CN105087283B - Efficient fermentation device for full-aroma kiwi fruit wine - Google Patents
Efficient fermentation device for full-aroma kiwi fruit wine Download PDFInfo
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- CN105087283B CN105087283B CN201510637670.9A CN201510637670A CN105087283B CN 105087283 B CN105087283 B CN 105087283B CN 201510637670 A CN201510637670 A CN 201510637670A CN 105087283 B CN105087283 B CN 105087283B
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- tail gas
- fermenter
- fermentation
- exhaust purifier
- gas purifier
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Abstract
The invention discloses an efficient fermentation device for full-aroma kiwi fruit wine. A fermentation vat and a tail gas purifier are connected through a flange; a stirring motor is connected with a cone cover through a hollow shaft and then is inserted into the fermentation vat, blades and liquid inlet holes are formed in the cone cover, air inlets are uniformly distributed and formed in the circumference of the upper part of the hollow shaft, a hydraulic disc in the fermentation vat is connected with a helical conveyor through a shaft, the helical conveyor is arranged on a bottom valve, and the cone bottom of the fermentation vat is connected with a compressed air pipe; a jacket is arranged outside the tail gas purifier, a middle pipe is arranged in the tail gas purifier, and the tail gas purifier and a helical fin tube form a jacket structure, and a cyclone is arranged at an outlet of the tail gas purifier. Air (oxygen) is automatically and conveniently supplemented into the fermentation vat, the liquid mixing action is complete and sufficient, and the fermentation efficiency is high; deposition and blocking of materials are prevented conveniently, reliably and efficiently; the tail gas purifier can complete heat transfer and mass transfer efficiently in a multi-level manner and has a good gas-liquid separation effect, the aroma leakage is effectively prevented, automatic and efficient fermentation of the full-aroma kiwi fruit wine is realized, and the device has important application value.
Description
Technical field
The present invention relates to a kind of whole spice type Yangtao wine efficient ferment apparatus.
Background technology
The important content that Yangtao wine is Kiwi berry intensive processing is made using Kiwi berry pulp, fruit juice fermentation, favorably
It is significant in extending the industrial chain of Kiwi berry processing and improving the added value of Kiwi berry.
But mainly or using traditional semi-enclosed fermentation, one is air to existing kiwi fruit wine fermentation（Oxygen）Drum
Enter insufficient and inconvenience, the speed of kiwi fruit wine fermentation is slow, time length, efficiency are low, need to increase special air and blast
Equipment, increases equipment investment, also causes unnecessary trouble；Two is that fragrance is easily leaked, thus to kiwi fruit wine product
Flavor effect is very big, but if incorrect sealing then easily causes the security incidents such as blast.
Therefore, if can design a kind of air it is automatically convenient blast, fragrance is not easy leakage and is not the Mi of pressure vessel
Monkey peach fruit wine efficient ferment apparatus, then with important actual application value.
The content of the invention
The technical problem to be solved in the present invention is exactly to overcome the deficiencies in the prior art, there is provided a kind of simple and practical, empty
Gas is automatically convenient to be blasted, fragrance is not easy leakage and be not the whole spice type Yangtao wine efficient ferment apparatus of pressure vessel.
To overcome the deficiencies in the prior art, the present invention to take technical scheme below：
A kind of whole spice type Yangtao wine efficient ferment apparatus, including fermenter and exhaust purifier, it is characterised in that：Send out
The intervalve of ferment bucket and exhaust purifier is detachably connected by flange, and exhaust purifier is linked back by overflow pipe and time liquid inclined tube
Fermenter；Fermenter is provided with manhole, liquid feed valve and heating jacket, and stirring motor inserts fermenter after hollow shaft connection cone cover
It is interior, blade and inlet opening are provided with cone cover, the air inlet that axle circumference uniform distribution is opened is arranged at hollow shaft top, and axle sleeve is arranged at hollow shaft bottom
Dynamic state limit and stable support function are played, surge disk and its axle sleeve are provided with fermenter, the disk that surges connects helical feed by axle
Device, on bottom valve, fermenter cone bottom Jing valves connect compressed air hose to auger conveyor；It is provided with chuck outside exhaust purifier to lead to
Cooling water or chilled water, inside is provided with open intervalve and constitutes jacket structured, helical fin cylinder with the helical fin cylinder of closing
Form for inwall welding helical fin, the gap of helical fin cylinder and exhaust purifier inwall is provided with inverted cone sieve dish, tail gas clean-up
Device outlet is provided with cyclone, and cyclone is formed by connecting with outer tube for axis by spinning disk.
The heating jacket is provided with heating agent inlet pipe and outlet pipe.
The tail gas recycle device chuck is provided with refrigerant inlet pipe and outlet pipe.
The core of the design is exactly that fermenter is detachably connected with exhaust purifier by flange.
Fermenter has heating jacket, operates the solid-phase materials such as certain liquid level, sucrose, yeast by opening manhole
Removable cover is added, and the liquid phase material such as carambola juice is added by liquid feed valve control, and stirring motor connects leaf by hollow shaft
The air inlet that axle circumference uniform distribution is opened is arranged at wheel cone cover, hollow shaft top, and bottom has axle sleeve to play dynamic state limit and stable support function.
The disk that surges connects auger conveyor by axle, and axle sleeve plays dynamic support and stabilization to axle, and bottom valve plays discharge control action.
Impeller cone cover connection hollow shaft is driven by motor and is rotated at a high speed, and inlet opening feed liquor is accelerated to be centrifuged by blade, along cone cover
Inner surface movement, is thrown away by boring shroud rim, so high speed liquid flow can be produced in upper speed cone cover and be produced vacuum then, so
Large quantity of air draws in mixed liquor stream along hollow shaft by air inlet by vacuum, is thrown away by boring shroud rim, realizes that gas liquid high-efficiency is mixed
Close and air（Oxygen）Supply.In addition, liquid stream drives the disk that surges by the vanelets that effect is surged on disk, the disk that surges is driven by axle
Dynamic auger conveyor, effectively prevents from boring the deposition of substrate material and blocking.
When speed of agitator it is relatively low, it is impossible to when realizing that enough vacuum complete the suction of gas, bottom can be bored by fermenter
Compressed air hose import air（Oxygen）, carry out oxygen and fill into and assist the carbon dioxide spilling that fermentation is produced；Simultaneously because
The addition of gas, causes localized liquid averag density to change, and produces density contrast convection current, in conjunction with stirring at low speed, realizes fermentation tank
Interior good convection current, the high efficiency for keeping the uniformity and gas of material to supplement can also prevent from boring the deposition blocking of substrate material, reach
Favourable fermentation condition.
The logical steam of heating jacket or hot water realize heat temperature raising, can also lead to cold water and be lowered the temperature, and the gas for overflowing liquid level is same
When can carry vapor, ammonia and become tail gas, gaseous mixture is realized reclaiming and tail gas clean-up by exhaust purifier, it is to avoid fragrance is let out
Leakage.
Exhaust purifier has chuck to lead to cooling water or chilled water, and intervalve is jacket structured with helical fin cylinder composition,
Overflow gas and top is risen to again by the downward water conservancy diversion of helical fin cylinder by intervalve, due to having spiral wing in helical fin cylinder
Piece, can realize guiding rotation to gas in interlayer, produce downward helical air flow path, be overflowed by helical fin cylinder lower edge
And dish is sieved through inverted cone, and overflowing from liquid level after good diffusion and rise, air-flow is forced cyclone in cyclone by spinning disk effect, can
With the liquid phase that effective centrifugation wherein may be carried, discharge gas is set to realize purification, liquid phase meeting automatic dipping wall flows back downwards.
The clean-up effect of exhaust purifier depends on overcoming difficulties the heat and mass transport for carrying out, the wherein controlled overflow pipe of liquid level
Position, many rear overflow pipes of condensate liquid can overflow, returning liquid inclined tube can effectively prevent return slag from blocking, chilled water and tail gas in chuck
Liquid phase has very high overall heat-transfer coefficient in clarifier, and liquid is good because temperature and gas overflowing can be produced in exhaust purifier
Automatic stirring convection circulation, helical fin cylinder has bigger gas phase side heat exchange area, while subsurface liquid phase can be passed efficiently
Heat, cooling ammonia condensing is realized to gas phase in cylinder, and the cryogenic gas that ullage point is spilled off realizes gas phase precooling in cylinder；Spiral wing
Swirling eddy can promote heat and mass transfer with effective disturbance air film in piece cylinder, carry out one-level cooling, condensation, gas-liquid separation, then
Dish liquid phase layer good diffusion is sieved through inverted cone, the heat and mass transfer of two grades of directly contacts is realized, realizes that fragrance efficiently catches, risen
Gas phase finally realizes once again cyclonic separation in cyclone, makes emission reach purification and requires.
The design adopts basic closed interlayer pot fermentation system, then supporting tail gas recycle fragrance, in the feelings that air capacity is larger
Under condition, the condensation and effectively recovery of fragrance is realized, while completing tail gas clean-up discharge.Exist in a large number in incoagulable gas and serious
In the case of affecting condensing interface heat and mass transport state, the high-efficiency condensation for realizing fragrance catches.
Compared with prior art, beneficial effects of the present invention are also resided in：
Fermentation atmosphere in the tub（Oxygen）Supplement convenient, liquid stream immixture automatically and improve abundant, fermentation efficiency is very high；Pass through
Liquid stream drives the disk that surges to prevent material deposition blocking convenient, reliable, efficient with auger conveyor；Exhaust purifier is multistage, efficient
Complete heat transfer, mass transfer, gas-liquid separation effect especially good, effectively prevent the leakage of fragrance.
The present invention realizes the automatical and efficient of whole spice type kiwi fruit wine fermentation, with important by above Integration ofTechnology
Using value.
Description of the drawings
Fig. 1 is the planar structure schematic diagram of the present invention
Fig. 2 is the three dimensional structure diagram of impeller cone cover.
Fig. 3 is the three dimensional structure diagram of disk of surging.
Fig. 4 is the three dimensional structure diagram of cyclone.
Fig. 5 is helical fin bobbin mouth three dimensional structure diagram.
Fig. 6 is helical fin cylinder section view three dimensional structure diagram.
Each label is represented in figure：
A, impeller cone cover；B, surge disk；C, cyclone；D, helical fin cylinder；1st, stirring motor；2nd, air inlet；3rd, manhole；
4th, liquid feed valve；5th, fermenter；6th, hollow shaft；7th, liquid level in fermenter；8th, heating agent inlet pipe；9th, heating jacket；10th, hollow shaft axle
Set；11st, heating agent outlet pipe；12nd, dish axle of surging set；13rd, auger conveyor；14th, bottom valve；15th, liquid inclined tube is returned；16th, compressed air hose；
21st, exhaust purifier；22nd, refrigerant outlet pipe；23rd, exhaust purifier liquid level；24th, overflow pipe；25th, chuck is freezed；26th, flow spiral
Path；27th, inverted cone sieve dish；28th, intervalve；29th, refrigerant inlet pipe；31st, cone cover；32nd, inlet opening；33rd, blade；34th, hollow axis hole；
35th, surge disk；36th, surge disk vanelets；37th, spinning disk；38th, axis；39th, outer tube；40th, helical fin.
Specific embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
As shown in Figure 1, Figure 2, the Yangtao wine efficient ferment apparatus of whole spice type shown in Fig. 3, Fig. 4, Fig. 5 and Fig. 6, including fermenter
5 and the intervalve 28 of exhaust purifier 21, fermenter 5 and exhaust purifier 21 be detachably connected by flange, exhaust purifier
21 by overflow pipe 24 and return liquid inclined tube 15 and are linked back fermenter 5；Fermenter 5 is provided with manhole 3, liquid feed valve 4 and heating jacket 9, stirs
Motor 1 is mixed by inserting in fermenter 5 after the connection cone of hollow shaft 6 cover 31, in cone cover 31 blade 33 and inlet opening 32 are provided with, it is hollow
The air inlet 2 that axle circumference uniform distribution is opened is arranged at the top of axle 6, and 10 dynamic state limits of axle sleeve and stable support function are arranged at the bottom of hollow shaft 6,
Surge disk 35 and its axle sleeve 12 are provided with fermenter 5, the disk 35 that surges connects auger conveyor 13 by axle, and auger conveyor 13 exists
14 on bottom valve, the cone of fermenter 5 bottom Jing valve connection compressed air hoses 16；Chuck 25 is provided with outside exhaust purifier 21 and leads to cooling water
Or chilled water, it is jacket structured with the helical fin cylinder D compositions closed that inside is provided with open intervalve 28, and helical fin cylinder D is
Inwall welding helical fin 40 is formed, and the gap of helical fin cylinder D and the inwall of exhaust purifier 21 is provided with inverted cone sieve dish 27, tail gas
The outlet of clarifier 21 is provided with cyclone C, and cyclone C is formed by connecting with outer tube for axis 38 by spinning disk 37.
The heating jacket 9 is provided with heating agent inlet pipe 8 and outlet pipe 11.
The tail gas recycle device chuck is provided with refrigerant inlet pipe 29 and outlet pipe 22.
The core of the design is exactly that fermenter 5 is detachably connected with exhaust purifier 21 by flange.
Fermenter 5 has heating jacket 9, and liquid level is 7, the activity that the solid-phase material such as sucrose, yeast passes through opening manhole 3
Cover plate is added, and the liquid phase material such as carambola juice is added by the control of liquid feed valve 4, and stirring motor 1 connects impeller by hollow shaft 6
The air inlet 2 that axle circumference uniform distribution is opened is arranged at cone cover A, the top of hollow shaft 6, and bottom has 10 dynamic state limits of axle sleeve to make with stable support
With.The disk B that surges connects auger conveyor 13 by axle, and axle sleeve 12 plays dynamic support and stabilization, 14 discharges of bottom valve to axle
Control action.
Impeller cone cover A connection hollow shafts 6 drive rotation at a high speed, the feed liquor of inlet opening 32 to accelerate centrifugation by blade 33 by motor 1,
Along cone 31 inner surface movements of cover, thrown away by 31 edges of cone cover, so can produce high speed liquid flow then in upper speed cone cover 31
Vacuum is produced, such large quantity of air draws in mixed liquor stream along hollow shaft 6 by air inlet 2 by vacuum, got rid of by 31 edges of cone cover
Go out, realize that gas liquid high-efficiency mixes and air（Oxygen）Supply.In addition, liquid stream is driven by the vanelets 36 that effect is surged on disk B
Surge disk, and the disk B that surges drives auger conveyor 13 by axle, effectively prevents from boring the deposition of substrate material and blocking.
When speed of agitator it is relatively low, it is impossible to when realizing that enough vacuum complete the suction of gas, bottom can be bored by fermenter
Compressed air hose 16 import air（Oxygen）, carry out oxygen and fill into and assist the carbon dioxide spilling that fermentation is produced；While by
In the addition of gas, cause localized liquid averag density to change, produce density contrast convection current, in conjunction with stirring at low speed, realize fermentation
Good convection current in tank, the high efficiency for keeping the uniformity and gas of material to supplement can also prevent from boring the deposition blocking of substrate material, reach
To favourable fermentation condition.
Heating jacket 9 leads to steam or hot water realizes heat temperature raising, can also lead to cold water and be lowered the temperature, and the gas for overflowing liquid level is same
When can carry vapor, ammonia and become tail gas, gaseous mixture is realized reclaiming and tail gas clean-up by exhaust purifier 21, it is to avoid fragrance
Leakage.
Exhaust purifier 21 has chuck 25 to lead to cooling water or chilled water, and intervalve 28 constitutes folder with helical fin cylinder D
Nested structure, overflows gas and rises to top again by the downward water conservancy diversion of helical fin cylinder D by intervalve 28, due to helical fin cylinder
There is helical fin 40 in D, guiding rotation can be realized to gas in interlayer, downward helical air flow path 26 is produced, by spiral shell
Rotation fin cylinder D lower edges are overflowed and sieve dish 27 through inverted cone, are overflowed from liquid level 23 after good diffusion and are risen, and air-flow is in cyclone C
By spinning disk 37 effect force cyclone, can effectively centrifugation wherein may carry liquid phase, make discharge gas realize purify,
Liquid phase meeting automatic dipping wall flows back downwards.
The clean-up effect of exhaust purifier 21 depends on overcoming difficulties the heat and mass transport for carrying out, and wherein liquid level 23 is controlled overflows
The position of flow tube 24, many rear overflow pipes 24 of condensate liquid can overflow, returning liquid inclined tube 15 can effectively prevent return slag from blocking, in chuck 25
Chilled water has very high overall heat-transfer coefficient with liquid phase in exhaust purifier, and liquid is due to temperature and gas overflowing in exhaust purifier
Good automatic stirring convection circulation can be produced, helical fin cylinder D has bigger gas phase side heat exchange area, while under liquid level 23
Liquid phase can realize cooling ammonia condensing to gas phase in cylinder with efficient heat transfer, and the cryogenic gas being partly spilled off on liquid level 23 realizes cylinder
Interior gas phase precooling；Swirling eddy can promote heat and mass transfer with effective disturbance air film in helical fin cylinder D, carry out one-level cold
But, condensation, gas-liquid separation, are then passed through the inverted cone sieve liquid phase layer good diffusion of dish 27, realize the heat and mass transfer of two grades of directly contacts,
Realize that fragrance efficiently catches, ascending vapor finally realizes once again cyclonic separation in cyclone C, making emission reach purification will
Ask.
