, and left end below is provided with cooling tube hot water outlet; Described recooling tower and after-fractionating tower are adjacent, and bottom is provided with recooling tower cold water inlet, and top layer is provided with recooling tower hot water outlet; Described ring-like distillation cascade is positioned at recooling tower, and one end is connected with distillation cascade by snap joint, and one end is wine outlet.
Pressure cooker charge door is provided with seal cover, seal cover adopt high-pressure pot cover to lock side formula or screw thread to lock side formula.
Single flash top of tower wine steam (vapor) outlet was provided with fitros.
The number of turns of ring-like distillation cascade and spiral steam pipe is some circles.
The invention has the beneficial effects as follows:
Provide a kind of second distillation secondary cooling wine brewing extraction element, connected to form by boiler, single flash tower, after-fractionating tower, cooling tube, a recooling tower, the wine steam that Steam Heating produces single flash tower mixes extraction mutually with auxiliary material wine or liquid vinasse in after-fractionating tower, be cooled to wine through cooling tube, a recooling tower again, and the spiral steam pipe in single flash tower expands can effectively prevent distilling with vinasse time, thereby make extraction more complete, reach the object of the concentration, purity and the quality that improve wine.
Brief description of the drawings
Below in conjunction with drawings and Examples, the present invention is further described.
Fig. 1 is the structural representation of the cooling wine brewing extraction element of a kind of second distillation secondary provided by the invention.
As scheme identify: 1, boiler, 2, steam pipe, 3, steam cock, 4, spiral steam pipe, 5, groove exhausting valve, 6, thermometer, 7, single flash tower, 8, pressure cooker charge door, 9, Pressure gauge, 10, cross fitros, 11, snap joint, 12, distillation cascade, 13, after-fractionating tower, 14, blow-off valve, 15, a cooling tube, 16, cooling tube cold water inlet, 17, cooling tube hot water outlet, 18, recooling tower, 19, ring-like distillation cascade, 20, recooling tower cold water inlet, 21, recooling tower hot water outlet, 22, wine outlet.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the cooling wine brewing extraction element of a kind of second distillation secondary of the present invention is further described.
As shown in the figure, the wine brewing extraction element that a kind of second distillation secondary is cooling, is characterized in that it comprises boiler 1, single flash tower 7, after-fractionating tower 13, cooling tube 15, recooling tower 18, ring-like distillation cascade 19.
Described boiler 1 top is provided with steam pipe 2, and steam pipe 2 is controlled and carried by steam cock 3, and it is to connect spiral steam pipe 4 to lead in the interior below of single flash tower 7 that a point two-way leads in single flash tower 7, one tunnels, and another a-road-through is in single flash tower 7 bottoms; Spiral steam pipe 4 plays and prevents that liquid vinasse from occurring the effect of expanding in when distillation, and two-way steam can to make vinasse be heated more even.
Described single flash tower 7 is adjacent with boiler 1, and top is provided with pressure cooker charge door 8, Pressure gauge 9 and wine steam (vapor) outlet, and wine steam (vapor) outlet coordinates installation by snap joint 11 with distillation cascade 12, by distillation cascade 12 connecting secondary destilling towers 13; Single flash top of tower wine steam (vapor) outlet was provided with fitros 10, and the wine steam that fitros 10 can be exported single flash tower 7 excessively filters, and plays deimpurity effect.
Described after-fractionating tower 13 is adjacent with single flash tower 7, after-fractionating tower 13 bottoms are provided with blow-off valve 14, top is provided with pressure cooker charge door 8, Pressure gauge 9 and wine steam (vapor) outlet equally, wine steam (vapor) outlet is provided with snap joint, coordinate installation by snap joint with distillation cascade 12, the wine steam that single flash tower 7 is exported is carried in after-fractionating tower 13 bottoms by distillation cascade 12, and wine steam mixes mutually with auxiliary material wine or liquid vinasse in after-fractionating tower 13, makes the last wine extracting more fragrant, denseer.
A described cooling tube 15 is positioned on the distillation cascade 12 between after-fractionating tower 13 and recooling tower 18, and right-hand member top is provided with cooling tube cold water inlet 17, and left end below is provided with cooling tube hot water outlet 16, carries out cooling in the mode of adverse current.
Described recooling tower 18 is adjacent with after-fractionating tower 13, and bottom is provided with recooling tower cold water inlet 20, and top layer is provided with recooling tower hot water outlet 21, and the hot water of outflow is stored in cistern in order to using next time.
Described ring-like distillation cascade 19 is positioned at recooling tower 18, one end is connected with distillation cascade 12 by snap joint, the other end is wine outlet 22, ring-like distillation cascade 19 can delay the speed of wine steam through recooling tower 18, extend cool time, make it change into wine completely, get object more completely to reach wine dipper.
When wine brewing is extracted, the steam that boiler 1 produces is carried in single flash tower 7 by two-way steam pipe, the wine steam producing filters by crossing fitros 10, wine steam after filtration is carried in after-fractionating tower 13 by steam pipe 12, wine steam mixes mutually with auxiliary material wine or liquid vinasse in after-fractionating tower 13, wine steam after second distillation is cooled to wine by a cooling tube 15, then in recooling tower 18, carry out secondary by ring-like distillation cascade 19 cooling, cooled wine flows out by wine outlet 22, in order to next step processing, reach the cooling object of second distillation secondary.
In sum, the present invention can effectively improve concentration, purity and the quality of wine, reaches extraction object more completely.
