CN105670867B - A kind of operating method of production line that brewing morat - Google Patents
A kind of operating method of production line that brewing morat Download PDFInfo
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- CN105670867B CN105670867B CN201610217092.8A CN201610217092A CN105670867B CN 105670867 B CN105670867 B CN 105670867B CN 201610217092 A CN201610217092 A CN 201610217092A CN 105670867 B CN105670867 B CN 105670867B
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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
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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
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- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
A kind of operating method of production line that brewing morat, wall-breaking machine is set between rewinding pond and fermentor, pressure and temp control cabinet is set between distiller and cooling tower, conducting wire is arranged in pressure and temp control cabinet between distiller, cooling tower respectively, steam generator is set between distiller and fermentor, steam transfer tube is set between steam generator and distiller lower section；The mulberries of picking mid-May green non-pollution, mulberries cannot clean direct weighing, broken wall is slurry in into wall-breaking machine, particulate matter in mulberries slurry is absorbed by the absorbent core in filter, it is had to enter into fermentor in four hours after mulberries picking, after fermentation, mulberries slurry pours into alembic, steam in alembic becomes steam after making mulberries slurry boiling, entering back into cooling tower cooler becomes morat, alcoholic strength can be distilled out in the wine of 67-70 degree one time, simplify distillation number, the excellent quality of morat obtained.
Description
Technical field
The present invention relates to brewing device, especially a kind of operating method for the production line for brewing morat.
Background technique
When existing fruit wine is brewed, load weighted raw material is poured into crusher and is crushed, is reloaded into fermentor, sent out
Blender in fermentation tank stirs evenly post-fermentation to particle, and since mulberries belong to perishable, perishable kind uses existing production
Equipment is long using handling time, will lead to it is broken be not thorough, it is longer that the time is expended before fermentation tank of setting out, and after fermentation tank of setting out,
It is not easy to stir evenly, makes mulberries be difficult to be sufficiently carried out fermentation, influence the quality of morat.
In view of the foregoing, the structure of existing wine brewing production equipment needs to improve.
Summary of the invention
Purpose of the invention is to overcome the shortcomings in the prior art, provides a kind of behaviour of production line for brewing morat
Make method, alcoholic strength can be distilled out in the wine of 67-70 degree one time, simplifies distillation number, refining effect is ideal, distiller energy
The enough very effective wine for extracting more high alcohol content, this production line greatly improve production efficiency, reduce production cost, make
The excellent quality of the morat obtained, structure is simple, and novel in design, easy to operate, easy to use, manufacturing cost is cheap.
The present invention to achieve the goals above, adopts the following technical scheme that a kind of operation of production line for brewing morat
Method, a kind of production line that brewing morat be by: material pond, sensor, display screen, wall-breaking machine, feeding warehouse, grout outlet,
Promote conveyer, fermentation tank, feed inlet, spare feed inlet, folding lid, filter, plush copper, grate, absorbent core, inner wall, liquid
Position meter, the first forced feed pump, the second forced feed pump, steam generator, alembic, steam collector, intercondenser, top
Condenser, pressure and temp control cabinet, cooling tower is held to constitute；Wall-breaking machine, distiller and cooling are set between rewinding pond and fermentor
Pressure and temp control cabinet is set between tower, and conducting wire, distiller is arranged in pressure and temp control cabinet between distiller, cooling tower respectively
Steam generator is set between fermentor, steam transfer tube is set between steam generator and distiller lower section；
The structure in the rewinding pond are as follows: material pond is cuboid or square, and sensor, material pond is arranged in the bottom surface quadrangle of material pond
Side wall on display screen is set, display screen side setting button inputs control area；Feeding warehouse is set above the wall-breaking machine, it is described
Setting promotes conveyer in feeding warehouse and the material pond；
The structure of the fermentor are as follows: the top surface setting feed inlet of fermentation tank and spare feed inlet, bottom surface are set as boring
