CN105586212B - The integration of equipments and method of rice wine semi-solid ferment - Google Patents
The integration of equipments and method of rice wine semi-solid ferment Download PDFInfo
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- CN105586212B CN105586212B CN201610136977.5A CN201610136977A CN105586212B CN 105586212 B CN105586212 B CN 105586212B CN 201610136977 A CN201610136977 A CN 201610136977A CN 105586212 B CN105586212 B CN 105586212B
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- 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
Abstract
The invention discloses a kind of integration of equipments of rice wine semi-solid ferment, it includes prefermentor group and rear fermentation tank group, the prefermentor group includes at least one main fermentation tank, the cooling worm being arranged in main fermentation tank and the circulation material conveying being arranged at outside main fermentation tank pump, material inlet is provided at the top of main fermentation tank, main fermentation tank tank body top is equipped with main fermentation tank Xun Huan discharge nozzle, main fermentation tank tank base is equipped with main fermentation tank feed back/discharge nozzle, fermentation tank group includes at least one rear fermentation tank, the cooling heat exchanger being arranged at outside rear fermentation tank and rear fermentation tank mash pump afterwards.The fermentation of rice wine is divided into preceding ferment phase and rear ferment phase by the present invention, use the preceding fermentation tank for accounting for 1/4 total fermentation volume, solve the problems, such as semi-solid ferment, simplify the rear fermentation tank for accounting for 3/4 total fermentation volume, it realizes the preceding fermentation tank that need to be cooled and the rear fermentation tank subregion that need to be kept the temperature arrangement, reduces the difficulty that feeds intake of semisolid material, reduce equipment investment, workshop investment, temperature control effect is improved, reduces energy consumption.
Description
Technical field
The present invention relates to the fermentation techniques that rice wine is produced using rice as raw material.
Background technology
Current rice wine fermenting has solid state fermentation, semi-solid ferment, liquid-state fermentation technology, existing rice wine semi-solid ferment
Technique is that rice and water are launched into cylinder or tank to ferment, ratio about 1：2, fermentation time 15~20 days, since rice is into tank
Water swelling afterwards, solid-liquid layering in earlier fermentation tank, material is very sticky, mobility is very poor, the temperature control ten of fermentation process
Divide difficulty, therefore, to solve climate control issues, existing rice wine fermenting can only use small-sized fermentation tank or cylinder, increase half
Feed intake difficulty and the temperature control difficulty of solid material (rice+water+song), considerably increase rice wine factory construction cost, constrain rice wine
The development of production.
The content of the invention
The purpose of the present invention is making up the deficiencies in the prior art, according to the situation of change of fermentation process material characteristic, provide
A kind of integration of equipments of rice wine solid state fermentation, the rice wine production cycle can be divided into primary fermentation and rear fermentation with improve temperature control effect,
Solve the problems, such as semi-solid ferment.
In order to realize foregoing invention purpose, present invention employs following technical schemes：
The integration of equipments of rice wine semi-solid ferment, it is characterised in that：Including prefermentor group and rear fermentation tank group, before described
Fermentation tank group includes at least one main fermentation tank, the cooling worm being arranged in main fermentation tank and the circulation material conveying being arranged at outside main fermentation tank
Pump, main fermentation tank top is provided with material inlet, main fermentation tank tank body top is equipped with main fermentation tank cycle discharge nozzle, main fermentation tank tank body bottom
Portion is equipped with main fermentation tank feed back/discharge nozzle,
Fermentation tank group includes at least one rear fermentation tank, the cooling heat exchanger being arranged at outside rear fermentation tank and rear fermentation tank wine with dregs afterwards
Liquid pump, rear fermentation tank tank base are equipped with rear fermentation tank feed pipe and rear fermentation tank discharge nozzle, and rear fermentation tank tank body top is returned equipped with rear fermentation tank
Expects pipe,
Main fermentation tank Xun Huan discharge nozzle is connected to the feed pipe of circulation material conveying pump by pipeline, and the discharge nozzle of circulation material conveying pump leads to
The preceding mash first branch is crossed to be connected to main fermentation tank feed back/discharge nozzle and be connected to rear fermentation tank charging by preceding mash the second branch
Pipe；Afterwards fermentation tank discharge nozzle connection after fermentation tank mash pump after by the rear mash first branch be connected to cooling heat exchanger into
Material mouth, fermentation tank feed back pipe after the discharge port of cooling heat exchanger is connected by pipeline, fermentation tank mash after rear fermentation tank discharge nozzle connection
Distillation workshop is sent to by rear mash the second branch after pump.
Preferably, the prefermentor group is composed in parallel by multiple main fermentation tanks.
