CN107012058A - One kind pressurization wine-distilling device - Google Patents
One kind pressurization wine-distilling device Download PDFInfo
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- CN107012058A CN107012058A CN201710359514.XA CN201710359514A CN107012058A CN 107012058 A CN107012058 A CN 107012058A CN 201710359514 A CN201710359514 A CN 201710359514A CN 107012058 A CN107012058 A CN 107012058A
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- chamber
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- condenser pipe
- wine
- distillery
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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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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Abstract
A kind of pressurization wine-distilling device of the present invention is related to wine brewing field, and in particular to a kind of wine-distilling device.Including distillery, collecting chamber, heating arrangements, condensing mechanism, condenser pipe is connected with collecting chamber；Distillery, which is externally provided with surge chamber and compression chamber, distillery, is provided with first piston, and first piston is provided with pressure-control valve and passage, and passage is arranged right below sprue, spring is fixed between sprue and distillery；Distillation chamber is connected by pressure-control valve with surge chamber, and surge chamber is connected by feed tube with distillation chamber, and check valve is provided with feed tube；Second piston is connected with compression chamber, expansion chamber is adjacent with distillation chamber, expanded by heating material of the boiling point at 100 DEG C to 150 DEG C is placed with expansion chamber, inlet chamber is connected with pressurizing chamber；Condensing mechanism includes liquefaction unit temperature reducing unit；Condenser pipe is switched provided with discharging.The present invention can effectively reduce the evaporation of material reclaimed water.
Description
Technical field
The present invention relates to wine brewing field, and in particular to a kind of wine-distilling device.
Background technology
General brewed wine, alcoholic strength is less than 20%, and the alcoholic strength in Spirit can then reach more than 60%, so only
The higher spirits of alcoholic strength can just be obtained by distillation.Steaming wine is carried out using alcohol is different with the boiling point of water, alcohol
Boiling point is less than the boiling point of water, so alcohol is easier volatilization.
Traditional distilling apparatus is mixed by heating medium of water vapour with material, and water vapour makes the alcohol in material
Evaporation, then condenses again the alcohol of evaporation, so just obtains the higher spirits of alcoholic strength.But traditional distilling apparatus is present
Following deficiency：Water vapour radiating is slow, and heat supply is unstable, causes that distilling effect is poor, cost height；Secondly, the water vapour heated
It can be blended in the alcohol of volatilization, be then condensed together with alcohol, so being still mixed with substantial amounts of water in the wine after distillation.
The Chinese patent of Application No. 200920052930.6 filed in 19 days March in 2009 discloses one kind without steam wine
Smart destilling tower, includes tower body, heater, and heater is an annular disk tubular structure；Heater passes through its underpart
Heat conduction oil-in and the conduction oil outlet on its top respectively communicate and constituted using conduction oil to heat medium with heat conduction oil boiler
Circulation loop.Annular disk tubular structure is made up of multiple annular disks being arranged above and below, and annular disk is along footpath by multiple ring pipes
To being spaced apart and be interconnected by conduit, each ring pipe in annular disk with adjacent annular disk above and below it is corresponding
Ring pipe connected by conduit.Destilling tower is first heated when being distilled to conduction oil, then by the conduction oil after heating
Annular coil pipe is passed through, conduction oil forms circulation loop in a distillation column.
The temperature of the conduction oil of this destilling tower is up to 360 DEG C, and temperature is significantly larger than in the boiling point of water, material at ambient pressure
Water can largely evaporate, vapor is blended in the alcohol of evaporation, then is condensed together, so same in obtained wine after distillation
Large quantity of moisture can be contained, this distillation mode, which will obtain the big wine of alcoholic strength, needs that distillation is repeated.Secondly, distillation tower height
Higher, the mixed gas of evaporation is during rising, and vapor can gradually be condensed into the globule, and now alcohol can dissolve in water again
In pearl, so the alcohol in mixed gas can be reduced further.
