CN208378840U - A kind of white spirit by solid state method continuous still system - Google Patents
A kind of white spirit by solid state method continuous still system Download PDFInfo
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- CN208378840U CN208378840U CN201820685687.0U CN201820685687U CN208378840U CN 208378840 U CN208378840 U CN 208378840U CN 201820685687 U CN201820685687 U CN 201820685687U CN 208378840 U CN208378840 U CN 208378840U
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- continuous still
- solid state
- white spirit
- state method
- cooler
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Abstract
The utility model discloses a kind of white spirit by solid state method continuous still systems, including feeder, continuous still mechanism and the condensing mechanism being sequentially communicated, and waste residue discharge mechanism are provided with below continuous still mechanism；The condensing mechanism includes the multisection type cooler that cooling temperature successively reduces, and every section of cooler is provided with base liquor collector, and base liquor collector is connected to cooler respectively by down-comer, passes through tracheae connection between adjacent cooler.Condensation is segmented using the utility model wine steam at different temperatures, obtains the base liquor of the different quality condensed under different temperatures.
Description
Technical field
The utility model relates to white liquor distilling apparatus fields, more particularly to a kind of white spirit by solid state method continuous still system.
Background technique
China's liquor production process is all distilled using intermittent uploading in rice steamer since ancient times, as the key during liquor production
Link, due to special technique requirement, this process is generally operated by skilled worker, and working environment is poor, works
Intensity is high, and wine quality is unstable with distillation yield out, becomes the key problem of puzzlement wine enterprise development.Industrial upgrading is pushed, into one
Step improves Business Economic Benefit and competitiveness, just seems particularly necessary.
Utility model content
Mainly solving the technical problems that providing a kind of white spirit by solid state method continuous still system, wine steam exists the utility model
It is segmented condensation under different temperatures, obtains the base liquor of the different quality condensed under different temperatures.
To reach above-mentioned technical purpose, the technical solution adopted in the utility model is as follows:
A kind of white spirit by solid state method continuous still system, it is characterised in that: including be sequentially communicated feeder, continuous still
Mechanism and condensing mechanism, and waste residue discharge mechanism is provided with below continuous still mechanism；The condensing mechanism includes cooling
The multisection type cooler that temperature successively reduces, every section of cooler is provided with base liquor collector, and base liquor collector passes through decline
Pipe is connected to cooler respectively, passes through tracheae connection between adjacent cooler.
Further, the continuous still mechanism include sealed digester, the blender that is arranged in digester, boiling
Pot top is respectively arranged with feed inlet and steam (vapor) outlet.
Further, the feeder is tube-type spiral conveyer, and is connected to the feed inlet at the top of digester.
Further, the steam (vapor) outlet is connected to multisection type cooler.
Further, the blender include the flat material blade being disposed over, the agitation blade that middle part is set and
Discharging blade arranged at the bottom, and three kinds of blades are both connected in same rotation axis.
Further, it is provided with bottom plate below the discharging blade in the digester, there is row's vinasse mouth and several on bottom plate
Steam inlet, each steam inlet are provided with cover board.
Further, the bottom plate is arranged with the bottom pot of connection steam pipe network, is provided with steam pipe and vinasse in the pot of bottom
Discharge screw machine.
Further, the waste residue discharge mechanism includes waste residue discharge belt feeder, plash, and is arranged in plash
Outlet of sewer；Waste residue discharge belt feeder is arranged in boiling pot bottom.
The beneficial effects of the utility model are: being in contrast to the prior art, the utility model changes existing cold
But mode condenses different material using the distribution of staged cooling temperature, respectively obtains the different base liquor of fragrance, each section of base
There is various flavor components in wine, after storing respectively, high quality liquor can be become by mutually blending by different taste.
Detailed description of the invention
Fig. 1 is white spirit by solid state method continuous still system structure diagram provided by the utility model.
Fig. 2 is condensing mechanism structural schematic diagram provided by the utility model.
Marked in the figure: 1 being feeder, 2 being digester, 3 be condensing mechanism, 4 be waste residue discharge belt feeder, 5 being ponding
Pond, 6 be outlet of sewer, 7 be flat material blade, 8 be agitation blade, 9 be discharging blade, 10 be bottom plate, 11 be one-step cooling device, 12
It is three-stage cooling device for two-step cooling device, 13,14 be four sections of coolers, 15 be down-comer, 16 be base liquor collector, 17 was gas
Pipe.
Specific embodiment
The utility model is described further with specific embodiment with reference to the accompanying drawing.
As Figure 1-Figure 2, a kind of white spirit by solid state method continuous still system, including the feeder 1, continuous being sequentially communicated
Mechanism and condensing mechanism 3 are distilled, and is provided with waste residue discharge mechanism below continuous still mechanism；The condensing mechanism 3 wraps
The multisection type cooler that cooling temperature successively reduces is included, every section of cooler is provided with base liquor collector 16, and base liquor collector
16 are connected to cooler respectively by down-comer 15, pass through the connection of tracheae 17 between adjacent cooler.
