CN203154851U - Alcohol distillation and purification apparatus - Google Patents
Alcohol distillation and purification apparatus Download PDFInfo
- Publication number
- CN203154851U CN203154851U CN 201320146623 CN201320146623U CN203154851U CN 203154851 U CN203154851 U CN 203154851U CN 201320146623 CN201320146623 CN 201320146623 CN 201320146623 U CN201320146623 U CN 201320146623U CN 203154851 U CN203154851 U CN 203154851U
- Authority
- CN
- China
- Prior art keywords
- alcohol
- outlet
- condenser
- tower body
- cooler
- 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 - Fee Related
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model discloses an alcohol distillation and purification apparatus which comprises a tower kettle and a tower body, wherein the tower kettle and the tower body are connected into an integral body; one end of the tower kettle is provided with a steam inlet; the tower kettle is provided with a thermometer interface; the other end of the tower kettle is provided with a dilute sulfuric acid inlet; the dilute sulfuric acid inlet is connected with a dilute alcohol high-position storage tank through a pipeline; the top of the tower body is provided with an alcohol steam outlet; one side of the top of the tower body is provided with a reflux port; the alcohol steam outlet leads to the condenser; the bottom of the condenser is provided with a condensate outlet and an alcohol outlet; the condensate outlet and the alcohol outlet lead to a buffer tank; the bottom of the buffer tank is connected with a cooler; the bottom of the cooler is provided with a thick alcohol outlet; the thick alcohol outlet is connected with a finished product tank; one side of the buffer tank is provided with a condensation tube; and the condensation tube is communicated with the reflux port. The utility model has the following advantages: the condenser and the cooler can perform condensation twice, so that the alcohol recovery efficiency is high; and the buffer tank arranged between the condenser and the cooler can achieve the goal of concentration, so that the alcohol concentration is high, and the purification rate is high.
Description
Technical field
The utility model relates to a kind of equipment for purifying, relates in particular to a kind of alcohol distillation equipment for purifying.
Background technology
At present, in the process that alcohol reclaims, generally be to mix with the liquid that intensification Guan Tongxu reclaims, the back alcohol gas that heats up volatilizees with water vapour, and the alcohol loss is big like this, and concentration is low, and the quantity of steam loss is big.So, be badly in need of a kind of improved technology and solve this problem.
The utility model content
The purpose of this utility model provides the high alcohol distillation equipment for purifying of a kind of organic efficiency.
The technical solution adopted in the utility model is:
The alcohol distillation equipment for purifying comprises tower reactor and tower body, and described tower reactor is connected with the tower body one,
Described tower reactor one end is provided with steam inlet, described tower reactor is provided with thermometer boss, the described tower reactor other end has the dilute sulfuric acid import, described dilute sulfuric acid import is connected by the high-order storage tank of pipeline and Diluted Alcohol, described tower body top is provided with the alcohol steam outlet, described tower body top one side is provided with refluxing opening, condenser is led in described alcohol steam outlet, described condenser bottom is provided with condensate outlet and alcohol outlet, surge tank is led in described condensate outlet and alcohol outlet, described surge tank bottom is connected with cooler, described cooler bottom is provided with the neutral spirits outlet, described neutral spirits outlet is connected with the finished product jar, and described surge tank one side has condenser pipe, and described condenser pipe is communicated with refluxing opening.
Described tower reactor is provided with Pressure gauge.
Described tower body is provided with the maintenance ladder.
Described neutral spirits outlet is provided with current divider.
The beneficial effects of the utility model: condenser and cooler can carry out twice condensation, make alcohol organic efficiency height, and the surge tank that is provided with between condenser and the cooler can reach concentrated purpose, make the alcohol concentration height, the purification rate height.
Description of drawings
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail.
Fig. 1 is structural representation of the present utility model.
Wherein: 1, tower reactor, 2, tower body, 3, the maintenance ladder, 4, steam inlet, 5, thermometer boss, 6, the dilute sulfuric acid import, 7, pipeline, 8, the high-order storage tank of Diluted Alcohol, 9, alcohol steam outlet, 10, refluxing opening, 11, condenser, 12, condensate outlet, 13, alcohol outlet, 14, surge tank, 15, cooler, 16, neutral spirits outlet, 17, the finished product jar, 18, condenser pipe, 19, current divider, 20, Pressure gauge.
The specific embodiment
As shown in Figure 1, alcohol distillation equipment for purifying of the present utility model, comprise tower reactor 1 and tower body 2, tower reactor 1 is connected with tower body 2 one, tower body 2 is provided with maintenance ladder 3, tower reactor 1 one ends are provided with steam inlet 4, tower reactor 1 is provided with thermometer boss 5, tower reactor 1 other end has dilute sulfuric acid import 6, dilute sulfuric acid import 6 is connected by the high-order storage tank 8 of pipeline 7 and Diluted Alcohol, tower body 1 top is provided with alcohol steam outlet 9, tower body 2 tops one side is provided with refluxing opening 10, and condenser 11 is led in alcohol steam outlet 9, and condenser 11 bottoms are provided with condensate outlet 12 and alcohol outlet 13, surge tank 14 is led in condensate outlet 12 and alcohol outlet 13, surge tank 14 bottoms are connected with cooler 15, and cooler 15 bottoms are provided with neutral spirits outlet 16, and neutral spirits outlet 16 is connected with finished product jar 17, surge tank 14 1 sides have condenser pipe 18, and condenser pipe 18 is communicated with refluxing opening 10.
Tower reactor 1 is provided with Pressure gauge 20, shows the still internal pressure, and neutral spirits outlet 16 is provided with current divider 19, and shunting enters finished product jar 17.
Condenser 11 can carry out twice condensation with cooler 15, makes alcohol organic efficiency height, and the surge tank 14 that is provided with between condenser 11 and the cooler 15 can reach concentrated purpose, makes the alcohol concentration height, the purification rate height.
Claims (4)
1. alcohol distillation equipment for purifying, comprise tower reactor and tower body, described tower reactor is connected with the tower body one, it is characterized in that: described tower reactor one end is provided with steam inlet, described tower reactor is provided with thermometer boss, the described tower reactor other end has the dilute sulfuric acid import, described dilute sulfuric acid import is connected by the high-order storage tank of pipeline and Diluted Alcohol, described tower body top is provided with the alcohol steam outlet, described tower body top one side is provided with refluxing opening, and condenser is led in described alcohol steam outlet, and described condenser bottom is provided with condensate outlet and alcohol outlet, surge tank is led in described condensate outlet and alcohol outlet, described surge tank bottom is connected with cooler, and described cooler bottom is provided with the neutral spirits outlet, and described neutral spirits outlet is connected with the finished product jar, described surge tank one side has condenser pipe, and described condenser pipe is communicated with refluxing opening.
2. alcohol distillation equipment for purifying according to claim 1, it is characterized in that: described tower reactor is provided with Pressure gauge.
3. alcohol distillation equipment for purifying according to claim 1 is characterized in that: described tower body is provided with the maintenance ladder.
4. alcohol distillation equipment for purifying according to claim 1 is characterized in that: described neutral spirits outlet is provided with current divider.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320146623 CN203154851U (en) | 2013-03-28 | 2013-03-28 | Alcohol distillation and purification apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320146623 CN203154851U (en) | 2013-03-28 | 2013-03-28 | Alcohol distillation and purification apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203154851U true CN203154851U (en) | 2013-08-28 |
Family
ID=49016076
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320146623 Expired - Fee Related CN203154851U (en) | 2013-03-28 | 2013-03-28 | Alcohol distillation and purification apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203154851U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103992930A (en) * | 2014-05-03 | 2014-08-20 | 张家口奥斯特不锈钢工程有限公司 | Novel efficient energy-saving wine distillation equipment |
-
2013
- 2013-03-28 CN CN 201320146623 patent/CN203154851U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103992930A (en) * | 2014-05-03 | 2014-08-20 | 张家口奥斯特不锈钢工程有限公司 | Novel efficient energy-saving wine distillation equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203154851U (en) | Alcohol distillation and purification apparatus | |
| CN203196511U (en) | Formaldehyde absorption system | |
| CN204932915U (en) | A kind of high-efficient energy-saving alcohol recovery tower | |
| CN201962221U (en) | Improved alcohol recovering device | |
| CN201704236U (en) | Ethylene glycol regenerating device | |
| CN205287661U (en) | Trace liquid distillation plant | |
| CN204411757U (en) | A kind of energy-conservation alcohol recovery device | |
| CN100584766C (en) | Full desorption system of hydrochloric acid | |
| CN203525678U (en) | Circulatory reaction kettle system | |
| CN202161827U (en) | Gooseneck-typed distilling device for purifying spice | |
| CN202366496U (en) | Alcohol distillation tower | |
| CN203829672U (en) | Energy-saving alcohol recovery tower | |
| CN203803132U (en) | Combined solvent deacidification, dechlorination and deamination equipment | |
| CN203355332U (en) | Continuous sebacic acid di-methyl ester rectification device | |
| CN203715538U (en) | Rectifying and purifying device for ethyl acetate under vacuum state | |
| CN201684577U (en) | Resin reaction kettle acid recovery device | |
| CN203530277U (en) | Mixed oil evaporation device | |
| CN210021247U (en) | Dealkynol device in isoprene production process | |
| CN203474699U (en) | Rectification type esterification reaction system for polycarboxylate water reducer | |
| CN203833594U (en) | Vinyl methyl ether filling pipe | |
| CN202909473U (en) | Negative pressure distillation tower for extracting crude benzene | |
| CN216677010U (en) | Alcohol rectification recovery tower | |
| CN201793175U (en) | Acetic acid storage device | |
| CN203648117U (en) | Methylal rectifying tower with external reactor | |
| CN202113838U (en) | Feed solution extracorporeal circulation system in process of dehydration and alcohol washing of plasticiser |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130828 Termination date: 20140328 |