CN2593870Y - Hot reflux energy-saving extracting concentrator - Google Patents
Hot reflux energy-saving extracting concentrator Download PDFInfo
- Publication number
- CN2593870Y CN2593870Y CN 03219331 CN03219331U CN2593870Y CN 2593870 Y CN2593870 Y CN 2593870Y CN 03219331 CN03219331 CN 03219331 CN 03219331 U CN03219331 U CN 03219331U CN 2593870 Y CN2593870 Y CN 2593870Y
- Authority
- CN
- China
- Prior art keywords
- steam
- extracting
- outlet
- utility
- pipeline
- 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
- 238000010992 reflux Methods 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 230000004087 circulation Effects 0.000 claims abstract description 8
- 238000000605 extraction Methods 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 4
- 238000004134 energy conservation Methods 0.000 claims description 5
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000005507 spraying Methods 0.000 abstract 1
- 239000013589 supplement Substances 0.000 abstract 1
- 239000012141 concentrate Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 235000014347 soups Nutrition 0.000 description 4
- 239000004480 active ingredient Substances 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 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
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
Landscapes
- Extraction Or Liquid Replacement (AREA)
Abstract
The utility model relates to a hot reflux energy-saving extracting concentrator used in the industries of pharmacy, foodstuffs, etc. The utility model comprises an extracting pot. A liquid outlet of the extracting pot which is connected with a concentrating device by a pipeline, and the concentrating device is composed of a steam heater and an evaporator in an outer circulation connecting mode. A steam outlet of the extracting pot is connected to a steam heater through a steam pipe. A steam outlet of the evaporator is connected to a water storage tank through a condenser pipeline. An outlet of the water storage tank is connected to a water intake spraying pipe of the extracting pot to form a continuous circulating and extracting mechanism through a backflow pipeline. The utility model can make steam which is produced by the extracting pot serve as a heat source of the steam heater. Recovered steam which is evaporated by the evaporator flows back and supplements into the extracting pot after being condensed. The utility model has the advantages of good energy-saving and water-saving effect, continuous circulation and extraction, good extracting and concentrating effect, and high production efficiency.
Description
Technical field: the utility model relates to the soup extraction enrichment facility that industries such as a kind of pharmacy, food are used.
Background technology: general extraction enrichment facility heats the soup that extracts and enters the enrichment facility heating and concentrate in extractor, the steam that extractor and evaporimeter produce is wanted emptying, the heat of steam does not utilize, the energy consumption height, relatively water wasting, high temperature concentrates the active ingredient of destroying medicine easily, and extracts to concentrate to need to divide and carry out for several times, and production efficiency is not high.
Summary of the invention: at the deficiencies in the prior art, the utility model provides a kind of and can effectively utilize the energy-conservation hot reflux of steam to extract enrichment facility.
The utility model comprises extractor, its liquid outlet connects the enrichment facility that is connected to form by steam heater and evaporimeter outer circulation by pipeline, the steam (vapor) outlet of extractor connects steam heater by steam pipe, the steam (vapor) outlet of evaporimeter connects water storing tank by condenser pipe, and the outlet of this water storing tank then constitutes continuous circulation extraction mechanism by the water inlet shower of reflux pump pipeline connection extractor.
The steam that the utility model can produce extractor makes full use of heat as the thermal source of steam heater, and the vapor (steam) temperature when soup concentrates is lower, makes the active ingredient of medicine purer.Refluxing after the indirect steam condensation of evaporator evaporation adds in the extractor, water saving effective, and the extraction that can circulate continuously, and production efficiency improves greatly.The utility model is volatile to extracting solution except that utilizing water vapour, as alcohol, wave fragrant wet goods good energy-conservation backflow effect is also arranged.
Further specify the utility model below in conjunction with drawings and Examples.
Description of drawings: Fig. 1 is the main structure schematic diagram of embodiment;
Fig. 2 is the vertical view of Fig. 1.
Embodiment: as shown in the figure, the liquid outlet of extractor connects the enrichment facility that is connected to form by steam heater 2 and evaporimeter 3 outer circulations by pipeline, the steam (vapor) outlet of extractor 1 connects steam heater 2 by steam pipe 5, the steam (vapor) outlet of evaporimeter 3 connects water storing tank 4 by condenser 6 pipelines, and the outlet of this water storing tank 4 then connects the continuous circulation extraction mechanism of water inlet shower 8 formations of extractor 1 by reflux pump 7 pipelines.
During work, the soup that extractor 1 heating is extracted enters that heating evaporation concentrates in the enrichment facility that steam heater 2 and evaporimeter 3 form, the steam of extractor 1 by steam pipe 5 supply steam heaters 2 as thermal source.The steam that evaporimeter 3 produces enters water storing tank 4 after cooling off by condenser 6, and water then refluxes by reflux pump 7 and water inlet shower 8 and adds to the extraction that circulates continuously in the extractor 1 in this water storing tank 4.The evaporimeter 3 of present embodiment is connected in parallel to two steam heaters 2, and one of them can connect the external steam source, and the steam that produces of extractor 1 can be with the heating of external steam source not enough the time like this.
Claims (2)
1, enrichment facility is extracted in a kind of energy-conservation hot reflux, comprise extractor, its liquid outlet connects the enrichment facility that is connected to form by steam heater and evaporimeter outer circulation by pipeline, it is characterized by: the steam (vapor) outlet of extractor (1) connects steam heater (2) by steam pipe (5), the steam (vapor) outlet of evaporimeter (3) connects water storing tank (4) by condenser (6) pipeline, and the outlet of this water storing tank (4) then connects the continuous circulation extraction mechanism of water inlet shower (8) formation of extractor (1) by reflux pump (7) pipeline.
2, enrichment facility is extracted in energy-conservation hot reflux according to claim 1, and it is characterized by: evaporimeter (3) is connected in parallel to two steam heaters (2), and one of them is connected with the external steam source.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03219331 CN2593870Y (en) | 2003-01-10 | 2003-01-10 | Hot reflux energy-saving extracting concentrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03219331 CN2593870Y (en) | 2003-01-10 | 2003-01-10 | Hot reflux energy-saving extracting concentrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2593870Y true CN2593870Y (en) | 2003-12-24 |
Family
ID=33755508
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03219331 Expired - Fee Related CN2593870Y (en) | 2003-01-10 | 2003-01-10 | Hot reflux energy-saving extracting concentrator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2593870Y (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102379811A (en) * | 2011-09-19 | 2012-03-21 | 天津大明制药设备厂 | Hot reflux traditional Chinese medicine extracting device with solar external circulation heating double-tank unit |
| CN102600634A (en) * | 2011-01-25 | 2012-07-25 | 福建中烟工业有限责任公司 | Improved hot-reflux extraction and concentration equipment |
| CN106310682A (en) * | 2015-06-23 | 2017-01-11 | 施丽菊 | High-temperature organic liquid energy-saving purification system |
| CN108939606A (en) * | 2018-09-18 | 2018-12-07 | 迪茗（上海）智能科技有限公司 | A kind of extraction concentration systems and method |
| CN109529403A (en) * | 2019-01-03 | 2019-03-29 | 沈奇光 | Energy-saving dual-use traditional Chinese medicine extraction, concentrator |
| CN111336829A (en) * | 2020-03-16 | 2020-06-26 | 昆明弘承商贸有限公司 | Steam heat energy recycling process for biological product processing and extraction |
| CN113637090A (en) * | 2021-08-10 | 2021-11-12 | 张明勋 | Paper mulberry branch and bark material separation, decoction and extraction system and method |
-
2003
- 2003-01-10 CN CN 03219331 patent/CN2593870Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102600634A (en) * | 2011-01-25 | 2012-07-25 | 福建中烟工业有限责任公司 | Improved hot-reflux extraction and concentration equipment |
| CN102600634B (en) * | 2011-01-25 | 2015-01-21 | 福建中烟工业有限责任公司 | Improved hot-reflux extraction and concentration equipment |
| CN102379811A (en) * | 2011-09-19 | 2012-03-21 | 天津大明制药设备厂 | Hot reflux traditional Chinese medicine extracting device with solar external circulation heating double-tank unit |
| CN106310682A (en) * | 2015-06-23 | 2017-01-11 | 施丽菊 | High-temperature organic liquid energy-saving purification system |
| CN108939606A (en) * | 2018-09-18 | 2018-12-07 | 迪茗（上海）智能科技有限公司 | A kind of extraction concentration systems and method |
| CN109529403A (en) * | 2019-01-03 | 2019-03-29 | 沈奇光 | Energy-saving dual-use traditional Chinese medicine extraction, concentrator |
| CN111336829A (en) * | 2020-03-16 | 2020-06-26 | 昆明弘承商贸有限公司 | Steam heat energy recycling process for biological product processing and extraction |
| CN113637090A (en) * | 2021-08-10 | 2021-11-12 | 张明勋 | Paper mulberry branch and bark material separation, decoction and extraction system and method |
| CN113637090B (en) * | 2021-08-10 | 2022-07-12 | 张明勋 | Paper mulberry branch and bark material separation, decoction and extraction system and method |
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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: 20031224 |