The content of the invention
The steaming wine dress that single flash can obtain the big wine of alcoholic strength need to be carried out it is an object of the invention to provide a kind of
Put.
To reach above-mentioned purpose, the technical scheme is that：One kind pressurization wine-distilling device, including distillery, collecting chamber,
Heating arrangements for heated material, the condenser pipe for exporting alcohol and the condensing mechanism for cooling, condenser pipe is with collecting
Room connection distillery is externally provided with distillation chamber and the top for being provided with surge chamber and compression chamber, distillery and distillery being divided into lower section
Pressurizing chamber the first piston slided up and down along distillery side wall, first piston is provided with pressure-control valve and supplies alcohol steam
The passage passed through, passage is arranged right below that the sprue of passage can be closed, and spring is fixed between sprue and distillery；Steam
Evaporate chamber to connect with surge chamber by pressure-control valve, surge chamber is connected by feed tube with distillation chamber, being provided with feed tube is used for
To the check valve of distillation chamber feed liquor；The second work that compression chamber is divided into expansion chamber and inlet chamber is slidably connected in compression chamber
Plug, expansion chamber is adjacent with distillation chamber, is placed with expanded by heating material of the boiling point at 100 DEG C to 150 DEG C in expansion chamber, inlet chamber and
Pressurizing chamber is connected；Condensing mechanism includes liquefaction unit and the temperature reducing unit cooled respectively to condenser pipe and surge chamber；Condensation
Pipe is provided with the discharging switch that condenser pipe was opened and closed in the realization that can be touched by pressure-control valve.
Steaming wine is carried out using the present apparatus, when initial, discharging switch closing condenser pipe, pressure-control valve are closed,
First expanded by heating material is placed into expansion chamber, then material is added in distillation chamber, now expanded by heating material is in not swollen
Swollen state.Heating arrangements are heated to the material in distillery, and temperature of charge rise, alcohol starts volatilization, and alcohol enters cold
It is condensed, and is stored in condenser pipe in solidifying pipe.Until the temperature of material reaches the boiling point of alcohol, the evaporation rate of alcohol reaches
Maximum, and now temperature of charge not yet reaches the boiling point of water, so water will not largely produce water vapour.In the process, by
Thermal expansion material is heated, and volume slowly starts increase, and second piston is moved downward, and the gas in inlet chamber enters in pressurizing chamber.
Because now pressurizing chamber connect with distillation chamber, so the air pressure in whole distillery increases, so the boiling point of alcohol and water on
Rise.
Heating arrangements continue to distill intracavitary material heat, temperature of charge continue rise, until temperature of charge reach by
The boiling point of thermal expansion material, now change is big rapidly for expanded by heating mass volume, and the gas in inlet chamber is quickly entered in pressurizing chamber,
Now first piston is pushed down rapidly, and sprue closing passage, the gas for now distilling intracavitary generation cannot be introduced into condensation
Guan Zhong.The air pressure constantly entered with the gas of inlet chamber in pressurizing chamber, pressurizing chamber continues to raise, and first piston continues downward fortune
It is dynamic.During first piston is moved down, the volume with distillation chamber constantly reduces, and the water and alcohol in material are steamed
Hair, so the air pressure of distillation intracavitary is constantly raised, and when distilling cavity pressure still less than pressurization cavity pressure, Stress control
Valve is opened, and the gases at high pressure in distillation chamber enter in surge chamber, and cooling mechanism cools to the gas for entering surge chamber, gas
Temperature reduction formation cryogenic liquid, liquid is entered in distillation chamber by feed tube and check valve again.
Due to the entrance of cryogenic liquid, the temperature of charge of distillation intracavitary is reduced rapidly, the reduction of expanded by heating mass temperature, body
Product reduces, and the gas in pressurizing chamber is by suction inlet chamber again.While pressure-control valve is opened, discharging switch is beaten
Open, the liquid wine in condenser pipe is fallen into collecting chamber.Air pressure reduction in pressurizing chamber, first piston is moved to pressurizing chamber, sprue
Passage is opened, the air pressure reduction of distillation intracavitary, pressure-control valve is closed；At the same time, discharging switch is re-closing off, in material
The alcohol of volatilization is reentered in condenser pipe by passage to be condensed, and is stored in condenser pipe, so constantly circulation, until
Alcohol in material is entirely vaporized.
