CN205258435U - Production line of fruit liquor - Google Patents
Production line of fruit liquor Download PDFInfo
- Publication number
- CN205258435U CN205258435U CN201521129255.4U CN201521129255U CN205258435U CN 205258435 U CN205258435 U CN 205258435U CN 201521129255 U CN201521129255 U CN 201521129255U CN 205258435 U CN205258435 U CN 205258435U
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- fruit
- stainless steel
- steel cask
- production line
- distillation
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- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a production line of fruit liquor, including the nonrust steel drum of a plurality of, the breakage, the peel after with the breakage in the fruit and the fruit seed that carry out fermentation, the fruit of fruit in same nonrust steel drum in proper order get rid of and will ferment after the fruit fractionation by distillation go out methyl alcohol and miscellaneous pure wine, through promoting nonrust steel drum transmission, form half continuous production's production line of fruit liquor between the adjacent station. The beneficial effects of the utility model are that: based on the general nonrust steel drum of slip of repacking, be equipped with low cost, the high efficiency that the broken whip of special fresh fruit, core separator and distiller form, the higher gear production line of fruit liquor that can produce the low miscellaneous mellow wine of low methyl alcohol. According to the capacity of nonrust steel drum, form daily output 9L - 72L alcohol degree and be 50% fruit liquor.
Description
Technical field
The utility model relates to fruit wine brewing field, is specifically related to a kind of production line of fruit distillate liquor.
Background technology
Because business is for fruit product phase and the requirement of buying phase, orchard has the mature fruit of 10-25% not haveWell utilized. Mature fruit sugar content is high, gives off a strong fragrance, but because maturity is high, difficultyIn long-distance transport.
Mature fruit is good liquor-making raw material, and a lot of orchards and enterprise once attempted brewing fermentation fruit wine,But the stability of fermentation fruit wine is poor compared with white wine, grape wine, beer stability, seriously affects quality,Cause fruit wine from eighties of last century the nineties later always in stagnating the stage of developing even atrophy.
Fruit distillate liquor is another option of fruit wine, but because distillation technique does not pass a test, first in Eaux-De-VieAlcohol fusel content is higher, easily causes and is still drank after a night and headache.
Utility model content
In sum, in order to overcome the deficiencies in the prior art, technical problem to be solved in the utility modelBe to provide a kind of production line of fruit distillate liquor.
The technical scheme that the utility model solves the problems of the technologies described above is as follows: a kind of production of fruit distillate liquorLine, comprises several stainless steel casks, and described stainless steel cask is cylindric, and the bottom of this stainless steel cask is provided withMovable pulley, described movable pulley comprises two rollers that be arranged in parallel and a universal wheel, and described rollerWith described universal wheel finished product word structure, stainless steel cask bottom corresponding between two described rollers keeps to the sideBackplate when place is provided with for the protection of stainless steel cask and supports stainless steel cask inclination operation;
This production line also comprises fruit smashing in described stainless steel cask the crushing mixer stirring, will breakPericarp in broken rear fruit and the fruit separator got rid of of seed and the fruit separated after fermentation is gone outThe distiller of methyl alcohol and fusel wine;
In same stainless steel cask, carry out successively the fragmentation of fermentation, the fruit of fruit, by fruit after fragmentationIn pericarp and fruit seed get rid of and by fermentation after fruit separated go out methyl alcohol and fusel wine, adjacentBetween station, transmit by promoting stainless steel cask, form the production of the fruit distillate liquor of semicontinuous productionLine.
The beneficial effects of the utility model are: taking the general stainless steel cask of slip of reequiping as basis, be equipped with speciallyBy low cost, the high efficiency of fruit smashing agitator, fruit stone separator and distiller composition, can produceThe production line of the high-grade fruit distillate liquor of the low fusel of low methyl alcohol. According to the capacity of stainless steel cask, form daily outputThe fruit distillate liquor that 9L-72L alcoholic strength is 50%.
On the basis of technique scheme, the utility model can also do following improvement:
Further, described crushing mixer comprises electric hand drill, the output connection rotating shaft of described electric hand drillUpper end, being wound with rotation at the peripheral ring of described rotating shaft lower end can broken fruit, and promotes fruit wine with dregs from upperAnd lower motion is pushed to fruit stone blunt of described stainless steel cask bottom.
