CN203458833U - Continuous extracting, concentrating and drying production line - Google Patents
Continuous extracting, concentrating and drying production line Download PDFInfo
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- CN203458833U CN203458833U CN201320603816.4U CN201320603816U CN203458833U CN 203458833 U CN203458833 U CN 203458833U CN 201320603816 U CN201320603816 U CN 201320603816U CN 203458833 U CN203458833 U CN 203458833U
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Abstract
The utility model provides a continuous extracting, concentrating and drying production line belonging to the technical field of plant extraction and solving the technical problem that a solvent for extraction can not be recycled or the solvent can not be directly used for extraction operation after being recovered in the prior art. The production line comprises an extracting tank, wherein a solvent tank is arranged above the extracting tank and is connected with the extracting tank, the extracting tank is connected with a first pump, the first pump is connected with a concentrator, the concentrator is connected with a first storage tank through a second pump, the first storage tank is also connected with a fourth pump, the fourth pump is connected with a powder spraying tower, the concentrator is also connected with a second storage tank, and the second storage tank is connected with the solvent tank after sequentially passing through a third pump, a cooler and a heat exchanger. By using the continuous extracting, concentrating and drying production line, the continuous extraction, concentration and dryness can be realized, and the solvent can be directly used for extraction operation after being extracted, so that the discharged solvent is reduced, and the production cost is reduced.
Description
Technical field
The utility model belongs to technical field of plant extraction, relates to a kind of equipment of plant extract, especially relates to a kind of continous way extraction, concentrated, drying production line.
Background technology
Owing to containing a large amount of active principles in plant, for these active principles are extracted, conventionally all can be extracted by the method that extractor adds solvent, the liquid after extraction concentrate with inspissator, after material after concentrating is spray-dried, becomes powder-product.
In existing extraction, concentrated, drying production line, the use extractor that people are more and inspissator, spray tower equipment integrating, but normally directly discharge of the solvent after inspissator is concentrated has caused pollution to environment; Also have after will solvent reclaiming and be used, but the solvent after reclaiming is normally placed in storage tank, directly do not put in solvent tank for extracting operation, thereby cause the use amount increase of solvent, cannot realize the direct recycling of solvent.
Utility model content
The purpose of this utility model is for the problems referred to above, and a kind of continous way extraction, concentrated, drying production line are provided; Solved that the existing extraction of prior art cannot be recycled with solvent or solvent cannot be directly used in the technical problem of extracting operation after reclaiming.
For achieving the above object, the utility model has adopted following technical proposal: a kind of continous way is extracted, concentrated, drying production line, comprise extractor, the top of described extractor is provided with a solvent tank and is connected with extractor, described extractor is connected with a pump, No. one pump is connected with inspissator, inspissator connects the first storage tank by No. two pumps, the first storage tank also connects pump No. four, No. four described pumps connect spray tower, inspissator also connects the second storage tank, and the second described storage tank is successively by being connected solvent tank after No. three pumps, cooler and heat exchangers.
In above-mentioned continous way, extract, in concentrated, drying production line, extractor successively by centrifuge with after surge tank, be connected pump No. one.
In above-mentioned continous way, extract, in concentrated, drying production line, centrifuge is arranged on the below of extractor, surge tank is arranged on the below of centrifuge.
In above-mentioned continous way, extract, in concentrated, drying production line, solvent tank is connected with extractor by valve.
In above-mentioned continous way, extract, in concentrated, drying production line, described centrifuge is horizontal screw centrifuge, tripod pendulum type batch centrifugal or disc centrifuge.
In above-mentioned continous way, extract, in concentrated, drying production line, described cooler is panel cooler or chimney cooler.
Compared with prior art, the utility model has the advantage of: can realize the extraction, concentrated and dry of continous way, and be directly used in extraction operation after solvent can being reclaimed, reduce the discharge of solvent, reduce production cost.
Accompanying drawing explanation
Fig. 1 is the structural representation that the utility model provides.
In figure, extractor 1, solvent tank 2, centrifuge 3, surge tank 4, inspissator 5, cooler 6, heat exchanger 7, valve 8, spray tower 9, pump 11, No. two pumps 12, No. three pumps 13, No. four pumps 14, the first storage tank 21, the second storage tank 22.
The specific embodiment
As shown in Figure 1, a kind of continous way is extracted, concentrated, drying production line, comprise extractor 1, the top of described extractor 1 is provided with a solvent tank 2 and is connected with extractor 1, described extractor 1 is connected with a pump 11, No. one pump 11 is connected with inspissator 5, inspissator 5 connects the first storage tank 21 by No. two pumps 12, the first storage tank 21 also connects pump 14 No. four, described No. four pumps 14 connect spray tower 9, inspissator 5 also connects the second storage tank 22, and the second described storage tank 22 is successively by No. three pumps 13, cooler 6 and the rear connection solvent of heat exchanger 7 tanks 2.In the present embodiment, in order to put forward highly enriched efficiency, inspissator 5 can preferably be selected as Multi-effect concentration devices such as two effects, triple effects, and in order to improve the efficiency of extraction, extractor 1 can preferably be selected percolate pot.