This programme has the beneficial effect that：（One）The boiling point of water is higher than alcohol, thus temperature reach the boiling point of alcohol and not
When reaching the boiling point of water, the alcohol in material largely evaporates, but not produces a large amount of water vapours, so the wine reclaimed water that condensation is obtained
Content it is less.Compression chamber pressurizes to distillation chamber, and pressure increase can make the elevation of boiling point of water, it is possible to which extension is only steamed
Hair alcohol, the stage for not evaporating water, the content of water can be reduced while alcohol is evaporated, so, it is only necessary to by once steaming
Evaporate and can obtain the big wine of alcoholic strength, it is not necessary to by distilling repeatedly, step can be simplified, improve production efficiency.
（Two）When the material for distilling chamber reaches the boiling point of water, sprue can avoid the vapor produced mixed into condenser pipe
Enter in the wine after distillation, it is possible to obtain the higher wine of alcoholic strength.
（Three）Material can be pressurizeed repeatedly, evaporate alcohol, cooling processing, completely can be steamed the alcohol in material
Hair, it is to avoid waste；And when collecting alcohol, the temperature of material is not up to the boiling point of water always, it is possible to be collected into alcoholic strength
High wine.
（Four）Expansion chamber and distillation chamber are disposed adjacent, and the temperature of distillation intracavitary material can control the body of expanded by heating material
Product, so as to reach the effect of pressurization, so the switch of control expansion chamber need not be set in addition, it is possible to reduce occur error and
Structure can be simplified.
（Five）When the temperature of material is not up to the boiling point of expanded by heating material, the volume of expanded by heating material only can be slow
Increase, makes inlet chamber gradually be pressurizeed to distillery, gradually rises the boiling point of water, can extend the time for only evaporating alcohol,
Evaporated more alcohol.When temperature of charge reaches the boiling point of expanded by heating material, expanded by heating mass volume is rapid
Expansion, makes water vapour cannot be introduced into condenser pipe.
（Six）Surge chamber can be such that the gas of entrance reduces rapidly, be passed through distillation chamber, it is possible to make distillation intracavitary
Temperature is reduced rapidly, it is to avoid produce a large amount of vapor again；Secondly, expanded by heating mass volume can also be made to reduce rapidly, pressurizeed
The gas of intracavitary is sucked back rapidly inlet chamber, the distilled spirit stage is restarted rapidly, it is possible to reduce what distillation stopped
Time, improve efficiency.
Preferred scheme one, as the further improvement to base case, condensing mechanism is to be coated on the pipe on the outside of condenser pipe
Road, temperature reducing unit is to be coated on the pipeline on the outside of surge chamber.Can make gaseous alcohol enter condenser pipe after, along condenser pipe by
Gradually to during one end motion of collecting chamber, temperature is gradually reduced, and is gradually liquefied.It can also ensure that the alcohol collected in condenser pipe is kept
Relatively low temperature, makes the alcohol of liquid be notheated volatilization.
Preferred scheme two, as the further improvement to preferred scheme one, liquefaction unit is close to collecting chamber one end and the external world
Water pipe is connected, and the liquefaction unit is connected close to distillery one end with temperature reducing unit.Now, the relatively low water of ambient temperature is from liquefaction
Unit flows to liquefaction unit close to distillery one end close to collecting chamber one end, then flows into temperature reducing unit.Because liquefaction unit needs
Gaseous alcohol is liquefied, so the temperature of the water in liquefaction unit is relatively low, and the water in liquefaction unit keeps flowing, finally from
The temperature for the water discharged in liquefaction unit is below the temperature of water vapour, so it is single that the water discharged from liquefaction unit is passed through into cooling
Member, the temperature of water is higher than into the steam temperature in surge chamber, so the water of liquefaction unit discharge equally can be to water vapour
Cooled, it is possible to realize reusing for the water that liquefaction unit is discharged, saving water resource.
Preferred scheme three, as the further improvement to preferred scheme two, condensing mechanism is removably to be coated on respectively
Condenser pipe and the ice cube bag of buffering outside.The temperature of ice is less than the temperature of water, so directly being condensed and being cooled using ice
Than using water condensation and the speed of cooling faster；And the wine liquid in condenser pipe can be made to keep lower temperature, institute due to ice cube
Can further reduce the volatilization of alcohol in wine liquid, wine liquid is set to keep larger alcoholic strength.
Preferred scheme four, is used as the further improvement to any one in preferred scheme two and preferred scheme three, ventilation
Hole is truncated cone-shaped, and sprue is cone and sprue lower end diameter is more than passage lower end diameter, and spring is fixed on sprue and distillation
Between the bottom of room.Passage is that cone, i.e. passage upper end diameter are less than lower end diameter, when sprue is entered in passage, circle
The profile of platform shape can also play guide effect, facilitate sprue to slip into.
Preferred scheme five, as the further improvement to preferred scheme four, heater is coated on distillation cavity outer wall.Increase
The contact area of heater and material in distillation chamber, can be such that more materials are heated simultaneously, it is possible to make material fast
Speed reaches the temperature higher than alcohol boiling point, improves vaporized alcohol efficiency.
Preferred scheme six, discharging switch includes being arranged on " T " shape threeth piston of the condenser pipe close to collecting chamber end,
3rd piston is provided with the fluid hole of " L " shape, and condensation tube end is provided with diameter and the 3rd piston small end diameter identical annular
It is raised；3rd piston top is provided with the electromagnet for being used for adsorbing the 3rd piston, and interior be provided with of pressure-control valve can be by pressure-control valve
Being used for of touching of flap close the controlling switch of electromagnet.When initial, electromagnet is opened, and the 3rd piston is adsorbed to electromagnetism
At iron, the fluid hole positioned at "T"-shaped 3rd piston small end side-walls is closed by annular protrusion, thus the wine liquid in condenser pipe without
Method flows out.When pressure-control valve is opened, the gases at high pressure that the flap of pressure-control valve is distilled intracavitary are promoted, and flap and then are touched
Dynamic controlling switch, electromagnet is closed, and the 3rd piston slide downward under the Action of Gravity Field of wine, the 3rd piston stretches out condensation
Pipe, now fluid hole is connected with collecting chamber, and the wine in condenser pipe is flowed into collecting chamber.When pressure-control valve is closed, flap stops
Only touch control switch, then electromagnet reopen, the 3rd piston is adsorbed upwards again, and fluid hole is closed.In electromagnet
During opening, annular protrusion can prevent from just flowing into collecting chamber, and in the 3rd piston slide downward, annular protrusion can prevent the 3rd
Piston is deviate from from condenser pipe.
Preferred scheme seven, pressure-control valve is connected by escape pipe with surge chamber, go out liquid switch include connection escape pipe and
Slided in the conduit of condenser pipe, conduit and be provided with piston rod, piston rod two ends are respectively and fixedly provided with the 4th piston, close to condenser pipe one end
4th piston closes condenser pipe, and the condenser pipe side wall relative with conduit is provided with the groove entered for the 4th piston, close to condensation
Stage clip is welded between the 4th piston and groove of pipe side.When initial, the 4th piston close to condenser pipe is located in condenser pipe,
And close condenser pipe.When pressure-control valve is opened, a large amount of gases at high pressure are entered in escape pipe, so close to the 4th of escape pipe the
Piston is promoted to condensation chamber one end, and until entering in groove, stage clip is compressed, and now piston rod enters in condenser pipe, and lives
Stopper rod is not enough to close condenser pipe, so the wine in condenser pipe enters in collecting chamber.After pressure-control valve closing, in escape pipe
Air pressure reduce, stage clip makes the 4th piston reclose condenser pipe.
Brief description of the drawings
The present invention is further detailed explanation with reference to the accompanying drawings and detailed description：
Fig. 1 is the structural representation of the embodiment of the present invention 1；
Fig. 2 is the state diagram when expanded by heating material of the embodiment of the present invention 1 is heated；
Fig. 3 is the structural representation of the discharging switch of the embodiment of the present invention 1；
Fig. 4 is the state diagram when expanded by heating material of the embodiment of the present invention 2 is heated；
Fig. 5 is the structural representation of the discharging switch of the embodiment of the present invention 2.
Embodiment
Reference is：Distillery 1, pressurizing chamber 11, distillation chamber 12, first piston 13, safety valve 131, passage 132,
Sprue 133, spring 134, collecting chamber 2, condenser pipe 21, annular protrusion 211, discharging switch the 22, the 3rd piston 23, fluid hole 231,
Electromagnet 232, the 4th piston 24, piston rod 25, stage clip 26, surge chamber 3, escape pipe 31, feed tube 32, compression chamber 4, inlet chamber
41st, expansion chamber 42, second piston 43, water pipe 51, temperature drop pipe 52.
Embodiment 1
As shown in Figure 1 and Figure 2, a kind of pressurization wine-distilling device, including distillery 1, collecting chamber 2, the heater for heated material
Structure, the condenser pipe 21 for exporting alcohol, the condensing mechanism for cooling, surge chamber 3 and compression chamber 4, condensing mechanism include liquid
Change unit and temperature reducing unit.The first piston 13 being provided with parallel to the bottom of distillery 1, first piston 13 are slided in distillery 1
Distillery 1 is divided into and is fixed with safety valve 131 on the distillation chamber 12 of lower section and the pressurizing chamber 11 of top, first piston 13 and passes through
Passage 132 of the upper end diameter less than the truncated cone-shaped of lower end diameter of first piston 13 is worn, passage 132 is arranged right below sealing
The conical sprue 133 of passage 132 is closed, spring 134 is welded between the lower end of sprue 133 and distillation chamber 12 bottom, stifled
The Action of Gravity Field lower spring 134 of block 133 is compressed, and now sprue 133 opens passage 132.The distillation bottom outer wall of chamber 12 is provided with
Adding thermal resistance, adding thermal resistance is heated to the material in distillation chamber 12.The top of pressurizing chamber 11 is connected with condenser pipe 21, condenser pipe
21 right-hand members are stretched into collecting chamber 2, and the right-hand member of condenser pipe 21, which is provided with, can close the discharging switch 22 of condenser pipe 21, and discharging switch 22 includes
The 3rd "T"-shaped piston 23 in condenser pipe 21 is slidably arranged in, the inner materials of the 3rd piston 23 are to be coated with rubber on the outside of iron, iron
Glue-line.The diameter of the lower end of 3rd piston 23, which is less than on the diameter of upper end, the 3rd piston 23, runs through the fluid hole 231 provided with " L " shape,
The lower end part of fluid hole 231 is in the lower end diameter smaller part of the 3rd piston 23.It is fixed on the condensation outer wall of the upper end of 3rd piston 23
Have in electromagnet 232, safety valve provided with the controlling switch for being used to close electromagnet 232 that can be touched by flap.Condenser pipe 21 is right
End is held to be provided with diameter and the lower end diameter identical annular protrusion 211 of the 3rd piston 23.It is arranged with outside condenser pipe 21 for condensing
The water pipe 51 of alcohol steam, the left end of water pipe 51 and right-hand member are equipped with opening, opening and the extraneous water inlet pipe 51 of the right-hand member of water pipe 51
Connection.
