CN108823050A - A kind of brewing system of vodka and GIN wine - Google Patents
A kind of brewing system of vodka and GIN wine Download PDFInfo
- Publication number
- CN108823050A CN108823050A CN201810510389.2A CN201810510389A CN108823050A CN 108823050 A CN108823050 A CN 108823050A CN 201810510389 A CN201810510389 A CN 201810510389A CN 108823050 A CN108823050 A CN 108823050A
- Authority
- CN
- China
- Prior art keywords
- rectifying
- slightly
- wine
- gin
- downspout
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12G—WINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
- C12G3/00—Preparation of other alcoholic beverages
- C12G3/02—Preparation of other alcoholic beverages by fermentation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a kind of vodka and the brewing systems of GIN wine, including pulverizer, saccharifying tank, installation for fermenting and distilling apparatus；The pulverizer is connected by vertical conveyer with saccharifying tank, and the saccharifying tank, installation for fermenting and distilling apparatus are sequentially connected by pipeline, and the distilling apparatus includes thick distillation unit and rectifier unit；The thick distillation unit include it is sequentially connected slightly evaporate alembic, slightly evaporate condenser and slightly evaporate collecting tank, it is described slightly evaporate alembic also respectively by two triple valves and GIN wine tower, thick evaporate fractionating column and connect；The rectifier unit includes sequentially connected rectifying alembic, rectifying condenser and rectifying collecting tank, and the rectifying alembic is also connect by two triple valves with high-rise rectifying fractionating column, low layer rectifying fractionating column respectively.Rationally, saccharification result is good, can select different distillation structures to make different types of wine according to production needs, be conducive to industrialized production application for structure of the invention design.
Description
Technical field
The present invention relates to brewing technical fields, and in particular to the brewing system of a kind of vodka and GIN wine.
Background technique
Wine brewing is the process using microbial fermentation production alcoholic beverage containing a certain concentration.Liquor-making raw material and wine brewing container,
It is two prerequisites of cereal wine brewing.Wherein the brew of white wine is mostly using starch-containing substance as raw material, as sorghum, corn, barley,
Wheat, rice, Peas etc., brewing process are broadly divided into two steps：It is to use aspergillus oryzae, aspergillus niger, aspergillus flavus etc. by starch first
Resolve into carbohydrate, referred to as saccharifying；Glucose fermentation is generated alcohol again by saccharomycete by second step, the thick flavor in white wine,
More esters, advanced esters, volatility free acid, acetaldehyde and furfural etc. are mainly also generated during the fermentation, white wine
Alcohol content is generally at 60 degree or more.
And vodka is also to belong to one of drinks, generallys use corn or potato is that raw material is made,
The technique of brewing mainly includes the following steps：Raw material crushing-saccharification-fermentation-distillation-storage.Wherein, corn or potato
Saccharifying, fermentation process and distillation process are all very big to the qualitative effects of the whiskey finally led to.For corn or horse
For bell potato saccharifying, the phenomenon that saccharifying tank in the prior art is easy to appear material coking and influence saccharification result；For
For fermentation process, fermentor in the prior art is easy to appear due to the uneven caused material of each position temperature of charge control
The different situation of ferment effect is to affect the quality of final product；For distillation process, in the prior art in order to
Enough the brewing better wine of mouthfeel generally can all carry out distilling twice or three times higher to obtain purity in distillation process
Wine, carry out repeatedly distill used by equipment situation generally comprise two ways at present, one is using a distiller to one
Alcohol after secondary distillation carries out reflux redistillation to realize second distillation；Another kind uses two distillers, is slightly to evaporate respectively
Distiller and rectifying distiller successively distill alcohol twice.
For the distillation mode using two distillers, a simple distillation only is carried out to alcohol due to slightly evaporating distiller,
Therefore the designed most structure of distiller that slightly evaporates is too simple in the prior art, has a single function, meanwhile, for brewing different product
For the drinks of kind, the required structure for slightly evaporating distiller can be had a certain difference, when the same manufacturer needs
When producing different types of wine, then need even to need to use more differences to slightly evaporating distiller and constantly being adjusted
Type slightly evaporates distiller, thus wastes a large amount of time cost, human cost and fund cost；And for using two steamings
For the distillation mode for evaporating device, entire distillation process also resides in rectifying distiller, existing rectifying for the control of alcohol purity
Although distiller can distill out the higher alcohol of concentration, a kind of alcohol that the rectifying distiller of specification is distilled is pure
Degree is limited in scope, and large range of change can not be carried out to required alcohol purity according to actual needs, especially for alcohol
In the case where purity requirement more harshness, rectifying distiller in the prior art is unable to meet production demand.
Summary of the invention
The present invention to solve the above-mentioned problems, provides a kind of reasonable in design, and saccharification result is good, can be according to production
The brewing system for needing to select different distillation structures to make different type wine.
The present invention adopts the following technical scheme that：
The brewing system of a kind of vodka and GIN wine, including pulverizer, saccharifying tank, installation for fermenting and distilling apparatus；It is described
Pulverizer is connected by vertical conveyer with saccharifying tank, and the saccharifying tank, installation for fermenting and distilling apparatus are successively connected by pipeline
It connects, the distilling apparatus includes thick distillation unit and rectifier unit；
The thick distillation unit includes slightly evaporating alembic, GIN wine tower, slightly evaporating fractionating column, slightly evaporate condenser and slightly evaporate collecting tank,
It is described slightly evaporate to be equipped at the top of alembic slightly evaporate downspout, it is described slightly to evaporate on downspout far from the end for slightly evaporating alembic one end and thick
Condenser is evaporated to be connected, it is described slightly to evaporate downspout also respectively by being set to two triple valves and GIN wine that slightly evaporate on downspout
Tower slightly evaporates fractionating column and is connected, described slightly to evaporate condenser and thick evaporate collecting tank and be connected；
The rectifier unit include rectifying alembic, high-rise rectifying fractionating column, low layer rectifying fractionating column, rectifying condenser and
Rectifying collecting tank, the top of the rectifying alembic are equipped with rectifying downspout, separate rectifying alembic on the rectifying downspout
The end of one end is connected with rectifying condenser, and the rectifying downspout is also respectively by be set on rectifying downspout two
Triple valve is connected with high-rise rectifying fractionating column, low layer rectifying fractionating column, and the rectifying evaporates condenser and is connected with rectifying collecting tank
It is logical.
As a preferred technical solution of the present invention, rabbling mechanism, the rabbling mechanism packet are equipped in the saccharifying tank
Include the agitating unit being set to inside saccharifying tank, the shaft being fixed on agitating unit and the electricity for being set to saccharifying tank top outer
The top of machine, the shaft is fixedly connected through saccharifying tank and with motor.
As a preferred technical solution of the present invention, the agitating unit include the fixed link being fixed in shaft and
It is set to the first mixing part and the second mixing part in fixed link, first mixing part and the second mixing part are respectively arranged at shaft
Opposite sides position at, first mixing part includes several equally distributed first stirring rods, first stirring rod
Medium position at be " W " character form structure, second mixing part includes several equally distributed second stirring rods, described the
Two stirring rods are equipped with several along the equally distributed stirring block of length direction of the second stirring rod, and the stirring block is three
Corner-shape structure.
As a preferred technical solution of the present invention, the GIN wine tower is equipped with GIN wine feed inlet and GIN wine discharges
Mouthful, the GIN wine feed inlet pass through slightly evaporate triple valve on downspout and it is thick evaporate downspout and be connected, the GIN wine discharge port
It directly evaporates downspout by pipeline and slightly and is connected, inside the GIN wine tower and positioned at GIN wine feed inlet and GIN wine discharge port
Between position at be equipped with filter layer, the filter layer be equipped with juniperko either plant perfume.
It is described slightly to evaporate fractionating column and evaporate feed inlet equipped with thick fraction as a preferred technical solution of the present invention, it is described
Thick fraction evaporate feed inlet pass through slightly evaporate triple valve on downspout and it is thick evaporate downspout and be connected, the thick fraction evaporates top of tower and sets
The thick fraction condenser for having and slightly evaporating fractionating column and being connected is equipped with thick fraction at the top of the thick fraction condenser and coagulates liquid outlet, described thick
Fraction coagulates liquid outlet and slightly evaporates downspout to be directly connected to by pipeline.
As a preferred technical solution of the present invention, the high level rectifying fractionating column is equipped with high-rise rectifying fractionation charging
Mouthful, the high level rectifying fractionation feed inlet is connected by the triple valve on rectifying downspout with rectifying downspout, the high level
The high-rise rectifying segregator being connected with high-rise rectifying fractionating column, the high level rectifying segregator top are equipped at the top of rectifying fractionating column
Portion is equipped with high-rise rectifying and segregates liquid outlet, and the high level rectifying fractional condensation liquid outlet and rectifying evaporate downspout and directly connected by pipeline
It connects.
