CN106916720B - White wine acid discharge equipment - Google Patents
White wine acid discharge equipment Download PDFInfo
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- CN106916720B CN106916720B CN201710320227.8A CN201710320227A CN106916720B CN 106916720 B CN106916720 B CN 106916720B CN 201710320227 A CN201710320227 A CN 201710320227A CN 106916720 B CN106916720 B CN 106916720B
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- white wine
- main body
- column main
- fractionating column
- acid discharge
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- 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
Abstract
The present invention provides white wine acid discharge equipment, is related to liquor production technical field, including fractionating column main body, condensing unit, reductive jar and liquid collecting tank；Inner chamber is provided with the fractionating column main body, the condensing unit is connected with the fractionating column main body, for condensed steam；And the heater for heating and at least one cold plate for liquid collecting are provided with the inner chamber；The cold plate is connected with condensing the temperature control equipment of plate temperature for controlling, and the cold plate lower end is provided with the collecting tank for collecting liquid on cold plate.White wine acid discharge equipment provided by the invention and white wine acid discharge method can reduce the acidic materials in white wine, make the pH of white wine closer to the pH of healthy human body, so people are when the white wine of same amount is drunk, reduce the injury to human body, the white wine Jing Guo acid discharge has entrance soft simultaneously, it is comfortable after waking up, fume unconspicuous feature small to human body excitant.
Description
Technical field
The present invention relates to liquor production technical field, more particularly, to a kind of white wine acid discharge equipment.
Background technology
The standard of white wine defines：Using Cereals as primary raw material, with Daqu, Chinese yeast or wheat bran and distiller's yeast etc. for diastatic fermentation
Agent, through boiling, saccharification, fermentation, distillation and manufactured Spirit.Also known as liquor, white spirit, aquavit etc..
Vinosity colourless (or micro- Huang) is transparent, and fragrant odour is pure, and entrance is sweet refreshing net, and alcohol content is higher, old through storing
After ripe, there is the compound fragrant based on esters.Using bent class, distiller's yeast as saccharifying ferment, using starchiness (saccharic) raw material,
Through boiling, saccharification, fermentation, distillation, ageing and all kinds of wine blent and brewed.
And said on stricti jurise, it is white wine that the assembled alcoholic drinks blent by edible alcohol and flavorant, which can not be then considered,
And it should be referred to as to contain spirituous beverage.
For each cell of human body all in " immersion " of liquid and the moment keeps balance, cell acid-base value (i.e. pH value) can be with
Detected by way of blood drawing.The normal range (NR) of blood of human body pH value be 7.35~7.45, pH be more than 7.45 when be alkalosis
(alkalosis) it is acid poisoning (acidosis) when, less than 7.35.When pH value is less than 6.9 or higher than 7.7, will give birth to
Critically ill danger.I.e. our body fluid should be in that alkalescent could keep normal physiological function and metabolism.
Grain always is in sour environment during the fermentation, so finished product white wine is acid.It is real with pH test paper
Border measurement test paper color is partially yellow, and acidity value is probably between 4-5.
In order to which people are while drinking, the injury to human body is reduced as far as possible, it is necessary to which the middle acid substance of white wine is removed,
So that pH of the temperature of white wine closer to human body, reduces injury of the white wine to human body.
The content of the invention
It is an object of the invention to provide white wine acid discharge equipment, to alleviate the skill for the injury that drinking white spirit is brought to human body
Art problem.
A kind of white wine acid discharge equipment provided by the invention, including fractionating column main body, condensing unit, reductive jar and liquid collecting tank；
Inner chamber is provided with the fractionating column main body, the condensing unit is connected with the fractionating column main body, for cold
Solidifying steam；And the heater for heating and at least one cold plate for liquid collecting are provided with the inner chamber；
The cold plate is connected with condensing the temperature control equipment of plate temperature for controlling, and is set in the cold plate lower end
The collecting tank for collecting liquid on cold plate is equipped with, the collecting tank is connected by the first connecting tube with the liquid collecting tank；
Charging aperture and discharging opening are provided with the fractionating column main body, the charging aperture horizontal level is not higher than the collection
Liquid bath, the discharging opening are connected by the 3rd connecting tube with the reductive jar；
Venthole and inlet opening are respectively arranged with the fractionating column main body, and the venthole horizontal level is higher than described
Collecting tank, the inlet opening horizontal level are less than the collecting tank；
The condensing unit includes condensation chamber, and radiating tube is provided with the condensation chamber；And on the condensing unit
It is provided with and connects water inlet and delivery port with condensation chamber；
The first condenser pipe is provided with the venthole, the second condenser pipe is provided with the inlet opening, and it is described
First condenser pipe and the second condenser pipe connect with the radiating tube.