Surge chamber 3 is connected with feed tube 32 and escape pipe 31, the connection of safety valve 131 distillation chamber 12 and escape pipe 31, outlet
Pipe 31 is bellows, and feed tube 32 is connected with distillation chamber 12, and being provided with feed tube 32 can only allow liquid to enter steaming from surge chamber 3
Evaporate the check valve of chamber 12.Temperature drop pipe 52 is arranged with outside surge chamber 3, the top and bottom of temperature drop pipe 52 are equipped with opening, cooling
The opening of the upper end of water pipe 52 and the open communication of the left end of water pipe 51, the opening of the lower end of temperature drop pipe 52 are connected with drainpipe, and water leads to
Cross drainpipe discharge.
Slided in compression chamber 4 and be provided with second piston 43 parallel to the bottom surface of compression chamber 4, second piston 43 is by compression chamber 4
It is divided into the expansion chamber 42 of lower section and the inlet chamber 41 of top.The side wall of expansion chamber 42 fits with the distillation side wall of chamber 12, expansion chamber
42 are bolted on the distillation side wall of chamber 12, and liquid toluene is stored in expansion chamber 42.Inlet chamber 41 connects with pressurizing chamber 11
It is logical.
When steaming wine, first material is added in distillation chamber 12, now safety valve 131 is closed, sprue 133 opens passage 132.
Then adding thermal resistance is heated to material, and temperature of charge rise, alcohol starts volatilization, and alcohol enters in condenser pipe 21 by water pipe
Water condensation formation liquid in 51, then be stored in condenser pipe 21.Until the temperature of material reaches the boiling point of alcohol, alcohol
Evaporation rate reaches maximum.In the process, triethylamine is heated, and volume starts increase, and second piston 43 is to inlet chamber 41 1
Gas in lateral movement, inlet chamber 41 enters in pressurizing chamber 11, the air pressure increase in distillery 1, the boiling point of alcohol and water on
Rise.Adding thermal resistance continues to heat material, and temperature of charge continues to rise, until temperature of charge reaches the boiling point of triethylamine, three second
Amine becomes gaseous state, and the volume of expansion chamber 42 becomes rapidly big, and the gas in inlet chamber 41 is quickly entered in pressurizing chamber 11, now first is lived
Plug 13 is pushed down, the closing passage 132 of sprue 133, so as the gas of inlet chamber 41 constantly enters pressurizing chamber 11, plus
The air pressure in chamber 11 is pressed to continue to raise, first piston 13 continues to move downward.The volume for distilling chamber 12 reduces, air pressure rise, directly
It is opened to safety valve 131, the gases at high pressure in distillation chamber 12 enter in surge chamber 3, at the same time, the flap of safety valve 131
Touch control switch, electromagnet is closed, and the 3rd piston is moved downward under the Action of Gravity Field of wine, until the fluid hole of " L " shape
Bottom be exposed, the wine of the liquid in condenser pipe 21 is fallen into collecting chamber 2.Water in temperature drop pipe 52 is to entering surge chamber
3 gas is cooled, and gas temperature reduces to form cryogenic liquid, and cryogenic liquid is entered by feed tube 32 and check valve again to be steamed
Evaporate in chamber 12.The temperature of charge reduction in chamber 12 is distilled, triethylamine temperature reduction, volume reduces flap touch control switch, electricity
Magnet 232 is closed, and the 3rd piston 23 is moved downward under the Action of Gravity Field of wine, until the bottom of the fluid hole 231 of " L " shape
Be exposed, the gas in pressurizing chamber 11 is by suction inlet chamber 41 again, the reduction of air pressure in pressurizing chamber 11, first piston 13 to
Upper motion, sprue 133 opens the air pressure reduction in passage 132, distillation chamber 12, and safety valve 131 is closed；At the same time, safety
The flap of valve 131 stops touch control switch, and electromagnet 232 is switched on again, and the 3rd piston 23 is inhaled upwards by electromagnet 232
Attached, the fluid hole 231 of " L " property is closed, then condenser pipe 21 is closed.The alcohol volatilized in material by passage 132 again
It is condensed, and is stored in condenser pipe 21 into condenser pipe 21, so constantly circulation, until the alcohol in material is all steamed
Hair.