Above-described embodiment, the just one of the more typical detailed description of the invention of the present invention, the common variation that those skilled in the art carries out within the scope of technical solution of the present invention and replacement all should be included in opereating specification of the present invention.
Claims (4)
1. the cooling wine brewing extraction element of second distillation secondary, is characterized in that it comprises boiler (1), single flash tower (7), after-fractionating tower (13), a cooling tube (15), recooling tower (18), ring-like distillation cascade (19); Described boiler (1) top is provided with steam pipe (2), steam pipe (2) is controlled and is carried by steam cock (3), divide two-way to lead in single flash tower (7), one tunnel is to connect spiral steam pipe (4) to lead to below in single flash tower (7), and another a-road-through is in single flash tower (7) bottom; Described single flash tower (7) is adjacent with boiler (1), top is provided with pressure cooker charge door (8), Pressure gauge (9) and wine steam (vapor) outlet, and wine steam (vapor) outlet coordinates installation by snap joint (11) with distillation cascade (12); Described after-fractionating tower (13) is adjacent with single flash tower (7), be connected by distillation cascade (12), after-fractionating tower (13) bottom is provided with blow-off valve (14), top is provided with pressure cooker charge door (8), Pressure gauge (9) and wine steam (vapor) outlet equally, and wine steam (vapor) outlet coordinates installation by snap joint with distillation cascade (12); A described cooling tube (15) is positioned on the distillation cascade (12) between after-fractionating tower (13) and recooling tower (18), right-hand member top is provided with cooling tube cold water inlet (17), and left end below is provided with cooling tube hot water outlet (16); Described recooling tower (18) is adjacent with after-fractionating tower (13), and bottom is provided with recooling tower cold water inlet (20), and top layer is provided with recooling tower hot water outlet (21); Described ring-like distillation cascade (19) is positioned at recooling tower (18), and one end is connected with distillation cascade (12) by snap joint, and one end is wine outlet (22).
2. the cooling wine brewing extraction element of a kind of second distillation secondary according to claim 1, is characterized in that described pressure cooker charge door (8) is provided with seal cover, seal cover adopt high-pressure pot cover to lock side formula or screw thread to lock side formula.
3. the cooling wine brewing extraction element of a kind of second distillation secondary according to claim 1, is characterized in that described single flash tower (7) top wine steam (vapor) outlet was provided with fitros (10).
4. the cooling wine brewing extraction element of a kind of second distillation secondary according to claim 1, is characterized in that described spiral steam pipe (4) and the number of turns of ring-like distillation cascade (19) are some circles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610170542.2A CN105586231A (en) | 2016-03-24 | 2016-03-24 | Two-time-distillation and two-time-cooling brewing extraction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610170542.2A CN105586231A (en) | 2016-03-24 | 2016-03-24 | Two-time-distillation and two-time-cooling brewing extraction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105586231A true CN105586231A (en) | 2016-05-18 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610170542.2A Pending CN105586231A (en) | 2016-03-24 | 2016-03-24 | Two-time-distillation and two-time-cooling brewing extraction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105586231A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107858254A (en) * | 2017-10-12 | 2018-03-30 | 广东省阳春酒厂有限公司 | A kind of energy-saving distilling equipment |
| CN107937229A (en) * | 2018-01-15 | 2018-04-20 | 沈墅 | A kind of high-purity white wine deep layer extracting system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20070131533A1 (en) * | 2003-04-25 | 2007-06-14 | Blum Stephan R | Distillation method |
| JP2007236210A (en) * | 2006-03-04 | 2007-09-20 | Nisshin:Kk | Distillation apparatus |
| CN102776110A (en) * | 2012-07-16 | 2012-11-14 | 泸州品创科技有限公司 | Device and method for extracting bouquet through multistage distillation |
| CN203079943U (en) * | 2013-02-20 | 2013-07-24 | 泸州品创科技有限公司 | Distilling and cooling device for brewing wine |
| CN203653528U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Brandy tower type distiller |
| CN205420349U (en) * | 2016-03-24 | 2016-08-03 | 龙岩市铭威厨房设备有限公司 | Redistillation secondary cooling's making wine extraction element |
-
2016
- 2016-03-24 CN CN201610170542.2A patent/CN105586231A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20070131533A1 (en) * | 2003-04-25 | 2007-06-14 | Blum Stephan R | Distillation method |
| JP2007236210A (en) * | 2006-03-04 | 2007-09-20 | Nisshin:Kk | Distillation apparatus |
| CN102776110A (en) * | 2012-07-16 | 2012-11-14 | 泸州品创科技有限公司 | Device and method for extracting bouquet through multistage distillation |
| CN203079943U (en) * | 2013-02-20 | 2013-07-24 | 泸州品创科技有限公司 | Distilling and cooling device for brewing wine |
| CN203653528U (en) * | 2013-10-08 | 2014-06-18 | 富阳步达水处理设备有限公司 | Brandy tower type distiller |
| CN205420349U (en) * | 2016-03-24 | 2016-08-03 | 龙岩市铭威厨房设备有限公司 | Redistillation secondary cooling's making wine extraction element |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107858254A (en) * | 2017-10-12 | 2018-03-30 | 广东省阳春酒厂有限公司 | A kind of energy-saving distilling equipment |
| CN107937229A (en) * | 2018-01-15 | 2018-04-20 | 沈墅 | A kind of high-purity white wine deep layer extracting system |
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| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160518 |
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