The continuous still mechanism includes sealed digester 2, the blender being arranged in digester 2,2 top of digester
It is respectively arranged with feed inlet and steam (vapor) outlet.The feeder 1 is tube-type spiral conveyer, and with digester 2 top into
Material mouth connection.
The steam (vapor) outlet is connected to multisection type cooler.The blender includes the flat material blade 7 being disposed over, sets
The agitation blade 8 and discharging blade 9 arranged at the bottom at middle part are set, and three kinds of blades are both connected to same rotation axis
On.It is provided with bottom plate 10 below discharging blade 9 in the digester 2, there is row's vinasse mouth and several steam inlets on bottom plate 10,
Each steam inlet is provided with cover board.The bottom plate 10 is arranged with the bottom pot of connection steam pipe network, is provided with steam in the pot of bottom
Pipe and vinasse discharging screw machine.In order to avoid steam is overflowed from discharging screw machine, it is equipped with valve on discharging screw machine outlet pipe section,
Prevent steam excessive with the material in screw machine and discharge nozzle.
The waste residue discharge mechanism includes waste residue discharge belt feeder 4, plash 5, and the sewage being arranged in plash 5
Outlet 6；Waste residue discharge belt feeder 4 is arranged in 2 bottom of digester.
In actual use, equipment is successively fixed, the steam pipe network designed using regular industrial, and by pipe network and steamed
Boiler furnace connection provides steam to stablize.Fermented grain enters at the top of digester 2 under air-tight state through tube-type spiral conveyer,
Blade 7 is smooth is distributed in digester 2 through flat material for fermented grain, until the fermented grain in digester 2 reaches setting material position.
Then start to distill, initially need to be about 30 minutes into steam distillation when distillation, to the wine evaporating completely in the fermented grain of lower part
After can open discharging main motor, drive discharging paddle that vinasse slag is discharged into discharging screw machine, opening the same of discharging main motor
Vinasse slag is discharged in Shi Qidong vinasse discharging screw machine, vinasse slag is sent into the centralized processing of waste residue pond through waste residue discharge belt feeder 4, together
When also start tube-type spiral conveyer start to distillation steaming bucket in continuous feed.The discharging main motor can meet torque to be any
The conventional motor of design requirement.
Wine steam exports export condensation through 2 top wine steam of digester, and the base liquor of acquisition is continuously, cannot to use biography
System mode, which is segmented, plucks wine, characteristic that can only be different using the boiling point of various fragrance matters in base liquor, using dividing temperature section cooling side
Formula obtains the different base liquor of quality, and the principle is as follows:
Present white liquor distilling steaming bucket mostly uses steam to heat greatly, and 100 DEG C of vapor (steam) temperature or more, pressure about 0.2~0.5 million
Pa.It specifically being distilled in steaming bucket, under pressure environment, the various material compositions in fermented grain relationship can steam by a certain percentage,
The liquor flavor ingredient up to more than 1000 of outflow, mutual boiling point difference are extremely greatly different.Such as: 20 DEG C of formaldehyde, 21 DEG C of acetaldehyde,
64.7 DEG C of methanol, 100.7 DEG C of formic acid, 78.3 DEG C of ethyl alcohol, 118.13 DEG C of ethyl lactate, 77 DEG C of ethyl acetate, ethyl hexylate 167
DEG C, 290 DEG C of glycerol, 100 DEG C of water etc., although various substances are mutually dissolved together in steaming bucket, boiling point is changed,
Distinctive evaporation coefficient is formed, gaseous state is become by liquid in steaming bucket, but these substances go out after steaming bucket with temperature, pressure environment
Change, the proportionate relationship of each material condensation changes again.What in high-temperature region, condensation ratio was most is high boiling substance, with
The component ratio that temperature reduces condensation can be different, and what finally discharge was most is that (such as: Maotai connects the control of wine temperature to low-boiling point material
At 40 DEG C, other breweries connect the control of wine temperature at 30 DEG C, exactly in order not to allow low-boiling harmful substance to condense, fall sulphur to idle discharge
Change the impurity such as hydrogen, formaldehyde, acetaldehyde).
As shown in Fig. 2, cooler is divided at least four sections by the utility model, 11 water temperature of one-step cooling device be adjusted to 79 DEG C~
81 DEG C, mainly cooling water and high boiling substance, these molecular weight of material are big, and boiling point is high, condense first in high temperature section.Such as: cream
The advanced fatty acid ester such as acetoacetic ester, ethyl hexylate, glycerol, they are indispensable in white wine, and can not be too many, excessive vinosity
It is astringent.12 water temperature of two-step cooling device is adjusted to 67 DEG C~69 DEG C, boilers between main 67 DEG C~79 DEG C of cooling, such as: ethyl alcohol,
The medium temperatures boilers such as ethyl acetate.13 water temperature of three-stage cooling device is adjusted to 40~52 DEG C, between main 40 DEG C~67 DEG C of cooling
Compared with low-boiling point material.Four sections of 14 water temperatures of cooler are adjusted to 30 DEG C, low-boiling point material between main 30 DEG C~40 DEG C of cooling.Remaining
30 DEG C of low-boiling point material emptyings below.
Using the different characteristic of these boiling point substances, the wine steam distilled out is successively continuously passed through to temperature difference
Cooler in, i.e. the temperature of change wine steam condensation, pressure environment make them respectively successively in the different cooler of temperature
It is cooling, just respectively obtain the different base liquor of fragrance.There is various flavor components in each section of base liquor, only ratio is different, stores respectively
After depositing, high quality liquor can be become by mutually blending by different taste.
The above description is only the embodiments of the present invention, and therefore it does not limit the scope of the patent of the utility model, all
Using equivalent structure or equivalent flow shift made by utility model specification and accompanying drawing content, it is applied directly or indirectly in it
His relevant technical field, is also included in the patent protection scope of the utility model.
Claims (8)
1. a kind of white spirit by solid state method continuous still system, it is characterised in that: including feeder, the continuous still being sequentially communicated
Structure and condensing mechanism, and waste residue discharge mechanism is provided with below continuous still mechanism；The condensing mechanism includes cooling temperature
The multisection type cooler successively reduced is spent, every section of cooler is provided with base liquor collector, and base liquor collector passes through down-comer
It is connected to respectively with cooler, passed through tracheae connection between adjacent cooler.
2. white spirit by solid state method continuous still system according to claim 1, it is characterised in that: continuous still mechanism packet
The blender for including sealed digester, being arranged in digester, digester top are respectively arranged with feed inlet and steam (vapor) outlet.
3. white spirit by solid state method continuous still system according to claim 1, it is characterised in that: the feeder is tubular type
Screw conveyor, and be connected to the feed inlet at the top of digester.
4. white spirit by solid state method continuous still system according to claim 2, it is characterised in that: the steam (vapor) outlet and multistage
The connection of formula cooler.
5. white spirit by solid state method continuous still system according to claim 2, it is characterised in that: the blender includes setting
Flat material blade above, the agitation blade and discharging blade arranged at the bottom that middle part is set, and three kinds of blades
It is both connected in same rotation axis.
6. white spirit by solid state method continuous still system according to claim 2, it is characterised in that: the discharging in the digester
It is provided with bottom plate below blade, has row's vinasse mouth and several steam inlets, each steam inlet to be provided with cover board on bottom plate.
7. white spirit by solid state method continuous still system according to claim 6, it is characterised in that: the bottom plate is arranged with company
Lead to the bottom pot of steam pipe network, steam pipe and vinasse discharging screw machine are provided in the pot of bottom.
8. white spirit by solid state method continuous still system according to claim 1, it is characterised in that: the waste residue discharge mechanism packet
Include waste residue discharge belt feeder, plash, and the outlet of sewer being arranged in plash；Waste residue discharge belt feeder is arranged in boiling
Pot bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820685687.0U CN208378840U (en) | 2018-05-09 | 2018-05-09 | A kind of white spirit by solid state method continuous still system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820685687.0U CN208378840U (en) | 2018-05-09 | 2018-05-09 | A kind of white spirit by solid state method continuous still system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208378840U true CN208378840U (en) | 2019-01-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820685687.0U Expired - Fee Related CN208378840U (en) | 2018-05-09 | 2018-05-09 | A kind of white spirit by solid state method continuous still system |
Country Status (1)
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114214162A (en) * | 2021-12-09 | 2022-03-22 | 广东省九江酒厂有限公司 | White spirit distillation device and method for reducing ethyl lactate content |
| CN114606090A (en) * | 2021-04-21 | 2022-06-10 | 滦南建国科技有限公司 | Device for forcibly removing formaldehyde and methanol for liquor making by distillation |
| CN114752461A (en) * | 2022-05-26 | 2022-07-15 | 四川水井坊股份有限公司 | Device and method for segmented liquor picking of white spirit |
-
2018
- 2018-05-09 CN CN201820685687.0U patent/CN208378840U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114606090A (en) * | 2021-04-21 | 2022-06-10 | 滦南建国科技有限公司 | Device for forcibly removing formaldehyde and methanol for liquor making by distillation |
| CN114214162A (en) * | 2021-12-09 | 2022-03-22 | 广东省九江酒厂有限公司 | White spirit distillation device and method for reducing ethyl lactate content |
| CN114214162B (en) * | 2021-12-09 | 2024-06-21 | 广东省九江酒厂有限公司 | White spirit distillation device and distillation method for reducing ethyl lactate content |
| CN114752461A (en) * | 2022-05-26 | 2022-07-15 | 四川水井坊股份有限公司 | Device and method for segmented liquor picking of white spirit |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190115 |