CN105670867A - Operation method of production line for brewing mulberry wine - Google Patents
Operation method of production line for brewing mulberry wine Download PDFInfo
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- CN105670867A CN105670867A CN201610217092.8A CN201610217092A CN105670867A CN 105670867 A CN105670867 A CN 105670867A CN 201610217092 A CN201610217092 A CN 201610217092A CN 105670867 A CN105670867 A CN 105670867A
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- mulberries
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- fermentation tank
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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
Abstract
Provided is an operation method of a production line for brewing mulberry wine.A wall breaking machine is arranged between a material collecting pond and a fermentation tank; a pressure and temperature control box is arranged between a distiller and a cooling tower; a wire is arranged between the pressure and temperature control box and the distiller, and a wire is arranged between the pressure and temperature control box and the cooling tower; a steam generator is arranged between the distiller and the fermentation tank, and a steam conveying pipe is arranged between the steam generator and the position below the distiller.Green and pollution-free mulberries are picked in the middle ten days of May, the mulberries are directly weighed without being cleaned and enter the wall breaking machine to be subjected to wall breaking and become pulp, particular matter in the mulberry pulp is absorbed by an adsorbing core in a filter, the mulberries must enter the fermentation tank within four hours after being picked, after fermentation, the mulberry pulp is poured into a distilling tank, steam in the distilling tank makes the mulberry pulp boil and become steam, the steam enters the cooling tower to be cooled and become mulberry wine, the wine with the alcoholic strength being 67-70 degrees can be obtained at a time in a distillation mode, the number of distillation times is reduced, and the quality of the made mulberry wine is good.
Description
Technical field
The present invention relates to brewing device, the working method of the production line of especially a kind of brew mulberries wine.
Background technology
During existing fruit wine brew, measured for title raw material is poured into and in crusher, carries out fragmentation, refill in fermentor tank, particle is stirred even secondary fermentation by the stirrer in fermentor tank, owing to mulberries belong to perishable, perishable kind, it may also be useful to existing equipment adopts handing time long, fragmentation can be caused not thorough, expend time in before entering fermentor tank longer, and after entering fermentor tank, not easily stir evenly, make mulberries be difficult to fully ferment, affect the quality of mulberries wine.
In view of the foregoing, the structure of existing wine brewing production unit needs to improve.
Summary of the invention
It is an object of the invention to overcome deficiency of the prior art, it is provided that the working method of the production line of a kind of brew mulberries wine, can distill out the wine of alcoholic strength at 67-70 degree for one time, having simplified distillation number of times, refining effect is desirable, and distiller can the wine of very effective extraction more high alcohol content, this production line greatly improves production efficiency, reducing production cost, the excellent quality of obtained mulberries wine, structure is simple, novel in design, easy to operate, it may also be useful to convenient, cheap for manufacturing cost.