Further, ten cold plates, and the corresponding collection of each cold plate are provided with the fractionating column main body
Liquid bath.
Further, at least one liquid collecting tank is connected by the second connecting tube with the reductive jar.
Further, in addition to for detecting the pH monitors of white wine pH in fractionating column main body.
Further, the fractionating column main body lower end is provided with sample tap.
Further, be provided with valve and supercharging device in the 3rd connecting tube, and the valve be arranged on it is described go out
Between material mouth and the supercharging device.
White wine acid discharge equipment provided by the invention can reduce the acidic materials in white wine, make the closer health of pH of white wine
The pH of human body, such people reduce the injury to human body, while the white wine Jing Guo acid discharge has when the white wine of same amount is drunk
Entrance is soft, comfortable after waking up, fume unconspicuous feature small to human body excitant.
The present invention also provides a kind of white wine acid discharge method, and the white wine acid discharge method comprises the following steps：
White wine is added in fractionating column main body, opening heater makes white wine seethe with excitement, and is adjusted by temperature control equipment
The temperature of cold plate, set gradually from bottom to top for 195 DEG C, 180 DEG C, 165 DEG C, 160 DEG C, 150 DEG C, 120 DEG C, 105 DEG C, 90
℃、75℃、60℃；White wine pH is measured more than 6.5 by pH monitors；Discharging opening is opened, the white wine after processing is transported to also
In former tank.
Further, the condensate liquid of 165 DEG C of cold plates, 150 DEG C of cold plates, 75 DEG C of cold plates and 60 DEG C of cold plates is added
Into reductive jar.
Further, one or two kinds of condensate liquid in 120 DEG C of cold plates and 105 DEG C of cold plates is added to reductive jar
In.
Further, the white wine heating and temperature control is between 70 DEG C -100 DEG C.
The production method of alkalescent white wine provided by the invention, the white wine of acidity can be removed in white wine acid discharge equipment
Acidic materials, it is in alkalescent after treatment to make acid white wine, and such white wine drinks such white wine closer to the pH of human body
Injury to human body is smaller compared to acid white wine；And original characteristic can be retained.
Brief description of the drawings
, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical scheme of the prior art
The required accompanying drawing used is briefly described in embodiment or description of the prior art, it should be apparent that, in describing below
Accompanying drawing is some embodiments of the present invention, for those of ordinary skill in the art, before creative work is not paid
Put, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is the structural representation of white wine acid discharge equipment provided in an embodiment of the present invention；
Fig. 2 is the A of white wine acid discharge equipment shown in Fig. 1 partial enlarged drawing；
Fig. 3 is the B of white wine acid discharge equipment shown in Fig. 1 partial enlarged drawing；
Fig. 4 is the C of white wine acid discharge equipment shown in Fig. 1 partial enlarged drawing.
Icon：100- fractionating column main bodys；101- ventholes；102- inlet openings；The condenser pipes of 103- first；104- second is condensed
Pipe；200-pH monitors；300- supercharging devices；400- reductive jars；The connecting tubes of 500- first；The connecting tubes of 600- the 3rd；700- is cold
Solidifying plate；800- collecting tanks；900- liquid collecting tanks；The connecting tubes of 110- second；120- condensing units；121- water inlets；122- delivery ports；
130- radiating tubes；140- charging apertures；150- discharging openings；160- sample taps；170- heaters；180- temperature control equipments.
Embodiment
Technical scheme is clearly and completely described below in conjunction with accompanying drawing, it is clear that described implementation
Example is part of the embodiment of the present invention, rather than whole embodiments.Based on the embodiment in the present invention, ordinary skill
The every other embodiment that personnel are obtained under the premise of creative work is not made, belongs to the scope of protection of the invention.