Shape, bottom center be arranged discharge nozzle, bottom surface side be arranged schlempe sealing cover, the side of fermentation tank set gradually from the bottom to top to
Lack a probe tube, at least one observation window and liquidometer are set on the tank skin of fermentation tank, setting is opened above spare feed inlet
Filter is arranged in closing lid, feed inlet upper seal, and folding lid, setting at least four below filter with inner surface are arranged above filter
The plush copper of a cambered surface protrusion, the plush copper top are arranged grate, cylindrical body absorbent core are arranged above grate, and the absorbent core uses
The active carbon fibrous absorption material directly bought from market；Drum-shaped inner wall, the upper and lower side difference of inner wall are set in fermentation tank
It is fixedly installed with top surface, bottom surface, vacuum layer, the first forced feed pump difference is constituted between the inner wall and fermentation tank inner surface
Hose is arranged between the discharge nozzle of subjacent in import with filter；Second forced feed pump respectively with the pulp of wall-breaking machine
Mouthful, hose is set between the import of filter；
The structure of the steam generator are as follows: setting heating furnace and water tank in steam generator, between heating furnace and water tank
Water pump is set, is provided with heat-generating pipe in heating furnace；
The structure of the distiller are as follows: the bottom surface and top surface of alembic are disposed as spherical surface, and inlet is arranged in top surface side,
Pressure gauge is arranged in the other side, and sealing cover is arranged above the inlet, and top face corresponds to the venthole setting pumpkin-shaped at center
Intercondenser, the top condenser and centre is arranged between steam collector top and top condenser in steam collector
Condenser is inverted funnel shape, and the volume of top condenser is less than the volume of intercondenser, the outlet of the steam collector
Circularhole diameter be less than the Circularhole diameter of import, the Circularhole diameter of the outlet of the intercondenser is less than the Circularhole diameter of import
Half, the Circularhole diameter of the outlet of the top condenser is less than the half of the Circularhole diameter of import, alembic
Subjacent discharge port is set, scarfing cinder lid is arranged in side below the outer wall of alembic, and outlet is arranged in the other side；
The structure of the cooling tower are as follows: wine inlet is arranged in cooling tower upper center, and water inlet, outer wall is arranged above outer wall
Wine outlet is arranged in lower section side, and water outlet is arranged in the other side；
Alcohol vapor delivery pipe is set between top condenser upper end and the wine inlet；
PLC automatic control system is set in the pressure and temp control cabinet, automatically controls the pressure in distiller and cooling tower
Power and temperature, which are maintained at, to be set in value range；
Mid-May picks the mulberries of green non-pollution, and to the same garden same period, the mulberries of picking make marks, respectively
Classification is stacked wait weigh, and before weighing, after being removed the peel by key-press input control area to material pond, zero setting, mulberries cannot be cleaned and directly be put
Enter material pond, the weight data that four sensors will test is transmitted to display screen, and the summation that four weight datas are added is equal to whole
Mulberries in material pond after the mulberries weight record in whole pond, are delivered to feeding warehouse by promotion conveyer by the mulberries weight in pond, then into
Entering broken wall in wall-breaking machine is slurry, and mulberries slurry is pumped through grout outlet, hose into the second forced feed, and the second forced feed pump generates
Pressure mulberries starched be delivered to filter through hose, mulberries slurry flows through absorbent core, grate enters fermentation tank, in mulberries slurry
Particulate matter is adsorbed core and is absorbed, and fermentation tank uses 30-32 tons, and liquidometer shows the volume of mulberries slurry in fermentation tank, mulberry
18-23 ton hour, which is added, in Shen slurry stops, and into fermentation tank, sugaring is to improve its alcoholic strength, while brewer yeast is added；Mulberries picking
It is had to enter into fermentor in four hours afterwards, mulberries are more than to begin within four hours to rot, is mouldy, rotten, are gradually become by light violet color
For brown purple or brown, mouthfeel can be sour, influences the quality of morat；Mulberries cannot clean, and cleaning will lead to the battalion in mulberries epidermis
Substance is supported to be lost；
The folding lid on filter is opened, used absorbent core is taken out, separately takes new absorbent core to be put into filter, mulberries
