CN208748066U - A kind of fruit wine distiller with reduction methanol content function - Google Patents
A kind of fruit wine distiller with reduction methanol content function Download PDFInfo
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- CN208748066U CN208748066U CN201821406654.4U CN201821406654U CN208748066U CN 208748066 U CN208748066 U CN 208748066U CN 201821406654 U CN201821406654 U CN 201821406654U CN 208748066 U CN208748066 U CN 208748066U
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Abstract
The utility model provides a kind of with the fruit wine distiller for reducing methanol content function, it is related to fruit wine distillation technique field, including thick gold-plating tower, rectifying column, cooler, thick gold-plating tower side wall is equipped with feeding pipe, thick gold-plating top of tower is equipped with the exhaust pipe being connected with rectifying column, thick gold-plating tower bottom is equipped with waste material comb, the Methanol Recovery pipe being communicated with the outside is equipped at the top of rectifying column, rectifying column top side wall is equipped with the connecting tube being connected with cooler, cooler bottom is equipped with the fruit wine collecting pipe being communicated with the outside, and is equipped with valve on each pipeline；Motor is equipped at the top of rectifying column, the rotation axis of motor stretches to and is fixed with agitating paddle on the inside and rotation axis of rectifying column, and rectifying tower side wall is equipped with temperature detect switch (TDS) and normal open switch parallel with one another, is equipped with temperature sensor in rectifying column；It is according to the present utility model a kind of with the fruit wine distiller for reducing methanol content function, the methanol in fruit wine can not only be effectively removed, and the fruit wine distilled is in good taste.
Description
Technical field
The utility model relates to fruit wine distillation technique fields, more particularly to a kind of with reduction methanol content function
Fruit wine distiller.
Background technique
Due to containing pectin, glycoside in the raw material of fruit wine production, and there is methoxyl group on pectin and glycoside molecular side chain,
When raw material is used for wine fermentation, under the action of organized enzyme, methoxyl group is easy to happen hydrolysis or alcohol radical exchange, thus raw
At methanol.Since methanol has strong toxicity to human body, because methanol can be oxidized to than methanol toxicity more in human metabolism
Strong formaldehyde and formic acid, and blindness, hepatopathy, even death can be led to by drinking the wine containing high carbinol content.Therefore demand is a kind of
The fruit wine distiller of methanol content can be reduced.
Utility model content
In order to overcome the drawbacks of the prior art, the utility model provides a kind of with the fruit wine steaming for reducing methanol content function
Device is evaporated, the methanol in fruit wine can not only be effectively removed, and the fruit wine distilled is in good taste.
For this purpose, the following technical solution is employed for the utility model:
The utility model provides a kind of with the fruit wine distiller for reducing methanol content function, including thick gold-plating tower, rectifying
Tower, cooler, the thick gold-plating tower side wall are equipped with the feeding pipe being communicated with the outside, and the feeding pipe is equipped with the first valve, institute
It states thick gold-plating top of tower and is equipped with the exhaust pipe being connected with the rectifying column, the exhaust pipe is equipped with the second valve, the thick gold-plating
Tower bottom is equipped with the waste material comb being communicated with the outside, and the waste material comb is equipped with third valve；It is set at the top of the rectifying column
There is the Methanol Recovery pipe being communicated with the outside, the Methanol Recovery pipe is equipped with the 4th valve, and the rectifying column top side wall is set
There is the connecting tube being connected with the cooler, the connecting tube is equipped with the 5th valve；The cooler bottom be equipped with it is outer
The fruit wine collecting pipe that portion is connected, the fruit wine collecting pipe are equipped with the 6th valve；Electricity is fixedly installed at the top of the rectifying column
Machine, the motor output shaft are fixed with rotation axis, and the rotation axis wears the inside for stretching to the rectifying column and described turn
Agitating paddle is fixed on moving axis, the rectifying tower side wall is fixedly installed with console, is equipped on the console mutually simultaneously
The temperature detect switch (TDS) and normal open switch of connection are fixedly installed with temperature sensor in the rectifying column.
In the preferable technical solution of the utility model, the cooler is U-shaped, and the connecting tube is far from the rectifying
One end of tower is located in the middle part of the side wall of the cooler.
In the preferable technical solution of the utility model, the rectifier bottoms are equipped with the weight being connected with the thick gold-plating tower
Multiple to utilize pipe, the recycling pipe is equipped with drawing liquid pump.
In the preferable technical solution of the utility model, liquid level is fixedly installed in the thick gold-plating tower and the rectifying column
Sensor, the console are equipped with the liquid level display being conductively connected with the liquid level sensor.
In the preferable technical solution of the utility model, the exhaust pipe tilts upwards along the direction far from the thick gold-plating tower
Setting.
In the preferable technical solution of the utility model, the connecting tube is tilted down along the direction far from the rectifying column
Setting.
The utility model has the following beneficial effects:
It is provided by the utility model a kind of with the fruit wine distiller for reducing methanol content function, pass through the thick gold-plating tower pair
Material solution predistillation tentatively reduces the content of water in fruit wine, then carries out two to material solution by the rectifying column
Secondary distillation, before this by the temperature detect switch (TDS) by the heating and temperature control of the rectifying column at 65 °~70 ° so that material solution
In methanol be constantly evaporated, greatly reduce the content of methanol in fruit wine, volatilized similar, continued to raw material to methanol
Solution is distilled, so that ethyl alcohol and aromatic substance, which evaporate and be passed through the cooler, carries out cooling condensation, the fruit obtained from
Not only methanol content is low for wine, moisture content is low, but also impurity is few in good taste；Wherein it can accelerate original by the way that the stirring slurry is arranged
The evaporation for expecting solution, saves distillation time, to reduce production cost；It, can be by institute by the way that the recycling is arranged
It states the residual solution containing higher concentration ethyl alcohol in rectifying column and again returns to the thick gold-plating tower and distilled, rationally repeat to make
With resource, production cost is reduced.
Detailed description of the invention
Fig. 1 is a kind of fruit wine distiller with reduction methanol content function that specific embodiment of the present invention provides
Structural schematic diagram.
In figure:
100, thick gold-plating tower；110, feeding pipe；111, the first valve；120, exhaust pipe；121, the second valve；130, waste material is arranged
Pipe；131, third valve；200, rectifying column；210, Methanol Recovery pipe；211, the 4th valve；220, connecting tube；221, the 5th valve
Door；230, recycling pipe；300, cooler；310, fruit wine collecting pipe；311, the 6th valve；400, motor；410, rotation axis；
411, agitating paddle；500, console；510, temperature detect switch (TDS)；520, normal open switch；600, temperature sensor；700, level sensing
Device；710, liquid level display；800, drawing liquid pump.
Specific embodiment
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art and technical solution are briefly described, it should be apparent that, it is described below
Attached drawing be only some embodiments of the utility model, for those of ordinary skill in the art, do not paying creativeness
Under the premise of labour, it can also be obtained according to these attached drawings other attached drawings.
It further illustrates the technical solution of the utility model below with reference to the accompanying drawings and specific embodiments, needs
Bright, the attached drawing in specific embodiment is only schematic diagram, is not defined to the size of device, actual size is with reality
Subject to object.
As shown in Figure 1, include thick gold-plating tower 100, rectifying column 200, cooler 300, thick 100 side wall of gold-plating tower be equipped with it is outer
The feeding pipe 110 that portion is connected, the feeding pipe 110 are equipped with the first valve 111, are equipped with and institute at the top of the thick gold-plating tower 100
The exhaust pipe 120 that rectifying column 200 is connected is stated, the exhaust pipe 120 is equipped with the second valve 121, thick 100 bottom of gold-plating tower
Equipped with the waste material comb 130 being communicated with the outside, the waste material comb 130 is equipped with third valve 131；The rectifying column 200
Top is equipped with the Methanol Recovery pipe 210 being communicated with the outside, and the Methanol Recovery pipe 210 is equipped with the 4th valve 211, the essence
It evaporates 200 top side wall of tower and is equipped with the connecting tube 220 being connected with the cooler 300, the connecting tube 220 is equipped with the 5th valve
Door 221；300 bottom of cooler is equipped with the fruit wine collecting pipe 310 being communicated with the outside, and sets on the fruit wine collecting pipe 310
There is the 6th valve 311；Motor 400 is fixedly installed at the top of the rectifying column 200,400 output shaft of motor, which is fixed with, to be turned
Moving axis 410, the rotation axis 410 wear the inside for stretching to the rectifying column 200 and are fixed in the rotation axis 410
Agitating paddle 411,200 side wall of rectifying column are fixedly installed with console 500, are equipped on the console 500 parallel with one another
Temperature detect switch (TDS) 510 and normal open switch 520, the model KSD301 of the temperature detect switch (TDS) 510 is fixed in the rectifying column 200
Temperature sensor 600 is installed, the model DS18B20 of the temperature sensor 600, the temperature sensor 600 and described
Temperature detect switch (TDS) 510 is conductively connected with external PLC controller, is again provided with the console 500 on the thick gold-plating tower 100.
Further, the cooler 300 is U-shaped, one end position of the connecting tube 220 far from the rectifying column 200
In the cooler 300 side wall close to center, the fruit wine steam entered from the connecting tube 220 is to the cold in cooler 300
Condensed on inner walls achievement wine liquid, and the cooler 300 of U-shaped not only can be cold to the sufficient space of fruit wine steam offer
It is solidifying, but also the fruit wine liquid for forming condensation is facilitated to be pooled to 300 bottom of cooler, consequently facilitating being collected from the fruit wine
Pipe 310 recycles the fruit wine liquid in the cooler 300.
Further, 200 bottom of rectifying column is equipped with the recycling pipe 230 being connected with the thick gold-plating tower 100, institute
It states recycling pipe 230 and is equipped with drawing liquid pump 800, the residual liquid after being distilled due to rectifying column 200 can also contain more second
Residual solution in the rectifying column 200 can be extracted into the thick gold-plating tower 100 by the drawing liquid pump 800 by the substances such as alcohol, residual
Remaining solution can be used as raw material again in the thick gold-plating tower 100, not only rationally utilize used resource in this way, and reduce
Produce ontology.
Further, it is fixedly installed with liquid level sensor 700 in the thick gold-plating tower 100 and the rectifying column 200, it is described
Console 500 is equipped with the liquid level display 710 being conductively connected with the liquid level sensor 700, and the liquid level sensor 700 is felt
The liquid level in the thick gold-plating tower 100 and the rectifying column 200 is answered, and gives bearing reaction to corresponding liquid level display
710, whether setting in this way needs to close heating device convenient for operator according to the height of liquid in destilling tower, is conducive to control and subtracts
The water content of few fruit wine, consequently facilitating the quality of the fruit wine of control preparation.
Further, the exhaust pipe 120 is obliquely installed upwards along the direction far from the thick gold-plating tower 100, due to water
Boiling point is 100 °, and the boiling point of ethyl alcohol is 78.3 °, so having partially liq when by the exhaust pipe 120 in the row
Tracheae 120 goes out to condense, wherein for other compositions, water is easy to condense at the exhaust pipe 120, be arranged in this way so that
Condensate liquid can enter thick gold-plating tower 100 along exhaust pipe 120, be conducive to the water content that control reduces fruit wine.
Further, the connecting tube 220 tilts down setting along the direction far from the rectifying column 200, is arranged in this way
Connecting tube 220 can prevent from flowing back into again in the rectifying column 200 in the fruit wine of the condensation in the cooler 300, make
At the repetition operation of the rectifying column 200, the distillation efficiency of device is not only reduced, energy consumption increase is also resulted in, increases
Production cost.
Work step:
(1) the first valve 111 is opened, the fruit wine after fermentation is then passed through from feeding pipe 110；
(2) the first valve 111 is closed, the second valve 121 is opened, starts the power supply of thick 100 heating device of gold-plating tower, closure is thick
The normal open switch 520 of gold-plating tower 100, so that the liquid in thick gold-plating tower 100 is heated distillation, at this moment the steam in thick gold-plating tower 100 is not
It is disconnected to enter in rectifying column 200 from exhaust pipe 120；
(3) it when the liquid level that the liquid level display 710 on thick gold-plating tower 100 is shown is 1/5 or so of initial liquid level, disconnects thick
The normal open switch 520 of gold-plating tower 100 closes the power supply of thick 100 heating device of gold-plating tower, closes the second valve 121, opens third valve
131 recycle the remaining liq in thick gold-plating tower 100 into shape from waste material comb 130；
(4) the 4th valve 211 is opened, the power supply of 200 heating device of rectifying column is started, temperature detect switch (TDS) 510 is closed, so that smart
It evaporates the liquid in tower 200 and is heated distillation, wherein temperature sensor 600 incudes the temperature in rectifying column 200, when rectifying column 200
When interior temperature is equal to or more than 70 °, PLC controller is in an off state temperature detect switch (TDS) 510, stops heating；Work as essence
When evaporating the temperature in tower 200 less than 65 °, PLC controller makes temperature detect switch (TDS) 510 be in closed state, continues to heat, at this moment smart
Methanol steam in gold-plating tower is discharged and is recovered constantly from Methanol Recovery pipe 210；
(5) when the liquid that the liquid level display 710 on rectifying column 200 is shown is 3/4 or so of initial liquid level, temperature is disconnected
Switch 510 is controlled, the 4th valve 211 is closed, opens the 5th valve 221, normal open switch 520 is closed, so that the liquid in rectifying column 200
Body is constantly heated distillation, and at this moment the fruit wine steam in rectifying column 200 constantly enters the progress of cooler 300 from connecting tube 220
It is cooling；
(6) it when the liquid that the liquid level display 710 on rectifying column 200 is shown is 1/4 or so of initial liquid level, disconnects normal
Switch 520 and the power supply for closing 200 heating device of rectifying column close the 5th valve 221；
(7) the steam cooling in device 300 to be cooled finishes, and opens the 6th valve 311, recycles from fruit wine collecting pipe 310 cold
But the fruit wine in device 300；
(8) it is finished to fruit wine recycling, closes the 6th valve 311；Start drawing liquid pump 800, by the residual solution in rectifying column 200
Body is extracted into thick gold-plating tower 100, so that distillating material of the fermentation fruit wine that is passed through of residual liquid and feeding pipe 110 as a new round,
Repeating above step can be carried out the distillation of a new round.
It is provided by the utility model a kind of with the fruit wine distiller for reducing methanol content function, first pass through the thick gold-plating tower
100 distill the raw material being passed through, due in water alcohol and aromatic substance all than water be easier volatilize so that distillation when
Alcohol and the quantity of aromatic substance volatilization are far more than water, and concentration can also improve when turning to steam, so that most methanol,
Ethyl alcohol, aromatic substance and part water are volatilized to enter into the rectifying column 200, and remainder water in the thick gold-plating tower 100
And ethyl alcohol, the aromatic substance of low concentration, the first time of fermentation fruit wine is purified to realize；Pass through the temperature detect switch (TDS) 510
The heating temperature controlled in the rectifying column 200 is between 65 ° to 70 °, and the boiling point of methanol is 64.7 °, the boiling point of ethyl alcohol
It is 78.3 °, so that the methanol in the rectifying column 200 in liquid is constantly evaporated, and ethyl alcohol and aromatic substance are then left and,
To constantly reduce methanol content in fruit wine solution, then the surplus solution in the rectifying column 200 is steamed again
It evaporates, so that ethyl alcohol and aromatic substance, which are constantly evaporated and are passed through the cooler 300, carries out condensing recovery, again reduces fruit
The content of water in wine, not only methanol content is low for the fruit wine obtained from, moisture content is low, but also impurity is few in good taste；Wherein lead to
It crosses and the stirring slurry is set can accelerate the evaporation of material solution, distillation time is saved, to reduce production cost；Pass through
The recycling is set, the residual solution containing higher concentration ethyl alcohol in the rectifying column 200 can be again returned to
The thick gold-plating tower 100 is distilled, and has rationally been reused resource, has been reduced production cost.
The utility model is described with reference to the preferred embodiments, and those skilled in the art know, is not departing from this reality
In the case where with novel spirit and scope, various changes or equivalence replacement can be carried out to these features and embodiment.This reality
It is not limited to the particular embodiment disclosed with novel, other embodiments fallen into claims hereof all belong to
In the range of the utility model protection.
Claims (6)
1. a kind of with the fruit wine distiller for reducing methanol content function, it is characterised in that:
Including thick gold-plating tower (100), rectifying column (200), cooler (300), thick gold-plating tower (100) side wall is equipped with and is communicated with the outside
Logical feeding pipe (110), the feeding pipe (110) are equipped with the first valve (111), be equipped at the top of the thick gold-plating tower (100) with
The exhaust pipe (120) that the rectifying column (200) is connected, the exhaust pipe (120) are equipped with the second valve (121), described thick
Gold-plating tower (100) bottom is equipped with the waste material comb (130) being communicated with the outside, and the waste material comb (130) is equipped with third valve
(131)；The Methanol Recovery pipe (210) being communicated with the outside, the Methanol Recovery pipe are equipped at the top of the rectifying column (200)
(210) it is equipped with the 4th valve (211), rectifying column (200) top side wall, which is equipped with, to be connected with the cooler (300)
Connecting tube (220), the connecting tube (220) are equipped with the 5th valve (221)；Cooler (300) bottom is equipped with and outside
The fruit wine collecting pipe (310) being connected, the fruit wine collecting pipe (310) are equipped with the 6th valve (311)；The rectifying column
(200) top is fixedly installed with motor (400), and motor (400) output shaft is fixed with rotation axis (410), the rotation
Axis (410) wears the inside for stretching to the rectifying column (200) and is fixed with agitating paddle in the rotation axis (410)
(411), rectifying column (200) side wall is fixedly installed with console (500), is equipped on the console (500) mutually simultaneously
The temperature detect switch (TDS) (510) and normal open switch (520) of connection, the rectifying column (200) is interior to be fixedly installed with temperature sensor (600).
2. according to claim 1 a kind of with the fruit wine distiller for reducing methanol content function, it is characterised in that:
The cooler (300) is U-shaped, and the connecting tube (220) is located at described cold far from the one end of the rectifying column (200)
But in the middle part of the side wall of device (300).
3. according to claim 1 a kind of with the fruit wine distiller for reducing methanol content function, it is characterised in that:
Rectifying column (200) bottom is equipped with the recycling pipe (230) being connected with the thick gold-plating tower (100), the repetition
Drawing liquid pump (800) are equipped with using pipe (230).
4. according to claim 1 a kind of with the fruit wine distiller for reducing methanol content function, it is characterised in that:
Liquid level sensor (700), the console are fixedly installed in the thick gold-plating tower (100) and the rectifying column (200)
(500) liquid level display (710) being conductively connected with the liquid level sensor (700) is installed.
5. according to claim 1 a kind of with the fruit wine distiller for reducing methanol content function, it is characterised in that:
The exhaust pipe (120) is obliquely installed upwards along the direction far from the thick gold-plating tower (100).
6. according to claim 1 a kind of with the fruit wine distiller for reducing methanol content function, it is characterised in that:
The connecting tube (220) tilts down setting along the direction far from the rectifying column (200).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821406654.4U CN208748066U (en) | 2018-08-29 | 2018-08-29 | A kind of fruit wine distiller with reduction methanol content function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821406654.4U CN208748066U (en) | 2018-08-29 | 2018-08-29 | A kind of fruit wine distiller with reduction methanol content function |
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| Publication Number | Publication Date |
|---|---|
| CN208748066U true CN208748066U (en) | 2019-04-16 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821406654.4U Active CN208748066U (en) | 2018-08-29 | 2018-08-29 | A kind of fruit wine distiller with reduction methanol content function |
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| CN (1) | CN208748066U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114480067A (en) * | 2022-01-14 | 2022-05-13 | 肥城金塔机械科技有限公司 | Device for reducing methanol in kiwi fruit wine and preparation method |
-
2018
- 2018-08-29 CN CN201821406654.4U patent/CN208748066U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114480067A (en) * | 2022-01-14 | 2022-05-13 | 肥城金塔机械科技有限公司 | Device for reducing methanol in kiwi fruit wine and preparation method |
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