As a preferred technical solution of the present invention, the low layer rectifying fractionating column is equipped with low layer rectifying fractionation charging
Mouthful, the low layer rectifying fractionation feed inlet is connected by the triple valve on rectifying downspout with rectifying downspout, the low layer
The low layer rectifying segregator being connected with low layer rectifying fractionating column, the low layer rectifying segregator top are equipped at the top of rectifying fractionating column
Portion is equipped with high-rise rectifying and segregates liquid outlet, and the high level rectifying fractional condensation liquid outlet and rectifying evaporate downspout and directly connected by pipeline
It connects.
The beneficial effects of the invention are as follows：
1, structure of the invention design rationally, is provided with the rabbling mechanism inside saccharifying tank and makes material in heating process
In be uniformly heated, can effectively avoid coking phenomenon caused by material hot-spot, gained produces after improving material saccharification
The quality of product；
2, the thick distillation unit that the present invention is arranged can provide convenience to produce different drinks kinds, so that distiller ontology
Function is more diversified；And be arranged GIN wine tower, slightly evaporate fractionating column and pass through triple valve respectively and slightly evaporate drop on alembic with slightly evaporating
Liquid pipe is connected, and according to the circulating direction for needing regulating three-way valve of actual production drinks kind and then can control drop when use
The flow direction of alcohol steam in liquid pipe, whole operation process are simple, convenient and fast；
3, the rectifier unit that the present invention is arranged can effectively improve resulting alcohol purity after distilling apparatus distillation；Simultaneously
High-rise rectifying fractionating column, low layer rectifying fractionating column pass through triple valve respectively and are connected with the rectifying downspout on rectifying alembic,
It can choose whether to connect high-rise rectifying fractionating column and low layer rectifying fractionating column according to actual needs when use, to reach control
The purpose of alcohol purity (then connects high-rise rectifying fractionating column, low layer rectifying fractionating column when needing the alcohol of higher degree to essence
Alcohol after evaporating alembic distillation carries out further vapor-liquid separation, then distills rectifying when not needing the alcohol of higher degree
Alcohol after tank distillation is fed directly to be condensed in rectifying condenser), whole operation process is simple, convenient and fast.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the brewing system of a kind of vodka of the present invention and GIN wine
Fig. 2 is the structural schematic diagram of saccharifying tank of the present invention；
Fig. 3 is the structural schematic diagram of the thick distillation unit of the present invention；
Fig. 4 is the structural schematic diagram of rectifier unit of the present invention；
Symbol description in figure：
Pulverizer 1, saccharifying tank 2, vertical conveyer 3, fermentor 4 slightly evaporate alembic 5, and GIN wine tower 6 slightly evaporates fractionating column 7,
Condenser 8 slightly is evaporated, slightly evaporates collecting tank 9, slightly evaporates downspout 10, rectifying alembic 11, high-rise rectifying fractionating column 12, low layer rectifying point
Evaporate tower 13, rectifying condenser 14, rectifying collecting tank 15, rectifying downspout 16, shaft 17, motor 18, fixed link 19, the first stirring
Bar 20, the second stirring rod 21, stirring block 22, GIN wine feed inlet 23, GIN wine discharge port 24, filter layer 25, thick fraction evaporates charging
Mouth 26, thick fraction condenser 27, thick fraction coagulate liquid outlet 28, and high-rise rectifying is fractionated feed inlet 29, and high-rise rectifying segregator 30 is high-rise
Rectifying segregates liquid outlet 31, and low layer rectifying is fractionated feed inlet 32, low layer rectifying segregator 33, and low layer rectifying segregates liquid outlet 34.
Specific embodiment
Presently in connection with attached drawing, the present invention will be described in further detail.
