CN205182226U - High -efficient distillation plant - Google Patents
High -efficient distillation plant Download PDFInfo
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- CN205182226U CN205182226U CN201520973431.6U CN201520973431U CN205182226U CN 205182226 U CN205182226 U CN 205182226U CN 201520973431 U CN201520973431 U CN 201520973431U CN 205182226 U CN205182226 U CN 205182226U
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Abstract
The utility model relates to a high -efficient distillation plant, including crude jar, pre -heater, heating cauldron, rectifying column, condenser, vapour and liquid separator, the collection tank that is linked together in order, the condenser includes first condenser and second condenser, and the return -air mouth of first condenser is linked together through the the second entrance of pipeline with the second condenser, vapour and liquid separator includes the separator body, sets up the first inlet of upper end to the side of the separator body and set up the second inlet on separator body top, and first inlet is linked together with the first export of first condenser, and the second inlet is linked together with the second export of second condenser. The utility model provides high heat transfer efficiency, heat energy obtains make full use of, and evaporation efficiency improves greatly simultaneously, is one set of energy -conservation, efficient distillation plant.
Description
Technical field
The utility model relates to a kind of chemical industry treating apparatus, especially relates to a kind of efficient distilling apparatus.
Background technology
Distillation is a kind of thermodynamic (al) separating technology, and it utilizes each component boiling point in mixing material or liquid-solid system different, low boiling component is evaporated, then condensation is to be separated the unit process of whole component, is the associating of evaporation and condensation two kinds of unit operations.With other separation means, as extraction, filtering for crystallizing etc. are compared, its advantage is not need to use other solvent beyond system components, thus ensures to introduce new impurity.
Distilling apparatus due to material heated time short, separation degree high, has been widely used in the extraction of the vitamin of pharmaceuticals industry and Chinese herbal medicine effective ingredients, petrochemical industry, food industry, all trades and professions such as cosmetics industry and agricultural.In chemical products production process, usually needing to adopt distilling apparatus to distill product, there is complex structure in existing distilling apparatus, operation inconvenience, the defects such as distilling effect difference.
Utility model content
In order to overcome the deficiency that prior art exists, the utility model provides that a kind of structure is simple, heat transfer efficiency is high, energy-conservation, efficient distilling apparatus.
A kind of efficient distilling apparatus, described device comprises the crude product tank, preheater, heating kettle, rectifying column, condenser, gas-liquid separator, the collecting tank that are connected in turn, and described crude product tank is connected by pump with between preheater; Described condenser comprises the first condenser and the second condenser, described first condenser comprises the first cylindrical shell, is arranged on the first entrance of the first cylindrical shell upper end, is arranged on first of the first cylindrical shell lower end the outlet and is arranged on the gas returning port of the first cylindrical shell side lower, described second condenser comprises the second cylindrical shell, is arranged on the second entrance of the second cylindrical shell upper end and is arranged on the second outlet of the second cylindrical shell lower end, and described gas returning port is connected with the second entrance by pipeline; Described gas-liquid separator comprises separator body, is arranged on the first inlet of separator body lateral upper end and is arranged on second inlet on separator body top, described first inlet and first exports and is connected, and the second inlet and second exports and is connected.
As preferably, described pump is provided with flowmeter with the pipeline be connected between preheater.
As preferably, the pipeline at described flowmeter two ends is respectively equipped with corresponding valve body.
The utility model structure is simple, and reasonable in design, the utility model improves heat transfer efficiency, and heat energy is fully used, and evaporation efficiency improves greatly simultaneously, is a set of energy-conservation, efficient distilling apparatus.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail, but the claimed scope of the utility model is not limited to this.
With reference to Fig. 1, a kind of efficient distilling apparatus, described device comprises the crude product tank 1, preheater 2, heating kettle 3, rectifying column 4, condenser, gas-liquid separator 5, the collecting tank 6 that are connected in turn, described crude product tank 1 is connected by pump 7 with between preheater 2, described pump 7 is provided with flowmeter 20 with the pipeline be connected between preheater 2, the pipeline at described flowmeter 20 two ends is respectively equipped with corresponding valve body 21, not only can monitor flow, and by the control of valve body, the flow of material effectively can be controlled.Described condenser comprises the first condenser 8 and the second condenser 9, described first condenser 8 comprises the first cylindrical shell 10, is arranged on the first entrance 11 of the first cylindrical shell upper end, is arranged on first of the first cylindrical shell lower end the outlet 12 and is arranged on the gas returning port 13 of the first cylindrical shell side lower, described second condenser 9 comprises the second cylindrical shell 14, is arranged on the second entrance 15 of the second cylindrical shell upper end and is arranged on the second outlet 16 of the second cylindrical shell lower end, and described gas returning port 13 is connected with the second entrance 15 by pipeline; Described gas-liquid separator 5 comprises separator body 17, is arranged on the first inlet 18 of separator body lateral upper end and is arranged on second inlet 19 on separator body top, described first inlet 17 and first exports 12 and is connected, and the second inlet 19 and second exports 16 and is connected.
This device is made up of crude product tank, pump, preheater, heating kettle, rectifying column, condenser, gas-liquid separator, collecting tank, crude product in-tank mixing solvent enters heating kettle through pump by preheater heating, stir lower mixed solvent evaporation and enter rectifying column, high boiling component is separated with low boiling component, low boiling component is collected through condenser, and high boiling component is stayed in heating kettle; Gas after rectifying enters the first condenser, liquid after first condenser condenses enters in gas-liquid separator through the first inlet and is separated, the gas cooled via return air mouth of non-total condensation enters the second condenser and continues condensation, and the liquid after the second condenser condenses enters in gas-liquid separator through the second inlet and is separated; Product introduction collecting tank after separation is collected.The arrangement increases heat transfer efficiency, heat energy is fully used, and evaporation efficiency improves greatly simultaneously, is a set of energy-conservation, efficient distilling apparatus.
Claims (3)
1. an efficient distilling apparatus, is characterized in that: described device comprises the crude product tank, preheater, heating kettle, rectifying column, condenser, gas-liquid separator, the collecting tank that are connected in turn, and described crude product tank is connected by pump with between preheater; Described condenser comprises the first condenser and the second condenser, described first condenser comprises the first cylindrical shell, is arranged on the first entrance of the first cylindrical shell upper end, is arranged on first of the first cylindrical shell lower end the outlet and is arranged on the gas returning port of the first cylindrical shell side lower, described second condenser comprises the second cylindrical shell, is arranged on the second entrance of the second cylindrical shell upper end and is arranged on the second outlet of the second cylindrical shell lower end, and described gas returning port is connected with the second entrance by pipeline; Described gas-liquid separator comprises separator body, is arranged on the first inlet of separator body lateral upper end and is arranged on second inlet on separator body top, described first inlet and first exports and is connected, and the second inlet and second exports and is connected.
2. efficient distilling apparatus according to claim 1, is characterized in that: described pump is provided with flowmeter with the pipeline be connected between preheater.
3. efficient distilling apparatus according to claim 2, is characterized in that: the pipeline at described flowmeter two ends is respectively equipped with corresponding valve body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520973431.6U CN205182226U (en) | 2015-11-30 | 2015-11-30 | High -efficient distillation plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520973431.6U CN205182226U (en) | 2015-11-30 | 2015-11-30 | High -efficient distillation plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205182226U true CN205182226U (en) | 2016-04-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520973431.6U Active CN205182226U (en) | 2015-11-30 | 2015-11-30 | High -efficient distillation plant |
Country Status (1)
| Country | Link |
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| CN (1) | CN205182226U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106237645A (en) * | 2016-10-19 | 2016-12-21 | 天津瑞岭化工有限公司 | A kind of water vapor distillation apparatus and its implementation |
-
2015
- 2015-11-30 CN CN201520973431.6U patent/CN205182226U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106237645A (en) * | 2016-10-19 | 2016-12-21 | 天津瑞岭化工有限公司 | A kind of water vapor distillation apparatus and its implementation |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230427 Address after: 311228 Linjiang Industrial Park, Xiaoshan District, Zhejiang, Hangzhou Patentee after: Zhejiang DINGLONG Technology Co.,Ltd. Patentee after: Inner Mongolia Dingli Technology Co.,Ltd. Address before: Toulong village, Binhuai Town, Binhai County, Yancheng City, Jiangsu Province Patentee before: JIANGSU DINGLONG TECHNOLOGY Co.,Ltd. |