The present invention is in order to realize above-mentioned purpose, adopt following technical scheme: the working method of the production line of a kind of brew mulberries wine, the production line of described a kind of brew mulberries wine be by: material pond, sensor, display screen, wall-breaking machine, feeding warehouse, grout outlet, promote conveyer, fermentation tank, opening for feed, opening for feed for subsequent use, folding lid, strainer, plush copper, grate, absorbent core, inwall, liquidometer, first pressure feeding pump, 2nd pressure feeding pump, steam generator, retort, steam collector, middle condenser, top condenser, pressure and temp controlling box, cooling tower is formed, between rewinding pond and fermentor tank, wall-breaking machine is set, pressure and temp controlling box is set between distiller and cooling tower, pressure and temp controlling box arranges wire respectively and between distiller, cooling tower, steam generator is set between distiller and fermentor tank, between below steam generator and distiller, vapor transmission pipe is set,
The structure in described rewinding pond is: material pond is rectangular parallelepiped or square, and the corner, bottom surface in material pond arranges sensor, and the sidewall in material pond arranges display screen, and display screen side arranges key-press input control area; Above described wall-breaking machine, feeding warehouse is set, in described feeding warehouse and described material pond, lifting conveyer is set;
The structure of described fermentor tank is: the end face of fermentation tank arranges opening for feed and opening for feed for subsequent use, bottom surface is set to taper, bottom center arranges discharging pipe, side, bottom surface arranges wine slag sealing cover, the side of fermentation tank arranges at least one stopple coupon from the bottom to top successively, the tank wall of fermentation tank arranges at least one viewing window and liquidometer, folding lid is set above opening for feed for subsequent use, opening for feed upper seal arranges strainer, folding lid is set above strainer, the plush copper of at least four cambered surface projections is set below filter with inner surface, above described plush copper, grate is set, right cylinder absorbent core is set above grate, described absorbent core adopts the active carbon fibrous absorption material directly bought from market, drum shape inwall is set in fermentation tank, the upper and lower ends of inwall is fixedly installed with end face, bottom surface respectively, form vacuum layer between described inwall and fermentation tank internal surface, between the discharging pipe of the first pressure feeding pump respectively and below the import of strainer, bottom surface, flexible pipe is set, 2nd pressure feeding pump respectively and the grout outlet of wall-breaking machine, strainer import between flexible pipe is set,
The structure of described steam generator is: arrange process furnace and water tank in steam generator, arranges water pump between process furnace and water tank, is provided with heat-generating pipe in process furnace;
The structure of described distiller is: the bottom surface of retort and end face are all set to sphere, end face side arranges fluid inlet, another side arranges tensimeter, above described fluid inlet, sealing cover is set, the production well at the corresponding center of top face arranges pumpkin-shaped steam collector, middle condenser is set above steam collector and between the condenser of top, described top condenser and middle condenser are down doline, the volume of top condenser is less than the volume of middle condenser, the Circularhole diameter of the outlet of described steam collector is less than the Circularhole diameter of import, the Circularhole diameter of the outlet of described middle condenser is less than 1/2nd of the Circularhole diameter of import, the Circularhole diameter of the outlet of described top condenser is less than 1/2nd of the Circularhole diameter of import, below the bottom surface of retort, discharge port is set, below the outer wall of retort, side arranges scarfing cinder lid, another side arranges outlet,
The structure of described cooling tower is: cooling tower upper center arranges wine inlet, arranges water-in above its outer wall, and below outer wall, side arranges wine outlet, and another side sets out the mouth of a river;
Between condenser upper end, described top and described wine inlet, alcohol vapor transfer lime is set;
Process furnace and water tank are set in described steam generator, water pump is set between process furnace and water tank, in process furnace, be provided with heat-generating pipe;
Arranging PLC automatic control system in described pressure and temp controlling box, the pressure and temperature automatically controlled in distiller and cooling tower remains on and is set in value range;
Pluck the mulberries of green non-pollution mid-May, the mulberries that the same garden same time period plucks are made marks, sort out to stack respectively and wait to weigh, before weighing, after material pond being removed the peel by key-press input control area, zero setting, mulberries can not clean directly puts into material pond, the weight data detected is transferred to display screen by four sensors, the summation of four weight data additions equals the mulberries weight in whole pond, after the mulberries weight record in whole pond, by promoting conveyer, the mulberries in material pond are delivered to feeding warehouse, entering broken wall in wall-breaking machine again is slurry, the particle that mulberries contain in starching is between positive and negative 0.3mm, mulberries are starched through grout outlet, flexible pipe enters the 2nd pressure feeding pump, mulberries slurry is delivered to strainer through flexible pipe by the pressure that the 2nd pressure feeding pump produces, mulberries slurry flows through absorbent core, grate enters fermentation tank, particulate matter in mulberries slurry is absorbed by absorbent core, fermentation tank adopts 30-32 ton, the volume of mulberries slurry in liquidometer display fermentation tank, mulberries slurry adds 18-23 ton hour to be stopped, in fermentation tank, sugaring is to improve its alcoholic strength, add brewer yeast simultaneously,Mulberries are plucked in latter four hours and must be entered in fermentor tank, and mulberries just started to rot more than four hours, mouldy, rotten, turn into brown purple or brown gradually from light violet look, and mouthfeel can be sour, affects the quality of mulberries wine; Mulberries can not clean, and cleaning can cause the nutritive substance in mulberries epidermis to run off;