Preferably, fermentation tank group is composed in parallel by fermentation tanks after multiple after described, the preceding mash of multiple main fermentation tanks the
Two branch circuit parallel connections are connected to rear fermentation tank feed pipe.
In order to strengthen heat insulation effect, the main fermentation tank and rear fermentation tank are both provided with heat exchange jacket.
Another object of the present invention is to provide a kind of method of rice wine semi-solid ferment, using equipment collection as described above
Implement into according to following steps：
Semisolid material enters main fermentation tank, and for material into there is the layering of water material after tank, material is small into after tank 2.5~3.5
Shi Kaidong circulation material conveyings pump, and upper strata liquid material is extracted from main fermentation tank Xun Huan discharge nozzle and is pumped to master through circulation material conveying
Main fermentation tank feed back/discharge nozzle of fermentation tank bottom promotes in tank material to stir, and helps material fermentation starting, when fermentation is into vigorous
Stop the forced circulation of circulation material conveying pump after phase, CO is carried out in main fermenting pot animated period2Recycling controls pressure inside the tank, opens
The cooling water pump of cooling worm in tank controls in tank temperature of charge at 30~35 degree, material into main fermentation tank 60~65 it is small when, according to
Testing result confirms that preceding mash is pumped to the rear fermentation tank feed pipe of rear fermentation tank bottom by ON cycle feeding engine after the completion of main ferment；
CO need to be full of in tank before fermentation tank charging afterwards2, after charging, material continues after-ripening, rear fermentation tank control hair in rear fermentation tank
After the completion of confirming fermentation after testing, distillery is pumped into rear fermentation tank mash for ferment temperature, after-ripening 12 days~15 days.
The fermentation of rice wine is divided into preceding ferment phase and rear ferment phase by the present invention, and in the preceding ferment phase, material is in solid-state and semisolid shape
State, poor fluidity, but caloric value is larger, to improve the degree of fermentation, solving the problems such as temperature control, before being carried out using special preceding fermentation tank
Fermentation carries out the circulation stirring of itself using circulation material conveying pump to material in preceding fermentation tank；After primary fermentation, material characteristic occurs
Large change, material liquefies substantially, good fluidity, and the degree of fermentation reduces, and caloric value greatly reduces, according to the temperature conditions of environment,
Based on heat preservation, therefore the cold and hot coiled pipe in tank is can remove with fermentation tank volume after expanding.Because a little uses of the invention account for 1/4 total hair
The preceding fermentation tank of ferment volume, solves the problems, such as semi-solid ferment, simplifies the rear fermentation tank for accounting for 3/4 total fermentation volume, and realizing need to be cold
But the preceding fermentation tank to cool down and the rear fermentation tank subregion that need to be kept the temperature arrangement, reduce the difficulty that feeds intake of semisolid material, reduce equipment
Investment, workshop investment, improve temperature control effect, reduce energy consumption.
Description of the drawings
Fig. 1 is the process flow diagram of the present invention.
Wherein, main fermentation tank 1, rear fermentation tank 2, circulation material conveying pump 3, rear fermentation tank mash pump 4, pipe plate 5, CIP reflux pumps 6 become
Frequency cooling water pump 7, first filter 8, first flowmeter 9, primary scene thermometer 10, the 3rd scene temperature meter 11, second changes
Hot device 12, secondary scene thermometer 13, the second filter 14, the preceding mash first branch 15, preceding mash the second branch 16, rear mash
The first branch 17, rear mash the second branch 18, second flowmeter 19
Specific embodiment
Below in conjunction with attached drawing, implementer's method of the invention is illustrated.
As shown in Figure 1, be integration of equipments of the present invention, it is described including prefermentor group and rear fermentation tank group
Prefermentor group includes at least one main fermentation tank 1, the cooling worm being arranged in main fermentation tank 1 and the cycling being arranged at outside main fermentation tank
Feeding engine 3, CO2The equipment such as recycling and CIP tube sheets.Material inlet is provided at the top of main fermentation tank, main fermentation tank tank body top is equipped with
Main fermentation tank Xun Huan discharge nozzle, main fermentation tank tank base are equipped with main fermentation tank feed back/discharge nozzle.Afterwards fermentation tank group include it is at least one after
Fermentation tank 2, the plate heat exchanger 12 being arranged at outside rear fermentation tank and rear fermentation tank mash pump the equipment such as 4.Fermentation tank tank base is equipped with afterwards
Fermentation tank feed pipe and rear fermentation tank discharge nozzle afterwards, rear fermentation tank tank body top are equipped with rear fermentation tank feed back pipe.Main fermentation tank Xun Huan discharge nozzle leads to
The feed pipe that pipeline is connected to circulation material conveying pump 3 is crossed, the discharge nozzle of circulation material conveying pump 3 is connected to by the preceding mash first branch 15
Main fermentation tank feed back/discharge nozzle and rear fermentation tank feed pipe is connected to by preceding mash the second branch 16.Afterwards after the connection of fermentation tank discharge nozzle
The feed inlet of heat exchanger 12 is connected after fermentation tank mash pump 4 by the rear mash first branch 17, the discharge port of heat exchanger 12 passes through pipe
Fermentation tank feed back pipe after the connection of road.Steaming is sent to by rear mash the second branch 18 after fermentation tank mash pump 4 after the connection of fermentation tank discharge nozzle afterwards
Evaporate workshop.
As preferred mode, the prefermentor group includes multiple main fermentation tanks, and then fermentation tank group includes multiple rear ferment
Tank, the preceding mash the second branch of multiple main fermentation tanks are connected in parallel to the feed pipe of some rear fermentation tank.Main fermentation tank and rear fermentation tank are respectively provided with
There is heat exchange jacket.
Semisolid material (rice+song+water) enters main fermentation tank 1 by the feed pipe of pipeline from main fermentation tank tank deck.Material into
There is the layering of water material in initial stage after tank, into tank after before 6 it is small when separation of solid and liquid it is obvious, upper strata (accounts for total material 2/5 for liquid
Volume), lower floor be solid-state (the mixing water swelling of wine cake and meal, material is more solid, accounts for total 3/5 volume of material), material
Poor fluidity is very poor.Material into after tank 3 it is small when or so can start circulation material conveying pump 3, recycled from the main fermentation tank on tank body top
Expects pipe extracts that upper strata liquid material is pumped through circulation material conveying, the preceding mash first branch 15 is pumped to the main fermentation tank feed back of pot bottom/go out
Expects pipe enters main fermentation tank 1, promotes Flow of Goods and Materials in tank, helps material fermentation starting, increases the degree of fermentation, shorten the main ferment time.By
It is strengthened in Matter Transfer, heat exchange efficiency also increases therewith, the temperature control of fermentation tank before being conducive to.When fermentation enters animated period
After can stop forced circulation, in main fermenting pot animated period, tank deck pipe is jumped to CO2Recovery channel carries out CO2Recycling, simultaneously
Pressure inside the tank is controlled by pressure retaining valve, material starts frequency conversion cooling water pump 7, control into the temperature change according to material in tank after tank
Temperature of charge processed is between 30~35 degree.Material is basically completed into main ferment after tank 56h, and caloric value is seldom, temperature substantially constant,
Material fluidity is fine, and viscosity is smaller, material into main fermentation tank 60 it is small when after, according to testing result, after the completion of confirming main ferment, from master
Fermentation tank feed back/discharge nozzle pumps fermentation tank 2 after 3 premenstrual mash the second branches 16 are pumped into through circulation material conveying.
Fermentation tank 2 need to be full of CO before feeding in tank afterwards2, enter from the material of main fermentation tank 1 from rear fermentation tank bottom feed pipe,
Continue after-ripening in rear fermentation tank, material is in rear fermentation tank substantially based on heat preservation.Can by tank body chuck and external circulation heat exchanging device into
Trip temperature controls, and when material need to exchange heat, may be pumped into plate heat exchanger cycle heat exchange.In rear ferment process, tank deck pipe jumps to
Pressure retaining valve controls pressure inside the tank.Material was in rear fermentation tank after-ripening 12 days, after the completion of confirming fermentation after testing, was pumped with rear fermentation tank mash
It is sent to distillery.
Fermentation process in main fermentation tank be material liquefaction and main fermentation processes, preceding about 3 days ferment phases.The fermentation of fermentation tank afterwards
Journey is karusen After-ripening, rear 12~17 days ferment phases.
The present invention include but is not limited to above-described embodiment and content shown in the drawings, it is other all with the present invention technology
The product structure that scheme has identical essentiality content is each fallen within protection scope of the present invention.
Claims (5)
1. the integration of equipments of rice wine semi-solid ferment, it is characterised in that：Including prefermentor group and rear fermentation tank group, sent out before described
Fermentation tank group includes at least one main fermentation tank, the cooling worm being arranged in main fermentation tank and the circulation material conveying being arranged at outside main fermentation tank
Pump, main fermentation tank top is provided with material inlet, main fermentation tank tank body top is equipped with main fermentation tank cycle discharge nozzle, main fermentation tank tank body bottom
Portion is equipped with main fermentation tank feed back/discharge nozzle,
Fermentation tank group includes at least one rear fermentation tank, the cooling heat exchanger being arranged at outside rear fermentation tank and rear fermentation tank mash afterwards
Pump, rear fermentation tank tank base are equipped with rear fermentation tank feed pipe and rear fermentation tank discharge nozzle, and rear fermentation tank tank body top is equipped with rear fermentation tank feed back
Pipe,
Main fermentation tank Xun Huan discharge nozzle is connected to the feed pipe of circulation material conveying pump by pipeline, and the discharge nozzle that circulation material conveying pumps passes through preceding
The mash first branch is connected to main fermentation tank feed back/discharge nozzle and is connected to rear fermentation tank feed pipe by preceding mash the second branch；Afterwards
It is connected to the feed inlet of cooling heat exchanger, cooling after the connection of fermentation tank discharge nozzle after fermentation tank mash pump by the rear mash first branch
Fermentation tank feed back pipe after the discharge port of heat transmission equipment is connected by pipeline, by rear after fermentation tank mash pump after rear fermentation tank discharge nozzle connection
Mash the second branch is sent to distillation workshop.
2. the integration of equipments of rice wine semi-solid ferment according to claim 1, it is characterised in that：The prefermentor group by
Multiple main fermentation tanks compose in parallel.
3. the integration of equipments of rice wine semi-solid ferment according to claim 2, it is characterised in that：It is described after fermentation tank group by
Fermentation tank composes in parallel after multiple, and the preceding mash the second branch of multiple main fermentation tanks is connected in parallel in rear fermentation tank feed pipe.
4. the integration of equipments of rice wine semi-solid ferment according to claim 1, it is characterised in that：The main fermentation tank and rear ferment
Tank is both provided with heat exchange jacket.
5. a kind of method of rice wine semi-solid ferment, using the integration of equipments as described in Claims 1 to 4 is any according to following step
It is rapid to implement：
Semisolid material enters main fermentation tank, material into occurring the layering of water material after tank, material into after tank 2.5~3.5 it is small when open
Dynamic circulation material conveying pump, upper strata liquid material are extracted from main fermentation tank Xun Huan discharge nozzle and are pumped to main fermentation tank through circulation material conveying
Main fermentation tank feed back/discharge nozzle of bottom promotes material in tank to stir, and helps material fermentation starting, after fermentation is into animated period
Stop the forced circulation of circulation material conveying pump, CO is carried out in main fermenting pot animated period2Recycling controls pressure inside the tank, opens in tank
The cooling water pump of cooling worm, control tank in temperature of charge, material into main fermentation tank 60~65 it is small when, according to testing result, confirm
Preceding mash is pumped to the rear fermentation tank feed pipe of rear fermentation tank bottom by ON cycle feeding engine after the completion of main ferment；
CO need to be full of in tank before fermentation tank charging afterwards2, material continues after-ripening in rear fermentation tank after charging, rear fermentation tank control fermentation temperature,
After the completion of confirming fermentation after testing, distillery is pumped into rear fermentation tank mash for after-ripening 12 days~15 days.
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| CN201610136977.5A CN105586212B (en) | 2016-03-10 | 2016-03-10 | The integration of equipments and method of rice wine semi-solid ferment |
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| CN105586212A CN105586212A (en) | 2016-05-18 |
| CN105586212B true CN105586212B (en) | 2018-05-22 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107502539A (en) * | 2017-09-19 | 2017-12-22 | 成都康辉生物科技有限公司 | Large Copacity installation for fermenting for solid biologic |
| CN107904094B (en) * | 2017-12-29 | 2023-11-17 | 宁波中乳机械有限公司 | Sake preparation system and preparation process thereof |
| CN109055089A (en) * | 2018-08-13 | 2018-12-21 | 贵州怀宫酒业销售有限公司 | Liquor made from sorghum continuous fermentation apparatus |
| CN111304028A (en) * | 2020-02-14 | 2020-06-19 | 上海傲中生物工程设备有限公司 | Solid-liquid combined fermentation tank |
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| CN104046554A (en) * | 2014-06-09 | 2014-09-17 | 湖北工业大学 | Semisolid circular deep vinegar brewing method and equipment |
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| CN1033171C (en) * | 1988-12-23 | 1996-10-30 | 许骏发 | Automated method and apparatus for semi-solid fermentation used in production of ancient quality rice vinegar and/or rice wine |
| JP2828210B2 (en) * | 1989-01-11 | 1998-11-25 | マルカン酢株式会社 | Automated semi-solid fermentation method for producing rice vinegar and / or rice wine of ancient quality |
| US9242881B2 (en) * | 2013-03-11 | 2016-01-26 | Jason Chia Hsing Shih | Secondary solid-phase anaerobic digestion producing more biogas |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103725605A (en) * | 2013-12-31 | 2014-04-16 | 陕西万源生物农业科技有限公司 | Fermentation tank and fermentation system |
| CN104046554A (en) * | 2014-06-09 | 2014-09-17 | 湖北工业大学 | Semisolid circular deep vinegar brewing method and equipment |
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