In the present embodiment, in order to the material extracting, can be food material or the medicinal raw materials such as tealeaves, buckwheat skin, coffee bean, cocoa bean, cassia seed.
The course of work of this device is, the material that needs are extracted is put in extractor 1, open valve 8 and regulate open degree, making solvent in solvent tank 2 enter into extractor 1 extracts, the solvent that is dissolved with material active ingredient after extraction liquid after centrifuge 3 Separation of Solid and Liquid flow in surge tank 4, and solid is directly discharged to outside centrifuge 3; Open No. one pump 11, liquid in surge tank 4 is driven in inspissator 5 and is concentrated, active ingredient after concentrated is driven into storage in the first storage tank 21 through No. two pumps 12, and No. four pumps 14 are delivered to spraying in spray tower 9 by the liquid after concentrated and are dried, and form the product of powder.The solvent being evaporated flow in the second storage tank 22, solvent in the second storage tank 22 is driven in solvent tank 2 through No. three pumps 13, in this process, if solvent needs cooling or heats and can carry out temperature adjusting by cooler 6 or heat exchanger 7, wherein, can optionally open as required one of them equipment in cooler 6 or heater 7, make the solvent temperature after reclaiming consistent with the temperature in solvent tank 2.
Claims (6)
1. continous way is extracted, concentrated, drying production line, comprise extractor (1), it is characterized in that, the top of described extractor (1) is provided with a solvent tank (2) and is connected with extractor (1), described extractor (1) is connected with a pump (11), a pump (11) is connected with inspissator (5), inspissator (5) connects the first storage tank (21) by No. two pumps (12), the first storage tank (21) also connects No. four pumps (14), described No. four pumps (14) connect spray tower (9), inspissator (5) also connects the second storage tank (22), described the second storage tank (22) is successively by No. three pumps (13), cooler (6) and the rear solvent tank (2) that is connected of heat exchanger (7).
2. continous way extraction according to claim 1, concentrated, drying production line, is characterized in that, extractor (1) is successively by being connected a pump (11) after centrifuge (3) and surge tank (4).
3. continous way extraction according to claim 2, concentrated, drying production line, is characterized in that, centrifuge (3) is arranged on the below of extractor (1), and surge tank (4) is arranged on the below of centrifuge (3).
4. according to the continous way extraction described in claim 1 or 2 or 3, concentrated, drying production line, it is characterized in that, solvent tank (2) is connected with extractor (1) by valve (8).
5. according to the continous way extraction described in claim 2 or 3, concentrated, drying production line, it is characterized in that, described centrifuge (3) is horizontal screw centrifuge, tripod pendulum type batch centrifugal or disc centrifuge.
6. according to the continous way extraction described in claim 1 or 2 or 3, concentrated, drying production line, it is characterized in that, described cooler (6) is panel cooler or chimney cooler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320603816.4U CN203458833U (en) | 2013-09-18 | 2013-09-18 | Continuous extracting, concentrating and drying production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320603816.4U CN203458833U (en) | 2013-09-18 | 2013-09-18 | Continuous extracting, concentrating and drying production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203458833U true CN203458833U (en) | 2014-03-05 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201320603816.4U Expired - Fee Related CN203458833U (en) | 2013-09-18 | 2013-09-18 | Continuous extracting, concentrating and drying production line |
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| Country | Link |
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| CN (1) | CN203458833U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108126361A (en) * | 2018-01-10 | 2018-06-08 | 轻工业环境保护研究所 | A kind of monosodium glutamate waste liquid is concentrated and dried device |
| CN108178216A (en) * | 2018-01-10 | 2018-06-19 | 轻工业环境保护研究所 | A kind of synergy enrichment facility |
| CN108619755A (en) * | 2018-07-19 | 2018-10-09 | 广州市海同机电设备有限公司 | A kind of plant extract, concentration, dry continuous intelligence make system |
| JP2019518590A (en) * | 2016-05-02 | 2019-07-04 | ナチュラル エクストラクション システムズ、 エルエルシー | Improved method and apparatus for extracting vegetable oil |
-
2013
- 2013-09-18 CN CN201320603816.4U patent/CN203458833U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2019518590A (en) * | 2016-05-02 | 2019-07-04 | ナチュラル エクストラクション システムズ、 エルエルシー | Improved method and apparatus for extracting vegetable oil |
| JP7020634B2 (en) | 2016-05-02 | 2022-02-16 | ナチュラル エクストラクション システムズ、 エルエルシー | How to extract oil from plant material |
| CN108126361A (en) * | 2018-01-10 | 2018-06-08 | 轻工业环境保护研究所 | A kind of monosodium glutamate waste liquid is concentrated and dried device |
| CN108178216A (en) * | 2018-01-10 | 2018-06-19 | 轻工业环境保护研究所 | A kind of synergy enrichment facility |
| CN108619755A (en) * | 2018-07-19 | 2018-10-09 | 广州市海同机电设备有限公司 | A kind of plant extract, concentration, dry continuous intelligence make system |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140305 Termination date: 20160918 |
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| CF01 | Termination of patent right due to non-payment of annual fee |