CN215627867U - White spirit distillation system - Google Patents
White spirit distillation system Download PDFInfo
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- CN215627867U CN215627867U CN202121819174.2U CN202121819174U CN215627867U CN 215627867 U CN215627867 U CN 215627867U CN 202121819174 U CN202121819174 U CN 202121819174U CN 215627867 U CN215627867 U CN 215627867U
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Abstract
The utility model discloses a white spirit distillation system which comprises a steaming barrel and a receiving equipment set, wherein the steaming barrel is provided with a steam inlet and a wine steam outlet, the receiving equipment set is provided with a wine steam input end, the steam inlet of the steaming barrel is used for being connected with a steam pipeline, the wine steam input end is connected with the wine steam outlet of the steaming barrel through a pipeline so as to receive wine steam obtained by distillation in the steaming barrel, condense and store the wine steam, and flow control parts are arranged on the steam pipeline, the wine steam outlet of the steaming barrel and the pipeline of the wine steam input end of the receiving equipment set. Compared with the prior art, the white spirit distillation system is provided with the flow control piece, the pressure in the retort barrel can be controlled according to requirements in each distillation stage so as to meet the optimal wine quality control, and the quality of the distilled wine can be effectively improved.
Description
Technical Field
The utility model belongs to the field of liquor preparation, and particularly relates to a liquor distillation system.
Background
The existing white spirit solid distillation system mainly comprises a distillation part and a cooling part, wherein the distillation part comprises a retort barrel, and the cooling part comprises a condensation cooler. In the existing distillation system, fermented grains are filled into a retort barrel before distillation begins, steam is introduced into the bottom of the retort barrel, the fermented grains in the retort barrel are heated from bottom to top by the steam to generate wine vapor, and the main components of the wine vapor are alcohol vapor, water vapor and flavor substances; the wine vapor evaporated from the retort barrel is led into a condensing cooler through a pipeline, and is cooled into normal-temperature wine liquid by a water cooling method and then discharged. In the whole distillation process of the distillation system, the pressure in the discrimination barrel cannot be controlled, variable pressure distillation cannot be realized, and the distillation system is not beneficial to wine quality control. In addition, in the middle and later stages of distillation, the alcohol content of the distilled spirit is reduced along with the reduction of the alcohol content in the fermented grains, so that low-alcohol tail spirit is produced in the middle and later stages, the yield of high-concentration wine is low, and the quality of the distilled spirit is low.
The existing white spirit distillation system needs further improvement to improve the quality of the white spirit.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the problem that the liquor quality of the existing distillation system is difficult to control, and provides a liquor distillation system which can adjust the air pressure in a retort barrel by controlling the output quantity of the retort barrel.
The white spirit distillation system comprises a steaming barrel and a receiving equipment set, wherein the steaming barrel is provided with a steam inlet and a wine vapor outlet, the receiving equipment set is provided with a wine vapor input end, the steam inlet of the steaming barrel is used for being connected with a steam pipeline, the wine vapor input end is connected with the wine vapor outlet of the steaming barrel through a pipeline so as to receive wine vapor obtained by distillation in the steaming barrel, the wine vapor is condensed and stored, and a flow control part is arranged on the pipeline between the wine vapor outlet of the steaming barrel and the wine vapor input end of the receiving equipment set.
Compared with the prior art, the white spirit distillation system is provided with the flow control piece, the pressure in the retort barrel can be controlled according to requirements in each distillation stage so as to meet the optimal wine quality control, and the quality of the distilled wine can be effectively improved. If the fermented grains are filled into a retort barrel for distilling white spirit, positive pressure distillation is carried out, stable air pressure is in a certain range, excessive small change is avoided, the air pressure is properly reduced in the middle and later periods of distillation, otherwise, after the alcohol content in the fermented grains is reduced, the liquor flowing speed is high due to excessive air pressure, water brought into the liquor is also high, and the quality of the liquor is deteriorated.