In the description of the invention, it is necessary to explanation, term " " center ", " on ", " under ", "left", "right", " vertical ",
The orientation or position relationship of the instruction such as " level ", " interior ", " outer " be based on orientation shown in the drawings or position relationship, merely to
Be easy to the description present invention and simplify description, rather than instruction or imply signified device or element must have specific orientation,
With specific azimuth configuration and operation, therefore it is not considered as limiting the invention.In addition, term " first ", " second ",
" the 3rd " is only used for describing purpose, and it is not intended that instruction or hint relative importance.
In the description of the invention, it is necessary to illustrate, unless otherwise clearly defined and limited, term " installation ", " phase
Even ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected, or be integrally connected；Can
To be mechanical connection or electrical connection；Can be joined directly together, can also be indirectly connected by intermediary, Ke Yishi
The connection of two element internals.For the ordinary skill in the art, with concrete condition above-mentioned term can be understood at this
Concrete meaning in invention.
As Figure 1-Figure 4, a kind of white wine acid discharge equipment provided by the invention, including fractionating column main body 100, condensing unit
120th, reductive jar 400 and liquid collecting tank 900；
Inner chamber is provided with the fractionating column main body 100, the condensing unit 120 connects with the fractionating column main body 100
Connect, for condensed steam；And it is provided with the inner chamber for the heater 170 of heating and at least one for liquid collecting
Cold plate 700；
The cold plate 700 controls the temperature control equipment 180 of the temperature of cold plate 700 to be connected with being used for, and described cold
The solidifying lower end of plate 700 is provided with the collecting tank 800 for collecting liquid on cold plate 700, and the collecting tank 800 passes through the first connection
Pipe 500 is connected with the liquid collecting tank 900；
Charging aperture 140 and discharging opening 150, the horizontal level of charging aperture 140 are provided with the fractionating column main body 100
Not higher than the collecting tank 800, the discharging opening 150 is connected by the 3rd connecting tube 600 with the reductive jar 400；
Venthole 101 and inlet opening 102 are respectively arranged with the fractionating column main body 100, and the venthole 101 is horizontal
Position is higher than the collecting tank 800, and the horizontal level of inlet opening 102 is less than the collecting tank 800；
The condensing unit 120 includes condensation chamber, and radiating tube 130 is provided with the condensation chamber；And in the condensation
It is provided with device 120 and water inlet 121 and delivery port 122 is connected with condensation chamber；
The first condenser pipe 103 is provided with the venthole 101, the second condensation is provided with the inlet opening 102
Pipe 104, and the condenser pipe 104 of first condenser pipe 103 and second connects with the radiating tube 130.
In certain embodiments, charging aperture 140 and discharging opening 150 are provided with fractionating column main body 100；By white wine by entering
Material mouth 140 adds fractionating column main body 100, white wine heating is made into its boiling by heater 170, temperature control equipment 180 is adjusted
The temperature of cold plate 700 is saved, other materials for carrying alcohol vapour, is peeled off on different cold plates 700, the thing after stripping
Matter is flowed into collecting tank 800, is flowed into by the first connecting tube 500 in liquid collecting tank 900.
Alcohol vapour persistently rises, and the first condenser pipe 103, the first condenser pipe 103 and radiating are entered from venthole 101
Pipe 130 connects, and the cold water of condensation chamber of the alcohol vapour in radiating tube 130 with entering from water inlet 121 carries out heat exchange, temperature
Elevated cold water discharges condensing unit 120 from delivery port 122, and alcohol vapour liquefies in radiating tube 130, by the second condenser pipe
104, entered from inlet opening 102 in fractionating column main body 100, with unevaporated white spirit mixed, continue to carry the impurity in white wine
Evaporation.
Treat that the acidic materials in white wine remove, white wine is transported in reductive jar 400 by discharging opening 150.
On above-described embodiment basis, further, ten cold plates are provided with the fractionating column main body 100
700, and the corresponding collecting tank 800 of each cold plate 700.
There are ten cold plates 700 in fractionating column main body 100, corresponding to the condensate liquid homomergic flow on each cold plate 700 enters
In collecting tank 800, then flowed into from collecting tank 800 by the first connecting tube 500 in liquid collecting tank 900.
Temperature control equipment 180 is connected with cold plate 700, by heating liquid or gas, liquid or gas is existed
Circulated in cold plate 700, cold plate 700 is controlled and is being appointed as temperature, or use other mode of heatings, such as electrical heating,
Directly cold plate 700 is heated, the temperature of cold plate 700 is reached the temperature specified.