Embodiment 2
As shown in figure 3, difference from Example 1 is, distillation chamber 12 is additionally provided with heating with the non-conterminous side-walls of expansion chamber 42
Resistance.Passage 132 is cylinder, and sprue 133 includes diameter and is less than the cylindrical plug of the diameter of passage 132 and is integrally formed
Diameter in plug lower end is more than above the pedestal of the diameter of passage 132, plug is welded with spring between the top of pressurizing chamber 11
134, under the Action of Gravity Field of sprue 133, spring 134 is in extended state, and sprue 133 opens passage 132.In expansion chamber 42
The material of storage is dimethylbenzene；Condenser pipe 21 and surge chamber 3, which are coated with cavity, cavity, can be put into ice cube.Escape pipe 31 with
Connected between condenser pipe 21 by fixed conduit, slided in conduit and be provided with piston rod 25, the left and right ends of piston rod 25 are welded
There is the 4th piston 24, the side wall relative with conduit of condenser pipe 21 is provided with groove, stage clip is welded between the 4th piston 24 and groove
26, stage clip 26 makes the 4th piston 24 closing condenser pipe 21 on right side when initial.
In distilling material, the adding thermal resistance set on the distillation side wall of chamber 12 can make material programming rate faster.Work as steaming
After the alcohol distillated enters in condenser pipe 21, ice cube quickly makes alcohol be condensed into liquid；Similarly, into the mixing in surge chamber 3
Gas is also quickly cooled, and then reduces the temperature in distillery 1.When safety valve 131 is opened, the air pressure in escape pipe 31
Increase, the 4th piston 24 is pressed into groove, and condenser pipe 21 is opened, and wine enters in collecting chamber 2.When safety valve 131 is closed, go out
Air pressure in tracheae 31 reduces, and stage clip 26 makes the 4th piston 24 set back, and the 4th piston 24 recloses condenser pipe 21.
Above-described is only the preferred embodiment of the present invention, it is noted that for those skilled in the art,
Without departing from the inventive concept of the premise, several modifications and improvements can also be made, these should also be considered as the guarantor of the present invention
Scope is protected, these effects and practical applicability for implementing all without the influence present invention.The present invention omits the technology of description, shape
Shape, construction part are known technology.
Claims (8)
1. one kind pressurization wine-distilling device, including distillery, collecting chamber, the heating arrangements for heated material, for exporting alcohol
Condenser pipe and condensing mechanism for cooling, the condenser pipe connects with collecting chamber；Characterized in that, the distillery peripheral hardware
There is the edge for being provided with surge chamber and compression chamber, the distillery and distillery being divided into the distillation chamber of lower section and the pressurizing chamber of top
The first piston that distillery side wall is slided up and down, the first piston is provided with pressure-control valve and for leading to that alcohol steam passes through
Stomata, the passage is arranged right below that the sprue of passage can be closed, and spring is fixed between the sprue and distillery；Institute
State distillation chamber to connect with surge chamber by pressure-control valve, the surge chamber is connected by feed tube with distillation chamber, the feed liquor
Being provided with pipe is used for the check valve to distillation chamber feed liquor；Slidably connected in the compression chamber by compression chamber be divided into expansion chamber and
The second piston of inlet chamber, the expansion chamber is adjacent with distillation chamber, and boiling point is placed with the expansion chamber at 100 DEG C to 150 DEG C
Expanded by heating material, the inlet chamber connects with pressurizing chamber；The condensing mechanism includes respectively entering condenser pipe and surge chamber
The liquefaction unit and temperature reducing unit of row cooling；The condenser pipe is provided with the realization that can be touched by pressure-control valve and opens and close
The discharging switch of condenser pipe.
2. a kind of pressurization wine-distilling device according to claim 1, it is characterised in that the liquefaction unit is to be coated on condensation
Pipeline on the outside of pipe, the temperature reducing unit is to be coated on the pipeline on the outside of surge chamber.
