CN208803048U - A kind of foreign wine production line - Google Patents
A kind of foreign wine production line Download PDFInfo
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- CN208803048U CN208803048U CN201821326357.9U CN201821326357U CN208803048U CN 208803048 U CN208803048 U CN 208803048U CN 201821326357 U CN201821326357 U CN 201821326357U CN 208803048 U CN208803048 U CN 208803048U
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- 235000014101 wine Nutrition 0.000 title claims abstract description 212
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 26
- 238000001816 cooling Methods 0.000 claims abstract description 131
- 239000007788 liquid Substances 0.000 claims abstract description 91
- 238000000855 fermentation Methods 0.000 claims abstract description 56
- 230000004151 fermentation Effects 0.000 claims abstract description 56
- 238000004821 distillation Methods 0.000 claims abstract description 30
- 238000000034 method Methods 0.000 claims abstract description 12
- 238000007710 freezing Methods 0.000 claims abstract description 10
- 230000008014 freezing Effects 0.000 claims abstract description 10
- 238000001556 precipitation Methods 0.000 claims abstract description 10
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 34
- 238000001704 evaporation Methods 0.000 claims description 22
- 230000008020 evaporation Effects 0.000 claims description 22
- 238000010438 heat treatment Methods 0.000 claims description 14
- 239000010865 sewage Substances 0.000 claims description 12
- 238000001914 filtration Methods 0.000 claims description 10
- 239000000498 cooling water Substances 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 239000003381 stabilizer Substances 0.000 claims description 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 abstract description 36
- 239000001760 fusel oil Substances 0.000 abstract description 12
- 239000000126 substance Substances 0.000 abstract description 12
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 230000001376 precipitating effect Effects 0.000 abstract description 5
- 239000002994 raw material Substances 0.000 abstract description 4
- 239000003507 refrigerant Substances 0.000 description 18
- 230000000694 effects Effects 0.000 description 10
- 239000002893 slag Substances 0.000 description 9
- 230000006835 compression Effects 0.000 description 6
- 238000007906 compression Methods 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 238000001514 detection method Methods 0.000 description 4
- 230000036760 body temperature Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000002787 reinforcement Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000007701 flash-distillation Methods 0.000 description 1
- 235000019990 fruit wine Nutrition 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000010563 solid-state fermentation Methods 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model discloses foreign wine production lines, successively include pulverizer, fermentation device for wine and Distallation systm according to production procedure.Fermentation device for wine includes fermentor and freezing precipitation tank, Distallation systm includes two or more distillers, distillation container in distiller is made of container and progress, raw material enters fermentation in fermentor after pulverizer crushes and enters finally into distillation in distiller subsequently into precipitating is precipitated in freezing precipitation tank.Using the structure of the utility model, the purity of foreign wine can be improved, and energy consumption can be reduced；It is high to the utilization rate of energy, it is more abundant to the cooling of wine steam, it avoids containing steam from the wine liquid exported in Distallation systm, while more can thoroughly remove the harmful substances such as methanol, fusel oil in wine liquid.
Description
Technical field
The utility model relates to foreign wine production lines, especially Distallation systm.
Background technique
The technical process for making foreign wine is general are as follows: selection-processing and fermentation-filtering distillation-storage.The main purpose of distillation is
Remove the harmful substances such as methanol, the fusel oil in wine liquid.
Fermentation is realized by fermentor, and wine fermentation process is a sterile, free of contamination process, and fermentor uses
Sterile system avoids and prevents the pollution of microbes in air, substantially prolong product shelf-life and product it is pure.?
During wine fermentation, the control of fermentation temperature is even more important.It is not easy to ferment if fermentation temperature is not achieved, to need to send out
The ferment time is long, seriously affects production efficiency and product fermented quality, if fermentation temperature is excessively high, whole tank fermentation liquid is easy to cause to become
Matter, and for foreign wine, the process of manufacturing generally comprises following steps: crushing, fermentation, distillation, storage, due to foreign wine pair
Relatively high in purity requirement, wine liquid can have impurity after fermentation, if directly distilled, can reduce the purity of foreign wine.Patent
Document CN201520956455.0, publication date are on April 27th, 2016, and it discloses a kind of fruit wine temperature control fermentors, including hair
Fermentation tank ontology, the fermentor ontology are provided with feed inlet, temperature control device, air stirrer, sewage pipe, wine outlet duct, slag tap
Mouth and filter plate, the temperature control device are mounted on the top of the fermentor ontology, and the cooling water system is mounted on the fermentation
Tank body interior, which is only filtered the wine liquid after fermentation simply by filter plate, for existing in wine liquid
Small particle molecule can not be filtered, so that the purity of foreign wine can not be improved, fermentation tank does not have heat insulation function, works as place
When weather more hot area, since external temperature is higher, so that needing lower cooling temperature in fermentor
It can be carried out cooling, improve energy consumption.
Distiller is the utensil using way of distillation separate substance.In ancient Chinese, distiller it be generally used for alchemy, system
Liquor, steaming floral water etc..The different purposes of distiller has different shape and origin.