Folding lid on opened filter, the absorbent core of taking-up, separately get new absorbent core and put into strainer, mulberries slurry flows through flexible pipe by the discharging pipe bottom fermentation tank and enters the first pressure feeding pump, mulberries slurry is delivered to strainer through flexible pipe by the pressure that the first pressure feeding pump produces, mulberries slurry flows through absorbent core, grate enters fermentation tank, particulate matter in mulberries slurry is absorbed by absorbent core, circulate as above, mulberries slurry is mixed, chemically examine from the sampling of the stopple coupon of fermentation tank side, after the admixture of mulberries slurry reaches the standard of setting, discharging pipe bottom fermentation tank is closed, strainer above opening for feed is removed, with folding lid, opening for feed is sealed, overall fermentor tank is made to be air-tight state, mulberries slurry fermentation is adopted thermophilic fermentation, leavening temperature in fermentor tank is set as 29-35 degree, the vacuum layer formed between inwall and fermentation tank internal surface ensures in whole fermenting process, mulberries slurry is not by the impact of external environment temperature,
The attenuation degree of mulberries slurry is observed by the viewing window on the tank wall of fermentation tank, and chemically examined by stopple coupon sampling, after the fermentation state of mulberries slurry reaches the standard of setting, sealing cover above the fluid inlet of retort is opened, discharging pipe bottom fermentation tank and between described fluid inlet, flexible pipe is set, mulberries slurry flows into retort through flexible pipe, after reaching the standard volume of setting, close the discharging pipe bottom fermentation tank, water in steam generator inner water tank flows into process furnace through water pump, heat-generating pipe in process furnace adopts the electric stove wire of 24 kilowatts, water is turned into steam by water heating by heat-generating pipe, vapour temperature is 110-120 DEG C, retort inner bottom part arranges disk-shaped tube, disk-shaped tube arranges core, on disk-shaped tube, change from small to big in the aperture of the core of ecto-entad, steam in steam generator enters in disk-shaped tube through vapor transmission pipe, steam is emerged from core, steam makes mulberries slurry roll in retort, the steam produced after mulberries slurry boiling upwards enters the steam collector of pumpkin-shaped, the alcoholic strength that steam circles round in the steam collector of pumpkin-shaped and overturns and add steam, again through the middle condenser of doline, the top condenser of doline enters alcohol vapor transfer lime, then cooling tower is entered through wine inlet, cooling fluid is flowed into by the water-in of cooling tower, flow out from water outlet, heat transfer tube in cooling tower adopts copper tube, steam and cooling fluid indirect heat exchange make steam turn into liquid mulberries wine, the pressure and temperature that PLC automatic control system in pressure and temp controlling box controls in distiller and cooling tower automatically remains on and is set in value range, mulberries wine is flowed out by wine outlet,
The alcoholic strength of first wine can reach 70 degree, and falling gradually is 60 degree, 55 degree, 50 degree, 45 degree, classifies filling storage for the mulberries wine of different interval alcoholic strength.
The invention has the beneficial effects as follows: present configuration is simple, novel in design, easy to operate, it may also be useful to convenient, cheap for manufacturing cost, quality is good, and life-time service not easily damages, it may also be useful to effective, is subject to the consistent favorable comment of client; The alcoholic strength of the wine that the present invention produces is at 67-70 degree, simplify distillation number of times, existing distiller needs distillation twice, the present invention can distill out the wine of alcoholic strength at 67-70 degree for one time, and refining effect is desirable, and distiller can the wine of very effective extraction more high alcohol content, this production line greatly improves production efficiency, reduce production cost, the excellent quality of obtained mulberries wine, it is applicable to popularity application.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the invention will be further described:
Fig. 1 is general assembly structural representation;
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, promote conveyer 2-4, fermentation tank 3-1, opening for feed 3-2, opening for feed 3-3 for subsequent use, folding lid 3-4, strainer 3-5, plush copper 3-51, grate 3-52, absorbent core 3-53, inwall 3-6, liquidometer 3-7, first pressure feeding pump 3-8, 2nd pressure feeding pump 3-9, steam generator 4, retort 5-1, steam collector 5-2, middle condenser 5-3, top condenser 5-4, pressure and temp controlling box 6, cooling tower 7.
