CN202279814U - Evaporative-cooling white spirit distilling condenser - Google Patents
Evaporative-cooling white spirit distilling condenser Download PDFInfo
- Publication number
- CN202279814U CN202279814U CN2011204299809U CN201120429980U CN202279814U CN 202279814 U CN202279814 U CN 202279814U CN 2011204299809 U CN2011204299809 U CN 2011204299809U CN 201120429980 U CN201120429980 U CN 201120429980U CN 202279814 U CN202279814 U CN 202279814U
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- transpiration
- water
- spray equipment
- water tank
- evaporative
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Abstract
The utility model relates to an evaporative-cooling white spirit distilling condenser which is characterized by comprising a shell, wherein the lower part of the shell is provided with a water tank; an evaporative-cooling heat exchanger and a spray device are installed on two side walls of the shell above the water tank; a water circulating pump is connected with the water tank and the spray device through water pipes; an exhaust blower is arranged on the side wall of the shell below the evaporative-cooling heat exchanger and the spray system; an air inlet is arranged above the heat exchanger and the spray device on the side wall of the shell opposite the exhaust blower; the inner side of the exhaust blower is provided with a demister; one side of the shell is provided with an end socket; an outlet pipe of the evaporative-cooling heat exchanger extends to the bottom of the end socket; and the upper part of the end socket is provided with a spirit discharge pipe which is connected with a spirit tank. The evaporative-cooling heat exchanger and the circulating water spraying are utilized, so that the spirit fume is subjected to reinforced heat exchange at the evaporative-cooling heat exchanger, thereby enhancing the heat exchange efficiency and the condensing efficiency of the spirit fume, increasing the yield of the white spirit, reducing the consumption of the cooling water and saving the water resources.
Description
Technical field
The utility model relates to a kind of condensing works, especially relates to a kind of transpiration-cooled white liquor distilling condensing works.
Background technology
Distillation is an important step during liquor is produced, and in still-process, wine vapour is produced finished product liquor at condensing works through the condensation cooling.At present, the condensing surface that white liquor distilling is used is introduced wine vapour in the condensing surface through pipeline usually, and water coolant and wine vapour directly carry out heat exchange through duct wall in condensing surface, and the hot water that forms after the heat exchange is directly discharged.Because carry out nature and the nonreinforcement heat exchange between wine vapour in condensing surface and the water coolant, the efficient of heat exchange is low, condensing temperature is higher, and the condensation efficiency of wine vapour is low, and simultaneously, cooling water consumption is big, causes the great amount of water resources waste.
The utility model content
The applicant has carried out research and has improved to above-mentioned problem, and a kind of transpiration-cooled white liquor distilling condensing works is provided; Improve the condensation efficiency of heat exchange efficiency and wine vapour, reduce the condensing temperature of wine vapour, improve liquor output; Reduce cooling-water consumption simultaneously, save water resources significantly.
In order to solve the problems of the technologies described above, the utility model adopts following technical scheme:
A kind of transpiration-cooled white liquor distilling condensing works; Comprise casing, the casing bottom is provided with water tank, and transpiration cooling interchanger and spray equipment are installed between two sidewalls of the casing above the water tank; Water circulating pump connects water tank and spray equipment through water pipe; The fan device is on the chassis sidewall below said transpiration cooling interchanger and the spray equipment, and blast inlet is arranged on the chassis sidewall relative with said fan in the top of interchanger and spray equipment, and the inboard of fan is provided with mist eliminator; One side of said casing is provided with end socket, and the outlet pipe of said transpiration cooling interchanger extends to the bottom of said end socket, and the top of said end socket is provided with wine drainage tube, and said wine drainage tube connects the wine jar.
Further:
Said transpiration cooling interchanger and spray equipment tilt to be installed between two sidewalls of the casing above the water tank.
Said transpiration cooling interchanger and spray equipment level are installed between two sidewalls of the casing above the water tank, and said transpiration cooling interchanger is a hyperchannel plate-fin dew point indirect evaporation cooling heat exchanger.
The inboard of said mist eliminator is provided with window shutter.
Be provided with the baffle plate of inclination before the said window shutter.
Said blast inlet place is provided with window shutter, is provided with flow deflector between said blast inlet and the said spray equipment.
The technique effect of the utility model is:
The disclosed a kind of transpiration-cooled white liquor distilling condensing works of the utility model utilizes transpiration cooling interchanger and recirculated water spray, makes fume strengthen heat exchange at the transpiration cooling interchanger; Improve the condensation efficiency of heat exchange efficiency and wine vapour; Reduce the condensing temperature of wine vapour, improve liquor output, reduce cooling-water consumption simultaneously; Save water resources significantly, advanced condensing equipment is provided to the traditional white liquor distilling technology of China.
Description of drawings
Fig. 1 is the structural representation of the utility model embodiment 1.
Fig. 2 is the structural representation of the utility model embodiment 2.
Embodiment
Below in conjunction with accompanying drawing the embodiment of the utility model is done further detailed explanation.
Embodiment 1
As shown in Figure 1; The utility model comprises casing 1; Casing 1 bottom is provided with water tank 9, and transpiration cooling interchanger 4 and spray equipment 5 inclination devices are between two sidewalls of the casing above the water tank 9, and water circulating pump 8 connects water tank 9 and spray equipment 5 through water pipe 7; In the present embodiment, water circulating pump 8 is a submersible pump.Fan 2 devices are on the sidewall of the casing 1 below transpiration cooling interchanger 4 and the spray equipment 5; In the top of transpiration cooling interchanger 4 and spray equipment 5 blast inlet 6 is set on the chassis sidewall relative with fan 2; Blast inlet 6 is provided with the air intake window shutter; Be provided with flow deflector 16 between blast inlet 6 and the spray equipment 5, flow deflector 16 can be the air-flow guiding that gets into spray equipment 5.The inboard of fan 2 is provided with mist eliminator 3; Mist eliminator 3 inboards are provided with window shutter 14; Be provided with the baffle plate 15 of inclination before the window shutter 14, window shutter 14 can suitably be regulated the wind direction that gets into mist eliminator 3, and baffle plate 15 blocks the inboard the place ahead at fan 2; The vaporific water droplet that top flows down is got into water tank 9 by baffle plate 15 resistance shelves, and reduces vaporific water droplet entering mist eliminator 3.Fan 2 and blast inlet 6 arranged transverselys, the air intake window shutter on the blast inlet 6 can suitably be regulated the air intake direction.One side of casing 1 is provided with end socket 10, and the outlet pipe 11 of transpiration cooling interchanger 4 extends to the bottom of end socket 10, and the top of end socket 10 is provided with wine drainage tube 12, and wine drainage tube 12 connects wine jar 13.In the present embodiment, transpiration cooling interchanger 4 adopts plate-fin transpiration cooling interchanger.
In use; The import 401 of transpiration cooling interchanger 4 connects the white liquor distilling device; The wine vapour that the white liquor distilling device distills out is strengthened heat exchange at transpiration cooling interchanger 4, and wine vapour is condensed into liquid drinks, flows into end socket 10; Drinks in the end socket 10 enter wine jar 13 through the wine drainage tube 12 on its top, become the liquor of finished product; Simultaneously under the effect of fan 2; Airflow gets into transpiration-cooled white liquor distilling condensing works from blast inlet 6; Transpiration-cooled white liquor distilling condensing works hollow air-flow by Fig. 1 in the arrow A direction pass through transpiration cooling interchanger 4 from top to bottom; Water circulating pump 8 passes through transpiration cooling interchanger 4 with the water in the water tank 9 from top to bottom through spray equipment 5, forms moisture film on the surface of transpiration cooling interchanger 4, and the transpiration cooling interchanger 4 that is evaporated to by airflow and spray moisture film dispels the heat like this; Simultaneously the wine vapour in the transpiration cooling interchanger 4 is strengthened heat exchange, airflow is removed water smoke by mist eliminator 3 before getting into fan 2.Owing to adopt the heat exchange method of spraying and sprinkling evaporation, not only improve the efficient of heat exchange, reduce the condensing temperature of wine vapour; Improve liquor output; And can reduce the use of water coolant in a large number, and since spray water flow to consistent with airflow direction, spray water is evenly distributed; The spray water loss significantly reduces, thereby reaches the purpose of further water saving.
Embodiment 2
As shown in Figure 2; Compare with embodiment 1; Transpiration cooling interchanger 4 adopts hyperchannel plate-fin dew point indirect evaporation cooling heat exchanger in the present embodiment, and transpiration cooling interchanger 4 and spray equipment 5 levels are installed between two sidewalls of the casing above the water tank, and other structure is identical with embodiment 1.The hyperchannel plate-fin dew point indirect evaporation cooling heat exchanger that present embodiment adopted, the applicant is open (application number: 201110029354.5), no longer specify at this in application for a patent for invention.
Hyperchannel plate-fin dew point indirect evaporation cooling heat exchanger is provided with cold wind import 402; Cold wind import 402 connects blower fan during use; To hyperchannel plate-fin dew point indirect evaporation cooling heat exchanger cold dry air is provided by blower fan, the flow through dry air passage of hyperchannel plate-fin dew point indirect evaporation cooling heat exchanger of cold dry air; The air-flow that the vaporific spray water of spray equipment 5 and fan 2 air drafts form gets into the wet air passage of hyperchannel plate-fin dew point indirect evaporation cooling heat exchanger; Wine vapour in wet air passage and dry air passage and the hot media channel is strengthened heat exchange, and wine vapour cools and is condensed into drinks.The heat exchanger effectiveness of this condensation process is higher; Under the situation of not using refrigerator and refrigeration agent, can wine vapour be cooled near the air dew point temperature; Realize the temperature drop bigger than other transpiration cooling interchanger; The condensation efficiency of wine vapour is higher, not only reduces energy consumption, and saves great amount of water resources.
Claims (6)
1. transpiration-cooled white liquor distilling condensing works; It is characterized in that: comprise casing; The casing bottom is provided with water tank; Transpiration cooling interchanger and spray equipment are installed between two sidewalls of the casing above the water tank, and water circulating pump connects water tank and spray equipment through water pipe, and the fan device is on the chassis sidewall below said transpiration cooling interchanger and the spray equipment; Blast inlet is arranged on the chassis sidewall relative with said fan in the top of interchanger and spray equipment, and the inboard of fan is provided with mist eliminator; One side of said casing is provided with end socket, and the outlet pipe of said transpiration cooling interchanger extends to the bottom of said end socket, and the top of said end socket is provided with wine drainage tube, and said wine drainage tube connects the wine jar.
2. according to the described transpiration-cooled white liquor distilling of claim 1 condensing works, it is characterized in that: said transpiration cooling interchanger and spray equipment tilt to be installed between two sidewalls of the casing above the water tank.
3. according to the described transpiration-cooled white liquor distilling of claim 1 condensing works; It is characterized in that: said transpiration cooling interchanger and spray equipment level are installed between two sidewalls of the casing above the water tank, and said transpiration cooling interchanger is a hyperchannel plate-fin dew point indirect evaporation cooling heat exchanger.
4. according to claim 2 or 3 described transpiration-cooled white liquor distilling condensing workss, it is characterized in that: the inboard of said mist eliminator is provided with window shutter.
5. according to the described transpiration-cooled white liquor distilling of claim 4 condensing works, it is characterized in that: the baffle plate that is provided with inclination before the said window shutter.
6. according to claim 2 or 3 described transpiration-cooled white liquor distilling condensing workss, it is characterized in that: said blast inlet place is provided with window shutter, is provided with flow deflector between said blast inlet and the said spray equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204299809U CN202279814U (en) | 2011-11-03 | 2011-11-03 | Evaporative-cooling white spirit distilling condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204299809U CN202279814U (en) | 2011-11-03 | 2011-11-03 | Evaporative-cooling white spirit distilling condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202279814U true CN202279814U (en) | 2012-06-20 |
Family
ID=46225989
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204299809U Expired - Fee Related CN202279814U (en) | 2011-11-03 | 2011-11-03 | Evaporative-cooling white spirit distilling condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202279814U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111500401A (en) * | 2020-04-28 | 2020-08-07 | 重庆盛山酒业有限公司 | Spray type internal cooling distillation device |
-
2011
- 2011-11-03 CN CN2011204299809U patent/CN202279814U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111500401A (en) * | 2020-04-28 | 2020-08-07 | 重庆盛山酒业有限公司 | Spray type internal cooling distillation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120620 Termination date: 20161103 |