CN204709860U - Reduce ethanol volatilization system in extract fluid process - Google Patents
Reduce ethanol volatilization system in extract fluid process Download PDFInfo
- Publication number
- CN204709860U CN204709860U CN201520374067.1U CN201520374067U CN204709860U CN 204709860 U CN204709860 U CN 204709860U CN 201520374067 U CN201520374067 U CN 201520374067U CN 204709860 U CN204709860 U CN 204709860U
- Authority
- CN
- China
- Prior art keywords
- ethanol
- storage tank
- intermediate storage
- extractor
- condenser
- 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
- Extraction Or Liquid Replacement (AREA)
Abstract
The utility model discloses ethanol volatilization system in a kind of minimizing extract fluid process, comprise extractor, at least one intermediate storage tank, condenser and ethanol collecting tank; The inlet of the intermediate storage tank described in the liquid outlet of described extractor is connected by pipeline; Condenser inlet described in described intermediate storage tank is connected by emptying pipe; Ethanol collecting tank inlet described in the liquid outlet of described condenser is connected by pipeline; Described condenser connects external refrigeration equipment by cooling water pipeline.The beneficial effects of the utility model are except carrying out cooling processing to boil-off gas in extractor in tapping process, and cooling provision taked by volatilization ethanol extract being put into intermediate storage tank process, more effectively reduce ethanol volatilization, improve ethanol recovery utilization rate.
Description
Technical field
The utility model relates to pharmaceutical technology sectors, is specifically related to ethanol volatilization system in a kind of minimizing extract fluid process.
Background technology
The method extracting active skull cap components from Chinese medicine and natural drug has solvent method, steam distillation and sublimed method etc.The range of application of latter two method is very limited, is in most cases to adopt solvent method.In solvent method, ethanol is the most frequently used a kind of organic solvent.Herbal pharmaceutical enterprise ethanol expense in leaching process is very large, the ethanol extract of heat often produces a large amount of ethanol volatilization gas when fluid, this not only can cause the waste of ethanol, also can increase concentration of alcohol in air, contaminated environment, and there is potential safety hazard.
For solving the problem, meeting production actual demand, proposing ethanol volatilization system in a kind of minimizing extract fluid process.
Utility model content
Technical problem to be solved in the utility model is to provide ethanol volatilization system in a kind of minimizing extract fluid process, cooling provision taked by volatilization ethanol extract being put into intermediate storage tank process, more effectively reduce ethanol volatilization, improve ethanol recovery utilization rate.
For solving the problems of the technologies described above, the utility model one reduces ethanol volatilization system in extract fluid process, comprises extractor, at least one intermediate storage tank, condenser and ethanol collecting tank;
The inlet of the intermediate storage tank described in the liquid outlet of described extractor is connected by pipeline;
Condenser inlet described in described intermediate storage tank is connected by emptying pipe;
Ethanol collecting tank inlet described in the liquid outlet of described condenser is connected by pipeline;
Described condenser connects external refrigeration equipment by cooling water pipeline.
Preferably, ethanol volatilization system in minimizing extract fluid process of the present invention, described extractor is dynamic extraction pot or multi-function extractor, and described extractor connects condenser, cooler and oil water separator successively by pipeline.
Further, ethanol volatilization system in minimizing extract fluid process of the present invention, one end that described extractor connects described intermediate storage tank has bleeder valve.
Further, ethanol volatilization system in minimizing extract fluid process of the present invention, one end that described intermediate storage tank top connects described extractor is provided with pipeline valve, and described intermediate storage tank and described ethanol collecting tank top are provided with exhaust-valve.
The beneficial effects of the utility model are except carrying out cooling processing to boil-off gas in extractor in tapping process, and cooling provision taked by volatilization ethanol extract being put into intermediate storage tank process, more effectively reduce ethanol volatilization, improve ethanol recovery utilization rate.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail:
Fig. 1 is the system schematic of ethanol volatilization system in minimizing extract fluid process of the present utility model.
Description of reference numerals in figure:
1, extractor; 2, intermediate storage tank;
3, ethanol collecting tank; 4, boil-off gas pipeline;
5, pipeline valve; 6, cooling water pipeline;
7, condenser; 8, cooler;
9, oil water separator; 10, evacuation port;
11, bleeder valve; 12, pipeline valve;
13, pipeline valve; 14, exhaust-valve;
15, emptying pipe; 16, fluid pipeline;
17, exhaust-valve; 18, bottom valve.
Detailed description of the invention
Ethanol volatilization system in a kind of minimizing extract fluid process is provided in accompanying drawing 1.
Comprise extractor 1, at least one intermediate storage tank 2, condenser 7 and ethanol collecting tank 3; The inlet of the intermediate storage tank 2 described in the liquid outlet of described extractor 1 is connected by pipeline; Described intermediate storage tank 2 connects described condenser 7 inlet by emptying pipe 15; Ethanol collecting tank 3 inlet described in the liquid outlet of described condenser 7 is connected by pipeline; Described condenser 7 connects external refrigeration equipment by cooling water pipeline 6.
Preferably, ethanol volatilization system in minimizing extract fluid process of the present invention, described extractor 1 is dynamic extraction pot or multi-function extractor, described extractor 1 connects condenser 7, cooler 8 and oil water separator 9 successively by pipeline, described extractor 1 be connected boil-off gas pipeline 4 between described condenser and be provided with pipeline valve 5.
Further, ethanol volatilization system in minimizing extract fluid process of the present invention, one end that described extractor 1 connects described intermediate storage tank 2 has bleeder valve 11.
Further, ethanol volatilization system in minimizing extract fluid process of the present invention, one end that described intermediate storage tank 2 top connects described extractor is provided with pipeline valve 12,13, and described intermediate storage tank 2 and described ethanol collecting tank 3 top are provided with exhaust-valve 14,17.
The emptying pipe 15 of each intermediate storage tank 2 of the utility model communicates, and is communicated with the condensation carrying out volatilization alcohol gas in condenser 7, and condenser 7 is provided with evacuation port 10; The fluid pipeline 16 of condenser 7 is communicated with ethanol collecting tank 3, carries out the collection of condensation ethanol; The exhaust-valve 17 of ethanol collecting tank keeps normally open, and bottom valve 18 is for discharging ethanol liquid in ethanol collecting tank.Put into intermediate storage tank 2 process at extractor 1 extract, in cooling water pipeline 6, cooling water is in flow regime always, cools, entered in ethanol collecting tank 3 through condensed ethanol liquid by fluid pipeline 16 ethanol of volatilization.
Claims (4)
1. an ethanol volatilization system in minimizing extract fluid process, is characterized in that: comprise extractor, at least one intermediate storage tank, condenser and ethanol collecting tank;
The inlet of the intermediate storage tank described in the liquid outlet of described extractor is connected by pipeline;
Condenser inlet described in described intermediate storage tank is connected by emptying pipe;
Ethanol collecting tank inlet described in the liquid outlet of described condenser is connected by pipeline;
Described condenser connects external refrigeration equipment by cooling water pipeline.
2. ethanol volatilization system in minimizing extract fluid process according to claim 1, it is characterized in that: described extractor is dynamic extraction pot or multi-function extractor, and described extractor connects condenser, cooler and oil water separator successively by pipeline.
3. ethanol volatilization system in minimizing extract fluid process according to claim 2, is characterized in that: one end that described extractor connects described intermediate storage tank has bleeder valve.
4. ethanol volatilization system in minimizing extract fluid process according to claim 2, is characterized in that: one end that described intermediate storage tank top connects described extractor is provided with pipeline valve, and described intermediate storage tank and described ethanol collecting tank top are provided with exhaust-valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520374067.1U CN204709860U (en) | 2015-06-03 | 2015-06-03 | Reduce ethanol volatilization system in extract fluid process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520374067.1U CN204709860U (en) | 2015-06-03 | 2015-06-03 | Reduce ethanol volatilization system in extract fluid process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204709860U true CN204709860U (en) | 2015-10-21 |
Family
ID=54308893
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520374067.1U Expired - Fee Related CN204709860U (en) | 2015-06-03 | 2015-06-03 | Reduce ethanol volatilization system in extract fluid process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204709860U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104897442A (en) * | 2015-05-12 | 2015-09-09 | 中国科学院地球环境研究所 | Method used for identifying aged liquor, and vacuum freezing transferring device |
-
2015
- 2015-06-03 CN CN201520374067.1U patent/CN204709860U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104897442A (en) * | 2015-05-12 | 2015-09-09 | 中国科学院地球环境研究所 | Method used for identifying aged liquor, and vacuum freezing transferring device |
| CN104897442B (en) * | 2015-05-12 | 2017-09-19 | 中国科学院地球环境研究所 | The authentication method and vacuum refrigeration transfer device of a kind of time white wine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204939435U (en) | A kind of family expenses essential oil distillation extraction device | |
| CN204400945U (en) | A kind of essential oil extraction device | |
| CN103923748A (en) | Volatile oil extracting, collecting and separating device | |
| CN103073145A (en) | System for recovering light oil from residual ammonia water | |
| CN204709860U (en) | Reduce ethanol volatilization system in extract fluid process | |
| CN202322781U (en) | Extracting system for volatile oil | |
| CN202148299U (en) | Volatile oil extraction oil-water separator with condensation | |
| CN202315399U (en) | Ethanol extraction tank | |
| CN204529808U (en) | pawpaw essential oil extracting device | |
| CN206372543U (en) | A kind of low-temperature negative-pressure purifying plant | |
| CN205170790U (en) | Spices draws enrichment facility | |
| CN204671922U (en) | A kind of pumping equipment for tower | |
| CN103834473A (en) | Taxus chinensis volatile oil extracting device | |
| CN202595097U (en) | Special equipment for tea oil leaching production | |
| CN209475631U (en) | The system for preparing biomass fuel using camphor oil leaf | |
| CN201710983U (en) | Solvent distilling apparatus for extracting capsochrome | |
| CN201692682U (en) | Novel volatile oil extraction equipment | |
| CN202554994U (en) | Two-level condensing device used for extracting volatile components inside traditional Chinese medicine | |
| CN205182241U (en) | Continuous extracting device | |
| CN204307410U (en) | A kind of honeysuckle extraction steams the online oil water separator of liquid | |
| CN205235458U (en) | Suo si extractor | |
| CN202237376U (en) | Water cooling and circulating device for supercritical carbon dioxide extraction equipment | |
| CN104399284B (en) | A kind of honeysuckle extraction steams the online oil water separator of liquid and process | |
| CN202569640U (en) | Solvent recycling device in medicine extraction | |
| CN208893643U (en) | A kind of Chinese medicine extraction processing initial concentration device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151021 Termination date: 20170603 |