CN106281824A - A kind of red wine distilling apparatus - Google Patents
A kind of red wine distilling apparatus Download PDFInfo
- Publication number
- CN106281824A CN106281824A CN201610645875.6A CN201610645875A CN106281824A CN 106281824 A CN106281824 A CN 106281824A CN 201610645875 A CN201610645875 A CN 201610645875A CN 106281824 A CN106281824 A CN 106281824A
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- China
- Prior art keywords
- distillation column
- tower
- preheating
- stock solution
- pipeline
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12G—WINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
- C12G1/00—Preparation of wine or sparkling wine
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
- C12H6/00—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages
- C12H6/02—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages by distillation
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Food Science & Technology (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
nullThe open a kind of red wine distilling apparatus of the present invention，Including preheating tower、Stock solution preheating pipe、Distillation column、Hot water circulating pump、Stock solution entrance、Stock solution exports、The distillation column pipeline of stock solution、Stock solution is to distillation column entrance、Distillation column exports、Condensation pipe、Red wine exports、Preheating water pipeline、Water vapour pipeline、Condensing tower，Distillation column one sidewall is provided with steam entry，Another sidewall of distillation column is provided with distillation column entrance，Distillation column entrance is connected by pipeline preheating tower，Distillation column top is provided with distillation column outlet，Distillation column outlet connects the condensation pipe having condensing tower，Condensing tower bottom is provided with wine liquid outlet，Condensing tower is connected to bottom preheating tower by the pipeline with hot water circulating pump，Stock solution entrance it is provided with bottom preheating tower，Preheating water pipeline and condensing water conduit it is also associated with between preheating tower and condensing tower，Between two towers, water (flow) direction is for be flowed to condensing tower by preheating tower by hot water circulating pump.
Description
Technical field
The invention belongs to Spirit technical field, particularly relate to a kind of red wine distilling apparatus.
Background technology
The distillation mode of red wine is to squeeze in boiler by the red wine stock solution of brew by circulating pump at present, traditional method
For directly heating bottom distillation column, it is easily caused distillation wine liquid and is heated inequality and bottom more part of being heated easily does pot, from
And affect distilling effect.The new-type distillation equipment of one set forth in the present invention, employing high-temperature steam inflow pipeline, and distillation pipeline
Trickle in distillation column inner loop, on the one hand can ensure that distillate is heated evenly, it is to avoid the situation of dry pot occurs, on the other hand
High-temperature steam is for recycling, and amount of residual heat may be used for preheating distillate, thus it is the most reduced to reach recycling of energy
The effect of the energy-saving and emission-reduction of thermal losses.
Summary of the invention
It is contemplated that overcome the defect of prior art, it is provided that a kind of red wine distilling apparatus, mainly distill work with red wine
Skill.Have steam temperature, flow velocity is controlled, it is to avoid the feature of the degree of viscous pot.
In order to solve above-mentioned technical problem, the present invention provides techniques below scheme:
A kind of red wine distilling apparatus, including preheating tower 1, stock solution preheating pipe 2, distillation column 3, hot water circulating pump 4, stock solution entrance 5,
Stock solution outlet 6, distillation column pipeline 7, distillation column entrance 8, distillation column outlet 9, condensation pipe 10, wine liquid outlet 11, preheating water pipe
Road 12, water vapour pipeline 13, condensing tower 14, distillation column 3 one sidewall is provided with steam entry 13, and another sidewall of distillation column 3 sets
Being equipped with distillation column entrance 8, distillation column entrance 8 is connected by pipeline has preheating tower 1, distillation column 3 top to be provided with distillation column outlet
9, distillation column outlet connects the condensation pipe 10 having condensing tower 14, and condensing tower 14 bottom is provided with wine liquid outlet 11, and condensing tower leads to
Cross the pipeline with hot water circulating pump 4 and be connected to bottom preheating tower 1, bottom preheating tower, be provided with stock solution entrance 5, preheating tower 1 with
Being also associated with preheating water pipeline 12 and condensing water conduit 10 between condensing tower 14, between two towers, water (flow) direction is for be led to by preheating tower 1
Superheated water circulating pump 4 flows to condensing tower 14.
Further, the hot water in condensing tower flows into preheating tower 1 by preheating water pipeline 12 and has preheated, and is cooled in by heat
Water-circulating pump 4 flows into condensing tower 14, completes a circulation of remaining silent.
Further, stock solution entrance 5 connects circulating pump motor.
Compared with prior art, the present invention has a following beneficial effect:
Benefit of the invention is, steam temperature, and flow velocity is controlled, compared with Conventional espresso method both flame mode of heating, and pole
The degree of viscous pot is avoided in big degree.The material that cannot evaporate gradually is precipitated to bottom distillation column, convenient periodically process.At energy
Amount utilize aspect, utilize water vapour heat distillation while, heat is tentatively sent to condensing tower and preheating tower, stock solution by
Low temperature has, during evaporation, the process slowly promoted, the utilization ratio of the energy simultaneously also improved, to a certain extent
Reduce coal-fired usage amount.The excretion of harmful gas is reduced during producing.The quality of red wine also has certain carrying
Rise.
Accompanying drawing explanation
Fig. 1 is the structural representation of red wine distilling apparatus of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing, the preferred embodiments of the present invention are illustrated, it will be appreciated that preferred reality described herein
Execute example be merely to illustrate and explain the present invention, be not intended to limit the present invention.
As it is shown in figure 1, a kind of red wine distilling apparatus, including preheating tower 1, stock solution preheating pipe 2, distillation column 3, hot water circuit
Pump 4, stock solution entrance 5, stock solution outlet 6, distillation column pipeline 7, distillation column entrance 8, distillation column outlet 9, condensation pipe 10, wine liquid go out
Mouth 11, preheating water pipeline 12, water vapour pipeline 13, condensing tower 14, distillation column 3 one sidewall bottom connects water vapour pipeline 13,
Another sidewall of distillation column 3 is provided with distillation column entrance 8, and distillation column entrance 8 is connected by pipeline preheating tower 1, distillation column 3 top
Being provided with distillation column outlet 9, distillation column outlet connects the condensation pipe 10 having condensing tower 14, and condensing tower 14 bottom is provided with wine liquid
Outlet 11, condensing tower 14 is by being connected to, bottom preheating tower 1, be provided with former bottom preheating tower with the pipeline of hot water circulating pump 4
Liquid entrance 5, stock solution entrance 5 connects circulating pump motor.Be also associated with between preheating tower 1 and condensing tower 14 preheating water pipeline 12 and
Condensing water conduit 10, between two towers, water (flow) direction is for being flowed to condensing tower 14 by preheating tower 1 by hot water circulating pump 4.Due to hot water
Temperature bigger than cold water density, so hot water is all the time on tower body top in two towers.By the effect of hot water circulating pump 4, condensing tower
In hot water flow into preheating tower 1 preheated by preheating water pipeline 12, be cooled in flowing into condensing tower by hot water circulating pump 4
14, complete a circulation of remaining silent.
Technological process is, water vapour enters distillation column 3 from water vapour pipeline 13, and it is Celsius that distillation column internal temperature reaches 120
Degree.Stock solution entrance 5 starts motor, and stock solution enters preheating tower 1, preheating tower top after slow flowing in stock solution preheating pipe 2
Stock solution outlet 6 flow to distillation column entrance 8 by stock solution to distillation column pipeline 7 and enters distillation column 3, at the height of distillation column 3 interior conduit
Under temperature effect, the red wine composition such as the ethanol in stock solution flashes to stock solution steam, and stock solution steam is from distillation column outlet 9 entrance condensing towers
The condensation pipe 10 of 14, condensing tower is internal for cooling water.Stock solution steam gradually cools down in condensation pipe 10, is condensed into Fructus Vitis viniferae
Wine.From wine liquid outlet 11 outflow, staff's fill technique carrying out other.
Preheating in red wine stock solution, distillation, during condensation, the heat exchange produced therewith is respectively at preheating tower 1, distillation column
3, condensing tower 14 is carried out.After equipment operation is normal, when red wine stock solution is passed through stock solution preheating pipe 2 by cryogenic liquid, absorb
Heat in preheated liquid water in preheating tower 1, temperature steps up, and enters in distillation column afterwards, again absorbs distillation interior conduit
In heat of vaporization become gas, after high-temperature gas enter condensation pipe, carry out with water in condensing tower in condensation pipe heat friendship
Change, be progressively condensed into liquid while release heat and flow out condensing tower.Hot water in condensing tower is again by preheating water pipeline 12
Flow into preheating tower.
The foregoing is only explanation embodiments of the present invention, be not limited to the present invention, for the technology of this area
For personnel, all within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. made, should be included in
Within protection scope of the present invention.
Claims (3)
1. a red wine distilling apparatus, including preheating tower, stock solution preheating pipe, distillation column, hot water circulating pump, stock solution entrance, former
Liquid outlet, the distillation column pipeline of stock solution, distillation column entrance, distillation column outlet, condensation pipe, wine liquid outlet, preheating water pipeline, water
Jet chimney, condensing tower, it is characterised in that distillation column one sidewall is provided with steam entry, another sidewall of distillation column is provided with
Distillation column entrance, distillation column entrance is connected by pipeline has preheating tower, distillation column top to be provided with distillation column outlet, and distillation column goes out
Mouth connects the condensation pipe having condensing tower, and condensing tower bottom is provided with wine liquid outlet, and condensing tower is by with hot water circulating pump
Pipeline is connected to bottom preheating tower, is provided with stock solution entrance bottom preheating tower, is also associated with preheating between preheating tower and condensing tower
Waterpipe and condensing water conduit, between two towers, water (flow) direction is for be flowed to condensing tower by preheating tower by hot water circulating pump.
Red wine distilling apparatus the most according to claim 1, it is characterised in that: the hot water in condensing tower passes through preheating water pipeline
Flow into preheating tower to have preheated, be cooled in flowing into condensing tower by hot water circulating pump, complete a circulation of remaining silent.
Red wine distilling apparatus the most according to claim 1, it is characterised in that: stock solution entrance connects circulating pump motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610645875.6A CN106281824A (en) | 2016-08-09 | 2016-08-09 | A kind of red wine distilling apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610645875.6A CN106281824A (en) | 2016-08-09 | 2016-08-09 | A kind of red wine distilling apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106281824A true CN106281824A (en) | 2017-01-04 |
Family
ID=57666878
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610645875.6A Pending CN106281824A (en) | 2016-08-09 | 2016-08-09 | A kind of red wine distilling apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106281824A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108114495A (en) * | 2017-12-23 | 2018-06-05 | 郑州赫恩电子信息技术有限公司 | A kind of energy-saving distillation equipment |
| CN109337788A (en) * | 2018-12-25 | 2019-02-15 | 湖北工业大学 | A kind of alcohol-flavonoid synchronous distillation tower and distillation method thereof |
| CN112662509A (en) * | 2020-12-16 | 2021-04-16 | 广东三友酿酒股份有限公司 | A distillation plant for producing five indicate wild peach wine |
| CN114410403A (en) * | 2022-01-27 | 2022-04-29 | 茅台学院 | Production method of tea-flavored brandy |
| CN114958533A (en) * | 2022-06-10 | 2022-08-30 | 疏勒县阿纳石榴干红酒业有限公司 | A distillation plant for red date wine production |
| CN117264713A (en) * | 2023-11-22 | 2023-12-22 | 汕头市黄姥爷酒业有限责任公司 | Environment-friendly and efficient brewing device |
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| CN2685341Y (en) * | 2004-03-15 | 2005-03-16 | 刘代锋 | Distilling apparatus for wines |
| CN1736527A (en) * | 2005-06-30 | 2006-02-22 | 广东中科天元再生资源工程有限公司 | Alcohol quinque-towel differential pressure distilling arrangement and technique thereof |
| CN200954401Y (en) * | 2006-09-25 | 2007-10-03 | 甘庆潜 | Energy-saving distillation apparatus |
| CN101376067A (en) * | 2008-10-08 | 2009-03-04 | 薛万杰 | Retorts |
| CN201473512U (en) * | 2009-09-03 | 2010-05-19 | 佛山市太吉酒厂有限公司 | Distilling system provided with preheating device |
| CN103252105A (en) * | 2013-05-29 | 2013-08-21 | 山东道先为能源科技有限公司 | Methyl alcohol pressure reducing and distilling device |
| CN205368317U (en) * | 2015-12-26 | 2016-07-06 | 赣州岑峰酒业有限责任公司 | Energy -saving high -efficiency wine steaming device |
-
2016
- 2016-08-09 CN CN201610645875.6A patent/CN106281824A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2685341Y (en) * | 2004-03-15 | 2005-03-16 | 刘代锋 | Distilling apparatus for wines |
| CN1736527A (en) * | 2005-06-30 | 2006-02-22 | 广东中科天元再生资源工程有限公司 | Alcohol quinque-towel differential pressure distilling arrangement and technique thereof |
| CN200954401Y (en) * | 2006-09-25 | 2007-10-03 | 甘庆潜 | Energy-saving distillation apparatus |
| CN101376067A (en) * | 2008-10-08 | 2009-03-04 | 薛万杰 | Retorts |
| CN201473512U (en) * | 2009-09-03 | 2010-05-19 | 佛山市太吉酒厂有限公司 | Distilling system provided with preheating device |
| CN103252105A (en) * | 2013-05-29 | 2013-08-21 | 山东道先为能源科技有限公司 | Methyl alcohol pressure reducing and distilling device |
| CN205368317U (en) * | 2015-12-26 | 2016-07-06 | 赣州岑峰酒业有限责任公司 | Energy -saving high -efficiency wine steaming device |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108114495A (en) * | 2017-12-23 | 2018-06-05 | 郑州赫恩电子信息技术有限公司 | A kind of energy-saving distillation equipment |
| CN108114495B (en) * | 2017-12-23 | 2020-04-07 | 安徽省二邦化工有限公司 | Energy-saving distillation equipment |
| CN109337788A (en) * | 2018-12-25 | 2019-02-15 | 湖北工业大学 | A kind of alcohol-flavonoid synchronous distillation tower and distillation method thereof |
| CN112662509A (en) * | 2020-12-16 | 2021-04-16 | 广东三友酿酒股份有限公司 | A distillation plant for producing five indicate wild peach wine |
| CN114410403A (en) * | 2022-01-27 | 2022-04-29 | 茅台学院 | Production method of tea-flavored brandy |
| CN114958533A (en) * | 2022-06-10 | 2022-08-30 | 疏勒县阿纳石榴干红酒业有限公司 | A distillation plant for red date wine production |
| CN117264713A (en) * | 2023-11-22 | 2023-12-22 | 汕头市黄姥爷酒业有限责任公司 | Environment-friendly and efficient brewing device |
| CN117264713B (en) * | 2023-11-22 | 2024-05-10 | 汕头市黄姥爷酒业有限责任公司 | Environment-friendly and efficient brewing device |
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| PB01 | Publication | ||
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| RJ01 | Rejection of invention patent application after publication | ||
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Application publication date: 20170104 |