On above-described embodiment basis, further, at least one liquid collecting tank 900 passes through the second connecting tube 110
It is connected with the reductive jar 400.
There is the second connecting tube 110 between liquid collecting tank 900 and reductive jar 400, the liquid that cold plate 700 condenses is given up a bit
No, some need to be added in reductive jar 400, have the material for needing to be added in reductive jar 400 by
Two connecting tubes 110 are connected in reductive jar 400.
On above-described embodiment basis, further, in addition to for detecting the pH of white wine pH in fractionating column main body 100
Monitor 200.
In white wine is constantly fractionated, the pH of white wine gradually rises, and the moment of pH monitors 200 monitors the pH of white wine, works as pH
When reaching more than 6.5, stop heating.
As shown in figure 4, on above-described embodiment basis, further, the lower end of fractionating column main body 100, which is provided with, to be taken
Sample mouth 160.
In order to preferably monitor the requirement whether processing of white wine acid discharge reaches processing parameter index, pass through sample tap
160 samplings are detected, and detection is qualified, i.e. white wine acid discharge is completed.
On above-described embodiment basis, further, valve and supercharging device are provided with the 3rd connecting tube 600
300, and the valve is arranged between the discharging opening 150 and the supercharging device 300.
In certain embodiments, there is valve in the 3rd connecting tube 600, filling is reduced when needing aged white wine being transported to
In, Open valve, start supercharging device 300, the white wine after processing is transported in reduction filling by the 3rd connecting tube 600.
The present invention also provides a kind of white wine acid discharge method, and the white wine acid discharge method comprises the following steps：
White wine is added in fractionating column main body, opening heater makes white wine seethe with excitement, and is adjusted by temperature control equipment
The temperature of cold plate, set gradually from bottom to top for 195 DEG C, 180 DEG C, 165 DEG C, 160 DEG C, 150 DEG C, 120 DEG C, 105 DEG C, 90
℃、75℃、60℃；White wine pH is measured more than 6.5 by pH monitors；Discharging opening is opened, the white wine after processing is transported to also
In former tank.
In certain embodiments, white wine is added in fractionating column main body, white wine is untreated former wine herein, in acid
Property；Heater is opened, is white wine micro-boiling, with the evaporation of ethanol, white wine keeps the increase of the constant temperature of micro-boiling；Second
After alcohol boiling, during evaporation, by the impurity in ethanol, such as caproic acid, lactic acid etc., carrier's evaporation, by 195
When DEG C cold plate, because caproic acid boiling point is at 205 DEG C, when by 195 DEG C of cold plates, the lower boiling material such as ethanol
Steam condition is kept, the caproic acid that alcohol vapour carries, is stripped out, is condensate on cold plate.
Have in white wine the lactic acid of 122 DEG C of caproic acid, the boiling point of 205 DEG C of acetic acid, the boiling point of 117 DEG C of boiling point, 162 DEG C of butyric acid and
Other esters fragrance matter boiling points are again between 70-200 degree；Such as 77 DEG C of ethyl acetate of boiling point, the ethyl hexanoate that 167 DEG C of boiling point,
The ethyl lactate that 154 DEG C of boiling point.
When white wine seethes with excitement, alcohol vapour rises entrainment of other impurities, is passing through 195 DEG C of cold plates, except oneself
Beyond acid, other impurities gasify on 195 DEG C of cold plates, continue to rise, and reach 180 DEG C of cold plates, also only caproic acid is warm herein
Degree is lower can to keep liquid, and after 180 DEG C, 195 DEG C of cold plates, the caproic acid plate that is condensed is collected；By 165 DEG C of cold plates,
Ethyl hexanoate is collected；By 160 DEG C of cold plates, butyric acid and ethyl hexanoate are collected；By 150 DEG C of cold plates, by lactic acid second
Ester is collected；By 120 DEG C of cold plates, lactic acid and ethyl lactate are collected；By 105 DEG C of cold plates, acetic acid and lactic acid are collected；
By 90 DEG C of cold plates, acetic acid is collected；By 75 DEG C of cold plates, ethyl acetate and acetic acid are collected；By 60 DEG C of cold plates,
Ethanol is collected.
In a preferred embodiment of the invention, it is 165 DEG C of cold plates, 150 DEG C of cold plates, 75 DEG C of cold plates and 60 DEG C are cold
The condensate liquid of solidifying plate is added in reductive jar.
165 DEG C of cold plates, 150 DEG C of cold plates, the condensate liquid of 75 DEG C of cold plates and 60 DEG C of cold plates be mainly ethyl hexanoate,
Ethyl lactate, ethyl acetate and acetic acid, ethanol；So a little condensate liquids are added in reductive jar, the characteristic of former wine can be kept.
In a preferred embodiment of the invention, by one or two kinds of condensation in 120 DEG C of cold plates and 105 DEG C of cold plates
Liquid is added in reductive jar.
120 DEG C of cold plate condensate liquids are mainly lactic acid and ethyl lactate, the condensate liquids of 105 DEG C of cold plates be mainly acetic acid and
Lactic acid；The difference of the white wine produced as needed, can selectivity 120 DEG C of cold plates and 105 DEG C of cold plates condensate liquid choosing
Selecting property adds.
In a preferred embodiment of the invention, further, the white wine heating and temperature control 85 DEG C -95 DEG C it
Between.
In certain embodiments, white wine is added by heater, it is remained fluidized state, micro-boiling is
Can；It is high to start concentration of alcohol, when 85 DEG C or so, former wine just disclosure satisfy that the requirement of processing, with the lasting steaming of former wine
Send out, ethanol content reduces in former wine, improves the temperature of heating, can just white wine is seethed with excitement；Due to weather reason, the quality of grain is not
Unanimously, the former wine for causing to produce also has certain difference, when the ethanol content of former wine is higher, can suitably reduce temperature,
During white wine acid discharge, make former wine micro-boiling.
With reference to specific embodiment, the present invention is described further.
Embodiment 1
White wine acid discharge method is present embodiments provided, is carried out in accordance with the following steps,
Former wine is added to fractionating column main body, the liquid level of former wine is not higher than charging aperture, former wine is entered by heater
Row heating is white wine micro-boiling, by temperature control equipment, adjusts the temperature of each cold plate, set gradually from top to bottom for
195℃、180℃、165℃、160℃、150℃、120℃、105℃、90℃、75℃、60℃；Condensing unit is opened, makes ethanol
Condensing reflux is in knockout tower main body；With the reduction of the ethanol in former wine, temperature is gradually risen, keeps former wine boiling；Pass through
PH in pH monitors monitoring former wine, after pH is more than 6.5, be sampled analysis, sample it is qualified after, by after treatment
Original wine is transported in reductive jar, then by the ethyl hexanoate of 165 DEG C of cold plates condensation, 150 DEG C of cold plates condensations ethyl lactate,
So a little condensate liquids are added to reductive jar by the ethyl acetate and the ethanol of acetic acid and 60 DEG C of cold plates of 75 DEG C of cold plate condensations
In, keep the characteristic of former wine；White wine of the reductive jar Jing Guo acid discharge is finally transported to next step, handled, so as to real
The acid discharge of former wine is showed.
The production method of alkalescent white wine provided by the invention, the white wine of acidity can be removed in white wine acid discharge equipment
Acidic materials, it is in alkalescent after treatment to make acid white wine, and such white wine drinks such white wine closer to the pH of human body
Injury to human body is smaller compared to acid white wine；And original characteristic can be retained.
Finally it should be noted that：Various embodiments above is merely illustrative of the technical solution of the present invention, rather than its limitations；To the greatest extent
The present invention is described in detail with reference to foregoing embodiments for pipe, it will be understood by those within the art that：Its according to
The technical scheme described in foregoing embodiments can so be modified, either which part or all technical characteristic are entered
Row equivalent substitution；And these modifications or replacement, the essence of appropriate technical solution is departed from various embodiments of the present invention technology
The scope of scheme.
Claims (6)
1. a kind of white wine acid discharge equipment, it is characterised in that including fractionating column main body, condensing unit, reductive jar and liquid collecting tank；
Inner chamber is provided with the fractionating column main body, the condensing unit is connected with the fractionating column main body, is steamed for condensing
Vapour；And the heater for heating and at least one cold plate for liquid collecting are provided with the inner chamber；
The cold plate is connected with condensing the temperature control equipment of plate temperature for controlling, and is provided with the cold plate lower end
For collecting the collecting tank of liquid on cold plate, the collecting tank is connected by the first connecting tube with the liquid collecting tank；
Charging aperture and discharging opening are provided with the fractionating column main body, the charging aperture horizontal level is not higher than the liquid collecting
Groove, the discharging opening are connected by the 3rd connecting tube with the reductive jar；
Venthole and inlet opening are respectively arranged with the fractionating column main body, and the venthole horizontal level is higher than the liquid collecting
Groove, the inlet opening horizontal level are less than the collecting tank；
The condensing unit includes condensation chamber, and radiating tube is provided with the condensation chamber；And set on the condensing unit
Have and connect water inlet and delivery port with condensation chamber；
The first condenser pipe is provided with the venthole, the second condenser pipe, and described first are provided with the inlet opening
Condenser pipe and the second condenser pipe connect with the radiating tube.