Embodiment
Below in conjunction with embodiment 1 and embodiment, the present invention is described in further detail:
Embodiment 1
Wall-breaking machine 2-1 is set between rewinding pond and fermentor tank, pressure and temp controlling box 6 is set between distiller and cooling tower 7, pressure and temp controlling box 6 arranges wire respectively and between distiller, cooling tower 7, steam generator 4 is set between distiller and fermentor tank, between below steam generator 4 and distiller, vapor transmission pipe is set;
The structure in described rewinding pond is: material pond 1-1 is rectangular parallelepiped or square, and the corner, bottom surface of material pond 1-1 arranges sensor 1-2, and the sidewall of material pond 1-1 arranges display screen 1-3, and display screen 1-3 side arranges key-press input control area; Above described wall-breaking machine 2-1, feeding warehouse 2-2 is set, arranges in described feeding warehouse 2-2 and described material pond 1-1 and promote conveyer 2-4;
The structure of described fermentor tank is: the end face of fermentation tank 3-1 arranges opening for feed 3-2 and opening for feed 3-3 for subsequent use, bottom surface is set to taper, bottom center arranges discharging pipe, side, bottom surface arranges wine slag sealing cover, the side of fermentation tank 3-1 arranges at least one stopple coupon from the bottom to top successively, the tank wall of fermentation tank 3-1 arranges at least one viewing window and liquidometer 3-7, folding lid 3-4 is set above opening for feed 3-3 for subsequent use, opening for feed 3-2 upper seal arranges strainer 3-5, folding lid 3-4 is set above strainer 3-5, the plush copper 3-51 of at least four cambered surface projections is set below strainer 3-5 internal surface, grate 3-52 is set above described plush copper 3-51, right cylinder absorbent core 3-53 is set above grate 3-52, described absorbent core 3-53 adopts the active carbon fibrous absorption material directly bought from market, drum shape inwall 3-6 is set in fermentation tank 3-1, the upper and lower ends of inwall 3-6 is fixedly installed with end face, bottom surface respectively, form vacuum layer between described inwall 3-6 and fermentation tank 3-1 internal surface, between the discharging pipe of the first pressure feeding pump 3-8 respectively and below the import of strainer 3-5, bottom surface, flexible pipe is set, 2nd pressure feeding pump 3-9 respectively and the grout outlet 2-3 of wall-breaking machine 2-1, strainer 3-5 import between flexible pipe is set,
The structure of described steam generator 7 is: arranges process furnace and water tank in steam generator 7, arranges water pump between process furnace and water tank, is provided with heat-generating pipe in process furnace;
The structure of described distiller is: the bottom surface of retort 5-1 and end face are all set to sphere, end face side arranges fluid inlet, another side arranges tensimeter, above described fluid inlet, sealing cover is set, the production well at the corresponding center of top face arranges pumpkin-shaped steam collector 5-2, middle condenser 5-3 is set above steam collector 5-2 and between the condenser 5-4 of top, described top condenser 5-4 and middle condenser 5-3 is down doline, the volume of top condenser 5-4 is less than the volume of middle condenser 5-3, the Circularhole diameter of the outlet of described steam collector 5-2 is less than the Circularhole diameter of import, the Circularhole diameter of the outlet of described middle condenser 5-3 is less than 1/2nd of the Circularhole diameter of import, the Circularhole diameter of the outlet of described top condenser 5-4 is less than 1/2nd of the Circularhole diameter of import, below the bottom surface of retort 5-1, discharge port is set, below the outer wall of retort 5-1, side arranges scarfing cinder lid, another side arranges outlet,
The structure of described cooling tower 7 is: cooling tower 7 upper center arranges wine inlet, arranges water-in above its outer wall, and below outer wall, side arranges wine outlet, and another side sets out the mouth of a river;
Between condenser 5-4 upper end, described top and described wine inlet, alcohol vapor transfer lime is set;
