CN103386208A - Novel tower distillation system - Google Patents
Novel tower distillation system Download PDFInfo
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- CN103386208A CN103386208A CN2012101448124A CN201210144812A CN103386208A CN 103386208 A CN103386208 A CN 103386208A CN 2012101448124 A CN2012101448124 A CN 2012101448124A CN 201210144812 A CN201210144812 A CN 201210144812A CN 103386208 A CN103386208 A CN 103386208A
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- tower
- destilling tower
- distillation
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- condenser
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Abstract
The invention discloses a novel tower distillation system. The novel tower distillation system comprises a distillation tower, a heating tube is arranged in the distillation tower, a condenser is arranged in the distillation tower, a collection bottle is arranged outside the distillation tower, and the collection bottle is connected with the internal of the distillation tower. The distillation system has the advantages of simple structure, simple principle, few needed apparatuses, rapid distillation, stable quality of the obtained distilled product, satisfying of the needs of subsequent production processes, and production cost reduction.
Description
Technical field
The present invention relates to a kind of Distallation systm, especially relate to a kind of novel tower-type Distallation systm, belong to the fields such as pharmacy, chemical industry.
Background technology
Distillation is a kind of thermodynamic (al) separating technology, and it utilizes each component boiling point difference in mixing material or liquid-solid system, makes the low boiling component evaporation, then condensation is the associating of evaporation and two kinds of unit operations of condensation to separate the unit process of whole component.With other separation means, wait and compare as extraction, its advantage is need not use system components other solvent in addition, thereby guarantees can not introduce new impurity.The mass transport process that refers to utilize the difference of each component volatilization in liquid mixture and component is separated.The steam that liquid boiling is produced imports condenser pipe, makes it cooling a kind of evaporation of liquid, the process of condensation of condensing into.Distillation is a kind of important operating technology of separating mixture, especially the separation for liquid mixture has important Practical significance to utilize the difference of each component volatilization degree in liquid mixture, liquid mixture partly vaporized and make the vapor portion condensation thereupon, thereby realizing the separation of its contained component.It is a kind of unit operations that mass transfer separates that belongs to.Be widely used in the fields such as oil refining, chemical industry, light industry.
Its principle is to separate the bi-component mixed liquor as example.It is partly vaporized the feed liquid heating, volatile components obtains enrichment in steam, and difficult volatile component also obtains enrichment in raffinate, and this has realized the separation of two components to a certain extent.The volatilization ability of two components differs larger, and above-mentioned enrichment degree is also larger.In industrial rectifying device, the liquid phase of part vaporization is directly contacted with the gas phase of partial condensation, to carry out the vapour-liquid interphase mass transfer, result is that the difficult volatile component in gas phase partly changes liquid phase over to, volatile components in liquid phase partly changes gas phase over to, has also namely realized simultaneously the part vaporization of liquid phase and the partial condensation of vapour phase.
The molecule of liquid has the tendency of from surface, overflowing due to molecular motion.This tendency increases along with the rising of temperature.If liquid is placed in airtight vacuum systems, fluid molecule overflows with keeping and forms steam on liquid level top, and the speed that makes finally molecule be overflowed by liquid is equated by the speed of getting back to liquid in steam with molecule, the pressure that the steam maintenance is certain.Steam on liquid level reaches capacity at this moment, is called saturated vapor, and the pressure that it is executed liquid level is called saturated vapour pressure.The saturated vapour pressure that experiment showed, liquid is only relevant with temperature, and namely liquid has certain vapour pressure at a certain temperature.Pressure when this refers to liquid and its balance of steam, irrelevant with the absolute magnitude of liquid in system and steam.At chemical process, need to distill material, traditional distillation equipment is because its efficiency is low, causes distilling the material mass that obtains unstable, affects follow-up production process.
Summary of the invention
The object of the invention is to overcome the shortcoming and defect of above-mentioned prior art, a kind of novel tower-type Distallation systm is provided, this Distallation systm simple in structure, principle is easy, need the equipment that uses few, can reach rapidly the purpose of distillation, the steady quality of the product that distills out, can meet the needs of subsequent production process, reduce production cost.
Purpose of the present invention is achieved through the following technical solutions: a kind of novel tower-type Distallation systm, comprise destilling tower, be provided with heating tube in described destilling tower, be provided with condenser in described destilling tower, destilling tower is outside equipped with receiving flask, described receiving flask and destilling tower internal communication.
The place of described receiving flask and destilling tower internal communication is provided with collector and every the foam device, the described below that is arranged on collector every the foam device.
Be provided with the water level pipe that communicates with destilling tower inside on the outer wall of described destilling tower.
Described condenser is arranged on the top of destilling tower inside.
Be provided with cooling water inlet and coolant outlet on the outer wall of described destilling tower, described cooling water inlet and coolant outlet all communicate with condenser.
Be provided with the filling opening that communicates with its inside on described destilling tower.
In sum, the invention has the beneficial effects as follows: this Distallation systm simple in structure, principle is easy, need the equipment that uses few, can reach rapidly the purpose of distillation, the steady quality of the product that distills out, can meet the needs of subsequent production process, reduce production cost.
Description of drawings
Fig. 1 is structural representation of the present invention.
Mark and corresponding parts title in accompanying drawing: 1-heating tube; 2-destilling tower; 3-receiving flask; 4-condenser; 5-cooling water inlet; 6-coolant outlet; 7-collector; 8-every the foam device; 9-filling opening; 10-water level pipe.
The specific embodiment
Below in conjunction with embodiment and accompanying drawing, the present invention is described in further detail, but embodiments of the present invention are not limited only to this.
Embodiment:
As shown in Figure 1, a kind of novel tower-type Distallation systm, comprise destilling tower 2, is provided with heating tube 1 in described destilling tower 2, is provided with condenser 4 in described destilling tower 2, and destilling tower 2 is outside equipped with receiving flask 3, described receiving flask 3 and destilling tower 2 internal communication.Collect by receiving flask 3 liquid that condenser 4 condensations are got off.
The place of described receiving flask 3 and destilling tower 2 internal communication is provided with collector 7 and every foam device 8, the described below that is arranged on collector 7 every foam device 8.Solution is after heating tube 1 heating, inner material produces evaporation, after condenser 4 condensations on top, becoming liquid is collected by collector 7, then flow in receiving flask 3 by pipeline, the foam that intercepts in heating process every foam device 8 enters into destilling tower 2 the first half, in order to avoid the effect of impact evaporation.
Be provided with the water level pipe 10 that communicates with destilling tower inside on the outer wall of described destilling tower 2.Observe at any time the position of solution in destilling tower 2 by water level pipe 10, keep the height of the height of solution higher than heating tube 1, to avoid security incident.
Described condenser 4 is arranged on the top of destilling tower 2 inside.Can distill better.
Be provided with cooling water inlet 5 and coolant outlet 6 on the outer wall of described destilling tower 2, described cooling water inlet 5 and coolant outlet 6 all communicate with condenser 4.By cooling water inlet 5 and coolant outlet 6, continue to pass into cooling water in condenser 4, keep the working effect of condenser 4.
Be provided with the filling opening 9 that communicates with its inside on described destilling tower 2.Add solution by filling opening 9 in destilling tower 2, guarantee the continuity of distillation.Filling opening 9 should be arranged on the middle and upper part of destilling tower 2 simultaneously, adds more easily solution.
Take aforesaid way, just can realize preferably the present invention.
Claims (6)
1. novel tower-type Distallation systm, it is characterized in that: comprise destilling tower (2), be provided with heating tube (1) in described destilling tower (2), be provided with condenser (4) in described destilling tower (2), destilling tower (2) is outside equipped with receiving flask (3), described receiving flask (3) and destilling tower (2) internal communication.
2. a kind of novel tower-type Distallation systm as claimed in claim 1, it is characterized in that: the place of described receiving flask (3) and destilling tower (2) internal communication is provided with collector (7) and every foam device (8), the described below that is arranged on collector (7) every foam device (8).
3. a kind of novel tower-type Distallation systm as claimed in claim 2, is characterized in that: be provided with the water level pipe (10) that communicates with destilling tower (2) inside on the outer wall of described destilling tower (2).
4. a kind of novel tower-type Distallation systm as claimed in claim 3 is characterized in that: described condenser (4) is arranged on the inner top of destilling tower (2).
5. a kind of novel tower-type Distallation systm as claimed in claim 4, it is characterized in that: be provided with cooling water inlet (5) and coolant outlet (6) on the outer wall of described destilling tower (2), described cooling water inlet (5) and coolant outlet (6) all communicate with condenser (4).
6. a kind of novel tower-type Distallation systm as described in any one in claim 1 to 5, is characterized in that: be provided with the filling opening (9) that communicates with its inside on described destilling tower (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101448124A CN103386208A (en) | 2012-05-11 | 2012-05-11 | Novel tower distillation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101448124A CN103386208A (en) | 2012-05-11 | 2012-05-11 | Novel tower distillation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103386208A true CN103386208A (en) | 2013-11-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012101448124A Pending CN103386208A (en) | 2012-05-11 | 2012-05-11 | Novel tower distillation system |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3937109A1 (en) * | 1989-11-07 | 1991-05-08 | Bela Medvey | Distn. of liq. contg. surfactants heated by microwaves - to counter bubble and froth formation |
| CN101108281A (en) * | 2006-07-17 | 2008-01-23 | 蒋建君 | Distillation equipment of conical baffled evaporator |
| CN201356988Y (en) * | 2009-01-20 | 2009-12-09 | 沂南县天成生物制品有限公司 | Energy-saving type alcohol recovery tower |
| CN201959583U (en) * | 2011-03-12 | 2011-09-07 | 倪建英 | Alcohol recovery tower |
| CN202569605U (en) * | 2012-05-11 | 2012-12-05 | 四川汇利实业有限公司 | Novel tower-type distillation system |
-
2012
- 2012-05-11 CN CN2012101448124A patent/CN103386208A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3937109A1 (en) * | 1989-11-07 | 1991-05-08 | Bela Medvey | Distn. of liq. contg. surfactants heated by microwaves - to counter bubble and froth formation |
| CN101108281A (en) * | 2006-07-17 | 2008-01-23 | 蒋建君 | Distillation equipment of conical baffled evaporator |
| CN201356988Y (en) * | 2009-01-20 | 2009-12-09 | 沂南县天成生物制品有限公司 | Energy-saving type alcohol recovery tower |
| CN201959583U (en) * | 2011-03-12 | 2011-09-07 | 倪建英 | Alcohol recovery tower |
| CN202569605U (en) * | 2012-05-11 | 2012-12-05 | 四川汇利实业有限公司 | Novel tower-type distillation system |
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Application publication date: 20131113 |