CN205420349U - Redistillation secondary cooling's making wine extraction element - Google Patents
Redistillation secondary cooling's making wine extraction element Download PDFInfo
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- CN205420349U CN205420349U CN201620229427.3U CN201620229427U CN205420349U CN 205420349 U CN205420349 U CN 205420349U CN 201620229427 U CN201620229427 U CN 201620229427U CN 205420349 U CN205420349 U CN 205420349U
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Abstract
The utility model relates to a redistillation secondary cooling's making wine extraction element, by the boiler, the single flash tower, the redistillation tower, the primary cooling pipe, the secondary cooling tower connects to form, the wine steam that steam heating made the single flash tower produce draws with interior auxiliary material wine or the liquid lees phase mixing of redistillation tower, pass through the primary cooling pipe again, the secondary cooling tower cooler becomes wine, and the spiral steam pipe in the single flash tower expands in the time of can effectually preventing the lees distillation, it is more complete that thereby the messenger draws, reach the concentration that improves wine, the mesh of purity and quality.
Description
Technical field
The utility model relates to a kind of wine brewing extraction element, particularly relates to the extraction element of a kind of second distillation cooling twice, is suitable to liquid vinasse and extracts application.
Background technology
Brewing technology can be divided into solid brewing and liquid brewing according to technique difference, and it is few that solid brewing method has water consumption, easily operates, invests not quite, is fermented into the features such as power is high, vinasse are disposable, Wine-making quality is good, consumption energy consumption grain is high, liquor ratio of raw material is low, and labour intensity is big, and therefore production cost is high；And liquid brewing method has with short production cycle compared with solid brewing method, 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, and fermenting raw materials is distilled；In brewing industry, distillation and cooling are requisite steps, and in prior art, by distilling apparatus, the liquor-making raw material after fermentation is carried out boiling and form wine steam, wine steam being imported to carries out condensation in condensing unit the most again and forms the wine of liquid, generally also exist wine steam extraction not exclusively, cool down the problems such as not in place, still-process occurs vinasse swelling, directly affects extraction efficiency and the concentration of wine, purity and the quality of wine.
Summary of the invention
The purpose of this utility model is to overcome drawbacks described above, the wine brewing extraction element of a kind of second distillation cooling twice provided, by the conveying of two-way steam, the vinasse in single flash tower are distilled, prevent vinasse from expanding, carry out wine brewing via second distillation cooling twice and extract operation.
For achieving the above object, the utility model is carried out in the following way.
The wine brewing extraction element of a kind of second distillation cooling twice, it is characterised in that it includes boiler, single flash tower, after-fractionating tower, cooling tube, recooling tower, a ring-like distillation cascade；Described boiler top is provided with steam pipe, and steam pipe controls conveying by steam cock, and a point two-way leads in single flash tower, and a road is to connect helicoidal stream pipe to lead to lower section in single flash tower, and another a-road-through is in single flash tower bottom；Described single flash tower is adjacent with boiler, and top is provided with pressure cooker charge door, Pressure gauge and wine steam (vapor) outlet, and wine steam (vapor) outlet coordinates installation by snap joint with distillation cascade；Described after-fractionating tower is adjacent with single flash tower, is connected by distillation cascade, and second distillation tower bottom is provided with blow-off valve, and top is again provided with pressure cooker charge door, Pressure gauge and wine steam (vapor) outlet, and wine steam (vapor) outlet coordinates installation by snap joint with distillation cascade；A described cooling tube is positioned on the distillation cascade between after-fractionating tower and recooling tower, and right-hand member is arranged over cooling tube cold water inlet, is provided with cooling tube hot water outlet below left end；Described recooling tower is adjacent with after-fractionating tower, 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 sealing lid, seal lid use 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.
Ring-like distillation cascade is some circles with the number of turns of helicoidal stream pipe.
The beneficial effects of the utility model are:
The wine brewing extraction element of a kind of second distillation cooling twice is provided, connected formed by boiler, single flash tower, after-fractionating tower, cooling tube, a recooling tower, the wine steam that steam heating makes single flash tower produce mixes extraction mutually with the auxiliary material wine in after-fractionating tower or liquid vinasse, it is cooled to wine again through cooling tube, a recooling tower, and the helicoidal stream pipe in single flash tower can effectively prevent from expanding during distilling with vinasse, so that extracting more complete, reach to improve the concentration of wine, purity and the purpose of quality.
Accompanying drawing explanation
With embodiment, the utility model is further illustrated below in conjunction with the accompanying drawings.
Fig. 1 is the structural representation of the wine brewing extraction element of a kind of second distillation cooling twice that the utility model provides.
Identify as schemed: 1, boiler, 2, steam pipe, 3, steam cock, 4, helicoidal stream 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
With specific embodiment, the wine brewing extraction element of a kind of second distillation cooling twice of the present utility model is further described below in conjunction with the accompanying drawings.
As it can be seen, the wine brewing extraction element of a kind of second distillation cooling twice, it is characterised in that it includes boiler 1, single flash tower 7, after-fractionating tower 13, cooling tube 15, recooling tower 18, a ring-like distillation cascade 19.
Described boiler 1 top is provided with steam pipe 2, and steam pipe 2 controls conveying by steam cock 3, and a point two-way leads in single flash tower 7, and a road is to connect helicoidal stream pipe 4 to lead to lower section in single flash tower 7, and another a-road-through is bottom single flash tower 7；Helicoidal stream pipe 4 plays and prevents liquid vinasse from the effect expanded occur when distillation, and two-way steam can make vinasse be heated evenly.
