CN204485365U - One Plants system for continuously extracting - Google Patents
One Plants system for continuously extracting Download PDFInfo
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- CN204485365U CN204485365U CN201520140180.3U CN201520140180U CN204485365U CN 204485365 U CN204485365 U CN 204485365U CN 201520140180 U CN201520140180 U CN 201520140180U CN 204485365 U CN204485365 U CN 204485365U
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Abstract
The utility model relates to a Plants system for continuously extracting, belongs to Continuous Flow extraction equipment technical field.It comprises tank body, pipeline and liquid pump; Tank body comprises hot-water cylinder and batch can, and described batch can comprises a tank, No. two tanks, No. three tanks and No. four tanks, and pipeline comprises material loading house steward, material loading branched pipe, feed back branched pipe, feed back house steward, backflow material loading branched pipe, tandem feed back pipe; The top of described batch can is all connected with material loading branched pipe and backflow material loading branched pipe, and the bottom of described batch can is all connected with feed back branched pipe and tandem feed back pipe; Feed back house steward is provided with at least three valves, and one is arranged between a tank and No. two tanks, and it two is arranged between No. two tanks and No. three tanks, and it three is arranged between No. three tanks and No. four tanks.The utility model can realize continuous dosing, continuous discharge, and eliminate batch between difference, reach and carry high product yield, reduce energy consumption, save solvent, the object of convenient operation.
Description
Technical field
The utility model relates to a Plants system for continuously extracting, belongs to Continuous Flow extraction equipment technical field.
Background technology
Continuous Flow is extracted can save solvent effectively, and carries high product yield, and therefore increasing enterprise all brings into use this technology.But different plants contains dissimilar natural active matter, its extracting method and Extraction solvent may have difference, react on equipment, also make device structure varied.If application number is the Chinese invention patent of 200610125091.7, disclose a kind of Chinese medicine continuous circulation and extract method for concentration and equipment, the equipment adopted comprises medicinal liquid extraction tank, solvent tank and alembic, its method adds Extraction solvent in alembic, constantly flow in extractor after conduit condensation through heating, after soaking medicinal material, after liquid level reach a certain height, extract enters in alembic by the whole siphon of Soxhlet capillarity automatically, continuous circulation, until extract completely, extract in alembic continues heating, a storage tank is imported stand-by after solvent condenses, liquid after concentrated can enter next process, solvent in storage tank can be used for extracting next time.The continuous extraction of this invention is to same batch materials from the continuous operation being dosed into the whole process of product output, but not the Continuous Flow in Modern Significance is extracted.Continuous Flow described here is extracted and is referred to the material adding different batches in multiple batch can, then with the extractant of rear extract together as first one, be intended to eliminate batch between difference, increase the yield of product, the extract such as adopting the 3rd road extraction process to produce backflows in second extraction process as the extractant of second extraction process, backflow in first extraction process as the extractant of first extraction process with the extract that second extraction process produces, moment keeps this extracting mode, until discharging, discharging is also the circulation discharging between different batch can, do like this and just can realize continuous dosing, continuous discharge, and eliminate batch between difference, reach and carry high product yield, reduce energy consumption, save solvent, the object of convenient operation.And existing extraction equipment is difficult to realize above-mentioned purpose.
Utility model content
The utility model will solve the problems of the technologies described above, thus provides a Plants system for continuously extracting.
The technical scheme that the utility model solves the problem is as follows:
One Plants system for continuously extracting, comprise some tank bodies, for connect tank body pipeline, be arranged on liquid pump on pipeline; Described tank body comprises hot-water cylinder and batch can, described batch can at least comprises a tank, No. two tanks, No. three tanks and No. four tanks, and described pipeline comprises a material loading house steward, some material loading branched pipes, some feed back branched pipes, feed back house steward, some backflow material loading branched pipes, some tandem feed back pipes; Each described pipeline is provided with at least one valve, the top of described batch can is all directly or indirectly connected with described material loading branched pipe and backflow material loading branched pipe, and the bottom of described batch can is all directly or indirectly connected with described feed back branched pipe and tandem feed back pipe; Described feed back house steward is provided with at least three valves, and one is arranged between a tank and No. two tanks, and it two is arranged between No. two tanks and No. three tanks, and it three is arranged between No. three tanks and No. four tanks.
The enforcement of the utility model technique scheme, can realize Continuous Flow and extract, can add the material of different batches in multiple batch can, then with rear extract together as front extractant together, the difference between can eliminating batch, increases the yield of product.
Preferred as technique scheme, the bottom of a described tank, No. two tanks, No. three tanks and No. four tanks is provided with independently discharge duct.
Preferred as technique scheme, described material loading house steward and feed back house steward are provided with described liquid pump.
Preferred as technique scheme, described hot-water cylinder is arranged at the technological process upstream of batch can, and is connected with each batch can with material loading branched pipe by described material loading house steward.
Preferred as technique scheme, by material loading house steward, material loading branched pipe, feed back branched pipe and feed back house steward between described batch can) realize parallel connection, realize series connection by the valve on material loading house steward, material loading branched pipe, tandem feed back pipe, feed back house steward and these pipelines.
Preferred as technique scheme, described extraction system realizes extracting continuously by the valve on tandem feed back pipe, feed back house steward, backflow material loading branched pipe and these pipelines.
In sum, the utility model has following beneficial effect:
The utility model can realize continuous dosing, continuous discharge, and eliminate batch between difference, reach and carry high product yield, reduce energy consumption, save solvent, the object of convenient operation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
In figure, No. 1 tanks, 2 No. two tanks, 3 No. three tanks, 4 No. four tanks, 5 hot-water cylinders, 6 liquid pumps, 7 pipelines, 8 valves;
7-1 material loading house steward, 7-2 material loading branched pipe, 7-3 feed back branched pipe, 7-4 feed back house steward, 7-5 backflow material loading branched pipe, 7-6 tandem feed back pipe, 7-7 discharge duct.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is further detailed.
This detailed description of the invention is only to explanation of the present utility model; be not to restriction of the present utility model; any change that those skilled in the art are done after having read description of the present utility model, as long as in the protection domain of claims, all will be subject to the protection of Patent Law.
As shown in Figure 1, a Plants system for continuously extracting, comprises some tank bodies, for connecting the pipeline 7 of tank body, the liquid pump 6 be arranged on pipeline; Described tank body comprises hot-water cylinder 5 and batch can, described batch can comprises a tank 1, No. two tanks 2, No. three tanks 3 and No. four tanks 4, and described pipeline 7 comprises a material loading house steward 7-1, four material loading branched pipe 7-2, four feed back branched pipe 7-3, feed back house steward 7-4, three backflow material loading branched pipe 7-5, some tandem feed back pipe 7-6; Each described pipeline is provided with at least one valve 8, the top of described batch can is all directly or indirectly connected with described material loading branched pipe 7-2 and backflow material loading branched pipe 7-5, and the bottom of described batch can is all directly or indirectly connected with described feed back branched pipe 7-3 and tandem feed back pipe 7-6; Described feed back house steward 7-4 is provided with at least three valves, and one is arranged between a tank 1 and No. two tanks 2, and it two is arranged between No. two tanks 2 and No. three tanks 3, and it three is arranged between No. three tanks 3 and No. four tanks 4.The bottom of a described tank 1, No. two tanks, 2, No. three tanks 3 and No. four tanks 4 is provided with independently discharge duct 7-7.Described material loading house steward 7-1 and feed back house steward 7-4 is provided with described liquid pump 6.Described hot-water cylinder 5 is arranged at the technological process upstream of batch can, and is connected with each batch can with material loading branched pipe 7-2 by described material loading house steward 7-1.Realized by material loading house steward 7-1, material loading branched pipe 7-2, feed back branched pipe 7-3 and feed back house steward 7-4 in parallel between described batch can, realize series connection by the valve on material loading house steward 7-1, material loading branched pipe 7-2, tandem feed back pipe 7-6, feed back house steward 7-4 and these pipelines.Described extraction system realizes extracting continuously by the valve on tandem feed back pipe 7-6, feed back house steward 7-4, backflow material loading branched pipe 7-5 and these pipelines.
The utility model concrete operations are as follows:
A tank is just carrying out carrying out carrying out first extraction in second extraction, No. four tanks in the 3rd road extraction, No. three tanks in discharging state, No. two tanks; Now corresponding valve state is:
Due to material loading house steward 7-1 and material loading branched pipe 7-2 conveying is solvent, and their valve is looked actual conditions and opened or close;
Valve on feed back branched pipe 7-3 only close a tank 1,
Valve Close All on feed back house steward 7-4;
The valve of backflow feeding tube 7-5 only opens No. two tanks 2;
The valve of tandem feed back pipe 7-6 is only closed between a tank 1 and No. two tanks 2;
The valve of discharge duct 7-7 only opens No. four tanks 4;
Thus guarantee that liquid flows to: the pattern (in this stage, the discharging of feed liquid is carried out at No. four tanks, and the discharging of material slag is carried out at a tank) of No. two tanks-No. three tanks-No. four tank-dischargings; Until complete one extraction again.Complete after this extracts together, tank 1 discharging is complete and load virgin material and add new solvent, it be equivalent to this extracted together before No. four tanks; No. two tanks 2 complete the 3rd road extraction needs discharging, and it is equivalent to this and has extracted last tank 1 together; No. three tanks 3 complete second extraction to be needed to carry out the 3rd road extraction, and it is equivalent to this and has extracted the first two number tank 2 together; No. four tanks 4 complete first and extract, and need to carry out second extraction, it be equivalent to this extracted together before No. three tanks 3.Now, only need corresponding adjustment valve, guarantee that the liquid of a new round flows to :-number tank-discharging of No. three tanks-No. four tanks; Guarantee before this one abstraction process back to back completes, complete the discharging to No. two tanks 2 and filling virgin material simultaneously.
Therefore after the utility model is implemented, always there are three in four tanks at any time all in the operation carrying out extracting, always circulate and a certain tank is carried out to the operation of discharging and filling virgin material.And the extractant that the extractant that the 3rd road extract extracts as second, second extract extract as first, complete first extract liquid as thick separation of products out; And complete the material extracted in the 3rd road and unload from batch can as material slag, achieve material, separation that liquid unloads tank.
Claims (6)
1. a Plants system for continuously extracting, is characterized in that: comprise some tank bodies, for connecting the pipeline (7) of tank body, the liquid pump (6) be arranged on pipeline; Described tank body comprises hot-water cylinder (5) and batch can, described batch can at least comprises a tank (1), No. two tanks (2), No. three tanks (3) and No. four tanks (4), and described pipeline (7) comprises a material loading house steward (7-1), some material loading branched pipes (7-2), some feed back branched pipes (7-3), feed back house steward (7-4), some backflow material loading branched pipes (7-5), some tandem feed back pipes (7-6); Each described pipeline is provided with at least one valve (8), the top of described batch can is all directly or indirectly connected with described material loading branched pipe (7-2) and backflow material loading branched pipe (7-5), and the bottom of described batch can is all directly or indirectly connected with described feed back branched pipe (7-3) and tandem feed back pipe (7-6); Described feed back house steward (7-4) is provided with at least three valves, and one is arranged between a tank (1) and No. two tanks (2), and it two is arranged between No. two tanks (2) and No. three tanks (3), and it three is arranged between No. three tanks (3) and No. four tanks (4).
2. a Plants system for continuously extracting according to claim 1, is characterized in that: the bottom of a described tank (1), No. two tanks (2), No. three tanks (3) and No. four tanks (4) is provided with independently discharge duct (7-7).
3. a Plants system for continuously extracting according to claim 1 and 2, is characterized in that: described material loading house steward (7-1) and feed back house steward (7-4) are provided with described liquid pump (6).
4. a Plants system for continuously extracting according to claim 1 and 2, is characterized in that: described hot-water cylinder (5) is arranged at the technological process upstream of batch can, and is connected with each batch can with material loading branched pipe (7-2) by described material loading house steward (7-1).
5. a Plants system for continuously extracting according to claim 1 and 2, it is characterized in that: realized by material loading house steward (7-2), material loading branched pipe (7-2), feed back branched pipe (7-3) and feed back house steward (7-4) in parallel between described batch can, realize series connection by the valve on material loading house steward (7-1), material loading branched pipe (7-2), tandem feed back pipe (7-6), feed back house steward (7-4) and these pipelines.
6. a Plants system for continuously extracting according to claim 1 and 2, is characterized in that: described extraction system realizes extracting continuously by the valve on tandem feed back pipe (7-6), feed back house steward (7-4), backflow material loading branched pipe (7-5) and these pipelines.
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CN201520140180.3U CN204485365U (en) | 2015-03-12 | 2015-03-12 | One Plants system for continuously extracting |
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CN201520140180.3U CN204485365U (en) | 2015-03-12 | 2015-03-12 | One Plants system for continuously extracting |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104759110A (en) * | 2015-03-12 | 2015-07-08 | 浙江天草生物科技股份有限公司 | Plant continuous extraction system |
CN109011687A (en) * | 2018-08-31 | 2018-12-18 | 王吟箫 | A kind of duo-sol extraction method |
-
2015
- 2015-03-12 CN CN201520140180.3U patent/CN204485365U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104759110A (en) * | 2015-03-12 | 2015-07-08 | 浙江天草生物科技股份有限公司 | Plant continuous extraction system |
CN109011687A (en) * | 2018-08-31 | 2018-12-18 | 王吟箫 | A kind of duo-sol extraction method |
CN109011687B (en) * | 2018-08-31 | 2020-11-27 | 山东洲星天然物提取智能设备有限公司 | Double-solvent extraction method |
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