Preferably, the wine vapor collecting device further comprises vacuum pumping equipment, the receiving equipment group is provided with an exhaust port, the wine vapor input end is communicated with the exhaust port, and the exhaust port is communicated with the vacuum pumping equipment through a pipeline. In this scheme, the wine vapour gets into and receives the group by the condensation, and the gas that fails the condensation remains in receiving equipment group and pipeline, and evacuation equipment opens the back, can take away remaining gas to cooperate with flow control spare, provide vacuum distillation's environment for the system.
Preferably, receiving equipment group includes cooling device and deposits the liquid container, cooling device includes evaporative condenser, the wine vapour input is established on evaporative condenser and is connected with its inner chamber, evaporative condenser is still including its inner chamber of intercommunication and external play liquid end, evaporative condenser is used for condensing wine vapour, it is used for receiving, saves wine liquid to deposit the liquid container, the upside at depositing the liquid container is established to the gas vent.
In order to improve the condensation efficiency of the wine vapor, the receiving equipment sets are provided with two sets, and each set comprises a first receiving equipment set and a second receiving equipment set, the evaporative condenser of the first receiving equipment set is provided with a wine vapor output end, the wine vapor input end of the evaporative condenser is communicated with the wine vapor outlet of the retort barrel, and the wine vapor output end of the evaporative condenser is connected with the wine vapor input end of the second receiving equipment set. In this scheme, the wine vapour that is not condensed in first receiving equipment group can be carried and continue the condensation in the second receiving equipment group to promote the condensation efficiency of wine vapour.
Preferably, the device also comprises a steam compressor, the evaporative condenser is a water-cooling heat exchanger, a first heat exchange channel and a second heat exchange channel are arranged in an inner cavity of the evaporative condenser, the first heat exchange channel is communicated with a wine steam input end and a liquid outlet end, a regenerated steam outlet communicated with the second heat exchange channel is arranged on the upper side of the evaporative condenser, the input end of the steam compressor is communicated with the regenerated steam outlet through a pipeline, and the output end of the steam compressor is communicated with a steam inlet of the retort barrel through a pipeline so as to form a steam recovery channel. In the scheme, after the steam compressor is started, water in the second heat exchange channel can be evaporated at a low temperature, is pumped into the inner cavity and then is pressurized and heated, and is conveyed into the retort barrel to distill the fermented grains, so that the consumption of new steam is reduced
Preferably, the device also comprises a waste liquid recovery device, wherein the waste liquid recovery device is connected with a wine vapor outlet of the screening barrel through a pipeline to form a waste vapor recovery channel so as to receive and liquefy tail vapor generated in the distillation process.
Further, the waste liquid recovery device comprises a switch valve, a condenser and a waste liquid recovery tank, wherein the waste liquid recovery tank is provided with a vacuumizing interface for communicating the inner cavity with the outside, the input end of the condenser is connected with a wine vapor outlet of the retort barrel through a pipeline, the switch valve is arranged on the pipeline between the condenser and the wine vapor outlet, a waste liquid inlet of the waste liquid recovery tank is connected with the output end of the condenser, and the vacuumizing equipment is connected with the vacuumizing interface through a pipeline to form a waste vapor recovery channel. In this scheme, waste liquid recovery unit can be used to collect the waste liquid to the tail gas that produces in the processing condensation process reduces and opens the rice steamer bucket and fall in a wretched state white cigarette and the smell in-process, thereby improves the production environment. After the distillation is finished, the vacuumizing equipment and the waste liquid recovery device are started, tail steam remained in the retort barrel is conveyed to the condenser, the tail steam is stored in the waste liquid recovery tank after being cooled, and gas which cannot be condensed is pumped away by the vacuumizing equipment, so that vacuum is formed in the retort barrel.
Preferably, the receiving equipment set further comprises a heat exchanger, the heat exchanger is provided with a first heat exchange channel and a second heat exchange channel, and the second heat exchange channel is communicated with the liquid outlet end of the evaporative condenser and the inlet of the liquid storage container.
