CN2763277Y - Distillation and condensation equipment for liquor - Google Patents
Distillation and condensation equipment for liquor Download PDFInfo
- Publication number
- CN2763277Y CN2763277Y CNU2005200328722U CN200520032872U CN2763277Y CN 2763277 Y CN2763277 Y CN 2763277Y CN U2005200328722 U CNU2005200328722 U CN U2005200328722U CN 200520032872 U CN200520032872 U CN 200520032872U CN 2763277 Y CN2763277 Y CN 2763277Y
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- condensing
- condenser
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Abstract
The utility model discloses a white spirit distillation and condensing device, which comprises at least one condenser. The condensing device is provided with a condensing chamber (11) which is formed by the encirclement of a shell body, a steam inlet pipe (12) and a steam outlet pipe (13) used for wine steam in and out, and a wine discharge pipe (14) used for discharging the wine from the condensing chamber (11), wherein the steam inlet pipe (12) and the steam outlet pipe (13) are communicated with the condensing chamber (11); a condensing pipe (40) used for passing cooling water passes through the condensing chamber (11). The utility model has the advantages that wine steam enters the condensing chamber from the steam inlet pipe arranged on the upper part of the condensing chamber, and the cooling water continuously flows through the condensing chamber from bottom to top in the condensing pipe; the cooling water and the wine steam carry out the forceful countercurrent heat exchange; the heat exchange efficiency is high, and the condensing and the cooling are thorough, thereby, the consumption for cooling water is reduced.
Description
Technical field
The utility model relates to a kind of condensing works, relates in particular to the condensing works that is used for white liquor distilling.
Background technology
Distillation is an important step during liquor is produced.In this step, make ethanol and other fragrance matters in the wine unstrained spirits be vaporized into wine vapour by the distillation of wine rice steamer, again wine vapour is introduced condensing works and produced finished product liquor through the condensation cooling.
At present, the condensing works of white liquor distilling is by an open container with place condenser in this container etc. to form.Since liquor and distillation plant appearred in the Tang Dynasty, the liquor production process technique variation was big, and the structural changes of condensing works is little, only improves to some extent on material, as adopting tin the earliest, then is improved to aluminium, then changed stainless steel over past ten years into and made.During production, by pipeline wine vapour is introduced in the condenser, water coolant is entered by container bottom, and water coolant and wine vapour carry out heat exchange, after the hot water that forms after the heat exchange is overflowed naturally by the top of container, enters in the ditch and flows away.
Mainly there is the defective of following two aspects in existing condensing works:
One, the weak effect of heat exchange, consumption of cooling-water is big
Water coolant is entered for one jiao by container bottom, local flow from bottom to top in container, owing to can form away short circuit during flow of cooling water, not comprehensive with contacting of condenser, carry out the partial non-imposed heat exchange of nature with the wine vapour in the condenser, the weak effect of its heat exchange, so consumption of cooling-water is big.Because container is open, hot water can't carry out recycling, not only caused a large amount of waves of water resources useless, also because the hot water temperature's higher (about 60 ℃) who discharges, the inflow stream ditch is with after ditch-water mixes, the ditch water temp is 30～40 ℃, and the very suitable microbial growth of this temperature is breeding, easily causes river to foul and water resource pollution;
Two, influence the yield of liquor and vinosity
The distillation of liquor mainly is to extract ethanol and ethanol is concentrated, and proposes the fragrance matter in the wine unstrained spirits, i.e. " give birth to perfume by fermentation, Titian is by distilling ".On same condensing works, successively finish the extraction of foreshot, finished wine, wine tail in chronological order, the classification of wine also with the operator through examining the hops decision, vinosity is difficult for guaranteeing.In addition, the fragrance ingredient in the liquor is very micro-, and improper if when distillation operation control has slightly, fragrance matter (particularly lower boiling composition) and ethanol can be gaseous phase runs away from the steam outlet pipe of condenser, thereby has influenced the quality and the productive rate of liquor.