Above-mentioned simply presently preferred embodiments of the present invention, not makees any pro forma restriction to the present invention.It is any to be familiar with sheet
The technical staff in field, in the case of without departing from technical solution of the present invention scope, all using the technology contents of the disclosure above
Many possible variations and modification, or the Equivalent embodiments for being revised as equivalent variations are made to technical solution of the present invention.Therefore, it is all
It is the content without departing from technical solution of the present invention, any simply repaiies to made for any of the above embodiments according to the technology of the present invention essence
Change, equivalent variations and modification, all should fall in the range of technical solution of the present invention protection.
Claims (3)
1. a kind of whole spice type Yangtao wine efficient ferment apparatus, including fermenter and exhaust purifier, it is characterised in that：Fermentation
The intervalve of bucket and exhaust purifier is detachably connected by flange, and exhaust purifier is linked back by overflow pipe and time liquid inclined tube and is sent out
Ferment bucket；Fermenter is provided with manhole, liquid feed valve and heating jacket, and stirring motor inserts fermenter after hollow shaft connection cone cover
It is interior, blade and inlet opening are provided with cone cover, the air inlet that axle circumference uniform distribution is opened is arranged at hollow shaft top, and axle sleeve is arranged at hollow shaft bottom
Dynamic state limit and stable support function are played, surge disk and its axle sleeve are provided with fermenter, the disk that surges connects helical feed by axle
Device, on bottom valve, fermenter cone bottom Jing valves connect compressed air hose to auger conveyor；It is provided with chuck outside exhaust purifier to lead to
Cooling water or chilled water, inside is provided with open intervalve and constitutes jacket structured, helical fin cylinder with the helical fin cylinder of closing
Form for outer tube welding helical fin, the gap of helical fin cylinder and exhaust purifier inwall is provided with inverted cone sieve dish, tail gas clean-up
Device outlet is provided with cyclone, and cyclone is formed by connecting with outer tube for axis by spinning disk.
2. whole spice type Yangtao wine efficient ferment apparatus according to claim 1, it is characterised in that：The heating jacket sets
There are heating agent inlet pipe and outlet pipe.
3. whole spice type Yangtao wine efficient ferment apparatus according to claim 1 or claim 2, it is characterised in that：The tail gas is net
Change device chuck and be provided with refrigerant inlet pipe and outlet pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510637670.9A CN105087283B (en) | 2015-10-07 | 2015-10-07 | Efficient fermentation device for full-aroma kiwi fruit wine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510637670.9A CN105087283B (en) | 2015-10-07 | 2015-10-07 | Efficient fermentation device for full-aroma kiwi fruit wine |
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| Publication Number | Publication Date |
|---|---|
| CN105087283A CN105087283A (en) | 2015-11-25 |
| CN105087283B true CN105087283B (en) | 2017-04-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510637670.9A Active CN105087283B (en) | 2015-10-07 | 2015-10-07 | Efficient fermentation device for full-aroma kiwi fruit wine |
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2579900Y (en) * | 2002-11-14 | 2003-10-15 | 锁现民 | Deep layer cultivation fermentation pot medicinal liquid sterilizing air inlet and outler device for edible mushroom |
| CN201276562Y (en) * | 2008-10-22 | 2009-07-22 | 方民 | Aerobic biofermentation tank for recycling tail gas |
| CN203782145U (en) * | 2014-04-02 | 2014-08-20 | 焦爱迪 | Biological fermentation tank with tail gas purification device |
-
2015
- 2015-10-07 CN CN201510637670.9A patent/CN105087283B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2579900Y (en) * | 2002-11-14 | 2003-10-15 | 锁现民 | Deep layer cultivation fermentation pot medicinal liquid sterilizing air inlet and outler device for edible mushroom |
| CN201276562Y (en) * | 2008-10-22 | 2009-07-22 | 方民 | Aerobic biofermentation tank for recycling tail gas |
| CN203782145U (en) * | 2014-04-02 | 2014-08-20 | 焦爱迪 | Biological fermentation tank with tail gas purification device |
Non-Patent Citations (1)
| Title |
|---|
| 发酵空气过程控制与节能;陆飞浩等;《发酵科技通讯》;20131031;第42卷(第4期);第50-53页 * |
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| Publication number | Publication date |
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| CN105087283A (en) | 2015-11-25 |
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