CN217628299U - Strong aromatic Chinese spirit fermentation tank set - Google Patents
Strong aromatic Chinese spirit fermentation tank set Download PDFInfo
- Publication number
- CN217628299U CN217628299U CN202220685491.8U CN202220685491U CN217628299U CN 217628299 U CN217628299 U CN 217628299U CN 202220685491 U CN202220685491 U CN 202220685491U CN 217628299 U CN217628299 U CN 217628299U
- Authority
- CN
- China
- Prior art keywords
- fermentation tank
- tank
- pipe
- heat exchanger
- cooling
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Classifications
-
- 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
The utility model relates to a strong aromatic white spirit fermentation tank group, which comprises a head end fermentation tank, a tail end fermentation tank and a plurality of intermediate fermentation tanks, wherein the tank bodies are all included, the top part in the tank body is provided with a spray pipe, the bottom part is provided with a pore plate, a yellow water collecting tank is arranged below the pore plate, a water pump is arranged in the yellow water collecting tank, and a cooling pipe group is arranged above the pore plate; the water pump in the head end fermentation tank is communicated with the head end heat exchanger, the water outlet end of the head end heat exchanger is communicated with the spray pipe of the middle fermentation tank, yellow water enters the spray pipe after passing through the water pump and the heat exchanger of the middle fermentation tank between two adjacent middle fermentation tanks, the water pump of the middle fermentation tank is communicated with the tail end heat exchanger, the tail end heat exchanger is communicated with the cooling water inlet main pipe, the cooling water inlet main pipe is communicated with the cooling pipe group, the cooling pipe group is communicated with the cooling water outlet main pipe through the water outlet branch pipe of the cooling pipe group, and the cooling water outlet main pipe is communicated with the water inlet end of the tail end heat exchanger. The utility model discloses the fragrance and the taste of strong aromatic white spirit have been improved, strong aromatic white spirit quality has been promoted.
Description
Technical Field
The utility model relates to a white spirit makes technical field, especially relates to a strong aromatic type white spirit fermentation tank group.
Background
Yellow water is a byproduct in the production of the strong aromatic Chinese spirits, the amount of the yellow water generated in the cellar is measured and the relation between the yellow water and the fermentation is researched by tracking the fermentation time and the temperature change of a cellar for testing the production of the strong aromatic Chinese spirits, the difference of the contents of the flavor substances of fermented grains in different layers in the cellar is comparatively analyzed, and the result shows that: the yield of the yellow water has a quadratic function relation with the fermentation time and the fermentation temperature, the main period of the formation of the yellow water is in the early stage of fermentation, and the faster the fermentation is, the more the yield of the yellow water is; in the fermentation process of the Luzhou-flavor liquor in a cellar, pure solid state fermentation is carried out in the early stage, pure solid state fermentation is carried out in the middle and later stages of the fermentation of unstrained spirits on the upper layer in the cellar, and yellow water soaking fermentation is carried out on the unstrained spirits on the middle and lower layers; after the fermented grains are soaked in yellow water, the ethyl caproate, the organic acid, the n-propanol and the n-butanol are all higher than the upper layer of the un-soaked grains, and the higher the fermentation grains are close to the bottom layer.
In order to reasonably utilize the yellow water, different amounts of yellow water are permeated into the top of the fermented grains at the later stage of the fermentation of the strong aromatic Chinese spirits, and the influence of the yellow water on the quality of the Chinese spirits is researched. The result shows that the yellow water permeating into the fermented grains of the strong aromatic Chinese spirits at the later stage of fermentation has no obvious influence on the yield of the total high-grade alcohol, but influences the generation of organic acid, aldehydes and tetraesters, and except that the yield of ethyl butyrate is lower than that of a group without the yellow water, the contents of the organic acid, acetaldehyde acetal, ethyl lactate, ethyl hexanoate and ethyl acetate are obviously increased, and are increased along with the increase of the addition amount of the yellow water. The sensory quality evaluation of each group of wine samples shows that the wine quality of 30 percent of yellow water addition is better than that of other wine samples in terms of aroma and taste.
And the brewing of the white spirit is carried out at a low temperature, and the white spirit is slowly fermented, so that the formation of alcohol and sweet substances and the formation of higher alcohol are favorably controlled. Therefore, how to solve the contradiction is to uniformly add a proper amount of yellow water into the fermented grains of the Luzhou-flavor liquor so as to improve the aroma and the taste of the Luzhou-flavor liquor, increase the yield of the polyhydric alcohol and the higher alcohol and improve the quality of the Luzhou-flavor liquor, which is a problem worthy of research.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a strong aromatic white spirit fermentation tank group improves the fragrance and the taste of strong aromatic white spirit, increases the output of polyol and senior mellow wine, promotes strong aromatic white spirit quality.
The utility model provides a technical scheme that its technical problem adopted:
a strong aromatic Chinese liquor fermentation tank group comprises a head end fermentation tank, a tail end fermentation tank and a plurality of intermediate fermentation tanks, wherein the head end fermentation tank, the tail end fermentation tank and the intermediate fermentation tanks all comprise tank bodies, spray pipes are arranged at the tops of the tank bodies, pore plates are arranged at the bottoms of the tank bodies, yellow water collecting tanks are arranged below the pore plates, water pumps are arranged in the yellow water collecting tanks, and cooling pipe groups are arranged above the pore plates; the water pump in the head end fermentation tank passes through the end of intaking of pipeline intercommunication head end heat exchanger, the play water end of head end heat exchanger passes through the shower of the first intermediate fermentation tank of pipeline intercommunication, between two adjacent intermediate fermentation tanks, and yellow water gets into the shower of another intermediate fermentation tank behind water pump and the heat exchanger of one of them intermediate fermentation tank, and the water pump of last intermediate fermentation tank passes through the end of intaking of pipeline intercommunication tail end heat exchanger, the play water end intercommunication cooling water inlet manifold of tail end heat exchanger, the cooling water inlet manifold communicates respective cooling tube group one end wherein through the water inlet branch pipe that each fermentation tank corresponds, the cooling tube group other end is through its respective outlet branch pipe intercommunication cooling water outlet main, the cooling water outlet main communicates the end of intaking of tail end heat exchanger.
Furthermore, the water outlet end of the head end heat exchanger is simultaneously communicated with the water inlet end of the cooling pipe group of the first intermediate fermentation tank through a pipeline, the water outlet end of the heat exchanger between the intermediate fermentation tanks is communicated with the water inlet end of the cooling pipe group of the rear intermediate fermentation tank through a pipeline, and the cooling water inlet main pipe is simultaneously communicated with the spray pipe of the head end fermentation tank through a pipeline.
Further, the cooling pipe group comprises an upper transverse pipe, a lower transverse pipe and a middle vertical pipe which are communicated with each other.
Furthermore, the upper transverse pipe and the lower transverse pipe are at least two pairs of annular pipes which correspond up and down, and the two adjacent upper transverse pipes and the lower transverse pipes are communicated through a plurality of connecting pipes.
Furthermore, the spray pipe is arranged to be annular, and a plurality of spray heads are uniformly distributed on the spray pipe.
Further, the tank body comprises an inner layer, an outer layer and a middle heat-insulating layer; the tank body is provided with a discharge hole at the upper side of the pore plate.
Furthermore, each pipeline of water inlet branch pipe, water outlet branch pipe and valve that need to be established all sets up the solenoid valve, still includes the PLC controller that is used for automatic control.
The fermentation time of the first-end fermentation tank, the middle fermentation tank and the tail-end fermentation tank is staggered, the yellow water generated by the fermentation tank which is fermented in the front is used for the fermentation of the fermentation tank at the back, and the yellow water is sprayed from the top in the tank from the initial stage of the fermentation, so that the yellow water soaking fermentation is uniformly carried out at each stage of the fermentation; moreover, the rear fermentation tank is soaked by the sprayed yellow water, so that the required optimal low-temperature state can be maintained, slow fermentation is carried out, and meanwhile, the yellow water generated by the front fermentation tank can enter a cooling pipe group in the front fermentation tank to cool the fermentation tank after being cooled by a corresponding heat exchanger; the yellow water generated by the tail end fermentation tank is mainly used for cooling each fermentation tank and can also be used for spraying yellow water in the head end fermentation tank; thus, a yellow water spraying circulation and a yellow water cooling circulation are formed, and the yellow water is fully used.
