CN107828619A - A kind of beer Spirit production system and technique - Google Patents
A kind of beer Spirit production system and technique Download PDFInfo
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- CN107828619A CN107828619A CN201711237232.9A CN201711237232A CN107828619A CN 107828619 A CN107828619 A CN 107828619A CN 201711237232 A CN201711237232 A CN 201711237232A CN 107828619 A CN107828619 A CN 107828619A
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- 235000013405 beer Nutrition 0.000 title claims abstract description 109
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 35
- 238000000034 method Methods 0.000 title claims abstract description 26
- 235000014101 wine Nutrition 0.000 claims abstract description 63
- 238000004821 distillation Methods 0.000 claims abstract description 45
- 239000007788 liquid Substances 0.000 claims abstract description 35
- 238000010438 heat treatment Methods 0.000 claims abstract description 25
- 239000002994 raw material Substances 0.000 claims abstract description 25
- 238000003860 storage Methods 0.000 claims abstract description 16
- 238000005516 engineering process Methods 0.000 claims abstract description 13
- 230000008676 import Effects 0.000 claims abstract description 6
- 238000012545 processing Methods 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 38
- 230000001476 alcoholic effect Effects 0.000 claims description 31
- 235000020015 schwarzbier Nutrition 0.000 claims description 10
- 235000020017 wheat beer Nutrition 0.000 claims description 7
- 239000000446 fuel Substances 0.000 claims description 5
- 230000033228 biological regulation Effects 0.000 claims description 3
- 230000006837 decompression Effects 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 102000010637 Aquaporins Human genes 0.000 claims 1
- 108010063290 Aquaporins Proteins 0.000 claims 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 9
- 239000000796 flavoring agent Substances 0.000 abstract description 5
- 235000019634 flavors Nutrition 0.000 abstract description 5
- 230000035622 drinking Effects 0.000 abstract description 3
- 239000000126 substance Substances 0.000 description 9
- 125000003118 aryl group Chemical group 0.000 description 8
- 230000008859 change Effects 0.000 description 7
- 239000003205 fragrance Substances 0.000 description 7
- 230000008569 process Effects 0.000 description 6
- 241000219095 Vitis Species 0.000 description 5
- 235000009754 Vitis X bourquina Nutrition 0.000 description 5
- 235000012333 Vitis X labruscana Nutrition 0.000 description 5
- 235000014787 Vitis vinifera Nutrition 0.000 description 5
- 239000000567 combustion gas Substances 0.000 description 4
- 239000004615 ingredient Substances 0.000 description 4
- 241000209140 Triticum Species 0.000 description 3
- 235000021307 Triticum Nutrition 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- 238000010563 solid-state fermentation Methods 0.000 description 3
- 241000894007 species Species 0.000 description 3
- 238000010025 steaming Methods 0.000 description 3
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000004508 fractional distillation Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 241000227425 Pieris rapae crucivora Species 0.000 description 1
- 238000003483 aging Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 235000013334 alcoholic beverage Nutrition 0.000 description 1
- 238000013475 authorization Methods 0.000 description 1
- 238000000998 batch distillation Methods 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 235000020097 white wine Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
- C12C12/00—Processes specially adapted for making special kinds of beer
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Health & Medical Sciences (AREA)
- Food Science & Technology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Microbiology (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
The present invention relates to a kind of beer Spirit production system, it includes destilling tower, returns solidifying device, condensing unit, water-bath chuck and heater, destilling tower includes some tower sections on bottom Chu Jiu rooms and top, the distillation tower bottom storage wine room is installed in water-bath chuck, the water-bath chuck bottom sets the heater, destilling tower top drum section, time solidifying device and condensing unit are sequentially connected, and the storage wine room is provided with wine liquid import, wine liquid outlet and steam (vapor) outlet；The condensing unit bottom is provided with collection device.The invention further relates to a kind of beer Spirit production technology, including the step of raw material addition, flame heating, beer distillation, finished product collection.The production system and technique of the present invention, distillation processing is carried out by destilling tower, time solidifying device and condensing unit to raw material beer liquid, obtains the wash of high alcohol content, while possess the beer flavor of raw material beer liquid, meet the demand of drinking of consumer.
Description
Technical field
The present invention relates to beer manufacture field, particularly a kind of beer Spirit production system and technique.
Background technology
Spirit refers to fermented wine or karusen and fermented grain etc. to pass through distillable strong alcoholic drink liquid.At present
Domestic and international distillation technique is mainly two kinds：Tower distillation and kettle formula；The whole still-process of tower distillation be it is continuous, can
The higher wine steam of alcoholic strength successively is obtained, is characterized in continuous still, yield is high, but obtained Spirit is single.Kettle
Alcoholic solution needs to distill repeatedly in formula distillation, can obtain the different Spirit of alcohol concentration per kettle, can be classified wine, it is special
Point is batch distillation, is yielded poorly.
Patent of invention (application publication number：CN107287066A a kind of continuous high-efficient fractional distillation equipment and technique) are disclosed
Method, the classification for grape wine are efficiently distilled, and a kind of energy of proposition is continuous, high yield production high-quality wine spirit, can protect
Deposit grape wine interior aromatic substance, remove harmful substance, the continuous high-efficient fractional distillation equipment and work that wine spirit is classified
Process.
Patent of invention (application publication number：CN107129891A a kind of wine spirit and preparation method thereof) is disclosed.Should
Method is U.S. happy for raw material with grape variety of making wine, obtains distilling former wine by broken squeezing, cold fermentation, single flash, then
Wine spirit is obtained through the step such as ageing, freezing, filtering, filling.The preparation method replaces steaming twice using disposable distillation
Evaporate, reduce energy consumption and distillation time.Obtained wine spirit product both has grape red fruit fruity, there is distillation technique again
The mellowness of imparting, wine body is harmonious, and the fruity and typical performance of wine more fully show.
Patent of invention (application publication number：The A of CN 106635709) a kind of distillation Brewing equipment is disclosed, for steaming at present
Evaporate equipment not preferably by temperature controlled fermentation, directly distillation, distillation etc. combines indirectly, a set of brand-new so as to provide
Multi-function brewing distillation equipment, meet foregoing wine brewing needs.
Utility model patent (Authorization Notice No.：The U of CN 203700326) disclose a kind of solid state fermentation steaming for being used to make wine
Evaporate equipment.The utility model provides discharge under a kind of upper feeding, convenient, clean equipment solid state fermentation distillation equipment.But should
Equipment is only applicable to solid state fermentation distillation.
In summary, although many people have carried out some innovations to wine brewing distillation equipment, all it is confined to condense,
And these equipment are directed to the distillation of white wine and grape wine more, and it is few for the distillation equipment and technique of beer.
The content of the invention
Distilled it is an object of the invention to overcome the deficiencies of the prior art and provide one kind using beer so that product
The fragrance of the existing beer of Spirit, there are the beer Spirit production system and technique of the high alcohol content of common white spirit again.
The present invention solves its technical problem and is achieved through the following technical solutions：
A kind of beer Spirit production system, it is characterised in that：Including destilling tower, return solidifying device, condensing unit, water-bath folder
Set and heater, destilling tower include some tower sections on bottom Chu Jiu rooms and top, and the distillation tower bottom storage wine room is installed on
In water-bath chuck, the water-bath chuck bottom sets the heater, destilling tower top drum section, returns solidifying device and condensing unit
It is sequentially connected, the storage wine room is provided with wine liquid import, wine liquid outlet and steam (vapor) outlet；The condensing unit bottom, which is provided with, collects
Device.
Moreover, the water-bath chuck bottom is provided with heat exchanging pipe, water-bath chuck inside is with the heat exchanging pipe by entering
Waterpipe, water return pipeline carry out circulation connection, DN32 welded type Hygiene Ball Valve A are installed on inlet channel, on water return pipeline
DN32 welded type Hygiene Ball Valves B is installed.
Moreover, pressure-reducing valve is installed on water-bath chuck.
Moreover, the heater is direct flame-type heater, including heating chamber, flame gun, heating chamber are located at institute
The bottom in water-bath chuck is stated, side is provided with heating gate in heating chamber, and heating gate sets the flame gun, the external combustion gas of flame gun
Tank, flame gun flame heat exchanging tubulation are heated, and water density, which diminishes, in heat exchanging pipe flows up, and drive water in water-bath chuck
Flow and uniformly heat, chimney is set in heating chamber.
Moreover, the upper column section of the destilling tower, time solidifying device, condensing unit are provided with visor and metallic thermometer.
Moreover, the destilling tower, time solidifying device and condensing unit are all connected with CIP systems.
A kind of beer Spirit production technology, it is characterised in that：The production technology comprises the following steps：
1) raw materials add：Raw material beer liquid is added in storage wine room, water-bath chuck adds a certain amount of water, condensation
Device is passed through condensed water；
2) flames heat：Fuel cartridge is opened, flame gun is lighted, the heat exchanging pipe in heating chamber is heated, heat exchange row
Water density, which diminishes, in pipe flows up, and drives water in water-bath chuck to flow and uniformly heat；
3) beer distills：Switched by regulating gas and the steam pressure of water-bath chuck decompression valve regulation water-bath chuck is
0.1-0.12Mp, carries out distillation processing to raw material beer liquid in storage wine room, and in still-process, control overhead temperature exists
75~79 DEG C or so, column bottom temperature is controlled at 100~105 DEG C or so, and temperature control is at 88~92 DEG C in tower；Return solidifying device water
Temperature is at 60~65 DEG C, 35~40 DEG C of condensing unit water temperature；
4) finished products are collected：In condensing unit bottom wine outlet beer Spirit finished product, beer Spirit finished product are contained with container
Alcoholic strength be 20% to 35%.
Moreover, in finished product collection step, during collected from Spirit output from 8-16 minutes beer Spirit, its wine
Precision is 60-65%.
Moreover, described raw material beer liquid is that commercially available industrial beer beer, IPA, Belgian wheat beer or stout are black
Beer, alcoholic strength >=6.8% of alcoholic strength >=2.5%, IPA of the commercially available industrial beer beer, the wine of Belgian wheat beer
Alcoholic strength >=5.5% of the black beer of precision >=4.8%, stout.
The advantages of the present invention are：
1st, this beer Spirit production system, raw material beer liquid is carried out by destilling tower, time solidifying device and condensing unit
Distillation is handled, and obtains the wash of high alcohol content, while possesses the beer flavor of raw material beer liquid, meets drinking for consumer
Demand.
2nd, this beer Spirit production system, heater are direct flame-type, and directly water-bath chuck is entered using combustion gas
Row heating, while directly use the water in combustion gas heat exchanging tubulation to be heated, water density, which diminishes, in tubulation flows up, with this
Drive the water in water-bath chuck to be flowed, make heating more quick, uniform, high-purity can obtain using the distillation of direct flame-type
With the beer Spirit of high alcohol content, and beer Spirit is set to retain the fragrance of beer to greatest extent.
3rd, this beer Spirit production system, pressure-reducing valve is installed on water-bath chuck, by water-bath jacket steam pressure
Power is controlled, and the too high then distillation speed of steam pressure is too fast, and vapor entrainment is too high so that under the alcoholic strength of beer Spirit
Drop；Steam pressure is too low, and distillation speed slows down distillation, and efficiency declines, by being controlled to water-bath jacket steam pressure,
Steam pressure is 0.1-0.12Mp, and distillation efficiency is high and stably.
4th, this beer Spirit production system, the upper column section of destilling tower, time solidifying device, condensing unit are provided with visor
And metallic thermometer, some internal states of the destilling tower in still-process can be observed, and gather in overhead, tower and
Column bottom temperature data.
5th, this beer Spirit production technology, raw material beer liquid is carried out by destilling tower, time solidifying device and condensing unit
Distillation is handled, and the alcoholic strength of beer Spirit finished product is 20% to 35%, and the alcoholic strength compared with raw material beer greatly improves, simultaneously
To possess the beer flavor of raw material beer liquid, meet the demand of drinking of consumer, all beer can be used to produce beer Spirit,
The flavor that different material beer distills out beer Spirit is different, and the whole production process of Spirit does not add any addition
Agent, at utmost retain the fragrance of raw material beer.
6th, this beer Spirit production technology, in finished product collection step, can also be collected separately from Spirit output when
The beer Spirit of 8-16 minutes is played, its alcoholic strength is 60-65%, turns into high alcohol content beer Spirit.
7th, this beer Spirit production technology, raw material are easy to obtain, and technical process is simple to operation, efficiency high, and beer steams
Evaporate wine finished product mouthfeel and unique flavor.
Brief description of the drawings
Fig. 1 is the production technological process of the present invention；
Fig. 2 is the process units front view of the present invention；
Fig. 3 is the process units top view of the present invention；
Fig. 4 is the process units Local map of the present invention；
Four kinds of beer aromatic substance species that Fig. 5 is the present invention change block diagram.
Description of reference numerals
1. destilling tower, 2. tower sections, 3. bimetallic thermometers, 4. visors, 5. visors, 6. bimetallic thermometers, 7. times solidifying dresses
Put, 8. bimetallic thermometers, 9.CIP systems, 10. condensing units, 11. collection devices, 12. sample taps, 13. wine outlets, 14. cigarettes
Chimney, 15. tubulations, 16. heating chambers, 17. water-bath chucks, 18. heat-insulation layers, 19. storage wine rooms, 20. pressure-reducing valves, 21. burning torches, 22.
Flame gun, 23. flow valves, 24. gas tanks, 25.DN32 welded type Hygiene Ball Valves A, 26. wine liquid imports, 27. visors, 28.DN32
Welded type Hygiene Ball Valve B, 29. filler, the outlet of 30. wine liquids, 31. delivery ports, 32. barometers, 33. glass-tube liquid level meters, 34.
Inlet channel, 35. water return pipelines.
Embodiment
Below by specific embodiment, the invention will be further described, and following examples are descriptive, is not limit
Qualitatively, it is impossible to which protection scope of the present invention is limited with this.
A kind of beer Spirit production system, it includes destilling tower 1, returns solidifying device 7, condensing unit 10, water-bath chuck 17
And heater, destilling tower include some tower sections on bottom Chu Jiu rooms 19 and top, distillation tower bottom storage wine room is installed on water-bath
In chuck, water-bath chuck bottom sets heater, and destilling tower top drum section, time solidifying device and condensing unit are sequentially connected.
50L beer liquid can be added in distillation tower bottom storage wine room, storage wine room is provided with wine liquid import 26, wine liquid exports
30th, the upper column section of steam (vapor) outlet destilling tower reduces vapor entrainment with this, improves distillation efficiency no less than four section towers.Wine liquid
Import and wine liquid outlet are respectively used to add raw material beer liquid and discharge waste liquid, are multi-stage column section above steam (vapor) outlet, and alcohol steams
Vapour enters multi-stage column section subsequently into Hui Ning, condensing unit by steam (vapor) outlet.Often section tower is provided with visor 4 and bimetallic temperature
Degree meter 3, for observing distillation situation.Store up and visor 27 is set on wine room.
Return on solidifying device and be mounted on visor 5 and bimetallic thermometer 6, for observing distillation situation.Return solidifying device and cold
Solidifying device is passed through cooling water and alcohol steam is cooled down, and distillation situation can be carried out by visor, metallic thermometer certain
Judgement.Condensing unit bottom is provided with collection device 11, and collection device is provided with sample tap 12 and wine outlet 13, and sample tap can be with
Spirit is sampled, wine outlet is used for being easy to beer Spirit finished product to discharge.Bimetallic temperature is installed at the top of condensing unit
Spend sensor 8.Each tower section of destilling tower, time solidifying device and condensing unit are all connected with CIP systems 9.
Water-bath chuck bottom is provided with heat exchanging pipe 15, inside water-bath chuck with heat exchanging pipe by inlet channel 34, return
Waterpipe 35 carries out circulation connection, and DN32 welded type Hygiene Ball Valve A, label 25, on water return pipeline are installed on inlet channel
DN32 welded type Hygiene Ball Valve B, label 28 are installed.Most 75L water can be added in water-bath chuck.Water-bath chuck also includes plus water
Mouth 29, delivery port 31, glass-tube liquid level meter 33, barometer 32.Pressure-reducing valve 20 is installed on water-bath chuck.Water-bath chuck is also set up
There is heat-insulation layer 18.Filler and delivery port are used for the addition and discharge for realizing water in water-bath chuck.Glass-tube liquid level meter is then used for
Whether the liquid level that observation adds water meets that distillation requires.Pressure-reducing valve can make the pressure of water-bath chuck be maintained at required pressure
By force, to ensure the uniformity of whole still-process, heat-insulation layer can be protected to the heat in water-bath chuck.DN32 welded types
Hygiene Ball Valve A and DN32 welded type Hygiene Ball Valve B is used for controlling the availability of tubulation, and shutoff valve A, valve B heat exchanging pipes lose effect
Effect occurs for fruit, opening valve A, valve B heat exchanging pipes.
Heater is direct flame-type heater, including heating chamber 16, flame gun 22, heating chamber are located at the water-bath
Bottom in chuck, side is provided with heating gate in heating chamber, and heating gate sets flame gun and burning torch 21, the external combustion gas of flame gun
Tank 24, flame gun flame heat exchanging tubulation are heated, and water density, which diminishes, in heat exchanging pipe flows up, and are driven in water-bath chuck
Water is flowed and uniformly heated, and chimney 14 is set in heating chamber.Flame gun has three, there is flow valve 23 on fuel cartridge, can pass through
Flow valve and flame gun number are adjusted to control the size of fire further to control distilling rate.
A kind of beer Spirit production technology, its production technology comprise the following steps：
1) raw materials add：Raw material beer liquid is added in storage wine room, water-bath chuck adds a certain amount of water, condensation
Device is passed through condensed water；Raw material beer liquid is commercially available industrial beer beer, IPA (India's light color ale), Belgian wheat
Beer or the black beers of stout, alcoholic strength >=6.8% of alcoholic strength >=2.5%, IPA of the commercially available industrial beer beer, Belgium
Alcoholic strength >=5.5% of the black beer of alcoholic strength >=4.8%, stout of wheat beer.
2) flames heat：Fuel cartridge is opened, flame gun is lighted, the heat exchanging pipe in heating chamber is heated, heat exchange row
Water density, which diminishes, in pipe flows up, and drives water in water-bath chuck to flow and uniformly heat；
3) beer distills：Switched by regulating gas and the steam pressure of water-bath chuck decompression valve regulation water-bath chuck is
0.1-0.12Mp, carries out distillation processing to raw material beer liquid in storage wine room, and in still-process, control overhead temperature exists
775~79 DEG C or so, column bottom temperature is controlled at 100~105 DEG C or so, and temperature control is at 88~92 DEG C in tower；Return solidifying device
Water temperature is at 60~65 DEG C, 35~40 DEG C of condensing unit water temperature；
4) finished products are collected：Beer Spirit finished product is contained with container in condensing unit bottom wine outlet, has Spirit output by oneself
Terminate to distillation, the alcoholic strength of the beer Spirit finished product after whole accesss is 20% to 35%.
In finished product collection step, the beer distillation of the 8-16 minutes from Spirit output can also be collected separately
Wine, its alcoholic strength are 60-65%.
Experimental result：
1st, alcoholic strength
The timing since beginning with wine and distilling out, an alcoholic strength was surveyed every two minutes, is as shown in table 1 commercially available industrial beer
The alcoholic strength change of wine, IPA, Belgian wheat, stout four kinds of beer of black beer.
The alcoholic strength change of 1 commercially available industrial beer of table, IPA, Belgian wheat, stout four kinds of beer of black beer
Four kinds of beer of the black beer of commercially available industrial beer, IPA, Belgian wheat, stout are using the present invention as can be seen from the above table
The change totality rule of the alcoholic strength of direct flame-type destilling tower production beer Spirit is basically identical.Heated using direct flame
Formula destilling tower carry out distillation test during, alcoholic strength raises rapidly within 2-4 minutes, then tend to be steady or slowly on
Rise, begun to decline in 20 minutes or so alcoholic strengthes, begin to ramp up to 35 minutes or so alcoholic strengthes or fluctuate up and down again, finally under
Drop to 20% or so and no longer go out wine, experiment terminates.With regard to being broadly divided into two experimental stages 0-35 point from the point of view of whole distillation test
Clock is the first stage, and 35-60 minutes are second stage.For above-mentioned all kinds of raw material beer, finished product is taken in 8-16 minutes, can be obtained
To alcoholic strength 60-65% high alcohol content beer Spirit.
2nd, fragrance ingredient：
Change to different time points fragrance ingredient in still-process is studied, and is different time points as shown in Figure 5
Gathered sample aromatic substance species variation diagram.Three kinds of beer of the black beer of IPA, Belgian wheat beer, stout as seen from the figure
Fragrance ingredient change it is essentially identical with the fragrance ingredient variation tendency in commercially available industrial beer beer still-process.Start just
When distillation, the aromatic substance in Spirit is minimum, as the aromatic substance in the progress Spirit of distillation gradually increases
It is more.Meanwhile by figure we it is also seen that the aromatic substance in other three kinds of beer is to be more than commercially available industrial beer beer
, the aromatic substance in its product of distillation is also to be more than commercially available industrial beer beer.
The still-process of four kinds of beer of contrast can show that the Snaps wine distilled out in 20-45 minutes most has,
Not only alcoholic strength is high and aromatic substance species is also more for Snaps wine now, while it is also most to go out capacity for liquor.
Embodiments of the invention and accompanying drawing, but it will be appreciated by those skilled in the art that：The present invention and institute are not being departed from
In attached spirit and scope by the claims, it is various replace, change and modifications all be it is possible, therefore, the scope of the present invention not office
It is limited to embodiment and accompanying drawing disclosure of that.
Claims (9)
- A kind of 1. beer Spirit production system, it is characterised in that：Including destilling tower, return solidifying device, condensing unit, water-bath chuck And heater, destilling tower include some tower sections on bottom Chu Jiu rooms and top, the distillation tower bottom storage wine room is installed on water Bathe in chuck, the water-bath chuck bottom sets the heater, destilling tower top drum section, return solidifying device and condensing unit according to Secondary connection, the storage wine room are provided with wine liquid import, wine liquid outlet and steam (vapor) outlet；The condensing unit bottom is provided with to collect and filled Put.
- 2. beer Spirit production system according to claim 1, it is characterised in that：The water-bath chuck bottom is provided with Heat exchanging pipe, water-bath chuck inside carries out circulation by inlet channel, water return pipeline with the heat exchanging pipe and connected, in water inlet pipe DN32 welded type Hygiene Ball Valve A are installed on road, DN32 welded type Hygiene Ball Valves B is installed on water return pipeline.
- 3. beer Spirit production system according to claim 2, it is characterised in that：Decompression is installed on water-bath chuck Valve.
- 4. beer Spirit production system according to claim 2, it is characterised in that：The heater is direct flame Formula heater, including heating chamber, flame gun, heating chamber are located at the bottom in the water-bath chuck, and side is provided with heating chamber Heating gate, heating gate set the flame gun, the external fuel cartridge of flame gun, and flame gun flame heat exchanging tubulation is heated, changed Water density, which diminishes, in hot tubulation flows up, and drives water in water-bath chuck to flow and uniformly heat, chimney is set in heating chamber.
- 5. beer Spirit production system according to claim 1, it is characterised in that：The upper column section of the destilling tower, Return solidifying device, condensing unit is provided with visor and metallic thermometer.
- 6. beer Spirit production system according to claim 1, it is characterised in that：The destilling tower, return solidifying device and Condensing unit is all connected with CIP systems.
- A kind of 7. beer Spirit production technology, it is characterised in that：The production technology comprises the following steps：1) raw materials add：Raw material beer liquid is added in storage wine room, water-bath chuck adds a certain amount of water, condensing unit It is passed through condensed water；2) flames heat：Fuel cartridge is opened, flame gun is lighted, the heat exchanging pipe in heating chamber is heated, in heat exchanging pipe Water density, which diminishes, to be flowed up, and drives water in water-bath chuck to flow and uniformly heat；3) beer distills：The steam pressure that valve regulation water-bath chuck is depressurized by regulating gas switch and water-bath chuck is 0.1- 0.12Mp, carries out distillation processing to raw material beer liquid in storage wine room, in still-process, control overhead temperature 75~ 79 DEG C or so, column bottom temperature is controlled at 100~105 DEG C or so, and temperature control is at 88~92 DEG C in tower；Solidifying device water temperature is returned to exist 60~65 DEG C, 35~40 DEG C of condensing unit water temperature；4) finished products are collected：In condensing unit bottom wine outlet beer Spirit finished product, the wine of beer Spirit finished product are contained with container Precision is 20% to 35%.
- 8. beer Spirit production technology according to claim 7, it is characterised in that：In finished product collection step, collected from The beer Spirit of 8-16 minutes from during Spirit output, its alcoholic strength are 60-65%.
- 9. beer Spirit production technology according to claim 7, it is characterised in that：Described raw material beer liquid is commercially available work Industry beer beer, IPA, Belgian wheat beer or the black beers of stout, alcoholic strength >=2.5% of the commercially available industrial beer beer, IPA alcoholic strength >=6.8%, alcoholic strength >=5.5% of the black beer of alcoholic strength >=4.8%, stout of Belgian wheat beer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711237232.9A CN107828619A (en) | 2017-11-30 | 2017-11-30 | A kind of beer Spirit production system and technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711237232.9A CN107828619A (en) | 2017-11-30 | 2017-11-30 | A kind of beer Spirit production system and technique |
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| Publication Number | Publication Date |
|---|---|
| CN107828619A true CN107828619A (en) | 2018-03-23 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711237232.9A Pending CN107828619A (en) | 2017-11-30 | 2017-11-30 | A kind of beer Spirit production system and technique |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108410681A (en) * | 2018-06-19 | 2018-08-17 | 青岛啤酒股份有限公司 | A kind of production method and gained hops Spirit of hops Spirit |
| CN108753554A (en) * | 2018-08-09 | 2018-11-06 | 遵义市永宏金属设备有限公司 | Spirit brewing wine rice steamer |
| WO2022039084A1 (en) * | 2020-08-18 | 2022-02-24 | アサヒグループホールディングス株式会社 | Distilled liquid and flavor enhancer for beer tasting beverage |
| AT17440U1 (en) * | 2020-03-30 | 2022-04-15 | Ulrich Kothe | Conversion kit for a brewing system as well as a combined brewing and distilling system |
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| GB278211A (en) * | 1926-11-29 | 1927-10-06 | Us Ind Alcohol Co | Improvement in process for the distillation of alcohol |
| US4286066A (en) * | 1980-06-24 | 1981-08-25 | Butler Robert S | Continuous fermentation and distillation apparatus |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108410681A (en) * | 2018-06-19 | 2018-08-17 | 青岛啤酒股份有限公司 | A kind of production method and gained hops Spirit of hops Spirit |
| CN108753554A (en) * | 2018-08-09 | 2018-11-06 | 遵义市永宏金属设备有限公司 | Spirit brewing wine rice steamer |
| AT17440U1 (en) * | 2020-03-30 | 2022-04-15 | Ulrich Kothe | Conversion kit for a brewing system as well as a combined brewing and distilling system |
| WO2022039084A1 (en) * | 2020-08-18 | 2022-02-24 | アサヒグループホールディングス株式会社 | Distilled liquid and flavor enhancer for beer tasting beverage |
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