3. a kind of pressurization wine-distilling device according to claim 2, it is characterised in that the liquefaction unit is close to collecting chamber one
End is connected with external water pipe, and the liquefaction unit is connected close to distillery one end with temperature reducing unit.
4. a kind of pressurization wine-distilling device according to claim 1, it is characterised in that the liquefaction unit and temperature reducing unit are
It is separately positioned on condenser pipe and the cavity for being used to accommodate ice cube of buffering outside.
5. a kind of pressurization wine-distilling device according to any one in claim 3 and 4, it is characterised in that the passage
For truncated cone-shaped, the sprue is more than passage lower end diameter for cone and sprue lower end diameter, the both ends of the spring respectively with
Sprue and distillery bottom are fixed or respectively with being fixed at the top of sprue and distillery.
6. a kind of pressurization wine-distilling device according to claim 5, it is characterised in that the heater is coated on distillation chamber
Outer wall.
7. a kind of pressurization wine-distilling device according to claim 6, it is characterised in that the discharging switch is cold including being arranged on
Solidifying pipe is close to the 3rd " T " shape piston of collecting chamber end, fluid hole of the 3rd piston provided with " L " shape, the condenser pipe
End is provided with diameter and the 3rd piston small end diameter identical annular protrusion；Rising to be provided with above the 3rd piston is used to adsorb
Being provided with the electromagnet of 3rd piston, the pressure-control valve can be by the flap shake-up of pressure-control valve for closing electromagnet
Controlling switch.
8. a kind of pressurization wine-distilling device according to claim 6, it is characterised in that the pressure-control valve passes through escape pipe
Be connected with surge chamber, it is described go out liquid switch include sliding provided with piston in the conduit that connects escape pipe and condenser pipe, the conduit
Bar, the piston rod two ends are respectively and fixedly provided with the 4th piston, the 4th piston closing condenser pipe close to condenser pipe one end, the condensation
The pipe side wall relative with conduit is provided with the groove entered for the 4th piston, close to condenser pipe side the 4th piston and groove it
Between be welded with stage clip.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710359514.XA CN107012058B (en) | 2017-05-19 | 2017-05-19 | Pressurized wine steaming device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710359514.XA CN107012058B (en) | 2017-05-19 | 2017-05-19 | Pressurized wine steaming device |
Publications (2)
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| CN107384719A (en) * | 2017-08-25 | 2017-11-24 | 遵义市永宏金属设备有限公司 | Wine brewing distilling apparatus |
| CN107384684A (en) * | 2017-08-25 | 2017-11-24 | 遵义市永胜金属设备有限公司 | Wine brewing tank |
| CN108410678A (en) * | 2018-05-31 | 2018-08-17 | 贵州省仁怀市水码头酿酒作坊 | Alcoholic equipment |
| CN108410679A (en) * | 2018-05-31 | 2018-08-17 | 贵州省仁怀市水码头酿酒作坊 | Steaming plant |
| CN108485896A (en) * | 2018-06-28 | 2018-09-04 | 贵州省仁怀市水码头酿酒作坊 | steam wine pot |
| CN108795634A (en) * | 2018-06-27 | 2018-11-13 | 贵州省仁怀市水码头酿酒作坊 | wine-making technology |
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| CN115006859A (en) * | 2022-07-21 | 2022-09-06 | 江苏锐深化工机械科技有限公司 | Explosion-proof distillation retort for chemical equipment |
| CN115141704A (en) * | 2022-07-15 | 2022-10-04 | 浙江省农业科学院 | Preparation method of Chinese spirit with Chinese torreya flavor |
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| CN108410679A (en) * | 2018-05-31 | 2018-08-17 | 贵州省仁怀市水码头酿酒作坊 | Steaming plant |
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| CN117239998A (en) * | 2023-11-14 | 2023-12-15 | 常州鑫鼎机电设备有限公司 | Integrated electric push rod |
| CN117239998B (en) * | 2023-11-14 | 2024-01-23 | 常州鑫鼎机电设备有限公司 | Integrated electric push rod |
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