CN108485893A - Continuous liquor steaming device and its continuous liquor steaming method - Google Patents
Continuous liquor steaming device and its continuous liquor steaming method Download PDFInfo
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- CN108485893A CN108485893A CN201810551527.1A CN201810551527A CN108485893A CN 108485893 A CN108485893 A CN 108485893A CN 201810551527 A CN201810551527 A CN 201810551527A CN 108485893 A CN108485893 A CN 108485893A
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- 238000010025 steaming Methods 0.000 title claims abstract description 106
- 238000000034 method Methods 0.000 title claims description 14
- 235000014101 wine Nutrition 0.000 claims abstract description 220
- 238000004821 distillation Methods 0.000 claims abstract description 62
- 239000007788 liquid Substances 0.000 claims abstract description 34
- 235000020097 white wine Nutrition 0.000 claims abstract description 17
- 238000009833 condensation Methods 0.000 claims description 6
- 230000005494 condensation Effects 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 4
- 235000013339 cereals Nutrition 0.000 description 69
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 5
- 240000007594 Oryza sativa Species 0.000 description 4
- 235000007164 Oryza sativa Nutrition 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 235000009566 rice Nutrition 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000009977 dual effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 235000015096 spirit Nutrition 0.000 description 2
- 240000006394 Sorghum bicolor Species 0.000 description 1
- 235000011684 Sorghum saccharatum Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000019441 ethanol Nutrition 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 235000015099 wheat brans Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
- C12H6/00—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages
- C12H6/02—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages by distillation
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Food Science & Technology (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Alcoholic Beverages (AREA)
Abstract
The present invention provides a kind of continuous liquor steaming device, including steaming wine tank, vinasse runner pipe and wine steam runner pipe, it steams to be formed in wine tank and steams wine space, steam thermal energy exchange area and distillation zone that wine space includes interconnected, it steams wine tank and is equipped with fermented grain charge door, vinasse runner pipe is installed in wine steam runner pipe to be steamed on wine tank, vinasse runner pipe and wine steam runner pipe extend to distillation zone via thermal energy exchange area, one end of vinasse runner pipe is located in distillation zone and positioned at the lower section for steaming liquid level in wine space, and the other end of vinasse runner pipe, which is located at, to be steamed outside wine tank；One end of wine steam runner pipe is located in distillation zone and positioned at the top for steaming liquid level in wine space, and the other end of wine steam runner pipe, which is located at, to be steamed outside wine tank.The continuous liquor steaming device can before it is distilled preheat fermented grain with wine steam using the vinasse of high temperature, to reach energy-efficient purpose；Meanwhile wine steam is cooled down using fermented grain, white wine is can be obtained it is not necessary that condenser is arranged, reduces equipment cost.
Description
Technical field
The present invention relates to steam wine technical field, and in particular to a kind of continuous liquor steaming device and its continuous liquor steaming method.
Background technology
White wine be using Cereals as primary raw material, with yeast, Chinese yeast or wheat bran and distiller's yeast etc. for saccharifying ferment, through boiling,
Saccharification, is distilled and manufactured Spirit at fermentation.It in Guangxi province, predominantly rice spirit, is represented, is belonged to three Hua Wei of Guilin
Chinese yeast odor type wine, is saccharifying ferment by raw material, Chinese yeast of rice, and with rice solid-state early period culture saccharification, the later stage adds water to turn cylinder
Semi liquid state ferments, and liquid distillate forms.Distillation is an important step in liquor production, in this step, is made by distillation
Ethyl alcohol and other fragrance matters in fermented grain are vaporized into wine vapour, then wine vapour is introduced condensing unit and is produced by condensation cooling
Product white wine；Vinasse are generated after fermented grain distillation, it is different from the white wine made using sorghum as raw material, it is made using rice as raw material white
Wine, the vinasse generated are liquid, and in the prior art, the high temperature vinasse after distillation are expelled directly out, and heat cannot get profit
With causing to waste.Furthermore the continuous liquor steaming device of the prior art, generally includes alembic and condenser.Fermented grain is in alembic
Distillation, the high temperature wine steam distilled are passed through condensation in condenser and obtain white wine liquid.In actual production, needed for fermented grain distillation
Thermal energy it is larger, generally require using coal to alembic provide heat source can be only achieved required thermal energy.In addition, continuous liquor steaming fills
It sets including alembic and condenser, equipment cost is relatively high.
Invention content
In view of the above problems, it is necessary to which a kind of energy-efficient continuous liquor steaming device is provided.
In order to achieve the above objectives, the technical solution adopted in the present invention is：
A kind of continuous liquor steaming device, including wine tank is steamed, it is formed in the steaming wine tank and steams wine space, the steaming wine space includes
Interconnected thermal energy exchange area and distillation zone, the steaming wine tank be equipped with fermented grain charge door, the fermented grain charge door with it is described
Thermal energy exchange area is connected to；The continuous liquor steaming device further includes vinasse runner pipe and wine steam runner pipe, the vinasse runner pipe
Setting is installed on the steaming wine tank and is spaced with the wine steam runner pipe, and the vinasse runner pipe is via the thermal energy
Exchange area extends to the distillation zone, and one end of the vinasse runner pipe is located in the distillation zone and is located at the steaming wine space
The other end of the lower section of interior liquid level, the vinasse runner pipe is located at outside the steaming wine tank；The wine steam runner pipe is via described
Thermal energy exchange area extends to the distillation zone, and one end of the wine steam runner pipe is located in the distillation zone and is located at the steaming
The other end of the top of liquid level in wine space, the wine steam runner pipe is located at outside the steaming wine tank；The vinasse runner pipe and
Valve is mounted on the wine steam runner pipe, the valve is located at outside the steaming wine tank.
Further, mounting hole is offered on the steaming wine tank, the mounting hole is connected to the thermal energy exchange area, described
Vinasse runner pipe includes inlet tube, connecting tube and overflow pipe, and the inlet tube is connected to the connection with the overflow pipe
The opposite end of pipe, and extend along towards the direction of liquid level in the steaming wine space；The connecting tube wears the mounting hole
And it is tightly connected with the steaming wine tank；The inlet tube is located in the distillation zone；The overflow pipe is located at the steaming wine space
Outside, the valve on the vinasse runner pipe is mounted on the overflow pipe.
Further, the overflow pipe includes first pipe, second pipe and third pipeline, the first pipe with it is described
Third pipeline is connect with the opposite end of the second pipe respectively, and is extended towards the same side of the second pipe,
The free terminal of the first pipe is connect with the connecting tube, and the opening of the free terminal of the third pipeline is downward；Institute
The top surface for stating second pipe and the free terminal of the inlet tube are located in same level；Valve on the vinasse runner pipe
On the second pipe.
Further, mounting hole is offered on the steaming wine tank, the mounting hole is connected to the thermal energy exchange area, described
Wine steam runner pipe includes air inlet pipe, communicating pipe and wine outlet duct, and the air inlet pipe is connected to the company with the wine outlet duct
The opposite end of siphunculus, the air inlet pipe extend along towards the direction of liquid level in the steaming wine space；The wine outlet duct is along separate
The direction for steaming liquid level in wine space extends；It wears the mounting hole communicating pipe and is tightly connected with the steaming wine tank；
The air inlet pipe is located in the distillation zone；The wine outlet duct is located at outside the steaming wine space, on the wine steam runner pipe
Valve was mounted on the communicating pipe.
Further, it is also equipped with fermented grain observation window on the steaming wine tank.
Further, the continuous liquor steaming device further includes heater, and the heater is located at outside the steaming wine tank, and position
Bottom in the distillation zone.
Further, the vinasse runner pipe is located at the top of the wine steam runner pipe.
Further, it is also equipped with fermented grain charge pipe at the fermented grain charge door, wine is installed on the fermented grain charge pipe
Unstrained spirits control valve.
Further, the material guiding hopper of back taper is also equipped at the top of the fermented grain charge pipe.
The present invention also provides a kind of continuous liquor steaming methods using above-mentioned continuous liquor steaming device, include the following steps：
Fermented grain is added from fermented grain charge door toward thermal energy exchange area, fermented grain flows to distillation zone from thermal energy exchange area；
Wine steam is located at one end in distillation zone from wine steam runner pipe and enters in wine steam runner pipe, and towards wine steam
Runner pipe is located at the end movement steamed outside wine tank, and in the process, wine steam flows through thermal energy exchange area, and and thermal energy from distillation zone
Heat exchange occurs for the fermented grain in exchange area, to preheat fermented grain, while wine steam being made to be able to condensation and obtain white wine liquid, opens wine
Valve on steam runner pipe may make white wine liquid is discharged via wine steam runner pipe to steam outside wine tank；
Vinasse are located at one end in distillation zone from vinasse runner pipe and enter in vinasse runner pipe, and towards vinasse runner pipe position
Moved in steaming the end outside wine tank, in the process, vinasse flow through thermal energy exchange area from distillation zone, and in thermal energy exchange area
Heat exchange occurs for fermented grain, to preheat fermented grain, while vinasse is cooled off, and opens the valve on vinasse runner pipe and may make
Vinasse discharge after cooling is steamed outside wine tank.
Due to the adoption of the above technical scheme, the invention has the advantages that：
1, continuous liquor steaming device of the invention and its continuous liquor steaming method, unheated fermented grain is added from thermal energy exchange area steams
Wine tank during unheated fermented grain is flowed to distillation zone, can be flowed over the high temperature vinasse come and wine steam from distillation zone
Preheating, to make full use of the thermal energy of vinasse and wine steam, since when reaching distillation zone, its temperature is improved fermented grain,
Thermal energy is reduced needed for fermented grain distillation, reaches energy-efficient purpose；And continuous liquor steaming device is only needed to be arranged in distillation zone bottom and be heated
Device it is not necessary that heater is arranged in the entire bottom part down for steaming wine tank, and enables the heater using electric energy to distillation
The fermented grain in area is heated.When wine steam flows through thermal energy exchange area, heat exchange can occur with unheated fermented grain, reach preheating
Fermented grain and the dual purpose for condensing wine steam so that the continuous liquor steaming device can be obtained white wine liquid without additionally mounted condenser
Body, it is convenient and practical, equipment cost can be reduced.
2, continuous liquor steaming device of the invention and its continuous liquor steaming method do not heat the direction of motion of fermented grain and high heat wine
The direction of motion of grain and the direction of motion of high temperature wine steam are substantially opposite, the efficiency of heat exchange can be improved, to improve the profit of energy
With rate.
Description of the drawings
Fig. 1 is the structural schematic diagram of continuous liquor steaming device in a better embodiment of the invention.
Main element symbol description
100- continuous liquor steamings device, 2- steam wine tank, 23- steams wine space, 232- thermal energy exchanges area, the distillation zones 234-, 24- wine
Unstrained spirits charge door, 25- mounting holes, 26- mounting holes, 4- vinasse runner pipe, 42- inlet tubes, 421- vinasse entrance, 44- connecting tubes,
46- overflow pipes, 462- first pipes, 464- second pipes, 466- thirds pipeline, the outlet of 467- vinasse, 6- wine steams runner pipe,
62- air inlet pipe, 621- wine steams entrance, 64- communicating pipes, 66- wine outlet ducts, the outlet of 661- white wine, the observation of 7- valves, 8- fermented grains
Window, 9- heaters, 10- fermented grains charge pipe, 11- fermented grains control valve, 12- material guiding hoppers, 200- liquid levels.
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation describes, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
It should be noted that when component is referred to as " being fixed on " another component, it can be directly on another component
Or there may also be components placed in the middle.When a component is considered as " connection " another component, it can be directly connected to
To another component or it may be simultaneously present component placed in the middle.When a component is considered as " being set to " another component, it
Can be set up directly on another component or may be simultaneously present component placed in the middle.Term as used herein is " vertical
", " horizontal ", "left", "right" and similar statement for illustrative purposes only.
Unless otherwise defined, all of technologies and scientific terms used here by the article and belong to the technical field of the present invention
The normally understood meaning of technical staff is identical.Used term is intended merely to description tool in the description of the invention herein
The purpose of the embodiment of body, it is not intended that in the limitation present invention.Term " and or " used herein includes one or more phases
Any and all combinations of the Listed Items of pass.
Refer to Fig. 1, a better embodiment of the invention provides a kind of continuous liquor steaming device 100, including steams wine tank 2 and
It is installed in the vinasse runner pipe 4 and wine steam runner pipe 6 steamed on wine tank 2.
Wine tank 2 is steamed for distilling fermented grain to obtain wine steam, and internal formed steams wine space 23, and it includes phase to steam wine space 23
Intercommunicated thermal energy exchange area 232 and distillation zone 234.It steams wine tank 2 and is equipped with fermented grain charge door 24, fermented grain charge door 24 is located at heat
It is connected at energy exchange area 232 and with thermal energy exchange area 232.It can be added into steaming wine tank 2 by fermented grain charge door 24 fresh
Fermented grain.
Vinasse runner pipe 4, which is installed in steam on wine tank 2 and be spaced with wine steam runner pipe 6, to be arranged.Vinasse runner pipe 4 is used for
Vinasse are discharged and steam wine tank 2.Vinasse runner pipe 4 extends to distillation zone 234 via thermal energy exchange area 232, and the one of vinasse runner pipe 4
It holds and is located in distillation zone 234, the other end of vinasse runner pipe 4, which is located at, to be steamed outside wine tank 2, and vinasse runner pipe 4 is located at steaming wine space
End in 23 is located at the lower section for steaming liquid level 200 in wine space 23, specially：It steams and offers mounting hole 25, mounting hole on wine tank 2
25 are connected to thermal energy exchange area 232.Vinasse runner pipe 4 includes inlet tube 42, connecting tube 44 and overflow pipe 46.Inlet tube 42 with overflow
Flow tube 46 is connected to the opposite end of connecting tube 44, and extends along towards the direction for steaming liquid level 200 in wine space 23；Even
Take over 44 wears mounting hole 25 and is tightly connected with wine tank 2 is steamed, and in the present embodiment, connecting tube 44 is welded on wine tank 2 is steamed
Together.It is understood that in other embodiments, connecting tube 44 can also be close by the realization such as sealing ring with steaming wine tank 2
Envelope connection.Inlet tube 42 is located in distillation zone 234, and the free terminal of inlet tube 42 is vinasse entrance 421, vinasse entrance 421
In the lower section for steaming liquid level 200 in wine space 23, so that vinasse enter.According to hot water and the cold water principle of stratification, hot water usually exists
Above cold water, it is therefore preferred that vinasse entrance 421 is circulated close to the liquid level 200 steamed in wine space 23 with ensuring to enter vinasse
The vinasse of pipe 4 are high temperature vinasse.Valve 7 is installed, which, which is located at, steams outside wine tank 2 on vinasse runner pipe 4.In this embodiment party
In formula, the valve 7 on vinasse runner pipe 4 is mounted on overflow pipe 46, in order to operate valve 7, and then is controlled by the valve 7
The break-make of vinasse runner pipe 4.
Overflow pipe 46, which is located at, to be steamed outside wine space 23, and in the present embodiment, overflow pipe 46 includes first pipe 462, second
Pipeline 464 and third pipeline 466, first pipe 462 are connect with the opposite end of second pipe 464 respectively with third pipeline 466,
And extend towards the same side of second pipe 464.The free terminal of first pipe 462 is connect with connecting tube 44, third pipe
The opening of the free terminal in road 466 downward, forms vinasse outlet 467；The freedom of the top surface and inlet tube 42 of second pipe 464
End is located in same level, is overflowed with a slower speed so that vinasse can export 467 from vinasse.If second pipe
464 top surface is higher than the free terminal of inlet tube 42, then causes vinasse that cannot smoothly be overflowed from vinasse outlet 467；If the second pipe
The top surface in road 464 is less than the free terminal of inlet tube 42, then vinasse may be caused to export 467 spilling excessive velocities from vinasse,
Reduce the effect of heat exchange.Valve 7 on vinasse runner pipe 4 is mounted on second pipe 464.
Wine steam runner pipe 6, which is used to wine steam being discharged, steams wine tank 2, and wine steam runner pipe 6 prolongs via thermal energy exchange area 232
Distillation zone 234 is extended to, one end of wine steam runner pipe 6 is located in distillation zone 234, and the other end of wine steam runner pipe 6, which is located at, to be steamed
Outside wine tank 2, and wine steam runner pipe 6 is located at the top for steaming the liquid level 200 in steaming wine space 23 of the end in wine space 23, tool
Body is：It steams and offers mounting hole 26 on wine tank 2, mounting hole 26 is located at thermal energy exchange area 232 and connects with thermal energy exchange area 232
It is logical.Wine steam runner pipe 6 includes air inlet pipe 62, communicating pipe 64 and wine outlet duct 66, and air inlet pipe 62 is connected to wine outlet duct 66
The opposite end of communicating pipe 64, air inlet pipe 62 extend along towards the direction for steaming liquid level 200 in wine space 23；Wine outlet duct 66 is along separate
The direction for steaming liquid level 200 in wine space 23 extends.It wears mounting hole 25 communicating pipe 64 and is tightly connected with wine tank 2 is steamed, in this reality
It applies in mode, communicating pipe 64 welds together with wine tank 2 is steamed.It is understood that in other embodiments, communicating pipe 64
It can be tightly connected by realizations such as sealing rings with wine tank 2 is steamed.Air inlet pipe 62 is located in distillation zone 234, the freedom of air inlet pipe 62
End forms wine steam entrance 621；Wine outlet duct 66, which is located at, to be steamed outside wine space 23, and the free terminal of wine outlet duct 66 forms white wine outlet
661.The valve 7 of control fluid on-off is installed, valve 7, which is located at, to be steamed outside wine tank 2 on wine steam runner pipe 6.In present embodiment
In, the valve 7 on wine steam runner pipe 6 was mounted on communicating pipe 64, in order to operate valve 7, and then was controlled by the valve 7
The break-make of wine steam runner pipe 6.
In the present embodiment, it steams on wine tank 2 and is also equipped with fermented grain observation window 8.Operator can pass through the fermented grain observation window 8
The position of liquid level 200 and the situation in steaming wine tank 2 in observation steaming wine tank 2.
In the present embodiment, continuous liquor steaming device 100 further includes heater 9, and heater 9, which is installed in, to be steamed outside wine tank 2, and
Bottom positioned at distillation zone 234.Heater 9, to form wine steam, is generated for carrying out heating distillation to fermented grain after fermented grain distillation
Vinasse.Coal, electric heat source etc. can be used in the heat source of heater 9.It is understood that heater 9 can be omitted, at this point, can adopt
It is heated with external heat source to steaming wine tank 2.
In the present embodiment, wine steam runner pipe 6 is located at the lower section of vinasse runner pipe 4.It is layered according to hot water and cold water
Principle, cold water are typically deposited on the bottom of container.Wine steam runner pipe 6 is disposed in proximity to steam the bottom of wine tank 2, it can be ensured that
Wine steam in wine steam runner pipe 6 reaches better condensation effect.
In the present embodiment, it is also equipped with fermented grain charge pipe 10 at fermented grain charge door 24, is installed on fermented grain charge pipe 10
Have fermented grain control valve 11, by fermented grain control valve 11 can control fermented grain charge pipe 10 break-make and fermented grain in fermented grain charge pipe
Flow velocity in 10.The top of fermented grain charge pipe 10 is also equipped with the material guiding hopper 12 of back taper, to be oriented to the flowing of fermented grain.
Present embodiment also provides a kind of continuous liquor steaming method using above-mentioned continuous liquor steaming device 100, including following step
Suddenly：
Fermented grain is added into thermal energy exchange area 232 from fermented grain charge door 24, fermented grain flows to distillation zone from thermal energy exchange area 232
234.In the present embodiment, it is continuously added to fermented grain into thermal energy exchange area 232 from fermented grain charge door 24 with a preset speed,
It is always positioned between vinasse entrance 421 and wine steam entrance 621 with ensuring to steam the liquid level 200 in wine tank 2.
Wine steam enters from the wine steam entrance 621 of wine steam runner pipe 62 in wine steam runner pipe 62, and towards white wine
661 movement of outlet, in the process, wine steam flows through thermal energy exchange area 232 from distillation zone 234, and in thermal energy exchange area 232
Fermented grain heat exchange occurs, to preheat fermented grain, while wine steam being made to be able to condensation and obtain white wine liquid, opens wine steam circulation
Valve 7 on pipe 6 may make white wine liquid is discharged via wine steam runner pipe 62 to steam outside wine tank 2.
Vinasse enter from the vinasse entrance 421 of vinasse runner pipe 4 in vinasse runner pipe 4, and are transported towards vinasse outlet 467
Dynamic, in the process, vinasse flow through thermal energy exchange area 232 from distillation zone 234, and occur with the fermented grain in thermal energy exchange area 232
Heat exchange to preheat fermented grain, while making vinasse cool off, and it is after may make cooling to open the valve 7 on vinasse runner pipe 4
Vinasse overflow and steam outside wine tank 2.
The continuous liquor steaming device 100 of embodiment of the present invention, unheated fermented grain is added from thermal energy exchange area 232 steams wine tank
2, during unheated fermented grain is flowed to distillation zone 234, the high temperature vinasse come can be flowed over from distillation zone 234 and be steamed with wine
Vapour preheats, to make full use of the thermal energy of vinasse and wine steam, since when reaching distillation zone 234, its temperature is improved fermented grain,
Therefore, thermal energy needed for fermented grain distillation is reduced, and reaches energy-efficient purpose.Meanwhile 100, continuous liquor steaming device is needed in distillation zone
Heater 9 is arranged in 234 bottoms, it is not necessary that heater 9 is arranged in the entire bottom part down for steaming wine tank 2, and makes the heater 9
The fermented grain of distillation zone 234 can be heated using electric energy.When wine steam flows through thermal energy exchange area 232, can with do not heat
Fermented grain occur heat exchange, reach preheating fermented grain and condense wine steam dual purpose so that the continuous liquor steaming device 100 is not necessarily to
Additionally mounted condenser can be obtained white wine liquid, convenient and practical, and can reduce equipment cost.In addition, not heating fermented grain
The direction of motion and the direction of motion of high temperature vinasse and the direction of motion of high temperature wine steam are substantially opposite, can improve the effect of heat exchange
Rate, to improve the utilization rate of energy.
In addition, also the length of vinasse runner pipe 4 and wine steam runner pipe 6 can be designed according to needs of production so that from
Vinasse outlet 467 discharge vinasse temperature be reduced to it is roughly the same with the temperature of unheated fermented grain, to make full use of vinasse
Thermal energy.
In the present embodiment, the connecting tube 44 of vinasse runner pipe 4 and the communicating pipe 64 of wine steam runner pipe 6 are straight
Pipe.It is appreciated that in other embodiments, the connecting tube 44 of vinasse runner pipe 4 and the communicating pipe 64 of wine steam runner pipe 6 can
Design in the shape of a spiral, to increase its contact area with fermented grain, and then can shorten the length for steaming wine tank 2, while ensuring hot friendship
Change efficiency.
It is appreciated that in other embodiments, steaming and being also covered with insulating layer (not shown) on the outer wall of wine tank 2, keep the temperature
Layer can reduce the loss for steaming heat in wine tank 2.
Above description is the detailed description for the present invention preferably possible embodiments, but embodiment is not limited to this hair
Bright patent claim, it is all the present invention suggested by technical spirit under completed same changes or modifications change, should all belong to
In the covered the scope of the claims of the present invention.
Claims (10)
1. a kind of continuous liquor steaming device, including wine tank is steamed, it is formed in the steaming wine tank and steams wine space, it is characterised in that：The steaming
Wine space includes interconnected thermal energy exchange area and distillation zone, and the steaming wine tank is equipped with fermented grain charge door, and the fermented grain adds
Material mouth is connected to the thermal energy exchange area；The continuous liquor steaming device further includes vinasse runner pipe and wine steam runner pipe, described
Vinasse runner pipe is installed on the steaming wine tank and is spaced setting, the vinasse runner pipe warp with the wine steam runner pipe
The distillation zone is extended to by the thermal energy exchange area, one end of the vinasse runner pipe is located in the distillation zone and is located at institute
The lower section for steaming liquid level in wine space is stated, the other end of the vinasse runner pipe is located at outside the steaming wine tank；The wine steam circulation
Pipe extends to the distillation zone via the thermal energy exchange area, one end of the wine steam runner pipe be located in the distillation zone and
The top of liquid level, the other end of the wine steam runner pipe are located at outside the steaming wine tank in the steaming wine space；The wine
Valve is mounted on poor runner pipe and the wine steam runner pipe, the valve is located at outside the steaming wine tank.
2. continuous liquor steaming device as described in claim 1, it is characterised in that：Mounting hole is offered on the steaming wine tank, it is described
Mounting hole is connected to the thermal energy exchange area, and the vinasse runner pipe includes inlet tube, connecting tube and overflow pipe, the inlet tube
The opposite end of the connecting tube is connected to the overflow pipe, and along the direction towards liquid level in the steaming wine space
Extend；The connecting tube wears the mounting hole and is tightly connected with the steaming wine tank；The inlet tube is located at the distillation zone
It is interior；The overflow pipe is located at outside the steaming wine space, and the valve on the vinasse runner pipe is mounted on the overflow pipe.
3. continuous liquor steaming device as claimed in claim 2, it is characterised in that：The overflow pipe includes first pipe, the second pipe
Road and third pipeline, the first pipe are connect with the opposite end of the second pipe respectively with the third pipeline, and
Extending towards the same side of the second pipe, the free terminal of the first pipe connect with the connecting tube, and described the
The opening of the free terminal of three pipelines is downward；The free terminal of the top surface of the second pipe and the inlet tube is located at same
On horizontal plane；Valve on the vinasse runner pipe is mounted on the second pipe.
4. continuous liquor steaming device as described in claim 1, it is characterised in that：Mounting hole is offered on the steaming wine tank, it is described
Mounting hole is connected to the thermal energy exchange area, and the wine steam runner pipe includes air inlet pipe, communicating pipe and wine outlet duct, the air inlet
Pipe and the wine outlet duct are connected to the opposite end of the communicating pipe, and the air inlet pipe is along towards liquid in the steaming wine space
The direction in face extends；Wine outlet duct direction of liquid level in far from the steaming wine space extends；It wears the communicating pipe described
Mounting hole is simultaneously tightly connected with the steaming wine tank；The air inlet pipe is located in the distillation zone；The wine outlet duct is located at the steaming
Outside wine space, the valve on the wine steam runner pipe was mounted on the communicating pipe.
5. continuous liquor steaming device as described in claim 1, it is characterised in that：Fermented grain observation is also equipped on the steaming wine tank
Window.
6. continuous liquor steaming device as described in claim 1, it is characterised in that：The continuous liquor steaming device further includes heater,
The heater is located at outside the steaming wine tank, and positioned at the bottom of the distillation zone.
7. continuous liquor steaming device as described in claim 1, it is characterised in that：The vinasse runner pipe is located at the wine steam stream
The top of siphunculus.
8. continuous liquor steaming device as described in claim 1, it is characterised in that：Fermented grain is also equipped at the fermented grain charge door to add
Expects pipe is equipped with fermented grain control valve on the fermented grain charge pipe.
9. continuous liquor steaming device as claimed in claim 8, it is characterised in that：It is also equipped with down at the top of the fermented grain charge pipe
The material guiding hopper of taper.
10. a kind of continuous liquor steaming method using continuous liquor steaming device as described in claim 1, which is characterized in that including following
Step：
Fermented grain is added from fermented grain charge door toward thermal energy exchange area, fermented grain flows to distillation zone from thermal energy exchange area；
Wine steam is located at one end in distillation zone from wine steam runner pipe and enters in wine steam runner pipe, and circulates towards wine steam
Pipe is located at the end movement steamed outside wine tank, and in the process, wine steam flows through thermal energy exchange area, and and thermal energy exchange from distillation zone
Heat exchange occurs for the fermented grain in area, to preheat fermented grain, while wine steam being made to be able to condensation and obtain white wine liquid, opens wine steam
Valve on runner pipe may make white wine liquid is discharged via wine steam runner pipe to steam outside wine tank；
Vinasse are located at one end in distillation zone from vinasse runner pipe and enter in vinasse runner pipe, and are located at towards vinasse runner pipe and steam
End movement outside wine tank, in the process, vinasse flow through thermal energy exchange area from distillation zone, and with the fermented grain in thermal energy exchange area
Heat exchange occurs, to preheat fermented grain, while vinasse are cooled off, opens the valve on vinasse runner pipe and may make cooling
Vinasse discharge afterwards is steamed outside wine tank.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810551527.1A CN108485893A (en) | 2018-05-31 | 2018-05-31 | Continuous liquor steaming device and its continuous liquor steaming method |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810551527.1A CN108485893A (en) | 2018-05-31 | 2018-05-31 | Continuous liquor steaming device and its continuous liquor steaming method |
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| CN108485893A true CN108485893A (en) | 2018-09-04 |
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| CN201810551527.1A Pending CN108485893A (en) | 2018-05-31 | 2018-05-31 | Continuous liquor steaming device and its continuous liquor steaming method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113444607A (en) * | 2021-07-16 | 2021-09-28 | 贵州特征微生物研究院有限公司 | Steam mixing type distillation equipment |
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