Has the advantages that: the utility model discloses utilize strong aromatic white spirit production by-product yellow water to carry out yellow water to each stage of strong aromatic white spirit fermentation evenly and soak, improved the fragrance and the taste of strong aromatic white spirit, simultaneously, utilize yellow water to carry out temperature regulation in to the fermentation cylinder, increased the output of polyol and senior mellow wine, promoted strong aromatic white spirit quality.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a schematic view of the structure within the canister body;
FIG. 3 is a schematic top view of a cooling tube stack;
in the figure, a first-end fermentation tank 1, a tank body 11, a spray pipe 12, a spray header 1201, a cooling pipe group 13, an upper transverse pipe 1311, a middle vertical pipe 1312, a lower transverse pipe 1313, a ring pipe 1301, a connecting pipe 1302, an upper transverse pipe 1311, a pore plate 14, a yellow water collecting tank 15, a middle fermentation tank 2, a tail-end fermentation tank 3, a first-end heat exchanger 4, a middle heat exchanger 5, a tail-end heat exchanger 6, a cooling water inlet header pipe 7, a water inlet branch pipe 71, a cooling water outlet header pipe 8, a water outlet branch pipe 81 and a water pump 9.
Detailed Description
The technical solution in the embodiments of the present invention will be described in further detail with reference to the accompanying drawings in the embodiments of the present invention.
Fig. 1 to 3 show a highly flavored type white spirit fermentation tank set, which includes a head-end fermentation tank 1, a tail-end fermentation tank 3 and a plurality of intermediate fermentation tanks 2, in this embodiment, as shown in fig. 1, the head-end fermentation tank 1, the tail-end fermentation tank 3 and the intermediate fermentation tanks 2 all include a tank body 11, a top fixed spray pipe 12 and a bottom fixed orifice plate 14 are arranged in the tank body 11, a yellow water collection tank 15 is arranged below the orifice plate 14, as shown in fig. 2, a conical funnel is arranged between the lower part of the orifice plate 14 and the yellow water collection tank 15, so as to facilitate rapid collection of yellow water, a water pump 9 is arranged in the yellow water collection tank 15, and a cooling pipe set 13 is fixed above the orifice plate 14; the water pump 9 in the head end fermentation tank 1 is communicated with the water inlet end of the head end heat exchanger 4 through a pipeline, the water outlet end of the head end heat exchanger 4 is communicated with the spraying pipe 12 of the first intermediate fermentation tank 2 through a pipeline, yellow water enters the spraying pipe 12 of the other intermediate fermentation tank 2 after passing through the water pump 9 of one intermediate fermentation tank 2 and the intermediate heat exchanger 5 between two adjacent intermediate fermentation tanks 2, the water pump 9 of the last intermediate fermentation tank 2 is communicated with the water inlet end of the tail end heat exchanger 6 through a pipeline, the water outlet end of the tail end heat exchanger 6 is communicated with the cooling water inlet main pipe 7, the cooling water inlet main pipe 7 is communicated with one end of the respective cooling pipe group 13 through the water inlet branch pipe 71 corresponding to each fermentation tank, the other end of the cooling pipe group 13 is communicated with the cooling water outlet main pipe 8 through the respective water outlet branch pipe 81, and the cooling water outlet main pipe 8 is communicated with the water inlet end of the tail end heat exchanger 6.
The water outlet end of the head end heat exchanger 4 is also communicated with the water inlet end of the cooling pipe group 13 of the first intermediate fermentation tank 2 through a pipeline, the water outlet end of the intermediate heat exchanger 5 between the intermediate fermentation tanks 2 is communicated with the water inlet end of the cooling pipe group 13 of the rear intermediate fermentation tank 2 through a pipeline, and the cooling water inlet main pipe 7 is also communicated with the spray pipe 12 of the head end fermentation tank 1 through a pipeline.
The cooling tube bank 13 includes an upper cross tube 1311, a lower cross tube 1313 and several intermediate vertical tubes 1312 in communication with each other. The upper horizontal pipes 1311 and the lower horizontal pipes 1313 are at least two pairs of ring pipes 1301 corresponding to each other up and down, as shown in fig. 3, two sets of ring pipes 1301 are provided in this embodiment, and two adjacent upper horizontal pipes 1311 and two adjacent lower horizontal pipes 1313 are connected through a plurality of connecting pipes 1302, and in this embodiment, the two adjacent upper horizontal pipes 1311 and the two adjacent lower horizontal pipes 1313 are connected through 6 connecting pipes 1302.