As shown in Figures 1 to 4, the brewing system of a kind of vodka and GIN wine, including pulverizer 1, saccharifying tank 2, fermentation dress
It sets and distilling apparatus；
The top of the saccharifying tank 2 is equipped with saccharification feed inlet, and the pulverizer 1 passes through vertical conveyer 3 and saccharification charging
The material that mouth is connected for crushing in by pulverizer 1, which is delivered in saccharifying tank 2, carries out saccharification filtering, the saccharifying tank 2
Bottom is equipped with saccharification discharge port；The installation for fermenting includes five fermentors 4 parallel with one another by pipeline, the fermentor 4
Side wall on fermentation feed inlet is equipped at the position of bottom end, the saccharification discharge port is connected with the feed inlet that ferments by pipeline
It connects, the pipeline between the saccharification discharge port and the feed inlet that ferments is equipped with mobile pump vehicle in order to flow out from saccharification discharge port
Saccharified liquid be delivered in fermentor 4 and ferment out of fermentation feed inlet, the bottom of the fermentor 4 is equipped with fermentation discharging
Mouthful；
The distilling apparatus includes thick distillation unit and rectifier unit；
The thick distillation unit includes slightly evaporating alembic 5, GIN wine tower 6, slightly evaporating fractionating column 7, slightly evaporate condenser 8 and slightly evaporate receipts
Collect tank 9, the thick top for evaporating alembic 5, which is equipped with, slightly evaporates downspout 10, and described slightly evaporate evaporates alembic 5 far from thick on downspout 10
The end of one end is connected with condenser 8 is slightly evaporated in order to will slightly evaporate and distill resulting low-concentration ethanol in alembic 5 and be delivered to
It slightly evaporates and is condensed in condenser 8；It is described slightly to evaporate downspout 10 also respectively by being set to two three slightly evaporated on downspout 10
Port valve and GIN wine tower 6 slightly evaporate fractionating column 7 and are connected, so as to slightly evaporate two triple valve controls on downspout 10 by control
System slightly evaporates the circulating direction of the low-concentration ethanol in downspout 10；Condenser 8 and the thick collecting tank 9 that evaporates of slightly evaporating passes through pipeline phase
Connection is cached in collecting tank 9 so that slightly evaporating the low-concentration ethanol condensed in condenser 8 and being able to enter slightly to evaporate；
The rectifier unit includes that rectifying alembic 11, high-rise rectifying fractionating column 12, low layer rectifying fractionating column 13, rectifying are cold
The top of condenser 14 and rectifying collecting tank 15, the rectifying alembic 11 is equipped with rectifying downspout 16, the rectifying downspout 16
The upper end far from 11 one end of rectifying alembic is connected with rectifying condenser 14, in order to distill institute in rectifying alembic 11
The alcohol in high concentration obtained, which is delivered in rectifying condenser 14, to be condensed；The rectifying downspout 16 is also respectively by being set to essence
It evaporates two on downspout 16 triple valves to be connected with high-rise rectifying fractionating column 12, low layer rectifying fractionating column 13, so as to logical
Cross the circulating direction of the alcohol in high concentration in two triple valves control rectifying downspout 16 on control rectifying downspout 16；It is described
Rectifying evaporates condenser 14 and is connected with rectifying collecting tank 15, so that the alcohol in high concentration condensed in rectifying condenser 14 can be into
Enter and is cached in rectifying collecting tank 15；
It is equipped with rabbling mechanism in the saccharifying tank 2, the rabbling mechanism includes the stirring list being set to inside saccharifying tank 2
Member, the shaft 17 being fixed on agitating unit and the motor 18 for being set to 2 top outer of saccharifying tank, the top of the shaft 17 is passed through
It is through at saccharifying tank 2 and is fixedly connected with motor 18；
The agitating unit includes the fixed link 19 being fixed in shaft 17 and is set in fixed link 19 first stirring
Portion and the second mixing part, first mixing part and the second mixing part are respectively arranged at the opposite sides position of shaft 17, institute
Stating the first mixing part includes six equally distributed first stirring rods 20, is " W " at the medium position of first stirring rod 20
Character form structure, second mixing part include six equally distributed second stirring rods 21, and second stirring rod 21 is equipped with
, along the equally distributed stirring block 22 of length direction of the second stirring rod 21, the stirring block 22 is inverted-triangular knot for several
Structure；The agitating unit using be set to the different mixing parts of 17 opposite sides of shaft respectively to the material in saccharifying tank 2 into
The stirring shearing in the horizontal and vertical direction of row, so that can not only enhance the degree of being heated evenly of material can also further increase object
The saccharification result of material；
On lateral wall on the GIN wine tower 6 close to lower end position at be equipped with GIN wine feed inlet 23, the GIN wine into
Material mouth 23 passes through the triple valve slightly evaporated on downspout 10 and is connected with downspout 10 is slightly evaporated so as to real by control triple valve
Now whether the low-concentration ethanol slightly evaporated in downspout 10 is transported in GIN wine tower 6, is leaned on the lateral wall of the GIN wine tower 61
GIN wine discharge port 24 is equipped at the position of nearly upper end, the GIN wine discharge port 24 directly evaporates 10 phase of downspout by pipeline and slightly
Connection slightly evaporates drop in order to enter in GIN wine tower 6 after low-concentration ethanol is reacted in GIN wine tower 6 to enter directly into
Continue previously to have conveyed in liquid pipe 10, inside the GIN wine tower 6 and between GIN wine feed inlet 23 and GIN wine discharge port 23
Filter layer 25 is equipped at position, the filter layer 25 is equipped with for producing difference to low-concentration ethanol steam steaming
The juniperko of type wine either plant perfume；
The position slightly evaporated on the lateral wall of fractionating column 7 close to lower end is equipped with thick fraction and evaporates feed inlet 26, described slightly to evaporate
Fractionation feed inlet 26, which passes through, slightly evaporates another triple valve on downspout 10 and the thick downspout 10 that evaporates is connected so as to pass through
Whether control triple valve is realized to be transported to the low-concentration ethanol slightly evaporated in downspout 10 slightly to evaporate in fractionating column 7 and be carried out further
Fractionation, it is described slightly to evaporate the thick fraction condenser 27 for being equipped at the top of fractionating column 7 and slightly evaporating fractionating column 7 and being connected, the thick fraction condenser
27 top is equipped with thick fraction and coagulates liquid outlet 28, and the thick fraction coagulates liquid outlet 28 and slightly evaporates downspout 10 directly to be connected by pipeline
It connects；
It is equipped with high-rise rectifying at the position of lower end on the side wall of the high level rectifying fractionating column 12 and is fractionated feed inlet 29,
The high level rectifying fractionation feed inlet 29 by the triple valve on rectifying downspout 16 be connected with rectifying downspout 16 so as to
It is enough whether the alcohol in high concentration in rectifying downspout 16 to be transported in high-rise rectifying fractionating column 12 by the realization of control triple valve
It is further fractionated, the top of the high level rectifying fractionating column 12 is equipped with the high level being connected with high-rise rectifying fractionating column 12
Rectifying segregator 30 is equipped with high-rise rectifying at the top of the high level rectifying segregator 30 and segregates liquid outlet 31, the high level rectifying point
Solidifying liquid outlet 31 and rectifying evaporate downspout 16 and are directly connected to by pipeline.
Position on the lateral wall of the low layer rectifying fractionating column 13 close to lower end is equipped with low layer rectifying and is fractionated feed inlet 32,
Low layer rectifying fractionation feed inlet 32 by the triple valve on rectifying downspout be connected with rectifying downspout 16 so as to
By control triple valve realize whether by the alcohol in high concentration in rectifying downspout 16 be transported in low layer rectifying fractionating column 13 into
Row is further to be fractionated, and the low layer essence being connected with low layer rectifying fractionating column 13 is equipped at the top of the low layer rectifying fractionating column 13
Fraction condenser 33 is equipped with high-rise rectifying at the top of the low layer rectifying segregator 33 and segregates liquid outlet 34, the high level rectifying fractional condensation
34 mouthfuls of liquid and rectifying evaporate downspout 16 and are directly connected to by pipeline out.
The technique brewing process of the present embodiment is summarized as follows：
Mainly comprise the following processes：Raw material crushing-saccharification-fermentation-distillation；
One, raw material crushing process：
Dried raw material (corn either potato) is crushed using pulverizer 1；
Two, saccharifying：
Pure water is passed through in saccharifying tank 2 first, and the pure water in saccharifying tank 2 is heated, when the temperature of pure water
When degree reaches 65 DEG C, the raw material crushed in pulverizer 1 is delivered to by vertical conveyer 3 and carries out being saccharified in saccharifying tank 2
Filter is to obtain corn either potato juice；
Three, fermentation process：
The corn either potato juice obtained after saccharification filtering will be delivered in fermentor 4, the jade in fermentor 4
Yeast is put into fermentor 4 jade to ferment with after being fermented when being cooled to set temperature by rice either potato juice again
Rice either potato juice (i.e. concentration be about 7.5% alcohol), time of the fermentation is 48h；
Four, distillation process：
1, distillation is slightly evaporated：
By after fermentation corn or potato juice be delivered to and slightly evaporate in alembic 5 and distill, it is described slightly to evaporate alembic 5
Low-concentration ethanol steam caused by interior distillation, which enters, slightly to be evaporated in downspout 10；It is at this time vodka if necessary to the drinks of production
When wine, then by slightly evaporate triple valve on downspout 10 close slightly evaporate connection between downspout 10 and GIN wine tower 6 and with it is thick
Evaporate the connection between fractionating column 7 so that the low-concentration ethanol steam for slightly evaporating in downspout 10 be directly entered slightly evaporate in condenser 8 into
Row condensation；
When drinks if necessary to production is GIN wine, then descending liquid is slightly evaporated by slightly evaporating the triple valve on downspout 10 and opening
Connection between pipe 10 and GIN wine tower and with slightly evaporate the connection between fractionating column 7 so that slightly evaporating the low concentration in downspout 10
Alcohol steam initially enter inside GIN wine tower 6 to inside GIN wine tower 6 juniperko or other plant fragrance fumigate, with
So that low-concentration ethanol is capable of forming different tastes, it is stifling after low-concentration ethanol pass through slightly to evaporate downspout 10 and enter again and slightly evaporate
It is further fractionated inside fractionating column 7, is slightly evaporated slightly evaporating the low-concentration ethanol steam after being fractionated inside fractionating column 7 and entering back into
The thick fraction condenser 26 at 7 top of fractionating column carries out a vapor-liquid separation to improve the purity of low-concentration ethanol, a vapor-liquid separation
Alcohol steam afterwards is slightly evaporated in condenser 8 and is condensed to obtain low-concentration ethanol again by slightly evaporating downspout 10 and finally enter
Liquid；
1, rectifying is distilled：
It is distilled slightly evaporating low-concentration ethanol liquid obtained in distillation and being delivered in rectifying alembic 11, the rectifying
Alcohol in high concentration steam caused by distilling in alembic 11 enters in rectifying downspout 16；At this time if necessary to the drinks of production
When purity requirement is not very high, then rectifying downspout 16 and high-rise rectifying point are closed by the triple valve on rectifying downspout 16
The connection between tower 12 and the connection between low layer rectifying fractionating column 13 are evaporated, so that the high wine in rectifying downspout 16
Smart steam is directly entered in rectifying condenser 14 and is condensed；
If necessary to production drinks purity requirement it is very high when, then essence is opened by the triple valve on rectifying downspout 16
The connection between downspout 16 and high-rise rectifying fractionating column 12 and the connection between low layer rectifying fractionating column 13 are evaporated, so that smart
It evaporates the alcohol in high concentration steam in downspout 16 and initially enters and be further fractionated in high-rise rectifying fractionating column 12, in high level
Alcohol in high concentration steam after being fractionated inside rectifying fractionating column 12 enters back into the high-rise rectifying point at high-rise 12 top of rectifying fractionating column
Condenser 30 carries out secondary vapor-liquid separation to improve the purity of alcohol in high concentration, and the alcohol in high concentration after secondary vapor-liquid separation passes through again
Rectifying downspout 16, which enters inside low layer rectifying fractionating column 13, to be further fractionated, inside low layer rectifying fractionating column 13
The bottom rectifying segregator 33 that alcohol in high concentration steam after fractionation enters back into 13 top of low layer rectifying fractionating column carries out vapour three times
Liquid is separated to further increase the purity of alcohol in high concentration, and the alcohol steam after vapor-liquid separation is again by through evaporating downspout three times
16 finally enter and are condensed in rectifying condenser 14 to obtain ultrahigh concentration alcohol liquid；Finally it is delivered to rectifying collecting tank 15
Inside cached.
Finally it should be noted that：These embodiments are merely to illustrate the present invention and do not limit the scope of the invention.In addition,
To those of ordinary skill in the art, other various forms of variations or change can also be made on the basis of the above description
It is dynamic.There is no necessity and possibility to exhaust all the enbodiments.And the obvious variation or change thus amplified out
It is dynamic to be still in the protection scope of this invention.
Claims (7)
1. the brewing system of a kind of vodka and GIN wine, including pulverizer (1), saccharifying tank (2), installation for fermenting and distilling apparatus；
It is characterized in that：The pulverizer (1) is connected by vertical conveyer (3) and saccharifying tank (2), the saccharifying tank (2), fermentation dress
It sets and is sequentially connected with distilling apparatus by pipeline, the distilling apparatus includes thick distillation unit and rectifier unit；
The thick distillation unit include slightly evaporate alembic (5), GIN wine tower (6), slightly evaporate fractionating column (7), slightly evaporate condenser (8) and slightly
Evaporate collecting tank (9), it is described slightly evaporate to be equipped at the top of alembic (5) slightly evaporate downspout (10), it is described it is thick evaporate it is separate on downspout (10)
It slightly evaporates the end of alembic (5) one end and slightly evaporates condenser (8) and be connected, it is described thick to evaporate downspout (10) and also pass through setting respectively
Fractionating column (7) is evaporated with GIN wine tower (6), slightly in thick two triple valves evaporated on downspout (10) to be connected, it is described slightly to evaporate condenser
(8) with slightly evaporate collecting tank (9) and be connected；
The rectifier unit includes rectifying alembic (11), high-rise rectifying fractionating column (12), low layer rectifying fractionating column (13), rectifying
The top of condenser (14) and rectifying collecting tank (15), the rectifying alembic (11) is equipped with rectifying downspout (16), the essence
It evaporates the end on downspout (16) far from rectifying alembic (11) one end to be connected with rectifying condenser (14), the rectifying descending liquid
Pipe (16) also passes through two triple valves being set on rectifying downspout (16) and high-rise rectifying fractionating column (12), low layer essence respectively
It evaporates fractionating column (13) to be connected, the rectifying evaporates condenser (14) and is connected with rectifying collecting tank (15).
2. the brewing system of a kind of vodka according to claim 1 and GIN wine, it is characterised in that：The saccharifying tank (2)
Interior to be equipped with rabbling mechanism, the rabbling mechanism includes being set to the internal agitating unit of saccharifying tank (2), being fixed on agitating unit
Shaft (17) and be set to the motor (18) of saccharifying tank (2) top outer, the top of the shaft (17) is through saccharifying tank
(2) and with motor (18) it is fixedly connected.
3. the brewing system of a kind of vodka according to claim 2 and GIN wine, it is characterised in that：The agitating unit
Including the fixed link (19) being fixed on shaft (17) and it is set to the first mixing part and the second mixing part on fixed link (19),
First mixing part and the second mixing part are respectively arranged at the opposite sides position of shaft (17), the first mixing part packet
Several equally distributed first stirring rods (20) are included, are " W " character form structure at the medium position of first stirring rod (20),
Second mixing part includes several equally distributed second stirring rods (21), and second stirring rod (21) is equipped with several
A equally distributed stirring block of length direction (22) along the second stirring rod (21), the stirring block (22) are inverted-triangular knot
Structure.
4. the brewing system of a kind of vodka according to claim 1 and GIN wine, it is characterised in that：The GIN wine tower
(6) it is equipped with GIN wine feed inlet (23) and GIN wine discharge port (24), the GIN wine feed inlet (23) is by slightly evaporating downspout
(10) triple valve on slightly evaporate downspout (10) and be connected, the GIN wine discharge port (24) directly evaporates drop by pipeline and slightly
Liquid pipe (10) is connected, and the GIN wine tower (6) is internal and between GIN wine feed inlet (23) and GIN wine discharge port (24)
Filter layer (25) are equipped at position, the filter layer (25) is equipped with juniperko or plant perfume.
5. the brewing system of a kind of vodka according to claim 1 and GIN wine, it is characterised in that：The thick fraction evaporates
Tower (7) is equipped with thick fraction and evaporates feed inlet (26), and the thick fraction evaporates feed inlet (26) and passes through three slightly evaporated on downspout (10)
Port valve with slightly evaporate downspout (10) and be connected, it is described slightly evaporate be equipped at the top of fractionating column (7) with slightly evaporate fractionating column (7) be connected it is thick
Fraction condenser (27), thick fraction condenser (27) top are equipped with thick fraction and coagulate liquid outlet (28), and the thick fraction coagulates liquid outlet
(28) and slightly downspout (10) is evaporated to be directly connected to by pipeline.
6. the brewing system of a kind of vodka according to claim 1 and GIN wine, it is characterised in that：The high level rectifying
Fractionating column (12) is equipped with high-rise rectifying and is fractionated feed inlet (29), and high level rectifying fractionation feed inlet (29) passes through rectifying descending liquid
Triple valve on pipe (16) is connected with rectifying downspout (16), is equipped at the top of the high level rectifying fractionating column (12) and high level essence
The high-rise rectifying segregator (30) that fractionating column (12) is connected is evaporated, high-rise rectifying is equipped at the top of the high level rectifying segregator (30)
It segregates liquid outlet (31), high level rectifying fractional condensation liquid outlet (31) and rectifying evaporate downspout (16) and is directly connected to by pipeline.
7. the brewing system of a kind of vodka according to claim 1 and GIN wine, it is characterised in that：The low layer rectifying
Fractionating column (13) is equipped with low layer rectifying fractionation feed inlet (32), and low layer rectifying fractionation feed inlet (32) passes through rectifying descending liquid
Triple valve on pipe (16) is connected with rectifying downspout (16), and (13) are equipped with and low layer essence at the top of the low layer rectifying fractionating column
The low layer rectifying segregator (33) that fractionating column (13) is connected is evaporated, high-rise rectifying is equipped at the top of the low layer rectifying segregator (33)
It segregates liquid outlet (34), high level rectifying fractional condensation liquid outlet (34) and rectifying evaporate downspout (16) and is directly connected to by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810510389.2A CN108823050A (en) | 2018-05-24 | 2018-05-24 | A kind of brewing system of vodka and GIN wine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810510389.2A CN108823050A (en) | 2018-05-24 | 2018-05-24 | A kind of brewing system of vodka and GIN wine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108823050A true CN108823050A (en) | 2018-11-16 |
Family
ID=64145444
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810510389.2A Pending CN108823050A (en) | 2018-05-24 | 2018-05-24 | A kind of brewing system of vodka and GIN wine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108823050A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111073780A (en) * | 2019-12-11 | 2020-04-28 | 温州大宇科技有限公司 | Traditional whisky brewing device capable of improving yield and production process thereof |
| CN113481077A (en) * | 2021-08-04 | 2021-10-08 | 杭州正久机械制造股份有限公司 | Multifunctional distillation device |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104342358A (en) * | 2013-08-07 | 2015-02-11 | 国家电网公司 | Fermentation fuel reactor and fermentation fuel production method |
| CN104357315A (en) * | 2014-10-17 | 2015-02-18 | 姜蓉生 | Vertical light wine solid-state continuous fermentation equipment and process |
| CN204918549U (en) * | 2015-08-06 | 2015-12-30 | 山东渠风食品科技有限公司 | Equipment of starch raffinate production alcohol |
| CN207031423U (en) * | 2017-07-04 | 2018-02-23 | 王嘉洋 | A kind of alcohol production device |
-
2018
- 2018-05-24 CN CN201810510389.2A patent/CN108823050A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104342358A (en) * | 2013-08-07 | 2015-02-11 | 国家电网公司 | Fermentation fuel reactor and fermentation fuel production method |
| CN104357315A (en) * | 2014-10-17 | 2015-02-18 | 姜蓉生 | Vertical light wine solid-state continuous fermentation equipment and process |
| CN204918549U (en) * | 2015-08-06 | 2015-12-30 | 山东渠风食品科技有限公司 | Equipment of starch raffinate production alcohol |
| CN207031423U (en) * | 2017-07-04 | 2018-02-23 | 王嘉洋 | A kind of alcohol production device |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111073780A (en) * | 2019-12-11 | 2020-04-28 | 温州大宇科技有限公司 | Traditional whisky brewing device capable of improving yield and production process thereof |
| CN113481077A (en) * | 2021-08-04 | 2021-10-08 | 杭州正久机械制造股份有限公司 | Multifunctional distillation device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4349628A (en) | Fermentation process for the manufacture of an organic compound | |
| CN108103112A (en) | A kind of technique that alcohol fuel is produced as raw material using cornstarch matter | |
| US10118107B1 (en) | Method and system for distilling alcohol in an alcohol production process | |
| CN101648847B (en) | Composite process of fuel alcohol and edible alcohol | |
| CN102665843A (en) | Systems and methods for alcohol recovery and concentration of stillage by-products | |
| KR20180037880A (en) | The method of distillation and Pot Still of Fermented wine | |
| CN205133573U (en) | Continuous type white spirit distilling machinery | |
| CA1172989A (en) | Multiple effect distillation method and apparatus | |
| CN108531342A (en) | A kind of production method and equipment of the neutral edible product that brews alcohol | |
| CN204702730U (en) | A kind of Novel steam distillation unit for liquor production by liquid fermentation | |
| JP4937050B2 (en) | Method for distillation of single-distilled liquor and apparatus used therefor | |
| CN108905240B (en) | Concentration method in production process of fermented cordyceps sinensis powder | |
| CN108823050A (en) | A kind of brewing system of vodka and GIN wine | |
| CN107058403A (en) | A kind of distiller's grains liquor is used for the method that full amylofermentation prepares ethanol | |
| CN101648848B (en) | Combined production method for fuel alcohol and edible alcohol | |
| CN205295296U (en) | Split type white spirit distiller | |
| US10392590B1 (en) | Method and system for distilling alcohol in an alcohol production process | |
| CN108823019A (en) | A kind of brewing system of whiskey | |
| CN102994304B (en) | Fermentation method and production method of liquor | |
| CN109704920A (en) | From the energy-saving process method and device of low concentration fermentation liquid production alcohol fuel | |
| Sato et al. | Solid‐state ethanol fermentation by means of inert gas circulation | |
| JP3784708B2 (en) | Distillation method and distillation apparatus used therefor | |
| CN208395146U (en) | The continuous distillation plant of liquid phase process Spirit | |
| CN202173793U (en) | Alcohol prefractionator reboiling system using centrifugal clear liquid as cyclic medium | |
| CN1210406C (en) | Method for energy-saving production of alcohol by sugar cane juice fermentation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information |
Address after: 311507 No. 551 Tangchuan Road, Tonglu Economic Development Zone, Tonglu County, Hangzhou City, Zhejiang Province Applicant after: Hangzhou Zhengjiu Machinery Manufacturing Co., Ltd. Address before: 311507 No. 551 Tangchuan Road, Tonglu Economic Development Zone, Tonglu County, Hangzhou City, Zhejiang Province Applicant before: Hangzhou Zhengjiu Machinery Manufacturing Co., Ltd. |
|
| CB02 | Change of applicant information | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181116 |
|
| RJ01 | Rejection of invention patent application after publication |