Slurry flows through hose by the discharge nozzle of fermentation tank bottom and pumps into the first forced feed, and the pressure that the first forced feed pump generates will
Mulberries slurry is delivered to filter through hose, and mulberries slurry flows through absorbent core, grate enters fermentation tank, the particulate matter quilt in mulberries slurry
Absorbent core is absorbed, and is recycled as above, make mulberries slurry be uniformly mixed, from the probe tube of fermentation tank side sample into
Row chemical examination after the admixture of mulberries slurry reaches the standard of setting, closes the discharge nozzle of fermentation tank bottom, will be on feed inlet
The filter of side is removed, and is sealed with folding lid to feed inlet, is made whole fermentor air-tight state, starches fermentation using high to mulberries
Temperature is fermented, and the fermentation temperature in fermentor is set as 29-35 DEG C, and the vacuum layer constituted between inner wall and fermentation tank inner surface is protected
Hinder in entire fermentation process, mulberries slurry is not influenced by ambient temperature；
The attenuation degree of mulberries slurry is observed by the observation window on the tank skin of fermentation tank, and is sampled and carried out by probe tube
Chemical examination opens the sealing cover above the inlet of alembic, fermentor after the yeastiness of mulberries slurry reaches the standard of setting
Hose is set between the discharge nozzle of body bottom and the inlet, and mulberries slurry flows into alembic through hose, reaches the standard of setting
After volume, the discharge nozzle of fermentation tank bottom is closed, the water in steam generator inner water tank flows into heating furnace, heating furnace through water pump
Interior heat-generating pipe uses 24 kilowatts of electric furnace heating wire, and heat-generating pipe, which heats water, becomes steam for water, and steam temperature is 110-120 DEG C,
Disk-shaped tube is arranged in bottom in alembic, and core is arranged on disk-shaped tube, and the aperture of the core of ecto-entad is changed from small to big on disk-shaped tube,
Steam in steam generator enters in disk-shaped tube through steam transfer tube, and steam is emerged from core, and steam is steaming mulberries slurry
Rolling in tank is evaporated, the steam generated after mulberries slurry boiling is upwardly into the steam collector of pumpkin-shaped, steaming of the steam in pumpkin-shaped
Convolution overturning increases the alcoholic strength of steam, then the top of the intercondenser through inverted funnel shape, inverted funnel shape in gas collector
Condenser enters alcohol vapor delivery pipe, then enters cooling tower through wine inlet, and coolant liquid is flowed by the water inlet of cooling tower, from
Water outlet outflow, the heat exchanger tube in cooling tower use copper tube, and steam and coolant liquid indirect heat exchange make steam become the mulberry of liquid
Shen wine, the PLC automatic control system in pressure and temp control cabinet automatically control the pressure and temperature in distiller and cooling tower and protect
It holds and is being set in value range, morat is flowed out by wine outlet；
The alcoholic strength of first wine can reach 70 degree, 60 degree, 55 degree, 50 degree, 45 degree is gradually reduced to, for different section alcoholic strengths
Morat classify filling storage.
The beneficial effects of the present invention are: the configuration of the present invention is simple, novel in design, easy to operate, easy to use, manufacturing cost
Cheap, high-quality, long-time service is hardly damaged, and using effect is good, by the consistent favorable comment of client；The alcohol for the wine that the present invention generates
Degree has simplified distillation number in 67-70 degree, and existing distiller needs to distill twice, and the present invention can distill out alcohol one time
The wine in 67-70 degree is spent, refining effect is ideal, and distiller is capable of the wine of very effective extraction more high alcohol content, this production line
Production efficiency is greatly improved, production cost is reduced, the excellent quality of morat obtained is suitble to popularity application.
Detailed description of the invention
The present invention will be further explained below with reference to the attached drawings:
Fig. 1 is general assembly structural schematic diagram；
In Fig. 1: material pond 1-1, sensor 1-2, display screen 1-3, wall-breaking machine 2-1, feeding warehouse 2-2, grout outlet 2-3, being promoted
Conveyer 2-4, fermentation tank 3-1, feed inlet 3-2, spare feed inlet 3-3, folding lid 3-4, filter 3-5, plush copper 3-51, grate
Sub- 3-52, absorbent core 3-53, inner wall 3-6, liquidometer 3-7, the first forced feed pump 3-8, the second forced feed pump 3-9, steam
Generator 4, alembic 5-1, steam collector 5-2, intercondenser 5-3, top condenser 5-4, pressure and temp control cabinet 6,
Cooling tower 7.
Specific embodiment
Below with reference to embodiment 1, invention is further described in detail with specific embodiment:
Embodiment 1
Wall-breaking machine 2-1 is set between rewinding pond and fermentor, pressure and temp control cabinet is set between distiller and cooling tower 7
6, conducting wire is arranged in pressure and temp control cabinet 6 between distiller, cooling tower 7 respectively, and steam is arranged between distiller and fermentor
Steam transfer tube is set between below generator 4, steam generator 4 and distiller；
The structure in the rewinding pond are as follows: material pond 1-1 is cuboid or square, and sensing is arranged in the bottom surface quadrangle of material pond 1-1
Device 1-2, display screen 1-3 is arranged on the side wall of material pond 1-1, and display screen 1-3 side setting button inputs control area；The wall-breaking machine
Setting promotes conveyer 2-4 in setting feeding warehouse 2-2, the feeding warehouse 2-2 and the material pond 1-1 above 2-1；
The structure of the fermentor are as follows: feed inlet 3-2 and spare feed inlet 3-3, bottom surface is arranged in the top surface of fermentation tank 3-1
Be set as taper, bottom center is arranged discharge nozzle, and bottom surface side is arranged schlempe sealing cover, the side of fermentation tank 3-1 by down toward
On set gradually at least one probe tube, at least one observation window and liquidometer 3-7 are set on the tank skin of fermentation tank 3-1, it is standby
With setting folding lid 3-4, feed inlet 3-2 upper seal above feed inlet 3-3, filter 3-5, setting above filter 3-5 are set
Below folding lid 3-4, filter 3-5 inner surface above the plush copper 3-51, the plush copper 3-51 of setting at least four cambered surfaces protrusion
Grate 3-52 is set, cylindrical body absorbent core 3-53 is set above grate 3-52, the absorbent core 3-53 is used and directly purchased from market
The active carbon fibrous absorption material bought；Drum-shaped inner wall 3-6 is set in fermentation tank 3-1, the upper and lower side of inner wall 3-6 respectively with top
Face, bottom surface fixed setting, constitute vacuum layer between the inner wall 3-6 and fermentation tank 3-1 inner surface, the first forced feed pumps 3-
8 respectively with the import of filter 3-5, subjacent discharge nozzle between hose is set；Second forced feed pump 3-9 respectively with it is broken
Hose is set between the import of the grout outlet 2-3, filter 3-5 of wall machine 2-1；
The structure of the steam generator 4 are as follows: setting heating furnace and water tank in steam generator 4, heating furnace and water tank it
Between water pump is set, be provided with heat-generating pipe in heating furnace；
The structure of the distiller are as follows: the bottom surface and top surface of alembic 5-1 is disposed as spherical surface, and feed liquor is arranged in top surface side
Mouthful, pressure gauge is arranged in the other side, and sealing cover is arranged above the inlet, and top face corresponds to the venthole setting pumpkin at center
Intercondenser 5-3, the top is arranged in shape steam collector 5-2, steam collector 5- between top and top condenser 5-4
End condenser 5-4 and intercondenser 5-3 is inverted funnel shape, and the volume of top condenser 5-4 is less than intercondenser 5-3's
Volume, the Circularhole diameter of the outlet of the steam collector 5-2 are less than the Circularhole diameter of import, the intercondenser 5-3's
The Circularhole diameter of outlet is less than the half of the Circularhole diameter of import, the Circularhole diameter of the outlet of the top condenser 5-4
Less than the half of the Circularhole diameter of import, the subjacent of alembic 5-1 is arranged discharge port, under the outer wall of alembic 5-1
Scarfing cinder lid is arranged in square side, and outlet is arranged in the other side；
The structure of the cooling tower 7 are as follows: wine inlet is arranged in 7 upper center of cooling tower, water inlet is arranged above outer wall, outside
Wine outlet is arranged in side below wall, and water outlet is arranged in the other side；
Alcohol vapor delivery pipe is set between the upper end top condenser 5-4 and the wine inlet；
PLC automatic control system is set in the pressure and temp control cabinet 6, is automatically controlled in distiller and cooling tower 7
Pressure and temperature, which is maintained at, to be set in value range；
Mid-May picks the mulberries of green non-pollution, and to the same garden same period, the mulberries of picking make marks, respectively
Classification is stacked wait weigh, and before weighing, after being removed the peel by key-press input control area to material pond 1-1, zero setting, mulberries cannot be cleaned directly
It is put into material pond 1-1, the weight data that four sensor 1-2 will test is transmitted to display screen 1-3, what four weight datas were added
Summation is equal to the mulberries weight in whole pond, after the mulberries weight record in whole pond, by promotion conveyer 2-4 by the mulberries in material pond 1-1
It is delivered to feeding warehouse 2-2, entering back into broken wall in wall-breaking machine 2-1 is slurry, and mulberries slurry enters the last the second through grout outlet 2-3, hose
Mulberries are starched and are delivered to filter 3-5, mulberries slurry stream through hose by feeding pump 3-9 processed, the pressure that the second forced feed pump 3-9 is generated
Enter fermentation tank 3-1 through absorbent core 3-53, grate 3-52, the particulate matter in mulberries slurry is adsorbed core 3-53 and is absorbed, fermented
Tank body 3-1 uses 30-32 tons, and liquidometer 3-7 shows the volume of mulberries slurry in fermentation tank 3-1, and 18-23 ton hour is added in mulberries slurry
Stop, into fermentation tank 3-1, sugaring is to improve its alcoholic strength, while brewer yeast is added；It is necessary in four hours after mulberries picking
Into in fermentor, mulberries are more than to begin within four hours to rot, is mouldy, rotten, gradually become brown purple or brown, mouth by light violet color
Sense can be sour, influences the quality of morat；Mulberries cannot clean, and cleaning will lead to the nutriment in mulberries epidermis and be lost；
The folding lid 3-4 on filter 3-5 is opened, used absorbent core 3-53 is taken out, new absorbent core 3-53 is separately taken to put
Entering in filter 3-5, mulberries slurry flows through hose by the discharge nozzle of the bottom fermentation tank 3-1 and pumps 3-8 into the first forced feed, the
The pressure that one forced feed pump 3-8 is generated, which starches mulberries, is delivered to filter 3-5 through hose, mulberries slurry flow through absorbent core 3-53,
Grate 3-52 enters fermentation tank 3-1, and the particulate matter in mulberries slurry is adsorbed core 3-53 and is absorbed, followed as above
Ring is uniformly mixed mulberries slurry, is chemically examined from the sampling of the probe tube of the side fermentation tank 3-1, and the admixture of mulberries slurry reaches
To after the standard of setting, the discharge nozzle of the bottom fermentation tank 3-1 is closed, the filter 3-5 above feed inlet 3-2 is removed,
Feed inlet 3-2 is sealed with folding lid 3-4, makes whole fermentor air-tight state, hot fermentation, hair are used to mulberries slurry fermentation
Fermentation temperature in fermentation tank is set as 29-35 DEG C, the vacuum layer guarantee constituted between inner wall 3-6 and fermentation tank 3-1 inner surface
In entire fermentation process, mulberries slurry is not influenced by ambient temperature；
The attenuation degree of mulberries slurry is observed by the observation window on the tank skin of fermentation tank 3-1, and is sampled by probe tube
It is chemically examined, after the yeastiness of mulberries slurry reaches the standard of setting, the sealing cover above the inlet of alembic 5-1 is beaten
It opens, hose is set between the discharge nozzle and the inlet of the bottom fermentation tank 3-1, mulberries slurry flows into alembic 5-1 through hose,
After the normal volume for reaching setting, the discharge nozzle of the bottom fermentation tank 3-1, the Shui Jingshui in 4 inner water tank of steam generator are closed
Pump flows into heating furnace, and the heat-generating pipe in heating furnace uses 24 kilowatts of electric furnace heating wire, and heat-generating pipe, which heats water, becomes steam for water, steams
Temperature degree is 110-120 DEG C, and disk-shaped tube is arranged in bottom in alembic 5-1, and core, ecto-entad on disk-shaped tube is arranged on disk-shaped tube
The aperture of core change from small to big, the steam in steam generator 4 enters in disk-shaped tube through steam transfer tube, and steam is from core
It emerges, steam makes mulberries slurry roll in alembic 5-1, and the steam generated after mulberries slurry boiling is upwardly into the steam of pumpkin-shaped
Collector 5-2, steam overturning of circling round in the steam collector 5-2 of pumpkin-shaped increase the alcoholic strength of steam, then through inverted funnel
The intercondenser 5-3 of shape, the top condenser 5-4 of inverted funnel shape enter alcohol vapor delivery pipe, then enter through wine inlet
Cooling tower 7, coolant liquid are flowed by the water inlet of cooling tower 7, are flowed out from water outlet, and the heat exchanger tube in cooling tower 7 uses copper tube,
Steam and coolant liquid indirect heat exchange make steam become the morat of liquid, the PLC automatic control system in pressure and temp control cabinet 6
Pressure and temperature in automatic control distiller and cooling tower 7, which is maintained at, to be set in value range, and morat is flowed out by wine outlet；
The alcoholic strength of first wine can reach 70 degree, 60 degree, 55 degree, 50 degree, 45 degree is gradually reduced to, for different section alcoholic strengths
Morat classify filling storage.
Claims (1)
1. a kind of operating method for the production line for brewing morat, a kind of production line that brewing morat is by material pond (1-
1), sensor (1-2), display screen (1-3), wall-breaking machine (2-1), feeding warehouse (2-2), grout outlet (2-3), promotion conveyer (2-
4), fermentation tank (3-1), feed inlet (3-2), spare feed inlet (3-3), folding lid (3-4), filter (3-5), plush copper (3-
51), grate (3-52), absorbent core (3-53), inner wall (3-6), liquidometer (3-7), the first forced feed pump (3-8), the last the second
Feeding pump (3-9) processed, steam generator (4), alembic (5-1), steam collector (5-2), intercondenser (5-3), top
Condenser (5-4), pressure and temp control cabinet (6), cooling tower (7) are constituted；It is characterized by: being arranged between rewinding pond and fermentor
Pressure and temp control cabinet (6) are arranged between distiller and cooling tower (7) in wall-breaking machine (2-1), and pressure and temp control cabinet (6) is respectively
Conducting wire is set between (7) with distiller, cooling tower, steam generator (4) are set between distiller and fermentor, steam generator
(4) steam transfer tube is set between distiller lower section；
The structure in the rewinding pond are as follows: material pond (1-1) is cuboid or square, and sensing is arranged in the bottom surface quadrangle of material pond (1-1)
Display screen (1-3) is arranged on the side wall of material pond (1-1) in device (1-2), and display screen (1-3) side setting button inputs control area；Institute
It states and feeding warehouse (2-2) is set above wall-breaking machine (2-1), the feeding warehouse (2-2) and the material pond (1-1) interior setting promote transmission
Machine (2-4)；
The structure of the fermentor are as follows: top surface setting feed inlet (3-2) of fermentation tank (3-1) and spare feed inlet (3-3), bottom
Face is set as taper, and bottom center is arranged discharge nozzle, and bottom surface side is arranged schlempe sealing cover, the side of fermentation tank (3-1) by
Under it is supreme set gradually at least one probe tube, at least one observation window and liquidometer are set on the tank skin of fermentation tank (3-1)
(3-7), spare feed inlet (3-3) top setting folding lid (3-4), feed inlet (3-2) upper seal setting filter (3-5),
Folding lid (3-4) is set above filter (3-5), at least four cambered surfaces of setting protrusion is convex below filter (3-5) inner surface
Head (3-51), plush copper (3-51) top are arranged grate (3-52), cylindrical body absorbent core (3- are arranged above grate (3-52)
53), the absorbent core (3-53) is using the active carbon fibrous absorption material directly bought from market；It is set in fermentation tank (3-1)
It sets drum-shaped inner wall (3-6), the upper and lower side of inner wall (3-6) is fixedly installed with top surface, bottom surface respectively, the inner wall (3-6) and hair
Constitute vacuum layer between fermentation tank body (3-1) inner surface, the first forced feed pump (3-8) respectively with the import of filter (3-5), bottom
Hose is set between discharge nozzle below face；Second forced feed pump (3-9) respectively with the grout outlet (2-3) of wall-breaking machine (2-1),
Hose is set between the import of filter (3-5)；
The structure of the steam generator (4) are as follows: setting heating furnace and water tank in steam generator (4), heating furnace and water tank it
Between water pump is set, be provided with heat-generating pipe in heating furnace；
The structure of the distiller are as follows: the bottom surface and top surface of alembic (5-1) are disposed as spherical surface, and feed liquor is arranged in top surface side
Mouthful, pressure gauge is arranged in the other side, and sealing cover is arranged above the inlet, and top face corresponds to the venthole setting pumpkin at center
Intercondenser (5- is arranged between steam collector (5-2) top and top condenser (5-4) in shape steam collector (5-2)
3), the top condenser (5-4) and intercondenser (5-3) are inverted funnel shape, and the volume of top condenser (5-4) is less than
The volume of intercondenser (5-3), the Circularhole diameter of the outlet of the steam collector (5-2) are less than the Circularhole diameter of import,
The Circularhole diameter of the outlet of the intercondenser (5-3) is less than the half of the Circularhole diameter of import, the top condensing
The Circularhole diameter of the outlet of device (5-4) is less than the half of the Circularhole diameter of import, the subjacent setting of alembic (5-1)
Scarfing cinder lid is arranged in the outer wall lower section side of discharge port, alembic (5-1), and outlet is arranged in the other side；
The structure of the cooling tower (7) are as follows: wine inlet is arranged in cooling tower (7) upper center, water inlet is arranged above outer wall, outside
Wine outlet is arranged in side below wall, and water outlet is arranged in the other side；
Alcohol vapor delivery pipe is set between the top condenser upper end (5-4) and the wine inlet；
PLC automatic control system is set in the pressure and temp control cabinet (6), is automatically controlled in distiller and cooling tower (7)
Pressure and temperature, which is maintained at, to be set in value range；
Mid-May picks the mulberries of green non-pollution, and to the same garden same period, the mulberries of picking make marks, and sort out respectively
It stacks wait weigh, before weighing, after being removed the peel by key-press input control area to material pond (1-1), zero setting, mulberries cannot be cleaned and directly be put
Enter material pond (1-1), the weight data that four sensors (1-2) will test is transmitted to display screen (1-3), four weight data phases
The summation added is equal to the mulberries weight in whole pond, after the mulberries weight record in whole pond, by promotion conveyer (2-4) by material pond (1-1)
Interior mulberries are delivered to feeding warehouse (2-2), enter back into wall-breaking machine (2-1) interior broken wall be slurry, mulberries slurry through grout outlet (2-3),
Hose enters the second forced feed pump (3-9), and mulberries are starched and are delivered to through hose by the pressure that the second forced feed pump (3-9) generates
Filter (3-5), mulberries slurry flows through absorbent core (3-53), grate (3-52) enters fermentation tank (3-1), the particle in mulberries slurry
Object is adsorbed core (3-53) and is absorbed, and fermentation tank (3-1) uses 30-32 tons, and liquidometer (3-7) shows fermentation tank (3-1)
The volume of interior mulberries slurry, 18-23 ton hour, which is added, in mulberries slurry stops, to fermentation tank (3-1) interior sugaring to improve its alcoholic strength, together
When brewer yeast is added；It is had to enter into fermentor in four hours after mulberries picking, mulberries are more than to begin to rot, send out for four hours
It is mould, rotten, brown purple or brown is gradually become by light violet color, mouthfeel can be sour, influences the quality of morat；Mulberries cannot clean, clearly
The nutriment that washing will lead in mulberries epidermis is lost；
The folding lid (3-4) on filter (3-5) is opened, used absorbent core (3-53) is taken out, separately takes new absorbent core (3-
53) it is put into filter (3-5), mulberries slurry flows through hose by the discharge nozzle of the bottom fermentation tank (3-1) and forces to feed into first
Mulberries are starched and are delivered to filter (3-5) through hose by material pump (3-8), the pressure that the first forced feed pump (3-8) generates, mulberries slurry
Flow through absorbent core (3-53), grate (3-52) enter fermentation tank (3-1), mulberries slurry in particulate matter be adsorbed core (3-53) institute
It absorbs, is recycled as above, be uniformly mixed mulberries slurry, sample and carry out from the probe tube of the side fermentation tank (3-1)
Chemical examination after the admixture of mulberries slurry reaches the standard of setting, is closed the discharge nozzle of the bottom fermentation tank (3-1), will be fed
Filter (3-5) above mouth (3-2) is removed, and is sealed with folding lid (3-4) to feed inlet (3-2), is kept whole fermentor close
Closed state uses hot fermentation to mulberries slurry fermentation, and the fermentation temperature in fermentor is set as 29-35 DEG C, inner wall (3-6) and hair
The vacuum layer constituted between fermentation tank body (3-1) inner surface ensures in entire fermentation process that mulberries are starched not by ambient temperature
It influences；
Observe the attenuation degree of mulberries slurry by observation window on the tank skin of fermentation tank (3-1), and by probe tube sample into
Row chemical examination beats the sealing cover above the inlet of alembic (5-1) after the yeastiness of mulberries slurry reaches the standard of setting
It opens, hose is set between the discharge nozzle and the inlet of the bottom fermentation tank (3-1), mulberries slurry flows into alembic through hose
(5-1) after the normal volume for reaching setting, closes the discharge nozzle of the bottom fermentation tank (3-1), steam generator (4) inner water tank
Interior water flows into heating furnace through water pump, and the heat-generating pipe in heating furnace uses 24 kilowatts of electric furnace heating wire, and heat-generating pipe heats water water
Become steam, steam temperature is 110-120 DEG C, and disk-shaped tube is arranged in the interior bottom of alembic (5-1), and core, disk is arranged on disk-shaped tube
The aperture of the core of ecto-entad is changed from small to big on shape pipe, and the steam in steam generator (4) enters dish type through steam transfer tube
In pipe, steam is emerged from core, and steam makes the rolling in alembic (5-1) of mulberries slurry, the steam generated after mulberries slurry boiling
It is upwardly into the steam collector (5-2) of pumpkin-shaped, steam convolution overturning in the steam collector (5-2) of pumpkin-shaped increases
The alcoholic strength of steam, then the top condenser (5-4) of the intercondenser (5-3) through inverted funnel shape, inverted funnel shape enter alcohol
Then vapor pipe enters cooling tower (7) through wine inlet, coolant liquid is flowed by the water inlet of cooling tower (7), from water outlet stream
Out, the heat exchanger tube in cooling tower (7) uses copper tube, and steam and coolant liquid indirect heat exchange make steam become the morat of liquid,
PLC automatic control system in pressure and temp control cabinet (6) automatically controls the pressure and temperature in distiller and cooling tower (7) and protects
It holds and is being set in value range, morat is flowed out by wine outlet；
The alcoholic strength of first wine can reach 70 degree, 60 degree, 55 degree, 50 degree, 45 degree is gradually reduced to, for the mulberry of different section alcoholic strengths
Shen wine classification filling storage.
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| CN108841472A (en) * | 2018-06-28 | 2018-11-20 | 广西浙缘农业科技有限公司 | Vinous fermentation device |
| CN108841473A (en) * | 2018-06-28 | 2018-11-20 | 广西浙缘农业科技有限公司 | Vinous fermentation system |
| CN108913411A (en) * | 2018-06-28 | 2018-11-30 | 广西浙缘农业科技有限公司 | Vinous fermentation equipment |
| CN109652465A (en) * | 2018-12-09 | 2019-04-19 | 百绿国际草业(北京)有限公司 | The technique and device of ethyl alcohol processed |
| CN113786359B (en) * | 2021-09-22 | 2024-03-08 | 王蕾 | Perfume containing natural plant components and preparation method thereof |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1254752A (en) * | 1999-10-25 | 2000-05-31 | 山东省肥城市轻工机械厂 | Equipment for brewing fruit spirit |
| CN205115429U (en) * | 2015-09-30 | 2016-03-30 | 安徽韵沣农业发展有限公司 | Morat fermenting installation |
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| JP4937050B2 (en) * | 2007-09-06 | 2012-05-23 | 正 矢崎 | Method for distillation of single-distilled liquor and apparatus used therefor |
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Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1254752A (en) * | 1999-10-25 | 2000-05-31 | 山东省肥城市轻工机械厂 | Equipment for brewing fruit spirit |
| CN205115429U (en) * | 2015-09-30 | 2016-03-30 | 安徽韵沣农业发展有限公司 | Morat fermenting installation |
Non-Patent Citations (1)
| Title |
|---|
| 果酒、果醋发酵装置的改进设计;徐海勇;《实验设计与技术》;20100228(第2期);第30页 |
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