2. white wine acid discharge equipment according to claim 1, it is characterised in that be provided with ten in the fractionating column main body
Cold plate, and the corresponding collecting tank of each cold plate.
3. white wine acid discharge equipment according to claim 2, it is characterised in that at least one liquid collecting tank connects by second
Adapter is connected with the reductive jar.
4. white wine acid discharge equipment according to claim 1, it is characterised in that also include being used to detect fractionating column main body words spoken by an actor from offstage
Wine pH pH monitors.
5. white wine acid discharge equipment according to claim 1, it is characterised in that the fractionating column main body lower end is provided with sampling
Mouthful.
6. the white wine acid discharge equipment according to claim any one of 1-5, it is characterised in that set in the 3rd connecting tube
There are valve and supercharging device, and the valve is arranged between the discharging opening and the supercharging device.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710320227.8A CN106916720B (en) | 2017-05-09 | 2017-05-09 | White wine acid discharge equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710320227.8A CN106916720B (en) | 2017-05-09 | 2017-05-09 | White wine acid discharge equipment |
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| Publication Number | Publication Date |
|---|---|
| CN106916720A CN106916720A (en) | 2017-07-04 |
| CN106916720B true CN106916720B (en) | 2018-02-06 |
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Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107384720A (en) * | 2017-08-31 | 2017-11-24 | 潘建军 | A kind of segment reflux solid continuous distillation machine and its distillating method |
| CN111979081A (en) * | 2020-08-19 | 2020-11-24 | 湖南桃花源酒业有限公司 | White spirit acid-discharging equipment and using method |
| CN112403005A (en) * | 2020-11-09 | 2021-02-26 | 湖南桃花源酒业有限公司 | Novel acid discharge equipment for white spirit production and processing and use method thereof |
| CN113416623B (en) * | 2021-08-10 | 2022-12-23 | 肖斌 | Acid equipment is arranged with dividing preface to white spirit production |
| CN114395462A (en) * | 2021-12-16 | 2022-04-26 | 山东运微供应链管理有限公司 | Acid equipment is arranged with dividing preface to white spirit production |
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|---|---|---|---|---|
| CN103394208A (en) * | 2013-08-15 | 2013-11-20 | 泸州品创科技有限公司 | White spirit fragrance component separation method and device |
| CN203498369U (en) * | 2013-10-15 | 2014-03-26 | 泸州品创科技有限公司 | Tower type distilled spirit fractional distillation device |
| CN104804970A (en) * | 2015-03-23 | 2015-07-29 | 中国食品发酵工业研究院 | Slightly alkaline Chinese spirit and production method thereof |
| CN105861255A (en) * | 2015-01-22 | 2016-08-17 | 王家隆 | Weak alkalization process for liquor |
| CN106334327A (en) * | 2016-08-30 | 2017-01-18 | 安徽安特食品股份有限公司 | Alcohol distilling production method |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103394208A (en) * | 2013-08-15 | 2013-11-20 | 泸州品创科技有限公司 | White spirit fragrance component separation method and device |
| CN203498369U (en) * | 2013-10-15 | 2014-03-26 | 泸州品创科技有限公司 | Tower type distilled spirit fractional distillation device |
| CN105861255A (en) * | 2015-01-22 | 2016-08-17 | 王家隆 | Weak alkalization process for liquor |
| CN104804970A (en) * | 2015-03-23 | 2015-07-29 | 中国食品发酵工业研究院 | Slightly alkaline Chinese spirit and production method thereof |
| CN106334327A (en) * | 2016-08-30 | 2017-01-18 | 安徽安特食品股份有限公司 | Alcohol distilling production method |
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| CN106916720A (en) | 2017-07-04 |
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