CN201384865Y - Steam-free alcohol distillation tower - Google Patents
Steam-free alcohol distillation tower Download PDFInfo
- Publication number
- CN201384865Y CN201384865Y CN200920052930U CN200920052930U CN201384865Y CN 201384865 Y CN201384865 Y CN 201384865Y CN 200920052930 U CN200920052930 U CN 200920052930U CN 200920052930 U CN200920052930 U CN 200920052930U CN 201384865 Y CN201384865 Y CN 201384865Y
- Authority
- CN
- China
- Prior art keywords
- annular
- conduction oil
- tower
- steam
- distillation tower
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000004821 distillation Methods 0.000 title claims abstract description 21
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims abstract description 19
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 abstract description 12
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000005265 energy consumption Methods 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 238000007599 discharging Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 2
- 241000282326 Felis catus Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000001256 steam distillation Methods 0.000 description 1
Images
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a steam-free alcohol distillation tower which comprises a tower body and a heating device; the heating device is in annular coiled tube structure; a heat conductive oil inlet arranged on the lower part of the heating device and the heat conductive oil outlet arranged on the upper part of the heating device are respectively communicated with a heat conductive oil pot to form a circulation loop with heat conductive oil as heating medium. The annular coiled tube structure is constructed by a plurality of annular coils arranged up and down, the annular coils are composed of a plurality of annular tubes distributed radially with interval and communicated with each other through guide tubes, each annular tube of the annular coils is communicated with the corresponding upper and lower annular tubes of adjacent annular coil through guide tubes. As heat conductive oil is adopted as heating medium, the temperature of heating oil can reach 360 DEG C, the heating energy is stable and the purity of product alcohol is greatly improved, no steam is generated; the heating area and the heat utilization rate are increased through the annular coiled tube structure. The steam-free alcohol distillation tower has high production efficiency, high safety, low energy consumption and low cost.
Description
Technical field
The utility model relates to a kind of alcohol distillation tower that adopts conduction oil heat conduction that alcohol distillation is separated, and specifically is a kind of no steam alcohol distillation tower.
Background technology
Traditional distilling apparatus with the water vapour be heat medium and mixing of materials together.The deficiency of its existence: water vapour heat radiation is slow, and the heat supply instability causes that its distilling effect is low, cost is high.In addition, its water vapour boiler safety coefficient is low, and at the easy incrustation of production process and the maintenance that stops production causes economic loss, labour intensity is big, makes Alcohol Production cost height.Simultaneously, cause the water vapour of heating after Ta Nei and mixing of materials cooling, to become useless mash discharge.At present, in the world alcohol waste mash is administered the still very big difficulty of existence.So it is the important channel of reducing environmental pollution that useless mash reduces discharging.
Summary of the invention
The purpose of this utility model is to provide a kind of do not have steam distillation, end product quality height, production efficiency height, safe and reduce the no steam alcohol distillation tower of discharging of waste liquid.
To achieve these goals, the technical solution adopted in the utility model and feature are: no steam alcohol distillation tower comprises: tower body, multilayer coil pipe conduction oil device is characterized in that: described multilayer coil pipe conduction oil device is a kind of ring-like coiled structure; The conduction oil inlet of multilayer coil pipe conduction oil device by its underpart with and the conduction oil outlet on top communicate with the outer conduction oil device of tower body respectively that to constitute with the conduction oil be the closed circuit of heat medium.
Described multilayer coil pipe conduction oil apparatus structure is to be made of the many groups of ring-like pipes that are arranged above and below, and to organize ring-like pipe radially spaced apart and be interconnected by conduit more, and the ring-like pipe of each in the ring-like coil pipe is connected by conduit with corresponding ring-like pipe up and down in the adjacent annular disk.
Described tower body is atmospheric distillation tower or differential distillation tower or first tower or smart tower or aldehyde tower.
Operation principle: no steam alcohol distillation separates, be to adopt conduction oil to heat, its device is a kind of ring-like coil arrangement form, constantly heating conduction oil by conduction oil (not contacting with material) recycles in coil pipe, form closed circuit, make full use of its heat energy, than original Steam Heating alcohol tower, no steam enters Ta Nei and mixing of materials, discharges and reduce relative useless mash.Adopt conduction oil as adding the thermal distillation medium, the temperature that is produced up to 360 ℃ about, conduction oil constantly heats tower outside by annular coil pipe, enters multilayer coil pipe conduction oil device by the tower bottom in ring pipe, material carries out separated by the principle that heat is passed, and produces wine vapour toward cat head output; Useless mash is discharged at tower bottom; Conduction oil is discharged in multilayer coil pipe conduction oil device top, forms closed circuit, and constantly heat cycles is used in pipe.
The beneficial effects of the utility model: adopt conduction oil as adding the thermal distillation medium, the temperature that is produced is up to 360 ℃, and heat energy is stable, and separated is effective.And the still-process of impurity that contains in the dry-steam and mixing of materials, improved the purity of finished product alcohol; Heater adopts the structure of annular disk tubular type, forms closed circuit in the pipe, and the inherent constantly heat cycles of heat-conducting oil pipes is used, and improves the heat energy utilization rate.Therefore, saved the required water yield of water vapour.The utlity model has production efficiency height, safe, low energy consumption, low cost, save water source and reduce the discharging of useless mash respectively, compare with traditional distilling apparatus and reduced about 20%.
Description of drawings
The utility model is described in further detail below in conjunction with accompanying drawing.
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the plan structure schematic diagram of multilayer coil pipe conduction oil device shown in Figure 1.
Among the figure: 1, tower body; 2, multilayer coil pipe conduction oil device; 3, conduction oil inlet; 4, conduction oil outlet; 5, conduit I; 6, ring pipe; 7, conduit.
As shown in Figure 1, no steam alcohol distillation tower includes tower body 1, multilayer coil pipe conduction oil device 2, and multilayer coil pipe conduction oil device 2 is positioned at the bottom of tower body 1, it is characterized in that: described multilayer coil pipe conduction oil device 2 is annular disk tubular structures; The conduction oil inlet 3 of multilayer coil pipe conduction oil device 2 by its underpart with and the conduction oil outlet 4 on top communicate with the heat conduction oil cauldron respectively that to constitute with the conduction oil be the closed circuit of heat medium.
As shown in Figure 1 and Figure 2, described multilayer coil pipe conduction oil device 2 structures are to be made of the many groups of ring-like pipes 6 that are arranged above and below, and to organize ring-like pipe 6 radially spaced apart and be interconnected by conduit 7 more, and the ring-like pipe of each in the ring-like coil pipe is connected by conduit I 5 with corresponding ring-like pipe up and down in the adjacent annular disk.
Described tower body is the differential distillation tower.
Claims (3)
1, a kind of no steam alcohol distillation tower comprises tower body (1), multilayer coil pipe conduction oil device (2), it is characterized in that: described multilayer coil pipe conduction oil device (2) is a kind of ring-like coiled structure; The conduction oil inlet (3) of multilayer coil pipe conduction oil device (2) by its underpart with and the conduction oil outlet (4) on top communicate with the outer conduction oil device of tower body respectively that to constitute with the conduction oil be the closed circuit of heat medium.
2, no steam alcohol distillation tower according to claim 1, it is characterized in that: described multilayer coil pipe conduction oil device (2) structure is to be made of the many groups of ring-like pipes (6) that are arranged above and below, and to organize ring-like pipe (6) radially spaced apart and be interconnected by conduit (7) more, and the ring-like pipe of each in the ring-like coil pipe is connected by conduit I (5) with corresponding ring-like pipe up and down in the adjacent annular disk.
3, no steam alcohol distillation tower according to claim 1 is characterized in that: described tower body (1) is atmospheric distillation tower or differential distillation tower or first tower or smart tower or aldehyde tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920052930U CN201384865Y (en) | 2009-03-19 | 2009-03-19 | Steam-free alcohol distillation tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920052930U CN201384865Y (en) | 2009-03-19 | 2009-03-19 | Steam-free alcohol distillation tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201384865Y true CN201384865Y (en) | 2010-01-20 |
Family
ID=41577386
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200920052930U Expired - Lifetime CN201384865Y (en) | 2009-03-19 | 2009-03-19 | Steam-free alcohol distillation tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201384865Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102716596A (en) * | 2012-07-06 | 2012-10-10 | 广东高科生物工程有限公司 | Five-tower differential-pressure energy-saving alcohol distillation device |
| CN109706051A (en) * | 2019-03-16 | 2019-05-03 | 石玉明 | Horizontal mixing type wine distiller |
-
2009
- 2009-03-19 CN CN200920052930U patent/CN201384865Y/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102716596A (en) * | 2012-07-06 | 2012-10-10 | 广东高科生物工程有限公司 | Five-tower differential-pressure energy-saving alcohol distillation device |
| CN102716596B (en) * | 2012-07-06 | 2014-08-06 | 广东高科生物工程有限公司 | Five-tower differential-pressure energy-saving alcohol distillation device |
| CN109706051A (en) * | 2019-03-16 | 2019-05-03 | 石玉明 | Horizontal mixing type wine distiller |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHANJIANG YUEHAI MACHINERY CO.,LTD Free format text: FORMER OWNER: LIN HAI Effective date: 20100623 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 524000 (LOCATED IN GUANGDONG YUEKAI MECHINARY WORKS), LINWU VILLAGE, HUANGPO TOWN, WUCHUAN CITY, GUANGDONG PROVINCE TO: 524000 HUANGPO TOWN, WUCHUAN CITY, GUANGDONG PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20100623 Address after: 524000 Guangdong city of Wuchuan Province Huang Po Zhen Patentee after: ZHANJIANG YUEHAI MACHINERY CO., LTD. Address before: Huang Po Zhen Lin Wu Cun 524000 Guangdong city of Wuchuan province (Kay Guangdong Guangdong Machinery Factory) Patentee before: Lin Hai |
|
| CX01 | Expiry of patent term |
Granted publication date: 20100120 |
|
| CX01 | Expiry of patent term |