Preferably, the vacuum pumping device is a vacuum pump.
Preferably, a flow control member is arranged on the steam pipeline. The scheme ensures that the system can control the input amount of new steam according to the input amount of the regenerated steam in the whole distillation process, reduces the consumption of the new steam, and can also control the input amount of the new steam to be matched with the output amount of wine gas according to requirements to adjust the pressure of the retort barrel.
Drawings
FIG. 1 is a schematic diagram of the present invention;
FIG. 2 is a system of the present invention, block diagram 1;
FIG. 3 is a system architecture of the present invention FIG. 2;
FIG. 4 is a system architecture of the present invention FIG. 2; .
Description of reference numerals:
the device comprises a retort barrel 1, a steam inlet 11, a wine steam outlet 13, a receiving equipment set 2, a first receiving equipment set 21, a second receiving equipment set 22, a wine steam input end 24, an evaporative condenser 25, a liquid outlet end 251, a regenerated steam outlet 252, a wine steam output end 253, a liquid storage container 26, an exhaust port 261, a heat exchanger 27, a flow control member 3, a control valve 6, a steam compressor 4, a steam recovery channel 41, a waste liquid recovery device 5, a switch valve 51, a condenser 52, a waste liquid recovery tank 53, a vacuumizing device 54 and a waste steam recovery channel 55.
Detailed Description
Referring to fig. 1-3, the white spirit distillation system of the utility model comprises a retort barrel 1 and a receiving equipment set 2, wherein the retort barrel 1 is provided with a steam inlet 11 and a wine steam outlet 13, the receiving equipment set 2 is provided with a wine steam input end 24, the steam inlet 11 of the retort barrel 1 is used for being connected with a steam pipeline, the wine steam input end 24 is connected with the wine steam outlet 13 of the retort barrel 1 through a pipeline so as to receive wine steam obtained by distillation in the retort barrel 1, condense and store the wine steam, and a flow control member 3 is arranged on the pipeline between the wine steam outlet 13 of the retort barrel 1 and the wine steam input end of the receiving equipment set 2.
In one embodiment, the flow control 3 is a flow regulating valve.
The system further comprises a vacuum-pumping device 54, the receiving device group 2 is provided with an exhaust port 261, the wine steam input end 24 is communicated with the exhaust port 261, and the exhaust port 261 is communicated with the vacuum-pumping device 54 through a pipeline. In this scheme, wine vapour gets into and receives the group by the condensation, and the gas that fails to condense remains in receiving equipment group 2 and pipeline, and evacuation equipment 54 opens the back, can take away remaining gas to cooperate with flow control 3, provide vacuum distillation's environment for the system.
Preferably, receiving equipment group 2 includes cooling device and liquid storage container 26, cooling device includes evaporative condenser 25, liquor vapour input end 24 establishes on evaporative condenser 25 and communicates its inner chamber, evaporative condenser 25 still includes its inner chamber of intercommunication and external play liquid end 251, evaporative condenser 25 is used for condensing liquor vapour, liquid storage container 26 is used for receiving, saving liquor, the upside at liquid storage container 26 is established to gas vent 261.
In an embodiment, the receiving apparatus set 2 further includes a heat exchanger 27, and the heat exchanger 27 is provided with a first heat exchange channel and a second heat exchange channel, and the second heat exchange channel communicates the liquid outlet end 251 of the evaporative condenser 25 with the inlet of the liquid storage container 26.
In order to improve the condensation efficiency of the wine vapor, the receiving device group 2 is provided with two groups, including a first receiving device group 21 and a second receiving device group 22, the evaporative condenser 25 of the first receiving device group 21 is provided with a wine vapor output end 253, the wine vapor input end 24 is communicated with the wine vapor outlet 13 of the retort barrel 1, and the wine vapor output end 253 is connected with the wine vapor input end 24 of the second receiving device group 22. In the scheme, the wine vapor which is not condensed in the first receiving equipment group 21 can be conveyed to the second receiving equipment group 22 for continuous condensation, so that the condensing efficiency of the wine vapor is improved.
Preferably, the device further comprises a vapor compressor 4, the evaporative condenser 25 is a water-cooled heat exchanger 27, a first heat exchange channel and a second heat exchange channel are arranged in an inner cavity of the evaporative condenser 25, the first heat exchange channel is communicated with the wine vapor input end 24 and the liquid outlet end 251, a regenerated vapor outlet 252 communicated with the second heat exchange channel is arranged on the upper side of the evaporative condenser 25, the input end of the vapor compressor 4 is communicated with the regenerated vapor outlet 252 through a pipeline, and the output end of the vapor compressor 4 is communicated with the vapor inlet 11 of the retort 1 through a pipeline to form a vapor recovery channel 41. In the scheme, after the steam compressor 4 is started, water in the second heat exchange channel can be evaporated at a low temperature, and is pumped into the inner cavity to be pressurized and heated, and then is conveyed into the retort barrel 1 to distill the fermented grains, so that the consumption of new steam is reduced.
In one embodiment, a flow control member is provided on the steam conduit.
In one embodiment, a control valve 6 for controlling the on-off of the pipeline is further arranged on the pipeline between the wine steam outlet 13 of the retort barrel 1 and the wine steam input end 24 of the receiving equipment group 2.
Preferably, the device also comprises a waste liquid recovery device 5, wherein the waste liquid recovery device 5 is connected with a wine vapor outlet of the screening barrel through a pipeline to form a waste vapor recovery channel so as to receive and liquefy tail vapor generated in the distillation process.
Further, the waste liquid recovery device 5 comprises a switch valve 51, a condenser 52 and a waste liquid recovery tank 53, wherein the waste liquid recovery tank 53 is provided with a vacuumizing interface for communicating an inner cavity with the outside, an input end of the condenser 52 is connected with the wine vapor outlet 13 of the retort 1 through a pipeline, the switch valve 51 is arranged on the pipeline between the condenser 52 and the wine vapor outlet 13, a waste liquid inlet of the waste liquid recovery tank 53 is connected with an output end of the condenser 52, and the vacuumizing equipment 54 is connected with the vacuumizing interface through a pipeline to form a waste vapor recovery channel 55. In this scheme, waste liquid recovery unit 5 can be used to collect the waste liquid, after the distillation, opens evacuation equipment 54 and waste liquid recovery unit 5, and the tail gas that remains in rice steamer bucket 1 is carried in condenser 52, is stored by the waste liquid recovery jar after the cooling, and the gas that can not condense is taken away by evacuation equipment 54 to make the interior vacuum that forms of rice steamer bucket 1.
In one embodiment, the condenser 52 may be an evaporative condenser, a water-cooled condenser, an air-cooled condenser, or the like.
In one embodiment, the evacuation device 54 is a vacuum pump.
Compared with the prior art, the white spirit distillation system is provided with the flow control member 3, the pressure in the retort barrel 1 can be controlled according to the requirement in each distillation stage to control the quality of the white spirit, and the quality of the distilled spirit can be effectively improved.
The working process is as follows:
the fermented grains in the retort barrel 1 are heated by conveying new steam to the retort barrel 1 through a steam pipeline, the generated wine steam is received, condensed and stored through the receiving equipment group 2, the pressure in the retort barrel 1 is controlled by controlling the wine steam output quantity of the retort barrel 1, and the pressure in the retort barrel can be controlled according to requirements in each stage of the distillation process so as to control the quality of the distilled wine.
In the distillation process, when the atmospheric distillation is required, the vacuumizing equipment 54 is kept closed, and the opening degree of the flow control part 3 is adjusted to control the output quantity of the wine vapor, so that the pressure of the retort barrel 1 is maintained in the atmospheric range; when the positive pressure distillation is needed, the vacuumizing equipment 54 is kept closed, the opening degree of the flow control part 3 is reduced to reduce the output quantity of the wine vapor, and the pressure of the retort barrel 1 is maintained in a positive pressure range; when vacuum distillation is required, evacuation device 54 is turned on to provide a vacuum environment for retort 1 and to control the vacuum value of retort 1 by adjusting the flow control. In the scheme, the vacuum distillation refers to reduced pressure distillation, and the vacuum degree of the retort barrel 1 is controlled by adjusting the flow control part 3.
Wine vapor enters the inner cavity of the evaporative condenser 25 from the wine vapor input end, the steam compressor 4 is started when the water temperature in the inner cavity reaches the set temperature, so that cooling water in the inner cavity of the evaporative condenser 25 is evaporated at a low temperature, low-temperature steam is discharged from the regenerated steam outlet 252 and enters the steam compressor 4, and is pressurized and heated by the steam compressor 4 and then conveyed into the retort barrel 1, so that the consumption of new steam in the retort barrel 1 can be reduced, and the conveying capacity of the new steam is reduced by the flow control member 3.
In the middle and later stages of distillation, the frequency of the steam compressor 4 of the first receiving equipment group 21 is automatically adjusted according to the water temperature in the evaporative condenser 25, so that the water temperature in the evaporative condenser 25 is kept between the condensation temperature of the wine vapor and the condensation temperature range of the water vapor, the low-concentration wine liquid is obtained by condensing the wine vapor, the low-concentration wine liquid condensed in the evaporative condenser 25 is conveyed to the heat exchanger 27 for cooling, and the cooled wine liquid is conveyed to the liquid storage container 26 for temporary storage; the wine vapor which is not condensed in the first receiving equipment group 21 enters the second receiving equipment group 22 for condensation, the frequency of the steam compressor 4 of the second receiving equipment group 22 is automatically adjusted according to the water temperature in the evaporative condenser 25, so that the water temperature in the evaporative condenser 25 is kept in the wine vapor condensation temperature range, high-concentration wine liquid is obtained by condensing the wine vapor, and the high-concentration wine obtained by condensation enters the heat exchanger 27 for cooling; after the distillation is finished, the waste liquid recovery device 5 is started, and tail gas in the retort barrel 1 is extracted to ensure that the retort barrel 1 is vacuumized.
Because the alcohol concentration of the fermented grains is high in the initial stage of distillation, and the concentration of distilled alcohol vapor is high, the first receiving equipment group 21 and the second receiving equipment group 22 are both used for preparing high-concentration wine, and in the middle and later stages of distillation, because the alcohol concentration of the fermented grains is reduced, after the liquid storage container 26 is replaced, low-concentration wine is prepared by the first receiving equipment group 21, and the reserved high-concentration alcohol vapor is used for preparing high-concentration wine, so that the efficiency of preparing high-concentration wine can be improved. In the latter stage of distillation, the water temperature of the evaporative condenser 25 is controlled by the activation frequency of the vapor compressors 4 of the two receiving equipment sets 2, so that the first receiving equipment set is used for preparing low-concentration wine and the second receiving equipment set 22 is used for preparing high-concentration wine, and most of the vapor components are condensed in the first receiving equipment set, so that the concentration of the wine vapor entering the second receiving equipment set 22 is high, and the quality of the high-concentration wine can be ensured.
Variations and modifications to the above-described embodiments may occur to those skilled in the art, which fall within the scope and spirit of the above description. Therefore, the present invention is not limited to the specific embodiments disclosed and described above, and some modifications and variations of the present invention should fall within the scope of the claims of the present invention. Furthermore, although specific terms are employed herein, they are used in a generic and descriptive sense only and not for purposes of limitation.
Claims (10)
1. White spirit distillation system, its characterized in that: the wine steam receiving device comprises a steaming barrel and a receiving equipment set, wherein the steaming barrel is provided with a steam inlet and a wine steam outlet, the receiving equipment set is provided with a wine steam input end, the steam inlet of the steaming barrel is used for being connected with a steam pipeline, the wine steam input end is connected with the wine steam outlet of the steaming barrel through a pipeline so as to receive wine steam obtained by distillation in the steaming barrel, the wine steam is condensed and stored, and a flow control part is arranged on the wine steam outlet of the steaming barrel and the pipeline of the wine steam input end of the receiving equipment set.
2. The white spirit distillation system according to claim 1, wherein: still include evacuation equipment, the receiving arrangement group is equipped with the gas vent, wine vapour input end with the gas vent intercommunication, and the gas vent passes through the pipeline intercommunication with evacuation equipment.
3. The white spirit distillation system according to claim 2, wherein: receiving equipment group includes cooling device and deposits the liquid container, cooling device includes evaporative condenser, the wine vapour input is established on evaporative condenser and is connected with its inner chamber, evaporative condenser is still including its inner chamber of intercommunication and external play liquid end, evaporative condenser is used for condensation wine vapour, it is used for receiving, saves wine liquid to deposit the liquid container, the upside at depositing the liquid container is established to the gas vent.
4. The white spirit distillation system according to claim 3, wherein: the receiving equipment sets are provided with two sets and comprise a first receiving equipment set and a second receiving equipment set, the evaporative condenser of the first receiving equipment set is provided with a wine vapor output end, the wine vapor input end of the evaporative condenser is communicated with a wine vapor outlet of the retort barrel, and the wine vapor output end of the evaporative condenser is connected with the wine vapor input end of the second receiving equipment set.
5. The white spirit distillation system according to claim 3, wherein: the wine steaming device is characterized by further comprising a steam compressor, the evaporative condenser is a water-cooling heat exchanger, a first heat exchange channel and a second heat exchange channel are arranged in an inner cavity of the evaporative condenser, the first heat exchange channel is communicated with a wine steam input end and a liquid outlet end, a regenerated steam outlet communicated with the second heat exchange channel is arranged on the upper side of the evaporative condenser, the input end of the steam compressor is communicated with the regenerated steam outlet through a pipeline, and the output end of the steam compressor is communicated with a steam inlet of the steaming bucket through a pipeline so as to form a steam recovery channel.
6. The white spirit distillation system according to claim 2, wherein: still include waste liquid recovery unit, waste liquid recovery unit passes through the pipeline and forms the waste steam recovery passageway with the wine vapour exit linkage of examining the bucket to receive, liquefy the tail gas that produces in the distillation process.
7. The white spirit distillation system according to claim 6, wherein: the waste liquid recovery device comprises a switch valve, a condenser and a waste liquid recovery tank, wherein the waste liquid recovery tank is provided with a vacuumizing interface for communicating an inner cavity with the outside, the input end of the condenser is connected with a wine vapor outlet of the retort barrel through a pipeline, the switch valve is arranged on a pipeline between the condenser and the wine vapor outlet, a waste liquid inlet of the waste liquid recovery tank is connected with the output end of the condenser, and vacuumizing equipment is connected with the vacuumizing interface through a pipeline so as to form the waste vapor recovery channel.
8. The white spirit distillation system according to claim 3, wherein: the receiving equipment set further comprises a heat exchanger, the heat exchanger is provided with a first heat exchange channel and a second heat exchange channel, and the second heat exchange channel is communicated with the liquid outlet end of the evaporative condenser and the inlet of the liquid storage container.
9. The white spirit distillation system according to claim 2, wherein: the vacuum pumping equipment is a vacuum pump.
10. The white spirit distillation system according to claim 5, wherein: and the steam pipeline is provided with a flow control element.
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| CN202121819174.2U CN215627867U (en) | 2021-08-05 | 2021-08-05 | White spirit distillation system |
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| CN202121819174.2U CN215627867U (en) | 2021-08-05 | 2021-08-05 | White spirit distillation system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113388484A (en) * | 2021-08-05 | 2021-09-14 | 佛山市丰川节能科技有限公司 | White spirit distillation system and distillation method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113388484A (en) * | 2021-08-05 | 2021-09-14 | 佛山市丰川节能科技有限公司 | White spirit distillation system and distillation method |
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