Further, described separator is while tilting described rust steel drum, can be along bucket wall and a bucket junction, the endThe square basket bamboo strainer that is deposited on bottom fruit stone is fished at turning.
Further, described distiller comprises the distillation stainless steel cask that loads the fruit after fermentation, in described steamingThe top of heating up in a steamer stainless steel cask is provided with heating kettle cover, covers and is provided with to described distillation stainless steel cask at this heating kettleThe air inlet of interior input heating steam and export the venthole of wine steam outside described distillation stainless steel cask.
Adopt the beneficial effect of above-mentioned further scheme to be: above-mentioned distiller is applicable to liquid state fermentation and solid-stateFermented distilled wine brewing process.
Further, described distiller comprises the distillation stainless steel cask that loads the fruit after fermentation, in described steamingThe top of heating up in a steamer stainless steel cask is provided with heating kettle cover, in this heating kettle cover, is provided with to described distillation stainless steel caskIn bottom extend heating tube, described heating kettle cover be also provided with outside described distillation stainless steel cask defeatedGo out the venthole of wine steam.
Adopt the beneficial effect of above-mentioned further scheme to be: above-mentioned distiller is applicable to the liquid of distillation without skin slagState fermentation fruit.
Further, described distiller comprises stainless steel cask, is provided with and adds on the top of described distillation stainless steel caskHot kettle cover is provided with the heat exchange of extending to the bottom in described distillation stainless steel cask in this heating kettle coverDevice, covers and is also provided with the venthole of exporting wine steam outside described distillation stainless steel cask at described heating kettle;
Described heat exchanger comprises the upper coil pipe in top, the lower coil pipe in bottom and connects on thisThe heating tube of coil pipe and lower coil pipe is provided with the electrical bar that heats water quality, described upper dish in described heating tubePipe and described lower coil pipe are also interconnected by return duct, are also provided with blast pipe on described heat exchanger,Exhaust outlet at described blast pipe is provided with pressure valve.
Adopt the beneficial effect of above-mentioned further scheme to be: above-mentioned distiller has been applicable to pomace or has had no resultThe liquid state fermentation fruit of slag.
Brief description of the drawings
Fig. 1 is the flow chart of production line production method;
Fig. 2 is the schematic diagram of stainless steel cask;
Fig. 3 is the schematic diagram of crushing mixer;
Fig. 4 is the schematic diagram of separator;
Fig. 5 is distiller the first embodiment;
Fig. 6 is distiller the second embodiment;
Fig. 7 is the third embodiment of distiller.
In accompanying drawing, the list of parts of each label representative is as follows:
1, stainless steel cask, 2, movable pulley, 3, broken agitator, 4, separator, 5, electric hand drill, 6,Rotating shaft, 7, blunt, 8, heating kettle cover, 9, air inlet, 10, steam drain, 11, heating tube, 12,Upper coil pipe, 13, lower coil pipe, 14, heating tube, 15, electrical bar, 16, return duct, 17, blast pipe,18, pressure valve.
Detailed description of the invention
Below in conjunction with accompanying drawing, principle of the present utility model and feature are described, example is only for separatingRelease the utility model, be not intended to limit scope of the present utility model.
As shown in Figure 1, a kind of production line production method of fruit distillate liquor, comprises the steps:
(1) prepare several columned and bottoms and be provided with the stainless steel cask (1) of movable pulley;
(2) in same stainless steel cask (1), carry out successively respectively fermentation, the fruit of fruit fragmentation,Pericarp in fruit after fragmentation and fruit seed are got rid of and and the fruit separated after fermentation is gone outMethyl alcohol and fusel wine;
(3) between adjacent stations, transmit by promoting stainless steel cask (1), form semicontinuous production waterThe production line of fruit Spirit.
The production line of aforementioned production method is as follows:
This production line comprises several stainless steel casks 1. As shown in Figure 2, described stainless steel cask 1 is cylinderShape, the bottom of this stainless steel cask 1 is also provided with movable pulley 2, and described movable pulley 2 comprises that two be arranged in parallelRoller and a universal wheel, and described roller and described universal wheel finished product word structure, roll described in twoBetween wheel, the corresponding stainless steel cask 1 bottom place of keeping to the side is provided with for the protection of stainless steel cask 1 and supports notBackplate when rust steel drum inclination operation. This production line also comprises by the interior fruit smashing of described stainless steel cask 1 alsoThe crushing mixer 3 that stirs, by the pericarp in fruit after fragmentation and the fruit separator 4 got rid of of seed andFruit separated after fermentation is gone out to the distiller of methyl alcohol and fusel wine. At same described stainless steel caskIn 1, carry out successively the fragmentation of fermentation, the fruit of fruit, the pericarp in fruit after fragmentation and fruit seed are removedFall and the fruit separated after fermentation is gone out to methyl alcohol and fusel wine, between adjacent stations, passing through to promote instituteState stainless steel cask 1 and transmit, form the production line of semicontinuous production fruit distillate liquor. With the slip of repackingGeneral stainless steel cask 1 is basis, is equipped with special fruit smashing agitator 3, fruit stone separator 4 and distillationLow cost, the high efficiency of device composition, the production that can produce the high-grade fruit distillate liquor of the low fusel of low methyl alcoholLine. According to the capacity of stainless steel cask, form the fruit distillate liquor that daily output 9L-72L alcoholic strength is 50%.
As shown in Figure 3, described crushing mixer 3 comprises electric hand drill 5, the output of described electric hand drill 5The upper end of connection rotating shaft 6, being wound with rotation at the peripheral ring of described rotating shaft 6 lower ends can broken fruit, andAnd promoting fruit wine with dregs moves from top to bottom fruit stone is pushed to blunt 7 of described stainless steel cask bottom. Use torchBore 5 clamping of crushing heads and be rotating shaft 6 and blunt 7, in stainless steel cask 1, complete fruit smashing, blunt 7Be three round and smooth blunt knives in fan shape edge, blunt 7 under the drive of electric hand drill 5, rotation can broken waterReally, and leave complete fruit stone, blunt 7 has certain angle, can promote fruit wine with dregs from top to bottomMove, fruit stone is pushed to the bottom periphery of stainless steel cask 1.
As shown in Figure 4, described separator 4 is while tilting described rust steel drum, can be along bucket wall and bucketThe square basket bamboo strainer that is deposited on bottom fruit stone is fished at the turning of junction, the end, establishes at this square basket bamboo strainerThere is handle. Separate fruit stone is a link of sweat in good time, and separator 4 is along bucket baseplane to bucketThe turning motion of wall and bucket junction, the end can be fished for the square basket bamboo strainer of fruit stone, separates and is deposited on bottomFruit stone.
Distiller has following three kinds of embodiments:
As shown in Figure 5, described distiller comprises the fruit loading after fermentation to the first distiller embodimentDistillation stainless steel cask 1, the open top of described distillation stainless steel cask 1 be provided with heating kettle cover 8,This heating kettle cover 8 be provided with to the air inlet 9 of the interior input heating steam of described distillation stainless steel cask 1 andTo the venthole 10 of the outer output wine of described distillation stainless steel cask 1 steam. Above-mentioned distiller is applicable to traditional waterFruit Spirit fermentation technique.
As shown in Figure 6, described distiller comprises the fruit loading after fermentation to the second distiller embodimentDistillation stainless steel cask 1, the open top of described distillation stainless steel cask 1 be provided with heating kettle cover 8,In this heating kettle cover 8, be provided with the heating tube 11 extending to the bottom in described distillation stainless steel cask 1, in instituteState on heating kettle cover 8 and be also provided with the venthole 10 of exporting wine steam outside described distillation stainless steel cask. Due toIf when pomace, heating tube 11 heating can cause pomace to be cohered in its surface in fermentation fruit, because ofThis above-mentioned distiller is applicable to the fermentation fruit of distillation without pomace.
As shown in Figure 7, described distiller comprises stainless steel cask 1 to the third distiller embodiment, in instituteThe top of stating distillation stainless steel cask 1 is provided with heating kettle cover 8, in this heating kettle cover 8, is provided with to described steamingHeat up in a steamer the heat exchanger that extend the bottom in stainless steel cask 1, on described heating kettle cover 8, be also provided with to describedThe venthole 10 of the outer output wine of distillation stainless steel cask 1 steam. Described heat exchanger comprises upper in topCoil pipe 12, lower coil pipe 13 in bottom and connect the heating tube 14 of coil pipe 12 and lower coil pipe on this,In described heating tube 14, be provided with the electrical bar 15 of heating water quality, described upper coil pipe 12 and described lower coil pipe13 are also interconnected by return duct 16, are also provided with blast pipe 17, described on described heat exchangerThe exhaust outlet of blast pipe 17 is provided with pressure valve 18.
Heat exchanger by upper coil pipe 12, lower coil pipe 13 in bottom and connect on this coil pipe 12 and underCoil pipe 13 and connect the heating tube 14 of coil pipe 12 and lower coil pipe 13 on this and form, electrical bar 15 is pacifiedBe contained in 14 li of heating tubes, this distiller adopts electrical bar 15 to heat. Hot water is up from heating tube 14Enter coil pipe 12, then enter lower coil pipe 13 by return duct 16, form and reflux and realize heat exchange.Blast pipe 17 and pressure valve 18 are for improving water temperature and overflowing superpressure steam, and pressure valve 18 produces pressureFor 70KPa (170KPa), corresponding water temperature is 113 DEG C, can meet the heat exchange of still-process,In the time that heat exchange area is enough large, does not have steam and overflow from pressure valve 18. Coil pipe 12 on heat exchangerFollowing part is immersed in fruit wine with dregs, and while avoiding heating, skin slag is bonded on pipeline, reduces heat transfer efficiency. HeatInterchanger is by being connected on heating kettle cover 8, and hot fume is by heating between kettle cover 8 and heat exchangerSpace enters pipeline, enters fractionator through wine steam venthole 10.
Above-mentioned distiller is SD wine distiller, is the core that produces fruit distillate liquor streamline, itRealize with being connected by corrugated stainless steel tubing and quick chuck of heating kettle cover 8. With normal fermentation workSkill difference, the production process of orchard fruit distillate liquor has been omitted broken special equipment and the technique of squeezing the juice,In operating sequence, also have difference, sweat is more succinct, more convenient, and its technical process shows as: notRust adds fruit → add bacterial classification → fragmentation → fermentation → separation pomace and really seed → fermentation → steaming in steel drumHeat up in a steamer.
Introduce the production line of a complete fruit distillate liquor below:
Fruit, after pretreatment, is put into stainless steel cask 1 and adds yeast, with special broken agitator3 in stainless steel cask by fruit smashing, start fermentation.
By the time, after wine cap forms, the pomace on stainless steel cask 1 top is separated to another not with common bamboo strainerIn rust steel drum 1, then the stainless steel cask of fermentation 1 is tilted, will be gathered in stainless steel cask with separator 4The fruit stone of 1 bottom is separated, and pomace and fruit juice ferment respectively.
After completing fermentation, distill. Select above-mentioned distiller according to practical condition, can isolateMethyl alcohol and fusel wine, produce high-quality fruit distillate liquor.
The stainless steel cask 1 completing after distillation can enter streamline again without cleaning, and enters again and againThe brewing process of the processing of row fruit, fragmentation, fermentation, separation fruit stone and distillation. Use stainless steel cask canGreatly reduce the cost of streamline, the specification of current general stainless steel cask is 40,50,60,70,80cm,Volume is respectively 50L, 98L, 170L, 400L, corresponding actual distillation use volume for 45L, 88L,153L, 360L. To distill 2 calculating every day, one group of streamline sunrise capacity for liquor (fermented wine 10 is spent,Spirit 50% is spent) be respectively 9L, 17.6L, 30.6L, 72L.
Heating kettle cover 8 adopts muff, can be energy-conservation, reduce production costs. Taking 98L stainless steel cask asExample, heating power 4800W, distillation power 2400W. A people can complete 4 groups of fruit distillate liquors lifesProduce line from being crushed to whole work of distillation.
The foregoing is only preferred embodiment of the present utility model, in order to limit the utility model, not allWithin spirit of the present utility model and principle, any amendment of doing, be equal to replacement, improvement etc., allWithin should being included in protection domain of the present utility model.
Claims (6)
1. a production line for fruit distillate liquor, comprises several stainless steel casks (1), it is characterized in that,Described stainless steel cask (1) is cylindric, and the bottom of this stainless steel cask (1) is provided with movable pulley (2),Described movable pulley (2) comprises two rollers that be arranged in parallel and a universal wheel, and described roller andDescribed universal wheel finished product word structure, stainless steel cask (1) bottom corresponding between two described rollers is closeBackplate when edge is provided with for the protection of stainless steel cask (1) and supports stainless steel cask (1) inclination operation;
This production line also comprises the crushing mixer of the interior fruit smashing of described stainless steel cask (1) stirring(3), by the pericarp in fruit after fragmentation and the fruit separator (4) got rid of of seed and by after fermentationFruit separated goes out the distiller of methyl alcohol and fusel wine;
In same stainless steel cask (1), carry out successively the fragmentation of fermentation, the fruit of fruit, by fragmentationPericarp in rear fruit and fruit seed are got rid of and the fruit separated after fermentation are gone out to methyl alcohol and fuselWine, transmits by promoting stainless steel cask (1) between adjacent stations, forms the fruit of semicontinuous productionThe production line of Spirit.
2. production line according to claim 1, is characterized in that, described crushing mixer (3)Comprise electric hand drill (5), the upper end of the output connection rotating shaft (6) of described electric hand drill (5), in instituteThe peripheral ring of stating rotating shaft (6) lower end is wound with rotation can broken fruit, and promote fruit wine with dregs from top to bottomMotion is pushed to fruit stone blunt (7) of described stainless steel cask bottom.
3. production line according to claim 1, is characterized in that, described separator (4) is for incliningWhen oblique described stainless steel cask, can fish for and be deposited on bottom fruit stone along the turning of bucket wall and bucket junction, the endSquare basket bamboo strainer, be provided with handle at this square basket bamboo strainer.
4. according to the arbitrary described production line of claims 1 to 3, it is characterized in that described distillerComprise the distillation stainless steel cask (1) of fruit loading after fermentation, at described distillation stainless steel cask (1)Open top is provided with heating kettle cover (8), on this heating kettle cover (8), is provided with to described distillation stainless steelThe air inlet (9) of input heating steam and defeated outside described distillation stainless steel cask (1) in bucket (1)Go out the venthole (10) of wine steam.
5. production line according to claim 4, is characterized in that, described distiller comprises loadingThe distillation stainless steel cask (1) of the fruit after fermentation, in the open top of described distillation stainless steel cask (1)Be provided with heating kettle cover (8), in this heating kettle cover (8), be provided with to described distillation stainless steel cask (1)The heating tube (11) that extend interior bottom is also provided with to described distillation on described heating kettle cover (8)Stainless steel cask is exported the venthole (10) of wine steam outward.
6. production line according to claim 4, is characterized in that, described distiller comprises stainlessSteel drum (1), is provided with heating kettle cover (8) on the top of described distillation stainless steel cask (1), add at thisIn hot kettle cover (8), be provided with the heat exchanger extending to the interior bottom of described distillation stainless steel cask (1),On described heating kettle cover (8), be also provided with the vapour that goes out of exporting wine steam outside described distillation stainless steel cask (1)Mouth (10);
Described heat exchanger comprises the upper coil pipe (12) in top, the lower coil pipe (13) in bottomAnd connect the heating tube (14) of coil pipe on this (12) and lower coil pipe, in described heating tube (14)Be provided with the electrical bar (15) of heating water quality, described upper coil pipe (12) and described lower coil pipe (13) are also logicalCross return duct (16) and be interconnected, on described heat exchanger, be also provided with blast pipe (17), describedThe exhaust outlet of blast pipe (17) is provided with pressure valve (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521129255.4U CN205258435U (en) | 2015-12-30 | 2015-12-30 | Production line of fruit liquor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521129255.4U CN205258435U (en) | 2015-12-30 | 2015-12-30 | Production line of fruit liquor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205258435U true CN205258435U (en) | 2016-05-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521129255.4U Expired - Fee Related CN205258435U (en) | 2015-12-30 | 2015-12-30 | Production line of fruit liquor |
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| Country | Link |
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| CN (1) | CN205258435U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105462764A (en) * | 2015-12-30 | 2016-04-06 | 桂林市农业科学院 | Production line of fruit distilled liquor and producing method thereof |
-
2015
- 2015-12-30 CN CN201521129255.4U patent/CN205258435U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105462764A (en) * | 2015-12-30 | 2016-04-06 | 桂林市农业科学院 | Production line of fruit distilled liquor and producing method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160525 Termination date: 20191230 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |