CN2516560Y

CN2516560Y - Distillation device for preparation of distilled liquor

Info

Publication number: CN2516560Y
Application number: CN01275218U
Authority: CN
Inventors: 阮仙化; 阮靖杰
Original assignee: Individual
Current assignee: Individual
Priority date: 2001-11-30
Filing date: 2001-11-30
Publication date: 2002-10-16
Anticipated expiration: 2011-11-30

Abstract

The utility model relates to a distillation apparatus for producing tequila, which mainly comprises an evaporation device, a first condensation device, a second condensation device, a collecting device and a negative pressure producing device. The utility model is characterized in that: the first condensation device and the second condensation device are connected bifurcately and are communicated with the evaporation device and the collecting device; the negative pressure producing device is communicated with the collecting device; when the evaporation device is heating the zymotic fluid, the negative pressure producing device can provide a negative pressure in the evaporation device, enabling the zymotic fluid to produce gasification under lower heating temperature, producing a tequila liquid with a better quality and reducing the waste of heating sources; the first condensation device and the second condensation device condensate and collect the vapor in different segments, respectively collecting the alcohol substance and aldehyde substance in the zymotic fluid.

Description

Make the water distilling apparatus of liquor

Technical field

The utility model is a water distilling apparatus of making liquor about a kind of, it mainly is to have an evaporation unit, first condensing works, second condensing works, one collection device and negative pressure generation device constitute, this first condensing works and second condensing works are the connections of making difference, be communicated with evaporation unit and collection device, the negative pressure generation device is to be communicated with collection device, when making evaporation unit heating fermented liquid, the negative pressure generation device provides a negative pressure in the evaporation unit, make fermented liquid under low Heating temperature, produce pneumatolysis, make the preferable liquor liquid of a quality, have the waste that reduces heating energy source; First condensing works and second condensing works condense to collect to the segmentation of steam and implement, and reach alcohols material and the aldehyde material collected respectively in the fermented liquid.

Background technology

As everyone knows, in order to remove the impurity in the fermented wine (fermented liquid), the ethanol concn that improves wine liquid and the time of seasoning thereof, fermented wine must be distilled again usually.Be after the wine fermentation brew is finished, if without distillation, it is not good not only to contain impurity, purity, and wine liquid can continue fermentation to cause acid bad, causes behind wine Kaifeng and to have drunk in must be during of short duration.Fermented wine (fermented liquid) is can decolour, take off flavor and deodorization and form colourless wine after distillation, remove impurity and improve ethanol concn, and also unlikely acid is bad after storing the several years, be with, the wine liquid after the general fermentation must be distilled.

The distillation plant of traditional wine liquid is divided into two kinds of single distillation method and continuous still battery methods, single distillation method is the still-process that carries out secondary with single distil container, to remove a large amount of moisture, obtain the higher wine liquid of ethanol concn, and when distilling for the second time, remove its wine liquid of still-process gained end to end, to remove to influential aldehydes of human body and methyl alcohol, the wine heart (Heart) of still-process gained in the middle of only getting is so to reach the manufacturing of liquor.

Be to use two distil containers to carry out the still-process of two-stage continuously with series system about the continuous still battery method, make still-process difference fractionation aldehydes and the methyl alcohol of two-stage, make in the wine liquid of distillation gained, contained alcohol is harmless ethanol, and its successional distillation plant can be made liquor liquid in a large number.Its major defect is:

1, above-mentioned two kinds of wine liquid distillation modes make the alcohol vaporization in the fermented liquid and the heat that provided, are the vinasse that sink to the bottom in the fermented liquid and impurity are had produce the empyreumatic facts to take place, and have a strong impact on the local flavor of distillation obtained wine thereby liquid;

2, the heat that the time provided of distillation also has the shortcoming of energy dissipation;

3 moreover, above-mentioned single distillation method is effectively to be collected in the aldehyde material that distillation the time is disengaged; Though above-mentioned continuous still battery method can have the advantage of a large amount of manufacturing liquor liquid, but its successional distillation mode can make gained distillatory wine liquid lose its original local flavor, and comparatively complicated on the setting of its structure and the processing procedure, and the too high shortcoming of cost and maintenance, operational inconvenience are arranged.

Summary of the invention

Main purpose of the present utility model provides a kind of water distilling apparatus of making liquor, mainly include: evaporation unit, first condensing works, second condensing works, collection device and negative pressure generation device, make the evaporation unit can be under lower Heating temperature, make fermented liquid produce distillment, and the steam that makes generation can be directed condensation and Fractional Collections reaches the purpose that obtains the liquor liquid that alcohol is purer and local flavor is preferable.

The purpose of this utility model is achieved in that a kind of water distilling apparatus of making liquor, it is characterized in that: it includes the airtight evaporation unit for the ccontaining heating of fermented liquid; First condensing works is communicated with this evaporation unit; The material-gathering device that is air-tight state is done being communicated with of difference with this first condensing works; Second condensing works is done being communicated with of difference with this first condensing works; The collection device that is air-tight state has first receiving tank, and this first receiving tank is to be communicated with second condensing works; The negative pressure generation device is communicated with first receiving tank of this collection device, is a negative pressure state in first receiving tank of this evaporation unit, material-gathering device and collection device.

This evaporation unit below has a heating source.This heating source is provided with the temperature control unit of control Heating temperature.This evaporation unit bottom has a catch basin.This evaporation unit bottom surface is concaved with a heating chamber, is provided with most smoke pipes in this heating chamber.This place, top, evaporation unit internal space establishes to be a circulation space, and the wall of this circulation space is provided with the dividing plate that majority is crisscross arranged.This first condensing works, second condensing works and material-gathering device are the connections of making difference with Y-tube, first path of this Y-tube is and being connected of this first condensing works exit end, the alternate path of this Y-tube is and being connected of this second condensing works inlet end, and the 3rd path of this Y-tube is and being communicated with of this material-gathering device.First path of this Y-tube and the height of alternate path are higher than the 3rd path.This collection device has second receiving tank that is sealed state in addition, and this second receiving tank and path between this second condensing works and first receiving tank are that the selection with operability is communicated with.To be communicated be to reach by a path control unit to the operability of path between this second receiving tank and this second condensing works and first receiving tank, and this second receiving tank, second condensing works and first receiving tank are communicated with simultaneously; Or this second condensing works is communicated with this second receiving tank path blockade with first receiving tank.This collection device has at least one the 3rd receiving tank that is sealed state in addition, and the path between the 3rd receiving tank and this second condensing works and first receiving tank and second receiving tank are communicated with the selection of operability.It is to reach by the alternate path control unit that the 3rd receiving tank is communicated with operability between second condensing works, first receiving tank, second receiving tank.This negative pressure generation device is the blast machine.This evaporation unit is communicated with a storage device by a carrier pipe road.This carrier pipe road is provided with valve body.This carrier pipe road is provided with a primary heater unit.This evaporation unit has a circulation device.

Further specify below in conjunction with the preferred embodiment conjunction with figs..

Description of drawings

Fig. 1 is an organigram of the present utility model.

Fig. 2 is a user mode synoptic diagram of the present utility model.

Fig. 3 is the organigram of the utility model embodiment 2.

Fig. 4 is the user mode synoptic diagram of the utility model embodiment 2.

Embodiment

Embodiment 1

Consult Fig. 1-shown in Figure 2, the utility model is to include: one is the evaporation unit 1 of air-tight state, have in it and can supply the ccontaining accommodation space 11 of fermented liquid, and be provided with a catch basin 110 in evaporation unit 1 bottom, and cell body bottom surface and be concaved with a heating chamber 12, and in this heating chamber 12 and be provided with most smoke pipes 121, so that a heating source 6 is when being implemented by heating chamber 12 belows heating, most smoke pipes 121 can have the function of assembling thermal source, and evaporation unit 1 top is to be provided with a vapour outlet 13, and locate to be that in the top position of accommodation space 11 circulation space 14 is arranged, be provided with most dividing plates 141 in the mode that is staggered and be provided with at interval on the wall of this circulation space 14, evaporation unit 1 is provided with a circulation device 17 in addition, can fermented liquid being done the enforcement circulate, this circulation device 17 mainly is to be preferred embodiment with a recycle pump 171, so that evaporation unit 1 epimere appropriate position is provided with a feedback outlet 15, and be communicated to recycle pump 171 with a feed back pipe 151, and evaporation unit 1 bottom is provided with a discharge port 16, and is communicated to recycle pump 171 with a discharge nozzle 161.

One first condensing works 2, be that prolong 21 with coiled coil is the example explanation in present embodiment, its prolong 21 is for having an inlet end 211 and an exit end 212, this inlet end 211 is vapour outlet 13 places that are connected in evaporation unit 1, and in the enforcement of the prolong 21 of first condensing works 2, provide the setting of a fan group 22, and first condensing works 2 is implemented for making gas cooling;

One second condensing works 3, be that prolong 31 with coiled coil is the example explanation in present embodiment, its prolong 31 is for having an inlet end 311 and an exit end 312, the inlet end 311 of its prolong 31 is to do being communicated with of difference by a Y-tube 32 with first condensing works 2, first path 321 that this Y-tube 32 is had and alternate path 322 provide being connected of inlet end 311 of the exit end 212 of first condensing works, 2 prolongs 21 and second condensing works, 3 prolongs 31, and the 3rd path 323 of Y-tube 32 provides the connection of a difference pipeline 324, and the position is set is higher than the 3rd path 323 of first path 321 of Y-tube 32 and alternate path 322, in addition, the prolong 31 of second condensing works 3 makes second condensing works 3 drag for the reality of making water-cooled for can be arranged in the tank 33;

One material-gathering device 34 that is air-tight state is to do being communicated with of difference with first condensing works 2, promptly is material-gathering device 34 is communicated with a branch pipe 324 with the 3rd path 323 of second condensing works, 3 Y-tubes 32.

One collection device 4 that is air-tight state has one first receiving tank 41, one storage area 411 that can supply liquor liquid to collect is arranged in this first receiving tank 4I, and on first receiving tank 41, establish the appropriate position, be to be provided with a feed port 412 and a port 413, and this feed port 412 is to be communicated with the exit end 312 of the prolong 31 of second condensing works 3.In addition, collection device 4 can have second receiving tank 42 that is air-tight state, this second receiving tank 42 is can a sub-feed tube 421 to be connected with the path of 41 of second condensing workss 3, first receiving tank, and be provided with a path control unit 44, so that going into 41 of first receiving tanks, second receiving tank 42 and second condensing works be communicated with for the selection of operability.

One negative pressure generation device 5 is to be communicated with the port 413 of collection device 4 first receiving tanks 41 by a compressed air pipe line 51.So that during negative pressure generation device 5 running, when the path between collection device 4 second receiving tanks 42 and first receiving tank 41 is opened, can provide first receiving tank 41, second receiving tank, 42 inside of evaporation unit 1, material-gathering device 34 and collection device 4 to have a negative pressure, and in the utility model, negative pressure generation device 5 is with the air compressor machine enforcement of oppositely bleeding.

Water distilling apparatus of the present utility model mainly contains following operation steps:

A. fermented liquid is inserted heating in the evaporation unit 1, and the Heating temperature that fermented liquid is remained between 50-80 ℃ is done the distillation operation.

B. when the fermented liquid of a step heats, provide evaporation unit 1 and 4 negative pressure between 500-750mmHg of collection device by negative pressure generation device 5;

C. the aldehyde material that makes in the steam to be contained (or material such as ester, ether, nonfermented candy, five carbon candys) is condensed by first condensing works 3 in advance and collects;

D. the alcohols material that makes in the steam to be contained is condensed by second condensing works 4;

E. make the pure class I liquid I Fractional Collections of d step, and collect methyl alcohol and ethanol respectively.

The utility model is put heating enforcement in eight evaporation units 1 at the fermented liquid of a step, when its fermented liquid is transformed into the gas rising, when gas arrives the circulation space 14 places of evaporation unit 1, the cyclone path that most layer dividing plate 141 are separated, the temperature of vaporised gas is descended, drop to one regularly and work as gas temperature, vaporised gas will be transformed into the globule and fall, when the globule when adding the fermented liquid of pining for, again can Yin Gaowen and be transformed into gas once more and rise, distill enforcement continuously with this, can get the preferable liquor liquid of a quality.

Again, fixedly keeping of Heating temperature is to make heating source 6 with a temperature control unit 61 controls.

Device of the present utility model, in above-mentioned a step, recycle pump 171 runnings are implemented, the fermented liquid that places in the evaporation unit 1 is circulated, except that can making fermented liquid heating the time has preferable heat exchange running, its also can prevent the deposition of vinasse, impurity and produce burn the facts;

In addition, the bump that produces by circulating is to help disengaging of aldehyde material in the fermented liquid, and injects fermented liquid in the evaporation units 1 by recycle pump 171 circulations, and it is to make vaporised gas have the circulation distillatory to implement that its generation has the reality of atomizing to drag.

The utility model is in the enforcement that a negative pressure is provided of b step, for doing an enforcement of bleeding in the storage area 411 that makes 5 pairs of collection device 4 first receiving tanks 41 of negative pressure generation device, make and be evaporation unit 1 airtight and that be communicated with, first receiving tank 41 of material-gathering device 34 and collection device 4, second receiving tank, the 42 inner negative pressure that produce, so that the fermented liquid in the evaporation unit 1 can (30-45 ℃) produce pneumatolysis under lower Heating temperature, and in the utility model, Heating temperature between a 70-80 that step is bestowed ℃, be because fermented liquid is under the negative pressure of 500-750mmHg, Heating temperature between 70-80 ℃, can make the liquor liquid of gained keep under the stable quality, there is steam faster to disengage, can reduce the waste of heating energy source with this, and the distillation benefit that it is taken place down in low temperature also can keep the original fragrance of fermented liquid.

Again, the set catch basin 110 in evaporation unit 1 bottom can make the indirect heating that is heated to be of fermentation, and because evaporation unit 1 respectively is the space of different pressures with catch basin 110, when so fermented liquid is done gasification enforcement in 70-80 ℃ Heating temperature, water in the catch basin 110 can't be evaporated gasification, and the temperature that is provided in the catch basin 110 is in the time of can filling fermented liquid once more in evaporation unit 1, and the temperature of catch basin 110 can improve the preparation temperature of fermented liquid rapidly, and the distillation gas of lifting equalization is arranged.

The utility model is in the enforcement of c collection step based on the material of aldehydes, by the proportion of the aldehyde material characteristic high than alcohols material, make steam the time through first condensing works 2, gasiform aldehyde condenses into liquid in advance, and the setting that the position must be higher than the 3rd path 323 that is provided with of first path 321 with alternate path 322 by Y-tube 32, aqueous aldehyde material can be flowed out by the 3rd path 323 of Y-tube 32, and collect by material-gathering device 34 via difference pipeline 324.

Again, the enforcement of c collection step aldehyde material, because of providing of b step negative pressure arranged, make through first condensing works 2 and as yet not agglomerative steam (alcohols material that proportion is less) can be subjected to the traction of negative pressure to import down second condensation dress tawny daylily 3, it is fused that the agglomerative steam can not produced with the aldehyde material of liquid state, or sewed by difference pipeline 324.

On the Fractional Collections methyl alcohol and ethanol operation of the utility model e step, for disengage the characteristic of methyl alcohol by fermented liquid in advance, and the path control unit 44 that makes collection device 4 earlier makes sub-feed tube 421 selective conductings, can collect the methanol liquid of condensing and disengaging in advance by second receiving tank 42 of collection device 4 by second condensing works 3, and reach one when an amount of in second receiving tank, 42 collecting amounts, path control unit 44 makes closing of sub-feed tube 421 electing property of path, and condensation water is imported in first receiving tank 41 by the prolong 31 of second condensing works 3, as shown in Figure 2, to collect ethanol liquid (being liquor liquid).

Embodiment 2

Consult Fig. 3-shown in Figure 4, for the setting of the receiving tank of collection device 4 quantitatively, the utility model is in parallel the connection to be provided with most receiving tanks, to collect respectively outside methyl alcohol and the ethanol, can collect the liquor liquid of different ethanol concns respectively in addition; Consult shown in Figure 3, collection device 4 is except that having first receiving tank 41 and second receiving tank 42, can be provided with the 3rd receiving tank 43 that at least one is close wall state in addition, the 3rd receiving tank 43 makes one to collect pipeline 431 respectively and be connected with sub-feed tube 421, and make and collect pipeline 431 respectively and reach with being connected to alternate path control unit 45 of sub-feed tube 421, make the 3rd receiving tank 43 and sub-feed tube 421 (i.e. second condensing works 3 and first receiving tank 41) that the selection conducting of operability be arranged.When path control unit 44 makes closing of sub-feed tube 421 electing property of path, and make first receiving tank 41 collect the liquor liquid when a certain amount of, for keeping first receiving tank, 41 collected liquor liquid that higher ethanol concn is arranged, because distillation time is of a specified duration more, the ethanol that distills out is few more, and can contain more water, for making path control unit 44 make the unlatching of sub-feed tube generation 1 electing property of path, and alternate path control unit 45 is collected the unlatching of electing property of pipeline respectively for order, so that the 3rd receiving tank 43 can be collected the lower liquor liquid of ethanol concn, as shown in Figure 4.

Do the collection respectively of different ethanol concns implements for liquor liquid, the utility model is to do the embodiment explanation so that one the 3rd receiving tank 43 to be set, right the utility model can increase according to required receipts ethanol concn number of degrees under, make the quantity that is provided with of the 3rd receiving tank 43 do most interpolations, and and make itself and second condensing works 3 do the selection conducting of operability.

Design of the present utility model still provides the setting of a storage device 7 in addition, this storage device 7 provides storing of fermented liquid to be distilled, and storage device 7 also is communicated with evaporation unit 1 with a carrier pipe road 71, and be provided with a valve body 711 on the carrier pipe road 71 in addition, so, so that evaporation unit 1 domestic demand is when injecting fermented liquid, opening body 711 for order opens, and start negative pressure generation device 5, fermented liquid in the storage device 7 can be inhaled in the evaporation unit 1, and when the fermented liquid in the evaporation unit 1 reach one an amount of after, valve body 711 is to distill operation.In addition, can provide a primary heater unit 712 on the carrier pipe road 71, so that before in the injection of the fermented liquid in the storage device 6 evaporation unit 1, can improve fluid temperature in advance.

From the above, the utility model and traditional continuous still battery equipment are compared down, the utlity model has the advantage of simplifying work flow and implementing structure, and the distillation of fermented liquid that the utility model provides are dragged in fact, can get a colory liquor, real non-traditional continuous still battery equipment can be reached; Moreover the utility model more is better than conventional art in the saving of the filtering of aldehyde material and heating energy source.

In sum, the utility model is that the contriver concentrates one's attention on to study and at first design through actual studying, and has novelty, creativeness and practicality.

Claims

1, a kind of water distilling apparatus of making liquor is characterized in that: it includes the airtight evaporation unit for the ccontaining heating of fermented liquid; First condensing works is communicated with this evaporation unit; The material-gathering device that is air-tight state is done being communicated with of difference with this first condensing works; Second condensing works is done being communicated with of difference with this first condensing works; The collection device that is air-tight state has first receiving tank, and this first receiving tank is to be communicated with second condensing works; The negative pressure generation device is communicated with first receiving tank of this collection device, is a negative pressure state in first receiving tank of this evaporation unit, material-gathering device and collection device.

2, the water distilling apparatus of manufacturing liquor according to claim 1 is characterized in that: this evaporation unit below has a heating source.

3, the water distilling apparatus of manufacturing liquor according to claim 2 is characterized in that: this heating source is provided with the temperature control unit of control Heating temperature.

4, the water distilling apparatus of manufacturing liquor according to claim 1 is characterized in that: this evaporation unit bottom has a catch basin.

5, the water distilling apparatus of manufacturing liquor according to claim 2 is characterized in that: this evaporation unit bottom surface is concaved with a heating chamber, is provided with most smoke pipes in this heating chamber.

6, the water distilling apparatus of manufacturing liquor according to claim 1 is characterized in that: this place, top, evaporation unit internal space establishes to be a circulation space, and the wall of this circulation space is provided with the dividing plate that majority is crisscross arranged.

7, the water distilling apparatus of manufacturing liquor according to claim 1, it is characterized in that: this first condensing works, second condensing works and material-gathering device are the connections of making difference with Y-tube, first path that this Y-tube had is and being connected of this first condensing works exit end, the alternate path of this Y-tube is and being connected of this second condensing works inlet end, and the 3rd path of this Y-tube is and being communicated with of this material-gathering device.

8, the water distilling apparatus of manufacturing liquor according to claim 7 is characterized in that: first path of this Y-tube and the height of alternate path are higher than the 3rd path.

9, the water distilling apparatus of manufacturing liquor according to claim 1, it is characterized in that: this collection device has second receiving tank that is sealed state in addition, and this second receiving tank and path between this second condensing works and first receiving tank are that the selection with operability is communicated with.

10, the water distilling apparatus of manufacturing liquor according to claim 9, it is characterized in that: to be communicated be to reach by a path control unit to the operability of path between this second receiving tank and this second condensing works and first receiving tank, and this second receiving tank, second condensing works and first receiving tank are communicated with simultaneously; Or this second condensing works is communicated with this second receiving tank path blockade with first receiving tank.

11, the water distilling apparatus of manufacturing liquor according to claim 9, it is characterized in that: this collection device has at least one the 3rd receiving tank that is sealed state in addition, and the path between the 3rd receiving tank and this second condensing works and first receiving tank and second receiving tank are communicated with the selection of operability.

12, the water distilling apparatus of manufacturing liquor according to claim 11 is characterized in that: it is to reach by the alternate path control unit that the 3rd receiving tank is communicated with operability between this second condensing works, first receiving tank, second receiving tank.

13, the water distilling apparatus of manufacturing liquor according to claim 1 is characterized in that: this negative pressure generation device is the blast machine.

14, the water distilling apparatus of manufacturing liquor according to claim 1 is characterized in that: this evaporation unit is communicated with a storage device by a carrier pipe road.

15, the water distilling apparatus of manufacturing liquor according to claim 14 is characterized in that: this carrier pipe road is provided with valve body.

16, the water distilling apparatus of manufacturing liquor according to claim 14 is characterized in that: this carrier pipe road is provided with a primary heater unit.

17, the water distilling apparatus of manufacturing liquor according to claim 1 is characterized in that: this evaporation unit has a circulation device.