A kind of full-automatic buffer pool tower is disclosed in the patent document that Chinese Patent Application No. is 201711391905.6
Formula continuous distiller, comprising: distillation bucket, heater, multistage continuous buffer pool, First Heat Exchanger, the second heat exchanger and condensation
Device.Multistage continuous buffer pool is installed in distillation bucket, and multistage continuous buffer pool includes multilayer buffer pool group, and each layer includes multiple
Buffer pool unit；Multilayer buffer pool group is sequentially connected from top to bottom so that all buffering pool units are connected；First Heat Exchanger tool
There are a first runner and second flow channel, wine liquid cold burden to be distilled can be from the entrance of second flow channel into simultaneously
Entered distillation bucket after the steam heating of first runner；Second heat exchanger will be for that will pass through First Heat Exchanger heating
Wine liquid cold burden further heats；Condenser is used to further be cooled to liquid by the cooling steam of First Heat Exchanger.This hair
The operation of bright achievable continuous feed distillation discharge waste material, realizes flash distillation, greatly reduces the use of cooling water, thermal effect
Rate utilizes maximization.
Although above structure produces beneficial effect, cannot be by methanol, fusel oil etc. but pass through a continuous distiller
Harmful substance more thoroughly remove.In addition, wine liquid cold burden enters in First Heat Exchanger through cold burden inlet pipe, wine liquid cold burden
During entering in First Heat Exchanger, the flowing of wine liquid cold burden be can not be limited, and therefore, heat-exchange power is relatively
It is few, it is unfavorable for making full use of the heat in wine steam, is also unfavorable for cooling down wine steam, the utilization rate of energy is relatively
It is low.In addition, need for wine steam to be cooled to liquid after wine steam is formed, and foregoing invention cannot carry out more wine steam
It is thoroughly cooling.
Summary of the invention
The purpose of the utility model is to provide a kind of foreign wine production lines can improve foreign wine using the structure of the utility model
Purity, and energy consumption can be reduced；It is high to the utilization rate of energy, it is more abundant to the cooling of wine steam, it avoids from Distallation systm
Contain steam in the wine liquid of middle output, while more can thoroughly remove the harmful substances such as methanol, fusel oil in wine liquid.
In order to achieve the above objectives, a kind of foreign wine production line successively includes pulverizer, fermentation device for wine according to production procedure
And Distallation systm；
Fermentation device for wine includes fermentor, and the top of the fermentor is equipped with second charging aperture, and the bottom of fermentor is set
There is the second wine outlet, further include freezing precipitation tank, the freezing precipitation tank includes the first tank body with stabilizer blade, first tank
Body is provided with first charging aperture, the first wine outlet, the first sewage draining exit, the first temperature control equipment, the first cooling device, first into
Material mouth setting in the first top of the tank, the first wine outlet and the first sewage outfalls setting in the first tank base, the second of fermentor
Wine outlet is connected by pipeline with the first charging aperture of freezing precipitation tank, and heat preservation is equipped between the inner wall and outer wall of the first tank body
Layer；
Distallation systm includes two or more distillers, and the distiller includes cooling heat exchange device and vaporising device,
The cooling heat exchange device includes pedestal, distillation container and heat-exchange tube；The vaporising device includes container for evaporation, is located at
Heating tube in container for evaporation and the wine steam pipe for being connected to container for evaporation upper end；It is characterized by: there is cavity in pedestal,
Be equipped with the cooling water inlet pipe that be connected to cavity close to the bottom of pedestal on pedestal, on pedestal close to the top of pedestal equipped with
The outlet pipe that cavity communicates；The distillation container includes the neck between two or more containers and connection adjacent container, is held
The cross section of device from it is lower be gradually increased to middle part after be gradually reduced upwards, neck is connected to adjacent container, the connection of nethermost container
On pedestal, wine inlet is equipped on uppermost container；One end of heat-exchange tube is connect with the output end of wine steam pipe, and heat is handed over
Then the other end for changing pipe enters after distilling container stretches out pedestal in cavity；Between container for evaporation and nethermost container
Equipped with wine liquid pipe；It is connected with communicating pipe between adjacent distiller, discharge pipe is equipped on communicating pipe.
The working principle of above-mentioned foreign wine production line is: raw material enters hair by second charging aperture after broken crusher machine
In fermentation tank, fermented wine liquid entered in freezing precipitation tank after cooling precipitating from the second wine outlet and first charging aperture formed it is cold
Cooking wine liquid, cold burden wine liquid are entered in distiller container by feed pipe through wine inlet, and the wine liquid in distiller container is from wine liquid
Pipe enters in container for evaporation, and heating tube, which carries out heating to the wine liquid in container for evaporation, allows wine liquid to form wine steam, wine steam warp
Wine steam pipe enters heat-exchange tube, flow through distillation container in heat-exchange tube in wine steam and distillation container in it is hydraulic into
Row heat exchange, the wine steam heat release flowed through in the heat-exchange tube in distillation container are pre-cooled, and then wine liquid enters in cavity
Heat-exchange tube in, in the cavity, wine steam is cooled to form wine liquid, and the leading portion of wine liquid is then shut off by discharge pipe discharge
The valve of discharge pipe allows wine liquid to repeat the above process from entering communicating pipe in next distiller.
In above-mentioned working principle, installation for fermenting is formed by increasing cooling settling tank after fermentor, so that by hair
Wine liquid after ferment enters cooling settling tank and is cooled down, since molecular motion slows down at low temperature, so that through everfermentation
The large-sized molecule precipitating contained in the filtered wine liquid of tank, and then the purity of foreign wine is improved, it is precipitated additionally, due to cooling
Insulating layer is equipped between the inner wall and outer wall of tank, so that cooling settling tank is influenced small, and then drop by ambient temperature
Low energy consumption.For wine liquid in distillation process, the harmful substances such as methanol, fusel oil are located at the front section of the very little of wine steam, therefore,
The cooled wine liquid of wine steam for leading portion is discharged from discharge pipe first, reaches and removes the harmful substances such as methanol, fusel oil
Purpose, and it is provided with multiple distillers interconnected in the present invention, therefore, to nuisances such as methanol, fusel oil
Matter is removed step by step, be can remove 95% or more the harmful substances such as methanol, fusel oil, is improved the quality of foreign wine.Cold burden wine liquid
During being entered in distillation container by wine inlet, due to being provided with container and neck, container is that middle part is small in ends greatly
Drum containers, connect adjacent accommodating neck passage cross section be less than container in middle part cross section, in this way, wine liquid is being distilled
When flowing in container, due to above structure, the flowing velocity of wine liquid can slow down, in this way, wine liquid and wine steam in distillation container
Heat exchange it is more abundant, more preferable to the pre-heat effect of wine liquid, the precooling effect of wine steam is also more preferable, improves energy
Utilization rate.Due to being provided with pedestal, the lower end of pedestal is arranged in cooling water inlet pipe, and the upper end of pedestal is arranged in outlet pipe, in this way,
On the contrary, cooling effect is more preferable, reduction remains in cooling wine liquid for the flow direction of cooling water and the flow direction of wine steam
Wine steam.
Further, first cooling device be arranged in the first tank interior and along the top of the first tank body to
Two or more the first spiral cooling pipe body of bottom setting, first temperature control equipment are fixed on the first tank body
On, and first temperature control equipment includes the first temperature of two or more that the first spiral cooling pipe body periphery is arranged in
Degree sensor and the two or more second temperature sensors being arranged between adjacent first spiral cooling pipe body, pass through
By the first cooling device be divided into multistage the first spiral cooling pipe body setting, and around the first spiral cooling pipe body and
Temperature sensor is designed between adjacent first cooling tube body to feed back around the first spiral cooling pipe body and adjacent first spiral shell
Different temperatures between rotating cooling tube body, so that temperature detection is carried out from multiple positions of cooling settling tank, then to cold
But the wine liquid in the multiple regions of settling tank carries out temperature adjustment, so as to accurately control temperature inside cooling settling tank
Degree improves product and makes quality.
Further, the first spiral cooling pipe body is fixed in first support, and first support is fixed on first
It is equipped with first between tank base and first support and the first inner tank wall and reinforces support rod, it is solid by being equipped in the first tank body
The first support of fixed first spiral cooling pipe body, so that the first spiral cooling pipe body is stably fixed at the first tank body
Interior, preventing from being fixed on merely in the first inner tank wall due to the first spiral cooling pipe body causes the first spiral cooling pipe body solid
Fixed unstable problem.
Further, described two or more the first temperature sensors are uniformly distributed along the circumferencial direction of the first tank body,
It can strictly control in cooling settling tank positioned at the temperature of different location around the first spiral cooling pipe body, it is more accurate to be conducive to
Ground controls cooling temperature.
Further, the fermentor includes the fermentation tank with stabilizer blade, and the fermentation tank is provided with second row
Dirty mouth, second temperature control device, the second cooling device, the second sewage outfalls setting is in fermentor tank base, and described second
Cooling device is the two or more that fermentor tank interior is arranged in and is arranged along the top of fermentation tank to bottom
Two spiral cooling pipe bodies, the second temperature control device is fixed on fermentation tank, and the second temperature control
Device processed includes that the two or more third temperature sensor on the second spiral cooling pipe body periphery is arranged in and is arranged in phase
Two or more 4th temperature sensors between adjacent second spiral cooling pipe body are more by the way that the second cooling device to be divided into
Section the second spiral cooling pipe body setting, and all set around the second spiral cooling pipe body and between adjacent cooling tube body
There is temperature sensor to feed back the not equality of temperature around the second spiral cooling pipe body and between adjacent second spiral cooling pipe body
Degree, so that temperature detection is carried out from multiple positions of fermentation tank, then to the wine liquid in the multiple regions of fermentor tube body
Temperature adjustment is carried out, so as to accurately control fermentor tank interior fermentation temperature, product is improved and makes quality.
Further, the second spiral cooling pipe body is fixed on the secondary support bracket, and second support is fixed on fermentor
It is equipped with second between tank base and second support and fermentor inner tank wall and reinforces support rod, by being set in fermentation tank
There is the second support for fixing the second spiral cooling pipe body, so that the second spiral cooling pipe body is stably fixed at fermentor
In tank body, preventing from being fixed on merely in fermentor inner tank wall due to the second spiral cooling pipe body leads to the second spiral cooling
The fixed unstable problem of tube body.
Further, the second support includes two or more second struts, and the bottom of the second strut is fixed on
The bottom of fermentation tank, the outer wall of the second strut are connected with the outer wall of the second spiral cooling tube body, due to second support letter
It singly include more than two second struts, and the bottom of the second strut is fixed on the bottom of fermentation tank, so that second
The structure of bracket is simple, and light quality.
Further, the first support includes two or more first struts, and the bottom of the first strut is fixed on
The bottom of first tank body, the outer wall of the first strut is connected with the outer wall of the first spiral cooling tube body, since first support is simple
Ground includes more than two first struts, and the bottom of the first strut is fixed on the bottom of the first tank body, so that first support
Structure it is simple, and light quality.Lower part is equipped with the first filter plate for deslagging filtering, the first mistake in first tank body
Filter plate is equipped with the first via hole passed through for the first strut, first filtering of the lower part setting for deslagging filtering in cooling settling tank
Plate stays in residue on the first filter plate by filtering in this way.
Further, it is set on the pipeline between the second wine outlet of the fermentor and the first charging aperture of cooling settling tank
There is pump, consequently facilitating the wine liquid for the second wine outlet of tank that ferments is imported into the first charging aperture of cooling settling tank.
Further, the cross section of container is circle.Heat-exchange tube in distiller container is coil pipe；Positioned at cavity
Interior heat-exchange tube is coil pipe.Using coil arrangement, heat exchange area is bigger, and heat exchange effect is good.Wine steam pipe is from input terminal
It is gradually reduced to output end section.The output end of wine steam pipe passes through a container below the container of the top.Wine liquid is preheating
Certain air pressure can be generated afterwards, when having reserved a container in the top of wine steam pipe, in this way, uppermost container to wine liquid because
Preheating is overflowed upwards provides space, and wine liquid is avoided to overflow from wine inlet.Neck is hollow cylindrical.
Detailed description of the invention
Fig. 1 is the schematic diagram of the utility model production line.
Fig. 2 is the structural schematic diagram of the fermentor of the utility model.
Fig. 3 is the structural schematic diagram of cooling settling tank in the utility model.
Fig. 4 is the schematic diagram of distiller.
Fig. 5 is the schematic diagram of Distallation systm.
Specific embodiment
The present invention will be further described in detail with reference to the accompanying drawings and detailed description.
As shown in Figure 1, foreign wine production line successively includes pulverizer (not shown), fermentation device for wine according to production procedure
300 and Distallation systm 1000.
Pulverizer is therefore existing equipment repeats no more in the present invention.The effect of pulverizer is by raw material powder
It is broken.
As shown in Figure 1 to Figure 3, wine fermentation tank includes fermentor 2 and cooling settling tank 1, and fermentor 2 and cooling precipitate
Tank 1 is connected by pipeline 3, and pipeline 3 is equipped with pump 31, convenient for importing the wine liquid of fermentor 2 in cooling settling tank 1.
The fermentor 2 includes the fermentation tank 21 with stabilizer blade, and the fermentation tank 21 is provided with second charging aperture
22, the second wine outlet 23, the second sewage draining exit 24, second temperature control device, the second cooling device, the setting of second charging aperture 22 exist
21 top of tank, the second wine outlet 23 and the setting of the second sewage draining exit 24 ferment in fermentation 21 bottom of tank, the second cooling dress
It is set to the spiral second cooling tube bodies 25 of three be arranged in inside fermentation tank 21, second temperature control device is to be arranged the
Multiple third temperature sensors 26 of two spiral cooling pipe bodies, 25 periphery different location, adjacent second spiral cooling pipe body
The 4th temperature sensor 261 also is provided between 25.
Fermentation tank 21 is arranged in lower part in the top of three 25 spontaneous fermentation tank tank bodies 21 of the second spiral cooling pipe body
Inside, the second spiral tube body 25 are equipped with the second refrigerant inlet 2501 and the second refrigerant exit 2502, the second refrigerant inlet 2501
It is fixed on the same side wall of fermentation tank 21 and exposes fermentation tank 21 is outer and refrigerant with the second refrigerant exit 2502
Pipeline (does not illustrate and) connection in figure, the second refrigerant inlet 2501 of each second spiral cooling pipe body 25 is arranged second
Second refrigerant inlet 2501 of the top of refrigerant exit 2502, the second spiral cooling pipe body 25 adjacent in this way goes out with the second refrigerant
Mouthfuls 2502 close, consequently facilitating the connection of adjacent second spiral cooling pipe body 25, and then by adjacent second spiral cooling pipe
Body forms the bigger region for needing to adjust temperature, consequently facilitating preferably controlling fermentor pot temperature.
Three the second spiral cooling pipe bodies 25 are fixed in second support 27, and second support is two or more cylindrical
Second strut 2701, in the present embodiment, the quantity of the second strut is 2, and the bottom end of two second struts 2701 is fixed on fermentation
The outer wall of 21 bottom of tank, the outer wall of the second strut 2701 and the second spiral cooling pipe body 25 welds, and can make the in this way
It is connected between two struts and the second spiral cooling pipe body 25 reliable；And second strut 2701 and fermentation 21 inner wall of tank between
Equipped with two or more reinforcement support rods 2702, so that the second spiral cooling pipe body 25 more steadily solid-state fermentation tank
In tank body 21.
It is provided with second exhaust port 28 at the top of fermentation tank 21, second exhaust port 28 is equipped with second exhaust fan 29,
In this way when staff enters the internal work of fermentation tank 21, maintain the circulation of air.Under 21 side wall of tank that ferments
Portion is equipped with the second slag notch 210, and easy cleaning goes out residue.Second lid is installed on second exhaust port 28 and the second slag notch 210
Plate 211, the second cover board 211 are fixed in second exhaust port and the second slag notch with the second handwheel 212, use the second cover board 211
Cooperate with the second handwheel 212, is easy to open second exhaust port 28 and the second slag notch 210, and good airproof performance.
Lower part setting is used for the second filter plate 213 of deslagging filtering in fermentation tank 21, sets on the second filter plate 213
There is second via hole corresponding with the second strut 2701, the second strut 2701 is fixed on fermentation tank 21 by the second via hole
Residue is stayed in filter plate by filtering in this way due to being provided with the second filter plate 213 in the lower part of fermentation tank 21 by bottom
On 213.
The cooling settling tank 1 includes the first tank body 11, and first tank body 11 is provided with first charging aperture 12, first
Wine outlet 13, the first sewage draining exit 14, the first temperature control equipment, the first cooling device, first charging aperture 12 are arranged in the first tank
In 11 bottom of the first tank body, the first cooling device is that setting exists for 11 top of body, the first wine outlet 13 and the setting of the first sewage draining exit 14
Three the spiral first cooling tube bodies 15 inside first tank body 11, the first temperature control equipment is that setting first is spirally cooling
Multiple first temperature sensors 16 of 15 periphery different location of tube body also are provided between adjacent first spiral cooling pipe body 15
Two temperature sensors 161；Insulating layer 1102, insulating layer 1102 are equipped between the inner wall 1103 and outer wall 1101 of first tank body 11
For froth bed or vacuum layer.
Three the first spiral cooling pipe bodies 15 are arranged in the first tank body 11 from the top of the first tank body 11 to lower part
Portion, the first spiral tube body 15 are equipped with the first refrigerant inlet 1501 and the first refrigerant exit 1502,1501 He of the first refrigerant inlet
First refrigerant exit 1502, which is fixed on the same side wall of the first tank body 11 and exposes, (schemes outside the first tank body 11 with refrigerant pipe
In do not illustrate come) connection, each first spiral cooling pipe body 15 the first refrigerant inlet 1501 setting go out in the first refrigerant
The top of mouth 1502, the first refrigerant inlet 1501 and the first refrigerant exit 1502 of the first spiral cooling pipe body 15 adjacent in this way
It is close, consequently facilitating the connection of adjacent first spiral cooling pipe body 15, and then adjacent first spiral cooling pipe body is formed
The bigger region for needing to adjust temperature, consequently facilitating preferably controlling cooling settling tank temperature.
Three the first spiral cooling pipe bodies 15 are fixed in first support 17, and first support is two or more cylindrical
First strut 1701, in the present embodiment, the quantity of the first strut is 2, and the bottom end of two first struts 1701 is fixed on first
The outer wall of 11 bottom of tank body, the outer wall of the first strut 1701 and the first spiral cooling pipe body 15 welds, and can make first in this way
It is connected between strut and the first spiral cooling pipe body 15 reliable；And first is equipped between strut 1701 and 11 inner wall of the first tank body
Two or more first reinforcement support rods 1702, so that the first spiral cooling pipe body 15 more steadily fixes the first tank
In body 11.
First row port 18 is provided at the top of the first tank body 11, first row port 18 is equipped with first exhaust fan 19, this
Sample maintains the circulation of air when staff enters the internal work of the first tank body 11.It is equipped in 11 lower sidewall of the first tank body
First slag notch 110, easy cleaning goes out residue.First cover board 111 is installed on first row port 18 and the first slag notch 110,
First cover board 111 is fixed on first row port and the first slag notch with the first handwheel 112, uses the first cover board 111 and first
Handwheel 112 cooperates, and is easy to open first row port 18 and the first slag notch 110, and good airproof performance.
Lower part setting is used for the first filter plate 113 of deslagging filtering in first tank body 11, and the first filter plate 113 is equipped with
First via hole corresponding with the first strut 1701, the first strut 1701 are fixed on the bottom of the first tank body 11 by the first via hole
Residue is stayed in the first filter plate by filtering in this way due to being provided with the first filter plate 113 in the lower part of the first tank body 11 by portion
On 113.
As shown in Figure 4 and Figure 5, Distallation systm 1000 includes two or more distillers 100, adjacent distiller 100 it
Between be connected with communicating pipe 200.
As shown in figure 4, the distiller 1000 includes cooling heat exchange device 1a and vaporising device 2a.
The cooling heat exchange device 1a includes pedestal 11a, distillation container 12a and heat-exchange tube 13a.Tool in pedestal 11a
There is cavity 111a, be equipped with the cooling water inlet pipe 113a being connected to cavity 111a close to the bottom of pedestal 11a on pedestal 11a,
The outlet pipe 114a communicated with cavity 111a is equipped with close to the top of pedestal on pedestal 11a；Close to pedestal on pedestal 11a
Tee tube 115a is installed, one end of tee tube 115a is mounted on the side wall of pedestal, tee tube 115a's on the side of bottom
Second end connect discharge pipe (not shown), on discharge pipe be equipped with valve, in figures 4 and 5, in order to the needs of expression show as
The tee tube of Figure 4 and 5, in fact, the second end of tee tube and third section are horizontally disposed so that it is convenient to cooled wine
Liquid stream goes out.
The distillation container 12a includes the neck 122a between two or more container 121a and connection adjacent container.
The cross section of container 121a from it is lower be gradually increased to middle part after be gradually reduced upwards, in the present embodiment, container 121a's is transversal
Face is circle, and container 121a is cydariform, and neck 122a is connected to adjacent container, and neck 122a is hollow cylindrical, the internal diameter of neck
Less than the cross sectional inner diameter in the middle part of container 121a, in this way, wine liquid, when flowing downward, container gives wine liquid bigger cavity,
Nethermost container is connected on pedestal 11a, and pedestal 11a is not connected to distillation container, and being equipped on uppermost container has
The upper neck 120a of wine inlet 123a is located at wine inlet 123a on upper neck and is hinged with container cover 14a, in upper neck 120a
On be hinged with compression bar, be hinged with screw rod in the side opposite with compression bar hinged place upper neck 120a, on compression bar be equipped with card slot, spiral shell
Nut is engaged on bar, which such as needs to compress container cover, first cover container cover, then allow compression bar across container
The top of lid allows the part of screw rod to snap onto card slot, then compresses compression bar by nut, realizes the compression of container cover, in order to
Sealing performance is improved, sealing ring is equipped between container cover and upper neck.One end of heat-exchange tube 13a and the output of wine steam pipe
End connection, the other end of heat-exchange tube 13a enters in cavity after distilling container and then stretches out pedestal and tee tube connects
It connects；Heat-exchange tube in distillation container is coil pipe；Heat-exchange tube within the cavity is coil pipe, and the heat in neck is handed over
Changing pipe is coil pipe；As shown in figure 4, since the space in container is greater than the space in neck, heat-exchange tube in container with
Heat-exchange tube in neck is connected by jointing, and the heat-exchange tube and the intracorporal heat-exchange tube of chamber in container pass through connector
Connection, connector is common pipe connector, in this way, heat-exchange tube can be mounted and dismounted, in addition, being located at the heat exchange in container
The outer diameter of the adjacent coil pipe of pipe is corresponding with the spatial form in container, i.e., from top to bottom, heat-exchange tube in container
The outer diameter of adjacent coil pipe becomes larger and then becomes smaller from small, in this way, the coil pipe of small outer diameter is to wine liquid when wine liquid is by container
Flowing velocity has restriction effect, and the coil pipe of big outer diameter and the heat exchange area of wine liquid are bigger, therefore, are more conducive to heat
Exchange.In the present invention, the outer diameter of coil pipe refers to the outer diameter of spiral heat-exchange tube.
The vaporising device 2a includes container for evaporation 21a, the heating tube 22a being located in container for evaporation and is connected to evaporation
The wine steam pipe 23a of container upper end.There is the wine liquid cavity 211a for containing wine liquid in container for evaporation 21a.Heating tube 22a is in wine liquid
Coil pipe is formed in cavity, wine liquid can be evenly heated in this way.Heating tube 22a is hot-water line, passes through the water inlet to heating tube
End is passed through hot water meeting steam and heats to wine liquid, and the hot water or steam by heat exchange are discharged from the outlet pipe of heating tube, in order to add
The boiler for generating steam or hot water can be arranged in the convenience of heat between the water inlet end and water outlet of heating tube.Wine steam pipe 23a
Input terminal be connected to the upper end of evaporator 21a, the output end of wine steam pipe 23a is connected to one end of heat-exchange tube, wine steam
The output end of pipe passes through a container below the container of the top.Wine liquid can generate certain air pressure after preheat, steam when in wine
A container has been reserved in the top of steam pipe, in this way, uppermost container provides space because preheating to overflow upwards to wine liquid, avoids
Wine liquid is overflowed from wine inlet.Section of the wine steam pipe from input terminal to output end is gradually reduced, in this way, wine steam pipe 23a's is defeated
Enter end convenient for receiving the more wine steam in container for evaporation, and after the section of wine steam pipe 23a gradually becomes smaller, can change
Become wine steam in the pressure of wine steam pipe 23a.
Wine liquid pipe 3a is equipped between container for evaporation 21a and nethermost container, the input terminal of wine liquid pipe 3a is connected to most lower
The close bottom position of the container in face, the output end of wine liquid pipe 3a are connected to container for evaporation 21a close to the position at top, in this way,
On the one hand it allows the wine liquid in container to be preferably flowed into container for evaporation 21a, on the other hand can be contained in container for evaporation 21a
More wine liquids are equipped with valve on wine liquid pipe, in this way, facilitating whether control wine liquid will be flowed into container for evaporation 21a.
Communicating pipe 200 is connected between adjacent distiller, one end of communicating pipe 200 is connected the three of a wherein distiller
In the second end of siphunculus, the other end of communicating pipe 200 is connected to the wine inlet of adjacent distiller.In order to allow wine liquid to enter down
In one distiller, pump 201 is equipped on communicating pipe 200.
As shown in Figure 1, feed pipe 400 is equipped between the first wine outlet 13 and the wine inlet of first distiller, charging
Pump 401 is installed on pipe 400.
The working principle of above-mentioned foreign wine production line is: raw material enters hair by second charging aperture after broken crusher machine
In fermentation tank, fermented wine liquid enters in freezing precipitation tank after cooling precipitating from the second wine outlet, pipeline 3 and first charging aperture
Cold burden wine liquid is formed, cold burden wine liquid is entered in distiller container by feed pipe through wine inlet from the first wine outlet, distiller
Wine liquid in container enters in container for evaporation from wine liquid pipe, and heating tube carries out heating to the wine liquid in container for evaporation and allows wine liquid shape
At wine steam, wine steam enters heat-exchange tube through wine steam pipe, flow through distillation container in heat-exchange tube in wine steam with
The hydraulic carry out heat exchange in container is distilled, the wine steam heat release flowed through in the heat-exchange tube in distillation container is pre-cooled, so
Wine liquid enters in the intracorporal heat-exchange tube of chamber afterwards, and in the cavity, wine steam is cooled to form wine liquid, and the leading portion of wine liquid passes through row
Outlet pipe discharge, is then shut off the valve of discharge pipe, and wine liquid is allowed to repeat the above process from entering communicating pipe in next distiller.
In above-mentioned working principle, installation for fermenting is formed by increasing cooling settling tank 1 after fermentor 2, so that by
Wine liquid after fermentation enters cooling settling tank 1 and is cooled down, since molecular motion slows down at low temperature, so that by hair
The large-sized molecule precipitating contained in the filtered wine liquid of fermentation tank 2, and then the purity of foreign wine is improved, additionally, due to cooling heavy
Insulating layer 1103 is equipped between the inner wall and outer wall of shallow lake tank 1, so that cooling settling tank 1 is influenced by ambient temperature
It is small, and then reduce energy consumption；It is arranged additionally by the first cooling device is divided into the first spiral cooling pipe of multistage body 15, and
Temperature sensor feedback the is designed with around one spiral cooling pipe body 15 and between adjacent first spiral cooling pipe body
Different temperatures around one spiral cooling pipe body 15 and between adjacent first spiral cooling pipe body 15, thus from the first tank
Multiple positions of body 11 carry out temperature detection, then carry out temperature adjustment (temperature to the wine liquid in the multiple regions of cooling settling tank 1
The control method that degree sensor detects that the temperature in multiple regions carries out temperature adjustment later is that the prior art is no longer tired herein
State), so as to accurately control cooling settling tank internal temperature；Simultaneously by the way that the second cooling device is divided into the second spiral of multistage
The cooling tube body 25 of formula is arranged, and around the second spiral cooling pipe body 25 and between adjacent second spiral cooling pipe body
Temperature sensor is designed with to feed back around the second spiral cooling pipe body 25 and between adjacent second spiral cooling pipe body 25
Different temperatures, thus from fermentation tank 21 multiple positions carry out temperature detection, then in the multiple regions of fermentor 2
Wine liquid carry out temperature adjustment (temperature sensor detect the control method for carrying out temperature adjustment after the temperature in multiple regions
It is not repeated herein for the prior art), product brewing quality is improved so as to accurately control fermentation temperature inside fermentor.
For wine liquid in distillation process, the harmful substances such as methanol, fusel oil are located at the front section of the very little of wine steam, because
This, the cooled wine liquid of the wine steam for leading portion is discharged from discharge pipe first, reaches and removes the harmful substances such as methanol, fusel oil
Purpose, and in the present invention be provided with multiple distillers interconnected, therefore, to nocuousness such as methanol, fusel oil
Substance is removed step by step, be can remove 95% or more the harmful substances such as methanol, fusel oil, is improved the quality of foreign wine.Cold burden wine
For liquid during being entered in distillation container by wine inlet, due to being provided with container and neck, container is the big both ends in middle part
Small drum containers, the neck passage cross section for connecting adjacent accommodating is less than the cross section at middle part in container, in this way, wine liquid is being steamed
It evaporates when being flowed in container, due to above structure, the flowing velocity of wine liquid can slow down, in this way, the wine liquid and wine in distillation container are steamed
The heat exchange of vapour is more abundant, more preferable to the pre-heat effect of wine liquid, and the precooling effect of wine steam is also more preferable, improves energy
Utilization rate.Due to being provided with pedestal, the lower end of pedestal is arranged in cooling water inlet pipe, and the upper end of pedestal is arranged in outlet pipe, this
On the contrary, cooling effect is more preferable, reduction is residual in cooling wine liquid for sample, the flow direction of cooling water and the flow direction of wine steam
Stay wine steam.
Claims (10)
1. a kind of foreign wine production line, it is characterised in that: according to production procedure successively include pulverizer, fermentation device for wine and distillation
System；
Fermentation device for wine includes fermentor, and the top of the fermentor is equipped with second charging aperture, and the bottom of fermentor is equipped with the
Two wine outlets further include freezing precipitation tank, and the freezing precipitation tank includes the first tank body with stabilizer blade, and first tank body is set
It is equipped with first charging aperture, the first wine outlet, the first sewage draining exit, the first temperature control equipment, the first cooling device, first charging aperture
In the first top of the tank, the first wine outlet and the first sewage outfalls setting in the first tank base, the second of fermentor goes out wine for setting
Mouth is connected by pipeline with the first charging aperture of freezing precipitation tank, and insulating layer is equipped between the inner wall and outer wall of the first tank body；
Distallation systm includes two or more distillers, and the distiller includes cooling heat exchange device and vaporising device, described
Cooling heat exchange device include pedestal, distillation container and heat-exchange tube；The vaporising device includes container for evaporation, is located at evaporation
Heating tube in container and the wine steam pipe for being connected to container for evaporation upper end；There is cavity, close to pedestal on pedestal in pedestal
Bottom be equipped with the cooling water inlet pipe that be connected to cavity, close to the top of pedestal equipped with the water outlet communicated with cavity on pedestal
Pipe；The distillation container includes the neck between two or more containers and connection adjacent container, and the cross section of container is under
It is gradually reduced upwards after being gradually increased to middle part, neck is connected to adjacent container, and nethermost container is connected on pedestal, most upper
The container in face is equipped with wine inlet；One end of heat-exchange tube is connect with the output end of wine steam pipe, the other end warp of heat-exchange tube
Pedestal is entered in cavity and then stretched out after crossing distillation container；Wine liquid pipe is equipped between container for evaporation and nethermost container；Phase
It is connected with communicating pipe between adjacent distiller, discharge pipe is equipped on communicating pipe.
2. foreign wine production line according to claim 1, it is characterised in that: first cooling device is to be arranged first
Tank interior and two or more the first spiral cooling pipe body being arranged along the top of the first tank body to bottom, described
One temperature control equipment is fixed on the first tank body, and first temperature control equipment includes that setting is spiral cold first
But first temperature sensor of two or more on tube body periphery and be arranged between adjacent first spiral cooling pipe body two
A or more second temperature sensor.
3. foreign wine production line according to claim 2, it is characterised in that: the first spiral cooling pipe body is fixed on
On one bracket, first support, which is fixed on the first tank base and is equipped with first between first support and the first inner tank wall, reinforces branch
Strut.
4. foreign wine production line according to claim 2, it is characterised in that: described two or more the first temperature sensors edge
The circumferencial direction of the first tank body be uniformly distributed.
5. foreign wine production line according to claim 1, it is characterised in that: the fermentor includes the fermentor tank with stabilizer blade
Body, the fermentation tank are provided with the second sewage draining exit, second temperature control device, the second cooling device, and the second sewage draining exit is set
It sets in fermentor tank base, second cooling device is fermentor tank interior to be arranged in and along fermentation tank
Two or more the second spiral cooling pipe body that top is arranged to bottom, the second temperature control device are fixed on fermentation
On tank, and the second temperature control device includes the two or more that the second spiral cooling pipe body periphery is arranged in
Third temperature sensor and two or more 4th temperature sensing being arranged between adjacent second spiral cooling pipe body
Device.
6. foreign wine production line according to claim 5, it is characterised in that: the second spiral cooling pipe body is fixed on
On two brackets, second support, which is fixed on fermentor tank base and is equipped with second between second support and fermentor inner tank wall, to be added
Strong support rod.
7. foreign wine production line according to claim 6, it is characterised in that: the second support includes two or more
Second strut, the bottom of the second strut are fixed on the bottom of fermentation tank, the outer wall of the second strut and the second spiral cooling tube
The outer wall of body is connected.
8. foreign wine production line according to claim 3, it is characterised in that: the first support includes two or more
First strut, the bottom of the first strut are fixed on the bottom of the first tank body, the outer wall of the first strut and the first spiral cooling tube body
Outer wall be connected；Lower part is equipped with the first filter plate for deslagging filtering in first tank body, on first filter plate
Equipped with the first via hole passed through for the first strut.
9. foreign wine production line according to claim 1, it is characterised in that: the second wine outlet of the fermentor and cooling are heavy
Pipeline between the first charging aperture of shallow lake tank is equipped with pump.
10. foreign wine production line according to claim 1, it is characterised in that: the cross section of container is circle；Positioned at distiller
Heat-exchange tube in container is coil pipe；Heat-exchange tube within the cavity is coil pipe；Wine steam pipe is cut from input terminal to output end
Face is gradually reduced；The output end of wine steam pipe passes through a container below the container of the top；Neck is hollow cylindrical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821326357.9U CN208803048U (en) | 2018-08-16 | 2018-08-16 | A kind of foreign wine production line |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821326357.9U CN208803048U (en) | 2018-08-16 | 2018-08-16 | A kind of foreign wine production line |
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| CN208803048U true CN208803048U (en) | 2019-04-30 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110272801A (en) * | 2019-07-24 | 2019-09-24 | 四川强学农业科技有限公司 | Wine boils in a kind of selenium-rich the Hakkas |
| CN114045198A (en) * | 2021-12-03 | 2022-02-15 | 枣阳市香木瓜技术开发服务中心 | Muskmelon distillation extraction method applied to muskmelon wine |
| CN115612590A (en) * | 2022-11-09 | 2023-01-17 | 湘潭林海机械制造有限公司 | Freezing energy-conserving filter unit that stews |
-
2018
- 2018-08-16 CN CN201821326357.9U patent/CN208803048U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110272801A (en) * | 2019-07-24 | 2019-09-24 | 四川强学农业科技有限公司 | Wine boils in a kind of selenium-rich the Hakkas |
| CN114045198A (en) * | 2021-12-03 | 2022-02-15 | 枣阳市香木瓜技术开发服务中心 | Muskmelon distillation extraction method applied to muskmelon wine |
| CN115612590A (en) * | 2022-11-09 | 2023-01-17 | 湘潭林海机械制造有限公司 | Freezing energy-conserving filter unit that stews |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Foreign wine production line Effective date of registration: 20200428 Granted publication date: 20190430 Pledgee: Guangdong Lechang Rural Commercial Bank Co.,Ltd. Pledgor: GUANGDONG CHATEAU YUMA WINE INDUSTRY Co.,Ltd. Registration number: Y2020980001852 |
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Date of cancellation: 20230425 Granted publication date: 20190430 Pledgee: Guangdong Lechang Rural Commercial Bank Co.,Ltd. Pledgor: GUANGDONG CHATEAU YUMA WINE INDUSTRY Co.,Ltd. Registration number: Y2020980001852 |
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Denomination of utility model: A foreign wine production line Effective date of registration: 20230427 Granted publication date: 20190430 Pledgee: Guangdong Lechang Rural Commercial Bank Co.,Ltd. Langtian Branch Pledgor: GUANGDONG CHATEAU YUMA WINE INDUSTRY Co.,Ltd. Registration number: Y2023980039425 |
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Granted publication date: 20190430 Pledgee: Guangdong Lechang Rural Commercial Bank Co.,Ltd. Langtian Branch Pledgor: GUANGDONG CHATEAU YUMA WINE INDUSTRY Co.,Ltd. Registration number: Y2023980039425 |
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Denomination of utility model: A foreign liquor production line Granted publication date: 20190430 Pledgee: Guangdong Lechang Rural Commercial Bank Co.,Ltd. Langtian Branch Pledgor: GUANGDONG CHATEAU YUMA WINE INDUSTRY Co.,Ltd. Registration number: Y2024980026779 |
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