In described steam generator 4, process furnace and water tank are set, water pump is set between process furnace and water tank, in process furnace, be provided with heat-generating pipe;
Arranging PLC automatic control system in described pressure and temp controlling box 6, the pressure and temperature automatically controlled in distiller and cooling tower 7 remains on and is set in value range;
Pluck the mulberries of green non-pollution mid-May, the mulberries that the same garden same time period plucks are made marks, sort out to stack respectively and wait to weigh, before weighing, after material pond 1-1 being removed the peel by key-press input control area, zero setting, mulberries can not clean directly puts into material pond 1-1, the weight data detected is transferred to display screen 1-3 by four sensor 1-2, the summation of four weight data additions equals the mulberries weight in whole pond, after the mulberries weight record in whole pond, by promoting conveyer 2-4, the mulberries in material pond 1-1 are delivered to feeding warehouse 2-2, entering broken wall in wall-breaking machine 2-1 again is slurry, the particle that mulberries contain in starching is between positive and negative 0.3mm, mulberries are starched through grout outlet 2-3, flexible pipe enters the 2nd pressure feeding pump 3-9, mulberries slurry is delivered to strainer 3-5 through flexible pipe by the pressure that the 2nd pressure feeding pump 3-9 produces, mulberries slurry flows through absorbent core 3-53, grate 3-52 enters fermentation tank 3-1, particulate matter in mulberries slurry is absorbed by absorbent core 3-53, fermentation tank 3-1 adopts 30-32 ton, liquidometer 3-7 shows the volume of mulberries slurry in fermentation tank 3-1, mulberries slurry adds 18-23 ton hour to be stopped, in fermentation tank 3-1, sugaring is to improve its alcoholic strength, add brewer yeast simultaneously, mulberries are plucked in latter four hours and must be entered in fermentor tank, and mulberries just started to rot more than four hours, mouldy, rotten, turn into brown purple or brown gradually from light violet look, and mouthfeel can be sour, affects the quality of mulberries wine, mulberries can not clean, and cleaning can cause the nutritive substance in mulberries epidermis to run off,
Folding lid 3-4 on opened filter 3-5, the absorbent core 3-53 of taking-up, separately get new absorbent core 3-53 and put into strainer 3-5, mulberries slurry flows through flexible pipe by the discharging pipe bottom fermentation tank 3-1 and enters the first pressure feeding pump 3-8, mulberries slurry is delivered to strainer 3-5 through flexible pipe by the pressure that the first pressure feeding pump 3-8 produces, mulberries slurry flows through absorbent core 3-53, grate 3-52 enters fermentation tank 3-1, particulate matter in mulberries slurry is absorbed by absorbent core 3-53, circulate as above, mulberries slurry is mixed, chemically examine from the sampling of the stopple coupon of fermentation tank 3-1 side, after the admixture of mulberries slurry reaches the standard of setting, discharging pipe bottom fermentation tank 3-1 is closed, strainer 3-5 above opening for feed 3-2 is removed, with folding lid 3-4, opening for feed 3-2 is sealed, overall fermentor tank is made to be air-tight state, mulberries slurry fermentation is adopted thermophilic fermentation, leavening temperature in fermentor tank is set as 29-35 degree, the vacuum layer formed between inwall 3-6 and fermentation tank 3-1 internal surface ensures in whole fermenting process, mulberries slurry is not by the impact of external environment temperature,
The attenuation degree of mulberries slurry is observed by the viewing window on the tank wall of fermentation tank 3-1, and chemically examined by stopple coupon sampling, after the fermentation state of mulberries slurry reaches the standard of setting, sealing cover above the fluid inlet of retort 5-1 is opened, discharging pipe bottom fermentation tank 3-1 and between described fluid inlet, flexible pipe is set, mulberries slurry flows into retort 5-1 through flexible pipe, after reaching the standard volume of setting, close the discharging pipe bottom fermentation tank 3-1, water in steam generator 4 inner water tank flows into process furnace through water pump, heat-generating pipe in process furnace adopts the electric stove wire of 24 kilowatts, water is turned into steam by water heating by heat-generating pipe, vapour temperature is 110-120 DEG C, retort 5-1 inner bottom part arranges disk-shaped tube, disk-shaped tube arranges core, on disk-shaped tube, change from small to big in the aperture of the core of ecto-entad, steam in steam generator 4 enters in disk-shaped tube through vapor transmission pipe, steam is emerged from core, steam makes mulberries slurry roll in retort 5-1, the steam produced after mulberries slurry boiling upwards enters the steam collector 5-2 of pumpkin-shaped, the alcoholic strength that steam circles round in the steam collector 5-2 of pumpkin-shaped and overturns and add steam, again through the middle condenser 5-3 of doline, the top condenser 5-4 of doline enters alcohol vapor transfer lime, then cooling tower 7 is entered through wine inlet, cooling fluid is flowed into by the water-in of cooling tower 7, flow out from water outlet, heat transfer tube in cooling tower 7 adopts copper tube, steam and cooling fluid indirect heat exchange make steam turn into liquid mulberries wine, the pressure and temperature that PLC automatic control system in pressure and temp controlling box 6 controls in distiller and cooling tower 7 automatically remains on and is set in value range, mulberries wine is flowed out by wine outlet,
The alcoholic strength of first wine can reach 70 degree, and falling gradually is 60 degree, 55 degree, 50 degree, 45 degree, classifies filling storage for the mulberries wine of different interval alcoholic strength.
Claims (1)
1. the working method of the production line of a brew mulberries wine, the production line of described a kind of brew mulberries wine be 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), promote conveyer (2-4), fermentation tank (3-1), opening for feed (3-2), opening for feed for subsequent use (3-3), folding lid (3-4), strainer (3-5), plush copper (3-51), grate (3-52), absorbent core (3-53), inwall (3-6), liquidometer (3-7), first pressure feeding pump (3-8), 2nd pressure feeding pump (3-9), steam generator (4), retort (5-1), steam collector (5-2), middle condenser (5-3), top condenser (5-4), pressure and temp controlling box (6), cooling tower (7) is formed, it is characterized in that: wall-breaking machine (2-1) is set between rewinding pond and fermentor tank, pressure and temp controlling box (6) is set between distiller and cooling tower (7), pressure and temp controlling box (6) respectively and distiller, cooling tower between (7), wire is set, steam generator (4) is set between distiller and fermentor tank, between below steam generator (4) and distiller, vapor transmission pipe is set,
The structure in described rewinding pond is: material pond (1-1) is rectangular parallelepiped or square, the corner, bottom surface of material pond (1-1) arranges sensor (1-2), arranging display screen (1-3) on the sidewall of material pond (1-1), display screen (1-3) side arranges key-press input control area; Described wall-breaking machine (2-1) top arranges feeding warehouse (2-2), arranges lifting conveyer (2-4) in described feeding warehouse (2-2) and described material pond (1-1);
The structure of described fermentor tank is: the end face of fermentation tank (3-1) arranges opening for feed (3-2) and opening for feed for subsequent use (3-3), bottom surface is set to taper, bottom center arranges discharging pipe, side, bottom surface arranges wine slag sealing cover, the side of fermentation tank (3-1) arranges at least one stopple coupon from the bottom to top successively, the tank wall of fermentation tank (3-1) arranges at least one viewing window and liquidometer (3-7), opening for feed for subsequent use (3-3) top arranges folding lid (3-4), opening for feed (3-2) upper seal arranges strainer (3-5), strainer (3-5) top arranges folding lid (3-4), the plush copper (3-51) of at least four cambered surface projections is set below strainer (3-5) internal surface, described plush copper (3-51) top arranges grate (3-52), grate (3-52) top arranges right cylinder absorbent core (3-53), described absorbent core (3-53) adopts the active carbon fibrous absorption material directly bought from market, drum shape inwall (3-6) is set in fermentation tank (3-1), the upper and lower ends of inwall (3-6) is fixedly installed with end face, bottom surface respectively, form vacuum layer between described inwall (3-6) and fermentation tank (3-1) internal surface, between the discharging pipe of the first pressure feeding pump (3-8) respectively and below the import of strainer (3-5), bottom surface, flexible pipe is set, 2nd pressure feeding pump (3-9) respectively and the grout outlet (2-3) of wall-breaking machine (2-1), strainer (3-5) import between flexible pipe is set,
The structure of described steam generator (7) is: steam generator arranges process furnace and water tank in (7), arranges water pump between process furnace and water tank, is provided with heat-generating pipe in process furnace;
The structure of described distiller is: bottom surface and the end face of retort (5-1) are all set to sphere, end face side arranges fluid inlet, another side arranges tensimeter, above described fluid inlet, sealing cover is set, the production well at the corresponding center of top face arranges pumpkin-shaped steam collector (5-2), middle condenser (5-3) is set between steam collector (5-2) top and top condenser (5-4), described top condenser (5-4) and middle condenser (5-3) are down doline, the volume of top condenser (5-4) is less than the volume of middle condenser (5-3), the Circularhole diameter of the outlet of described steam collector (5-2) is less than the Circularhole diameter of import, the Circularhole diameter of the outlet of described middle condenser (5-3) is less than 1/2nd of the Circularhole diameter of import, the Circularhole diameter of the outlet on described top condenser (5-4) is less than 1/2nd of the Circularhole diameter of import, below the bottom surface of retort (5-1), discharge port is set, below the outer wall of retort (5-1), side arranges scarfing cinder lid, another side arranges outlet,
The structure of described cooling tower (7) is: cooling tower (7) upper center arranges wine inlet, arranges water-in above its outer wall, and below outer wall, side arranges wine outlet, and another side sets out the mouth of a river;
Between condenser (5-4) upper end, described top and described wine inlet, alcohol vapor transfer lime is set;
Described steam generator arranges process furnace and water tank in (4), arranges water pump between process furnace and water tank, is provided with heat-generating pipe in process furnace;
Arranging PLC automatic control system in described pressure and temp controlling box (6), the pressure and temperature automatically controlled in distiller and cooling tower (7) remains on and is set in value range;
Pluck the mulberries of green non-pollution mid-May, the mulberries that the same garden same time period plucks are made marks, sort out to stack respectively and wait to weigh, before weighing, after material pond (1-1) being removed the peel by key-press input control area, zero setting, mulberries can not clean directly puts into material pond (1-1), the weight data detected is transferred to display screen (1-3) by four sensors (1-2), the summation of four weight data additions equals the mulberries weight in whole pond, after the mulberries weight record in whole pond, by lifting conveyer (2-4), the mulberries expected in pond (1-1) are delivered to feeding warehouse (2-2), entering wall-breaking machine (2-1) interior broken wall again is slurry, the particle that mulberries contain in starching is between positive and negative 0.3mm, mulberries are starched through grout outlet (2-3), flexible pipe enters the 2nd pressure feeding pump (3-9), mulberries slurry is delivered to strainer (3-5) through flexible pipe by the pressure that the 2nd pressure feeding pump (3-9) produces, mulberries slurry flows through absorbent core (3-53), grate (3-52) enters fermentation tank (3-1), particulate matter in mulberries slurry is absorbed by absorbent core (3-53), fermentation tank (3-1) adopts 30-32 ton, liquidometer (3-7) shows the volume of the interior mulberries slurry of fermentation tank (3-1), mulberries slurry adds 18-23 ton hour to be stopped, to fermentation tank (3-1) interior sugaring to improve its alcoholic strength, add brewer yeast simultaneously, mulberries are plucked in latter four hours and must be entered in fermentor tank, and mulberries just started to rot more than four hours, mouldy, rotten, turn into brown purple or brown gradually from light violet look, and mouthfeel can be sour, affects the quality of mulberries wine, mulberries can not clean, and cleaning can cause the nutritive substance in mulberries epidermis to run off,
Folding lid (3-4) on opened filter (3-5), the absorbent core (3-53) of taking-up, separately get new absorbent core (3-53) and put into strainer (3-5), mulberries slurry flows through flexible pipe by the discharging pipe of fermentation tank (3-1) bottom and enters the first pressure feeding pump (3-8), mulberries slurry is delivered to strainer (3-5) through flexible pipe by the pressure that the first pressure feeding pump (3-8) produces, mulberries slurry flows through absorbent core (3-53), grate (3-52) enters fermentation tank (3-1), particulate matter in mulberries slurry is absorbed by absorbent core (3-53), circulate as above, mulberries slurry is mixed, chemically examine from the sampling of the stopple coupon of fermentation tank (3-1) side, after the admixture of mulberries slurry reaches the standard of setting, the discharging pipe of fermentation tank (3-1) bottom is closed, the strainer (3-5) of opening for feed (3-2) top is removed, with folding lid (3-4), opening for feed (3-2) is sealed, overall fermentor tank is made to be air-tight state, mulberries slurry fermentation is adopted thermophilic fermentation, leavening temperature in fermentor tank is set as 29-35 degree, the vacuum layer formed between inwall (3-6) and fermentation tank (3-1) internal surface ensures in whole fermenting process, mulberries slurry is not by the impact of external environment temperature,
The attenuation degree of mulberries slurry is observed by the viewing window on the tank wall of fermentation tank (3-1), and chemically examined by stopple coupon sampling, after the fermentation state of mulberries slurry reaches the standard of setting, sealing cover above the fluid inlet of retort (5-1) is opened, between the discharging pipe of fermentation tank (3-1) bottom and described fluid inlet, flexible pipe is set, mulberries slurry flows into retort (5-1) through flexible pipe, after reaching the standard volume of setting, close the discharging pipe of fermentation tank (3-1) bottom, water in steam generator (4) inner water tank flows into process furnace through water pump, heat-generating pipe in process furnace adopts the electric stove wire of 24 kilowatts, water is turned into steam by water heating by heat-generating pipe, vapour temperature is 110-120 DEG C, retort (5-1) inner bottom part arranges disk-shaped tube, disk-shaped tube arranges core, on disk-shaped tube, change from small to big in the aperture of the core of ecto-entad, steam in steam generator (4) enters in disk-shaped tube through vapor transmission pipe, steam is emerged from core, steam makes mulberries slurry roll in retort (5-1), the steam produced after mulberries slurry boiling upwards enters the steam collector (5-2) of pumpkin-shaped, the alcoholic strength that steam circles round in the steam collector (5-2) of pumpkin-shaped and overturns and add steam, again through the middle condenser (5-3) of doline, the top condenser (5-4) of doline enters alcohol vapor transfer lime, then cooling tower (7) is entered through wine inlet, cooling fluid is flowed into by the water-in of cooling tower (7), flow out from water outlet, heat transfer tube in cooling tower (7) adopts copper tube, steam and cooling fluid indirect heat exchange make steam turn into liquid mulberries wine, the pressure and temperature that PLC automatic control system in pressure and temp controlling box (6) controls in distiller and cooling tower (7) automatically remains on and is set in value range, mulberries wine is flowed out by wine outlet,
The alcoholic strength of first wine can reach 70 degree, and falling gradually is 60 degree, 55 degree, 50 degree, 45 degree, classifies filling storage for the mulberries wine of different interval alcoholic strength.
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