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 with distillation cascade 12, by distillation cascade 12 connecting secondary destilling tower 13 by snap joint 11；Single flash top of tower wine steam (vapor) outlet was provided with fitros 10, crosses fitros 10 and can filter the wine steam of single flash tower 7 output, plays deimpurity effect.
Described after-fractionating tower 13 is adjacent with single flash tower 7, blow-off valve 14 it is provided with bottom after-fractionating tower 13, top is again provided with pressure cooker charge door 8, Pressure gauge 9 and wine steam (vapor) outlet, wine steam (vapor) outlet is provided with snap joint, installation is coordinated with distillation cascade 12 by snap joint, the wine steam of single flash tower 7 output is transported in after-fractionating tower 13 bottom by distillation cascade 12, and wine steam mixes mutually with the auxiliary material wine in after-fractionating tower 13 or liquid vinasse, makes the wine finally extracted more fragrant, richer.
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 is arranged over cooling tube cold water inlet 17, is provided with cooling tube hot water outlet 16, cools down in a counter-current fashion below left end.
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 case next time uses.
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 wine steam through the speed of recooling tower 18, extend cool time, make it be melted into wine completely, take purpose more completely reaching wine dipper.
When wine brewing is extracted, the steam that boiler 1 produces is transported in single flash tower 7 by two-way steam pipe, the wine steam produced filters by crossing fitros 10, wine steam after filtration is transported in after-fractionating tower 13 by steam pipe 12, wine steam mixes mutually with the auxiliary material wine in after-fractionating tower 13 or liquid vinasse, wine steam after second distillation is cooled to wine by a cooling tube 15, then in recooling tower 18, cooling twice is carried out by ring-like distillation cascade 19, wine after cooling is flowed out by wine outlet 22, in case next step processes, reach the purpose of second distillation cooling twice.
In sum, the utility model can effectively improve the concentration of wine, purity and quality, reaches to extract purpose more completely.
Embodiment described above, the simply one of the more typical detailed description of the invention of the utility model, the usual variations and alternatives that those skilled in the art is carried out in the range of technical solutions of the utility model all should be included in opereating specification of the present utility model.
Claims (4)
1. the wine brewing extraction element of a second distillation cooling twice, it is characterised in that it includes boiler (1), single flash tower (7), after-fractionating tower (13), cooling tube (15), recooling tower (18), a ring-like distillation cascade (19)；Described boiler (1) top is provided with steam pipe (2), steam pipe (2) controls conveying by steam cock (3), two-way is divided to lead in single flash tower (7), one tunnel is to connect helicoidal stream pipe (4) to lead to lower section 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), it is connected by distillation cascade (12), after-fractionating tower (13) bottom is provided with blow-off valve (14), top is again 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 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 is arranged over cooling tube cold water inlet (17), is provided with cooling tube hot water outlet (16) below left end；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).
The wine brewing extraction element of a kind of second distillation cooling twice the most according to claim 1, it is characterised in that described pressure cooker charge door (8) is provided with sealing lid, seal lid use high-pressure pot cover to lock side formula or screw thread to lock side formula.
The wine brewing extraction element of a kind of second distillation cooling twice the most according to claim 1, it is characterised in that described single flash tower (7) top wine steam (vapor) outlet was provided with fitros (10).
The wine brewing extraction element of a kind of second distillation cooling twice the most according to claim 1, it is characterised in that described helicoidal stream pipe (4) is some circles with the number of turns of ring-like distillation cascade (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620229427.3U CN205420349U (en) | 2016-03-24 | 2016-03-24 | Redistillation secondary cooling's making wine extraction element |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620229427.3U CN205420349U (en) | 2016-03-24 | 2016-03-24 | Redistillation secondary cooling's making wine extraction element |
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| CN205420349U true CN205420349U (en) | 2016-08-03 |
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| CN201620229427.3U Active CN205420349U (en) | 2016-03-24 | 2016-03-24 | Redistillation secondary cooling's making wine extraction element |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105586231A (en) * | 2016-03-24 | 2016-05-18 | 龙岩市铭威厨房设备有限公司 | Two-time-distillation and two-time-cooling brewing extraction device |
| CN107603837A (en) * | 2017-09-07 | 2018-01-19 | 重庆市红槽坊酒业有限公司 | A kind of new distilling machinery |
| CN113322143A (en) * | 2021-02-03 | 2021-08-31 | 邵阳学院 | Tea wine processing technology and processing equipment thereof |
-
2016
- 2016-03-24 CN CN201620229427.3U patent/CN205420349U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105586231A (en) * | 2016-03-24 | 2016-05-18 | 龙岩市铭威厨房设备有限公司 | Two-time-distillation and two-time-cooling brewing extraction device |
| CN107603837A (en) * | 2017-09-07 | 2018-01-19 | 重庆市红槽坊酒业有限公司 | A kind of new distilling machinery |
| CN113322143A (en) * | 2021-02-03 | 2021-08-31 | 邵阳学院 | Tea wine processing technology and processing equipment thereof |
| CN113322143B (en) * | 2021-02-03 | 2022-06-07 | 邵阳学院 | Tea wine processing technology and processing equipment thereof |
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