The spray pipe 12 is arranged in a ring shape, and a plurality of spray heads 1201 are uniformly distributed.
The tank body 11 comprises an inner layer, an outer layer and an intermediate heat-insulating layer; the tank body 11 is provided with a discharge hole on the upper side of the pore plate 14.
The fermentation time of the head end fermentation tank 1, the middle fermentation tank 2 and the tail end fermentation tank 3 is staggered, yellow water generated by the fermentation tank which is fermented in the front is used for the fermentation of the fermentation tank at the back, and the yellow water is sprayed from the top in the tank from the initial fermentation stage, so that the yellow water soaking fermentation is uniformly carried out at each stage of the fermentation; moreover, the rear fermentation tank is soaked by the sprayed yellow water, so that the required optimal low-temperature state can be maintained, slow fermentation is carried out, and meanwhile, the yellow water generated by the front fermentation tank can be cooled by a corresponding heat exchanger and then enters the cooling pipe group 13 in the rear fermentation tank to cool the fermentation tank; the yellow water generated by the tail end fermentation tank 3 is mainly used for cooling each fermentation tank and can also be used for spraying yellow water in the head end fermentation tank 1; thus, a yellow water spraying circulation and a yellow water cooling circulation are formed, and the yellow water is fully used.
The discharge port can be provided with an automatic opening and closing valve, such as a pneumatic valve which is driven by a cylinder to open and close; all set up temperature sensor, all set up level sensor in the yellow water collection tank 15 in the jar body 11, branch 71, play water pipe 81 and each pipeline that need establish the valve of intaking all set up the solenoid valve, still including the PLC controller that is used for automatic control. The PLC receives data of the corresponding temperature sensor and the corresponding liquid level sensor, so that actions of the corresponding water pump 9, the heat exchanger and the corresponding electromagnetic valve are controlled, and yellow water spraying circulation and yellow water cooling circulation are automatically controlled.
To sum up, the utility model discloses obvious beneficial effect does: the utility model discloses utilize strong aromatic white spirit production by-product yellow water to carry out yellow water to each stage of strong aromatic white spirit fermentation evenly and soak, improved the fragrance and the taste of strong aromatic white spirit, simultaneously, utilize yellow water to carry out temperature regulation in to the fermentation cylinder, increased the output of polyol and senior mellow wine, promoted strong aromatic white spirit quality.
Finally, it should be noted that: the above embodiments are only used to illustrate the technical solution of the present invention, and not to limit the same; although the present invention has been described in detail with reference to the foregoing embodiments, those skilled in the art will understand that: the technical solutions described in the foregoing embodiments may still be modified, or some technical features may be equivalently replaced; such modifications and substitutions do not depart from the spirit and scope of the present invention.
Claims (7)
1. A strong aromatic Chinese liquor fermentation tank group is characterized by comprising a head end fermentation tank, a tail end fermentation tank and a plurality of intermediate fermentation tanks, wherein the head end fermentation tank, the tail end fermentation tank and the intermediate fermentation tanks all comprise tank bodies, spray pipes are arranged at the tops of the tank bodies, pore plates are arranged at the bottoms of the tank bodies, a yellow water collection tank is arranged below the pore plates, a water pump is arranged in the yellow water collection tank, and a cooling pipe group is arranged above the pore plates; the water pump in the head end fermentation tank passes through the end of intaking of pipeline intercommunication head end heat exchanger, the play water end of head end heat exchanger passes through the shower of the first intermediate fermentation tank of pipeline intercommunication, between two adjacent intermediate fermentation tanks, and yellow water gets into the shower of another intermediate fermentation tank behind water pump and the heat exchanger of one of them intermediate fermentation tank, and the water pump of last intermediate fermentation tank passes through the end of intaking of pipeline intercommunication tail end heat exchanger, the play water end intercommunication cooling water inlet manifold of tail end heat exchanger, the cooling water inlet manifold communicates respective cooling tube group one end wherein through the water inlet branch pipe that each fermentation tank corresponds, the cooling tube group other end is through its respective outlet branch pipe intercommunication cooling water outlet main, the cooling water outlet main communicates the end of intaking of tail end heat exchanger.
2. The Luzhou-flavor liquor fermentation tank set according to claim 1, wherein the water outlet end of the first-end heat exchanger is also communicated with the water inlet end of the cooling pipe set of the first intermediate fermentation tank through a pipeline, the water outlet end of the heat exchanger between the intermediate fermentation tanks is communicated with the water inlet end of the cooling pipe set of the rear intermediate fermentation tank through a pipeline, and the cooling water inlet main pipe is also communicated with the spray pipe of the first-end fermentation tank through a pipeline.
3. The Luzhou flavor liquor fermenter according to claim 1, wherein the cooling pipe set comprises an upper horizontal pipe, a lower horizontal pipe and a middle vertical pipe which are communicated with each other.
4. The Luzhou-flavor liquor fermentation tank set according to claim 3, wherein the upper transverse pipes and the lower transverse pipes are at least two pairs of annular pipes corresponding to each other up and down, and the two adjacent upper transverse pipes and the two adjacent lower transverse pipes are communicated through a plurality of connecting pipes.
5. The Luzhou-flavor liquor fermentation tank set according to claim 1, wherein the spray pipes are arranged in a ring shape, and a plurality of spray heads are uniformly distributed.
6. The Luzhou-flavor liquor fermentation tank set according to claim 1, wherein the tank body comprises an inner layer, an outer layer and an intermediate insulating layer; the tank body is provided with a discharge hole at the upper side of the pore plate.
7. The Luzhou-flavor liquor fermentation tank set according to claim 1, wherein the water inlet branch pipe, the water outlet branch pipe and each pipeline needing to be provided with valves are provided with electromagnetic valves, and the Luzhou-flavor liquor fermentation tank set further comprises a PLC controller for automatic control.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220685491.8U CN217628299U (en) | 2022-03-28 | 2022-03-28 | Strong aromatic Chinese spirit fermentation tank set |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220685491.8U CN217628299U (en) | 2022-03-28 | 2022-03-28 | Strong aromatic Chinese spirit fermentation tank set |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217628299U true CN217628299U (en) | 2022-10-21 |
Family
ID=83646061
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220685491.8U Active CN217628299U (en) | 2022-03-28 | 2022-03-28 | Strong aromatic Chinese spirit fermentation tank set |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217628299U (en) |
-
2022
- 2022-03-28 CN CN202220685491.8U patent/CN217628299U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107475016B (en) | White spirit fermentation device | |
| CN106701518B (en) | Daqu strengthening method for reducing Daqu dosage and improving vinegar quality | |
| US20190300827A1 (en) | Beer Brewing Device, Brewing Process Thereof, And its boil and fermentation module | |
| CN104087464B (en) | The brewing method of onion grape wine | |
| CN204702730U (en) | A kind of Novel steam distillation unit for liquor production by liquid fermentation | |
| CN104830620A (en) | Solid-state-method-based fermenting method of Luzhou-flavor liquor | |
| CN105007762A (en) | Method for producing non-alcoholic beer-flavored malt beverage | |
| CN107012103A (en) | Low yield fusel oil yeast and its application in mechanization production Chinese yeast former wine | |
| CN217628299U (en) | Strong aromatic Chinese spirit fermentation tank set | |
| CN111019780A (en) | Production method of noble rot wine | |
| CN111004691A (en) | Process for preparing low-alcohol brewed beer from hawthorn | |
| CN211199182U (en) | Distillation equipment for liquid fermented grains | |
| CN109022204A (en) | The Hakkas's rice wine and its production technology | |
| CN101319232B (en) | Method for preparing ethyl alcohol with corn fermentation | |
| CN201495212U (en) | High-efficiency acetic acid bioreactor | |
| CN116769555A (en) | Production process of bubble yellow wine | |
| CN107904133B (en) | Method for producing rose vinegar by pump reflux method | |
| CN102925312B (en) | Method for aging draft yellow wine | |
| US20190040343A1 (en) | System and method for building a high density fermented beverage | |
| EA036267B1 (en) | Fermentation tank with side ports and method of operation | |
| CN211713041U (en) | Grape wine brewing and storing device | |
| CN209024495U (en) | A kind of bean cotyledon fermentation vat with brine recycling function | |
| CN206051991U (en) | A kind of automatic acetotor | |
| CN210048732U (en) | Fermentation cylinder with temperature control device | |
| CN216890872U (en) | Making wine fermenting installation convenient to accuse temperature keeps warm |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |