专利摘要:
A method and apparatus for macerating and fermenting grapes in the presence of carbon dioxide, the picked grapes being put in a hopper in clusters and fed therefrom by a screw conveyor to an intermittently pulsating pump located below a fermentation vat being filled, and carbon dioxide being drawn from this vat, and others in the installation, and reinjected into the mixture of partially crushed grapes and their must as it is being conducted in a pipe from the pump upwardly into the vat against the back-pressure of the contents therein.
公开号:SU886754A3
申请号:SU782617906
申请日:1978-05-24
公开日:1981-11-30
发明作者:Эгретье Мишель
申请人:За витель К ПАТЕНТУ;
IPC主号:
专利说明:

(5) INSTALLATION FOR TRANSFERRING RAW MATERIALS INTO A FLEXIBLE VAN DURING CARBON EFFICIENCY WINE PRODUCTION
one
The invention refers to the food industry, namely to winemaking.
A known installation for transferring raw materials to the fermentation tank in the production of wines by carbon dioxide maceration, which contains a collector, a screw conveyor for moving the year with ridges, located in the lower part of the collection, a fermentation tank and a piping system for raw materials and carbon dioxide 1J respectively.
However, when using a known installation, the contents are squeezed out of the overwhelming majority of the year and the subsequent fermentation takes place in a continuous liquid medium, which degrades the quality of the finished wine.
The purpose of the invention is to improve the quality of the finished product.
The goal is achieved by the fact that the installation for transferring raw materials to the fermentation tank in the production of wines by carbon dioxide maceration, containing a collector, a screw conveyor for moving the year with ridges, is 26 MERACATION
The fermentation tank and the piping system for raw materials and carbon dioxide, respectively, in the lower part of the collection, are equipped with a volumetric pump communicated with a screw conveyor, the inlet of which is located below the level of the lower part of the fermentation tank and connected to the upper part of the fermentation tank the carbon dioxide supply line and communicated with the raw material supply pipe at a point located in the outlet nozzle of the volcometric pump, while the screw ansporter configured with a step in the direction of movement uvelichivayuschims year with ridges.
权利要求:
Claims (1)
[1]
FIG. 1 shows schematically an installation for transferring raw materials to a fermentation tank in the production of wines by carbon dioxide maceration; in fig. 2 a screw conveyor, in longitudinal section} in FIG. 3 and - volumetric pump in cross section, in two phases of the rotor position. The installation comprises a collector 1, a screw conveyor 2 for moving the year with ridges, located at the bottom of the collector, a volumetric pump 3 and a fermenting vessel k. The inlet 5 of the volumetric pump 3 communicated with the screw conveyor 2 is located below the level of the lower part of the fermentation tank 4, and the pump is connected to the upper part of the tub k by the raw material supply pipe 6 equipped with an injector 7; Injector 7 is installed on the carbon dioxide supply line 8 and communicated with the pipeline 6 of the feed at the point located in the zone of the outlet 9 of the volumetric pump. The screw conveyor 2 is made in increments that increase in the direction of movement the year with ridges, and the pump 3 is equipped with a rotor 10 and a flap 11 hinged on the axis 12. The installation works as follows. Berries with crests are loaded into box 1, from which the conveyor 2 years move without squeezing. In the direction of the inlet 5 to the pump 3. The increased conveyor pitch in the zone of the pump inlet ensures that the year is pumped to a vacuum state. Volumom1 reticular 3 feeds years into pipeline 6, we assume that when the rotor 10 rotates the years it rotates, pressure periodically increases in the pump cavity. At the end of the compression stroke, the rotor opens the above cavity, which communicates through the outlet 9 with the pipeline cavity 6 feedstock feedstock. As a result of the hydraulic shock arising at this moment, the shell is broken for a year and the internal content (not more than 5) is released. By pipeline 6, the mass with ridges, surrounded by a partially separated liquid, is fed to the fermentation tank. Moreover, the years surrounded by a liquid express an incompressible mixture, kstorz moves through the pipeline 6 without a year of compression. At the beginning of the journey through pipeline 6, the mixture of the year of liquid with the purpose of preventing the development of the oxidation process is exposed to carbon dioxide supplied through injector J. Thus, the designs of the variable-screw screw conveyor from the volumetric pump ensure that the contents of the year remain inside the shell of the latter. As a result, the subsequent fermentation proceeds mainly inside the shell of each year, providing high quality wine. An apparatus for transferring raw materials to a fermentation tank in the production of wines by carbon dioxide maceration, comprising a collection, a screw conveyor for moving the year with ridges, located in the lower part of the collection, a fermentation tank and a pipeline system for raw materials and carbon dioxide, respectively, characterized in that In order to improve the quality of the finished product, it is equipped with a volumetric pump communicated with a screw conveyor, the inlet of which is located below the level of the lower part of the fermentation tank. and connected by a pipeline, feeding the raw material with its upper part and an injector installed on the carbon dioxide supply pipeline and communicating with the raw material supply pipeline at a point located in the outlet nozzle of the volumetric pump, while the screw conveyor is made in increments in the direction of movement year combed Sources of information taken into account in the examination 1. French Patent No. 23P8 (3, Cl. C 12 G 1/04, published 1977.
类似技术:
公开号 | 公开日 | 专利标题
SU886754A3|1981-11-30|Unit for pumping raw material in fermentation tank at wine production by carbon dioxide maceration
FI58655C|1981-03-10|APPARATUR FOER FRAMSTAELLNING AV SOCKER AV HEMICELLULOSAHALTIGA RAOAEMNEN I SYNNERHET FOER FRAMSTAELLNING AV XYLOS AV XYLANHALTIGA RAOAEMNEN
EP3484945B1|2020-06-03|Method for treating lignocellulosic biomass by impregnation and steam explosion
US20130129573A1|2013-05-23|System and apparatus to extract and reduce dissolved hemi-cellulosic solids in biomass following pre-hydrolysis
CN102131940A|2011-07-20|Method for low water hydrolysis or pretreatment of polysaccharides in a lignocellulosic feedstock
US4025356A|1977-05-24|Method for continuous hydrolysis of pentose containing material and apparatus for implementing the method
RO111201B1|1996-07-30|Peat extraction process and plant for its extraction thereof
CN211595585U|2020-09-29|Reation kettle is used in processing of cedar wood bits extraction essential oil
US3256808A|1966-06-21|Screw press extractor
US4643088A|1987-02-17|Method and device for extracting juice from fruit
CN1284586A|2001-02-21|Method for treatment of biological base filamentary material
US3851087A|1974-11-26|Process for countercurrent pomace washing
CN207129460U|2018-03-23|Mature vinegar storage tank
CN207086123U|2018-03-13|A kind of horizontal ultrasonic wave added two-phase spiral centrifuge
US1880772A|1932-10-04|Apparatus for producing methane
CN205395232U|2016-07-27|Natural pond sediment degree of depth dehydration subassembly
US3256800A|1966-06-21|Cooker-digester
RU2382082C1|2010-02-20|Method of production of hydrolysate from starch-containing material
CN107447057A|2017-12-08|A kind of biomass continuous hydrolysis and the device of compression forming
CN212164748U|2020-12-18|Filling device based on goose sausage fermentation
SU765353A1|1980-09-23|Unit for producing fermentized wort from pulp
SU281158A1|1969-11-30|
RU1770356C|1992-10-23|Plant for continuous fermentation of grape pulp
CN212353021U|2021-01-15|Reducing mechanism for feed production
US3401040A|1968-09-10|Continuous separation of juice from grape solids
同族专利:
公开号 | 公开日
FR2392115A1|1978-12-22|
FR2392115B1|1980-02-15|
ES470186A1|1979-01-01|
US4238511A|1980-12-09|
IT7823801D0|1978-05-25|
IT1096231B|1985-08-26|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题

US3741770A|1971-08-20|1973-06-26|Olphen G Van|Preparation of wine|IT1165777B|1982-11-05|1987-04-29|Primo Melandri|VINIFICATION PROCESS AND PLANT TO IMPLEMENT IT|
NZ207360A|1983-03-23|1987-06-30|Hickinbotham Winemakers|Method and apparatus for producing wine by full carbonic maceration|
FR2545500A1|1983-05-05|1984-11-09|Imeca Oenologie|Process and installation for winemaking under carbon dioxide pressure|
US4952417A|1987-02-09|1990-08-28|Ramon Escola Gallart|Apparatus for incorporating gas into a sugar mass|
DE3708465A1|1987-03-16|1988-09-29|Kohlensaeurewerk Deutschland|METHOD FOR PREPARING WINE|
US5468508A|1991-10-17|1995-11-21|The University Of British Columbia|Preservation of fresh fruit juices and fruit juice blends|
US5869114A|1994-03-18|1999-02-09|Labatt Brewing Company Limited|Production of fermented malt beverages|
US5304384A|1993-03-23|1994-04-19|Labatt Brewing Company Limited|Improvements in production of fermented malt beverages|
US5695795A|1993-03-23|1997-12-09|Labatt Brewing Company Limited|Methods for chill-treating non-distilled malted barley beverages|
USRE36897E|1993-03-23|2000-10-03|Labatt Brewing Company Limited|Methods for chill treating non-distilled malted barley beverages|
AR041675A1|2002-10-28|2005-05-26|Linde Ag|PROCESS TO COOL HARVESTED GRAPES AND APPARATUS TO PRODUCE WINE|
IT1393121B1|2009-03-05|2012-04-11|Air Liquide Italia S P A|METHOD AND PLANT FOR THE REMOVAL OF DISSOLVED OXYGEN AND MAINTENANCE IN CONTROLLED GRAPE ATMOSPHERE, OR OTHER VEGETABLE PRODUCTS, IN MECHANICAL MEANS OF COLLECTION, TRANSPORT AND STORAGE|
MD586Z|2012-04-04|2013-08-31|Иван ПРИДА|Process for producing red wine|
RU2684718C1|2018-12-03|2019-04-11|Олег Максимович Швецов|Carbon dioxide maceration|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
FR7717294A|FR2392115B1|1977-05-26|1977-05-26|
[返回顶部]