The utility model content
Technical problem to be solved in the utility model provides a kind of white liquor distilling condensing works, and it has good heat exchange efficient and condensation cooling performance, can reduce consumption of cooling-water significantly.
The technical scheme that its technical problem that solves the utility model adopts is: white liquor distilling condensing works of the present utility model, include at least one condenser, it is characterized in that: described condenser has the condensing chamber that is surrounded by housing, with steam inlet pipe, the steam outlet pipe that communicate with this condensing chamber for the turnover of wine vapour, and the wine drainage tube of wine being discharged condensing chamber; The prolong that passes through for water coolant passes through described condensing chamber.
In technique scheme, described steam inlet pipe is positioned at the top of condensing chamber, and described steam outlet pipe is positioned at the bottom of condensing chamber, and described wine drainage tube then is positioned at the lower end of condensing chamber.
The beneficial effects of the utility model are, wine vapour is entered in the condensing chamber by the steam inlet pipe on condensing chamber top, the water coolant condensing chamber that then in prolong, from bottom to top continued to flow, water coolant and wine vapour carry out compulsory counterflow heat exchange, its heat exchange efficiency height, the condensation cooling is comparatively thorough, thereby consumption of cooling-water is minimized.
Condensing works of the present utility model can be made up of an above-mentioned condenser, also can be composed in series by pipeline by the above-mentioned condenser more than two or two.Under a kind of situation in back, the steam inlet pipe of back first-stage condenser links to each other with the steam outlet pipe of previous stage condenser, and the water shoot of back first-stage condenser links to each other with the water inlet pipe of previous stage condenser, and the cooled liquor of condensation is discharged from the wine outlet of every condenser lower end.The condensing works that the condenser plural serial stage forms utilizes the temperature difference relation of water coolant and wine vapour, the repeats condensation cooling, wine vapour condensation cooling fully, productive rate is improved, fragrance matter extracts fully, help improving vinosity, and water coolant repeatedly utilizes the further consumption of cooling-water that reduced, utilize the temperature head between each condensing chamber, then can realize the grading extraction of institute's output liquor in the condensation process.
The initial input aperture of water coolant be the most not the level condenser water inlet pipe, the water coolant delivery port is the water shoot of first step condenser.The temperature of each condensing chamber and mutual temperature head can be made things convenient for and ideal control by the flow of adjusting the input aperture water coolant.
For helping the realization of temperature head between each condensing chamber, adapt to the temperature difference relation of water coolant and wine vapour better, in the above-mentioned condensing works, rise by first step condenser, the heat exchange area of each condenser successively decreases successively.
Description of drawings
This specification sheets comprises following four width of cloth accompanying drawings:
Fig. 1 is the structural representation of the utility model condensing works;
Fig. 2 is the sectional view along A-A line among Fig. 1;
Fig. 3 is the sectional view along B-B line among Fig. 1;
Among Fig. 4 condensing works of the present utility model is applied to the synoptic diagram of a kind of arrangement form of white liquor distilling production
Component, position and numbering among the figure: first step condenser 1, second stage condenser 2, third stage condenser 3, housing 10, condensing chamber 11, steam inlet pipe 12, steam outlet pipe 13, wine drainage tube 14, row's aldehyde device 14, upper casing 20, drip chamber 21, water shoot 22, lower casing 30, intake chamber 31, water inlet pipe 32, prolong 40.
Embodiment
Below in conjunction with drawings and Examples the utility model is further specified.
A condenser that includes at least as shown in Figure 1 of the present utility model, this condenser has the condensing chamber 11 that is surrounded by housing 10, with steam inlet pipe 12, the steam outlet pipe 13 that communicate with this condensing chamber 11 for the turnover of wine vapour, and wine discharged the wine drainage tube 14 of condensing chamber 11, there are the some prolongs 40 that pass through for water coolants to pass through described condensing chamber 11.
Condenser can be settled at any angle.Shown in Fig. 1 is vertical state, and steam inlet pipe 12 is positioned at the top of condensing chamber 11, and steam outlet pipe 13 is positioned at the bottom of condensing chamber 11,14 lower ends that are positioned at condensing chamber 11 of wine drainage tube.Wine vapour enters in the condensing chamber 11 by the steam inlet pipe 12 on condensing chamber 11 tops, the water coolant condensing chamber 11 that then in prolong 40, from bottom to top continued to flow, water coolant and wine vapour carry out compulsory counterflow heat exchange, its heat exchange efficiency height, the condensation cooling is comparatively thorough, thereby consumption of cooling-water is minimized.
As Fig. 1, Fig. 2, shown in Figure 4, also be connected with upper casing 20, lower casing 30 respectively in housing 10 upper ends, lower end, wherein: upper casing 20 has the drip chamber 21 that communicates with prolong 40 water outlets, and the water shoot 22 that communicates with this drip chamber 21; Lower casing 30 has the intake chamber 31 that communicates with prolong 40 water-ins, and the water inlet pipe 32 that communicates with this intake chamber 31.For ease of the cleaning of incrustation scale, upper casing 20, lower casing 30 and housing 10 removably connect by bolt etc.
Prolong 40 can be tubulation, the serpentine tube of setting or the pipe of the shape that rises in the shape of a spiral.Serpentine tube, spiral tube can further increase heat interchanging area, and straight tube is convenient processing and manufacture then, also are convenient to routine maintenance and incrustation scale and clean.
Condensing works of the present utility model can be made up of an above-mentioned condenser, also can be composed in series by pipeline by the above-mentioned condenser more than two or two.As shown in Figure 2, condensing works is composed in series by pipeline by a plurality of condensers, and promptly the steam inlet pipe of back first-stage condenser links to each other with the steam outlet pipe of previous stage condenser, and the water shoot of back first-stage condenser links to each other with the water inlet pipe of previous stage condenser.
As shown in Figure 2, the initial input aperture of water coolant be the most not the level condenser water inlet pipe, this water inlet pipe is provided with the valve of controlled chilling discharge, the water coolant delivery port is the water shoot of first step condenser, on this water shoot indicating thermometer can be set.For helping the realization of temperature head between each condensing chamber, adapt to the temperature difference relation of water coolant and wine vapour better, rise by first step condenser, the heat exchange area of each condenser successively decreases successively.
Embodiment:
Fig. 4 shows a kind of composition-formed of the utility model condensing works.As shown in the drawing, condensing works is composed in series by first step condenser 1, second stage condenser 2, third stage condenser 3.The wine vapour that comes out from the liquor rice steamer, at first enter first step condenser 1, the wine that is not condensed at first step condenser 1 enters second stage condenser 2, the wine vapour (on a small quantity) that is not condensed in the second stage condenser 2 enters third stage condenser 3, will be by all condensation coolings in final a spot of wine vapour third stage condenser 3.The initial input aperture of water coolant is the water inlet pipe of third stage condenser 3, and this water inlet pipe is provided with the valve of controlled chilling discharge.The water coolant delivery port is the water shoot of first step condenser 1, and this water shoot is provided with indicating thermometer.Water coolant at first enters third stage condenser 3, enter second stage condenser 2 then, enter first step condenser 1 again, heat of condensation (high temperature and low temperature) realizes adverse current pressure heat exchange in condensing works, wine vapour is the multiple condensation cooling in three grades of condensers, make wine vapour can obtain abundant condensation cooling and " race wine " phenomenon can not occur, its technique effect is very desirable.Cool off of wine drainage tube 14 outflows of the liquor of generation from each condenser lower end through condensation.
The condensing works of present embodiment has utilized the temperature difference relation of water coolant and wine vapour, the repeats condensation cooling, wine vapour condensation cooling fully, productive rate is improved, fragrance matter extracts fully, help improving vinosity, and water coolant repeatedly utilizes the further consumption of cooling-water that reduced, utilize the temperature head between each condensing chamber, then can realize the grading extraction of institute's output liquor in the condensation process.
For helping the realization of temperature head between each condensing chamber, adapt to the temperature difference relation of water coolant and wine vapour better, from first step condenser 1, the heat exchange area of each condenser successively decreases successively.In the present embodiment, the heat exchange area of three grades of condensers is followed successively by 6m
2, 4m
2, 2m
2
Three grades of interior wine vapour, temperature of cooling water and temperature difference of condensing chamber concern as following table:
| First step condenser 1 | Second stage condenser 2 | | The input aperture | |
| Water coolant | 60～70 | 40～50 | 30～40 | 10～15℃ |
| Wine vapour | 100℃ | 80～90℃ | 60～70℃ |
The temperature of each condensing chamber and mutual temperature head can be controlled easily by the cooling water flow that adjustment enters third stage condenser 3.
As shown in Figure 4, the wine drainage tube of third stage condenser 3 is provided with row's aldehyde device 15, gets rid of the unwanted lower boiling aldehyde type impurities of small part by the water temperature in control exit, improves liquor mouthfeel, not Shang Tou purpose to reach.
As shown in Figure 4, the hot water that the cooling back forms is delivered to elevated tank by the water shoot of first step condenser 1, can carry out secondary and utilize again, as be used for raw materials for production spice and wine unstrained spirits cooling water and domestic water etc., but save energy, water resources and reduce production costs.
It is pointed out that top described principles more of the present utility model that just explain through diagrams, because the those of ordinary skill in constructed field is easy to carry out on this basis some modifications and change.Therefore, this specification sheets be not be the utility model to be confined to shown in and in described concrete structure and the scope of application, so every the corresponding modify and equivalent that might be utilized all belongs to the claim that the utility model is applied for.
Claims (10)
1, a kind of white liquor distilling condensing works, include at least one condenser, it is characterized in that: described condenser has the condensing chamber (11) that is surrounded by housing (10), with steam inlet pipe (12), the steam outlet pipe (13) that communicate with this condensing chamber (11) for the turnover of wine vapour, and the wine drainage tube (14) of wine being discharged condensing chamber (11); The prolong (40) that passes through for water coolant passes through described condensing chamber (11).
2, white liquor distilling condensing works according to claim 1 is characterized in that: described steam inlet pipe (12) is positioned at the top of condensing chamber (11); Described steam outlet pipe (13) is positioned at the bottom of condensing chamber (11); Described wine drainage tube (14) then is positioned at the lower end of condensing chamber (11).
3, white liquor distilling condensing works according to claim 1, it is characterized in that: described housing (10) upper end, lower end also are connected with upper casing (20), lower casing (30) respectively, wherein: upper casing (20) has the drip chamber (21) that communicates with prolong (40) water outlet, and the water shoot (22) that communicates with this drip chamber (21); Lower casing (30) has the intake chamber (31) that communicates with prolong (40) water-in, and the water inlet pipe (32) that communicates with this intake chamber (31).
4, white liquor distilling condensing works according to claim 1 is characterized in that: described upper casing (20), lower casing (30) removably connect with housing (10).
5, white liquor distilling condensing works according to claim 1 is characterized in that: described prolong (40) can be the pipe of vertical tubulation, serpentine tube or the shape that rises in the shape of a spiral.
6, white liquor distilling condensing works according to claim 1, it is characterized in that: described condensing works is composed in series by pipeline by a plurality of condensers, promptly the steam inlet pipe (12) of back first-stage condenser links to each other with the steam outlet pipe of previous stage condenser, and the water shoot of back first-stage condenser links to each other with the water inlet pipe of previous stage condenser.
7, white liquor distilling condensing works according to claim 6 is characterized in that: in the described condensing works, the initial input aperture of water coolant be the most not the level condenser water inlet pipe, this water inlet pipe is provided with the valve of controlled chilling discharge; The water coolant delivery port is the water shoot of first step condenser, and this water shoot is provided with indicating thermometer.
8, white liquor distilling condensing works according to claim 6 is characterized in that: in the described condensing works, risen by first step condenser, the heat exchange area of each condenser successively decreases successively.
9, white liquor distilling condensing works according to claim 6 is characterized in that: in the described condensing works, the most the wine drainage tube of level condenser is not provided with row's aldehyde device (15).
10, according to any described white liquor distilling condensing works in the claim 6～9, it is characterized in that: described condensing works is composed in series by first step condenser (1), second stage condenser (2), third stage condenser (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2005200328722U CN2763277Y (en) | 2005-01-18 | 2005-01-18 | Distillation and condensation equipment for liquor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2005200328722U CN2763277Y (en) | 2005-01-18 | 2005-01-18 | Distillation and condensation equipment for liquor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2763277Y true CN2763277Y (en) | 2006-03-08 |
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ID=36140824
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2005200328722U Expired - Fee Related CN2763277Y (en) | 2005-01-18 | 2005-01-18 | Distillation and condensation equipment for liquor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2763277Y (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104178405A (en) * | 2013-05-22 | 2014-12-03 | 贵州国台酒庄有限公司 | Condensation device of wine steam produced by distillation of wine brewing industry |
| CN104593212A (en) * | 2015-01-21 | 2015-05-06 | 贵州茅台酒股份有限公司 | Condenser structure for receiving wine at high temperature |
| CN106148146A (en) * | 2016-08-31 | 2016-11-23 | 湖北稻花香酒业股份有限公司 | Condenser automatic water-saving temperature control system and control method |
| CN107586685A (en) * | 2017-10-23 | 2018-01-16 | 泸州品创科技有限公司 | Board-like white wine condenser |
| CN108148707A (en) * | 2018-02-08 | 2018-06-12 | 平南县科力酿酒机械制造有限公司 | White spirit brewing technique |
| CN108165440A (en) * | 2018-02-08 | 2018-06-15 | 平南县科力酿酒机械制造有限公司 | Distillation brewing equipment |
| CN108753557A (en) * | 2018-06-12 | 2018-11-06 | 安徽省强家庄生态农业有限公司 | A kind of cooling device in wine processing |
| CN111544918A (en) * | 2020-05-19 | 2020-08-18 | 常州海克莱化学有限公司 | Condensing equipment for distillation plant |
| CN113214954A (en) * | 2021-06-17 | 2021-08-06 | 劲牌有限公司 | Distillation device for reducing proportion of white spirit tails and application thereof |
-
2005
- 2005-01-18 CN CNU2005200328722U patent/CN2763277Y/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104178405A (en) * | 2013-05-22 | 2014-12-03 | 贵州国台酒庄有限公司 | Condensation device of wine steam produced by distillation of wine brewing industry |
| CN104593212A (en) * | 2015-01-21 | 2015-05-06 | 贵州茅台酒股份有限公司 | Condenser structure for receiving wine at high temperature |
| CN104593212B (en) * | 2015-01-21 | 2017-02-22 | 贵州茅台酒股份有限公司 | Condenser structure for receiving wine at high temperature |
| CN106148146A (en) * | 2016-08-31 | 2016-11-23 | 湖北稻花香酒业股份有限公司 | Condenser automatic water-saving temperature control system and control method |
| CN107586685A (en) * | 2017-10-23 | 2018-01-16 | 泸州品创科技有限公司 | Board-like white wine condenser |
| CN108148707A (en) * | 2018-02-08 | 2018-06-12 | 平南县科力酿酒机械制造有限公司 | White spirit brewing technique |
| CN108165440A (en) * | 2018-02-08 | 2018-06-15 | 平南县科力酿酒机械制造有限公司 | Distillation brewing equipment |
| CN108753557A (en) * | 2018-06-12 | 2018-11-06 | 安徽省强家庄生态农业有限公司 | A kind of cooling device in wine processing |
| CN111544918A (en) * | 2020-05-19 | 2020-08-18 | 常州海克莱化学有限公司 | Condensing equipment for distillation plant |
| CN113214954A (en) * | 2021-06-17 | 2021-08-06 | 劲牌有限公司 | Distillation device for reducing proportion of white spirit tails and application thereof |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |