CN201880396U - Extraction equipment for producing sea buckthorn lycopene capsules - Google Patents
Extraction equipment for producing sea buckthorn lycopene capsules Download PDFInfo
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- CN201880396U CN201880396U CN201020546658XU CN201020546658U CN201880396U CN 201880396 U CN201880396 U CN 201880396U CN 201020546658X U CN201020546658X U CN 201020546658XU CN 201020546658 U CN201020546658 U CN 201020546658U CN 201880396 U CN201880396 U CN 201880396U
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Abstract
The utility model discloses extraction equipment for producing sea buckthorn lycopene capsules. The extraction equipment comprises a water inlet pipe, an oil-water layer-separation device, a U-shaped pipe, a first branch pipe, a second branch pipe, an oil phase guide pipe, a water phase guide pipe, a guide sleeve, polytetrafluoroethylene sealing gaskets, rubber clamping pads, a liquid guide pipe, a guide pipe, an auxiliary collector, a water outlet pipe and a rubber hose, which are connected with one another; the upper part of an extraction device is connected with the water phase guide pipe, the oil phase guide pipe and the liquid guide pipe below the auxiliary collector respectively; the lower part of the extraction device is connected with the oil-water layer-separation device through the liquid guide pipe; the first branch pipe and the second branch pipe are respectively arranged on two sides of the liquid guide pipe in the oil-water layer-separation device; one branch pipe is connected with the oil phase guide pipe and the other branch pipe is connected with the U-shaped pipe below the liquid guide pipe; the water inlet pipe and the water outlet pipe are respectively arranged on the oil-water layer-separation device; and the rubber hose is connected with the oil-water layer-separation device, the extraction device and the auxiliary collector respectively. The extraction equipment disclosed by the utility model is extensively applied to the extraction field in the production of the sea buckthorn lycopene capsules.
Description
Technical field
The utility model relates to the separating and purifying technology field of active ingredients of plants, specifically is meant a kind of extraction equipment technical field that is used to produce sea-buckthorn lycopene capsule.
Background technology
Biological big son generally is to separate to obtain from animal and plant cells, compares with general chemicals, and the separation and purification of biomolecule has following characteristics: the content of large biological molecule is generally lower in the material liquid; Material liquid is multi-component mixture, and molecular weight distribution is extremely wide, and macromolecule materials such as nucleic acid, protein, polysaccharide, lipoid, phosphatide and lipopolysaccharides are arranged, and low molecular weight substances such as amino acid, organic bronsted lowry acids and bases bronsted lowry are also arranged; The less stable of large biological molecule, chemical property own are stable inadequately, meet thermal lability, meet easily degraded of acid, make the separation and purification condition comparatively harsh; Quality requirement to final products is very high, and the large biological molecule product generally is fine product such as medicine, biological reagent or food, must reach the requirement of pharmacopeia, reagent standard and codex Alimentarius.
At present, the unit that can select for use of the separation and purification of biomolecular material is quite limited.The biomolecule coarse-grain generally can extract or rare salt, diluted alkaline extract by water, carries out elementary purifying through unit operations such as absorption, extraction, precipitation and centrifugations again, and wherein typical isolation and purification method is " water extract-alcohol precipitation " method.The device of separation and purification mainly contains centrifugal separating device, settler, ion interchange unit, affine adsorbent equipment, gel filtration and ultrafiltration apparatus etc.These devices differ from one another: centrifugal separating device can adapt to very wide scale scope, limits but its usefulness can be subjected to the effect of concentration of raw material and precipitation operation; Settler can be handled a large amount of materials equally, and it is subjected to the interfering material effect littler than absorption or chromatography, but will consume a large amount of reagent and long processing time; Ion interchange unit is used for removing the compound that later separation is exerted an influence, and product purity is higher, but wants little several magnitude compared with centrifugal separating device on production capacity; Affine adsorbent equipment is the most typical with affinity chromatography, its selectivity and specificity are extremely strong, be that other device is incomparable, but fill the affinity chromatography column technology and in development, run into some because of restricted, compression and diffusion low as flow velocity, filler particles are transmitted slowly, thereby are difficult to large-scale application; Gel filtration is usually used in the separation and the desalination of protein, polysaccharide aggregation, because the Capacity Ratio of the glue filter medium that rises is less, so the treating capacity of process is little, the last of the purge process of generally being everlasting is used in the processing together; Ultrafiltration can normal-temperature operation, device is simple, energy consumption is low and selectivity is higher, has become the important means of separating mixture, but filtering rate descends and the film pollution is the subject matter that ultrafiltration runs in actual applications.At present, dialyse with continuous dialysis apparatus in the laboratory that abroad has, convenient and quick, but disposal ability is still less than normal, and the height of its efficient often depends on the concentration and the purity of crude product again.
At present, the steam that contains the aqueous solution of volatile matter in sea-buckthorn, the tomato enters extraction equipment through conduit, and after extraction, the discharge, standing demix gets final product.The extraction process of volatile matter is a discontinuous in the existing plant, promptly is discontinuous operation, therefore, has influenced operating efficiency.
Summary of the invention
The utility model is exactly at the problems referred to above, and a kind of extraction element of increasing work efficiency is provided.
The utility model adopts following technical scheme: the utility model comprises extraction element, the top of extraction element links to each other with the liquid conduits of water conduit, oil phase conduit, auxilliary storage below respectively, the below of its structural feature extraction element links to each other with oil-water decanter by liquid conduits, the both sides of the liquid conduits in the oil-water decanter are respectively arranged with arm, an arm links to each other with the oil phase conduit, and another arm links to each other with liquid conduits below U-shaped pipe: oil-water decanter is provided with water inlet pipe, outlet pipe respectively; The same respectively oil-water decanter of rubber hose, extraction element, auxilliary storage link to each other.
The extraction element that the utility model provides is used to produce sea-buckthorn lycopene capsule is made up of water inlet pipe, oil-water decanter, U-shaped pipe, first arm, second arm, oil phase conduit, water conduit, guide pin bushing, polytetrafluoroethylene sealing gasket, rubber clamp pad, liquid conduits, conduit, auxilliary storage, outlet pipe and rubber hose.Wherein, the top of extraction element links to each other with the liquid conduits of water conduit, oil phase conduit, auxilliary storage below respectively, the below of extraction element links to each other with oil-water decanter by liquid conduits, the both sides of the liquid conduits in the oil-water decanter are respectively arranged with first arm, second arm, an arm links to each other with the oil phase conduit, and another arm links to each other with liquid conduits below U-shaped pipe; Oil-water decanter is provided with water inlet pipe, outlet pipe respectively; The same respectively oil-water decanter of rubber hose, extraction element, auxilliary storage link to each other.
The utility model compared with prior art has the following advantages and beneficial effect:
Because the utility model is provided with oil-water decanter, the smaller liquid of proportion in the liquid after the just feasible extraction, (wherein oil phase participates in extraction process again to the oil phase heating kettle after arm feeds back to the oil phase conduit, plant volatile in the oil phase is stayed in the oil phase heating kettle, finally in the oil phase heating kettle, obtain plant volatile): the water that proportion is bigger the liquid is through the U-shaped pipe, arm feeds back in the water heating kettle, is added in the water conduit again, participates in extraction process again; Like this, just realize the serialization of extracting operation, thereby improved operating efficiency.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is a left view of the present utility model.
Among Fig. 1-2,1-water inlet pipe, 2-oil-water decanter, 3-U shape pipe, 4-first arm, 5 one the second arms, 6-oil phase conduit, 7-water conduit, 8-guide pin bushing, the 9-extraction element, 10-polytetrafluoroethylene sealing gasket, 11-rubber clamp pad, the 12-liquid conduits, the 13-conduit, 14-assists storage, the 15-outlet pipe, the 16-rubber hose.
The specific embodiment
Below in conjunction with drawings and Examples, the utility model is done detailed description further.
Shown in accompanying drawing, the utility model comprises extraction element (9), the top of extraction element (9) links to each other with the liquid conduits (12) of water conduit (7), oil phase conduit (6), auxilliary storage (14) below respectively, the below of extraction element (9) links to each other by the same oil-water decanter of liquid conduits (12) (2), the both sides of the liquid conduits (12) in the oil-water decanter (2) are respectively arranged with first arm (4), second arm (5), an arm (5) links to each other with oil phase conduit (6), and the same liquid conduits of another arm (4) (12) below U-shaped pipe (3) links to each other; Oil-water decanter (2) is provided with water inlet pipe (1), outlet pipe (15) respectively: the same respectively oil-water decanter of rubber hose (16) (2), extraction element (9), auxilliary storage (14) link to each other.
Oil-water decanter (2) can be glass material; Can directly observe layering, backflow effect, be convenient to continuous operation.
Junction between the pipe of water conduit (7), oil phase conduit (6) is polytetrafluoroethylene sealing gasket (10); Pipe joint is outward a rubber clamp pad (11).
Below in conjunction with a description of drawings course of action of the present utility model:
Oil vapour in the oil phase conduit (6), the aqueous solution steam that contains plant volatile enter respectively in the guide pin bushing (8) of extraction element (9): cooling water enters auxilliary storage (14), extraction element (9), oil-water decanter (2) respectively through rubber hose (16).
Major part becomes liquid under the effect of above-mentioned two kinds of steams cooling water outside guide pin bushing (8), through liquid conduits (12), enters oil-water decanter (2); The fraction steam is liquid and flows back in the extraction element (9) through the cooling of the auxilliary outer water of storage (14) conduit (13).The liquid of the interior proportion smaller portions of oil-water decanter (2) enters in the oil phase conduit (6), and the liquid of proportion major part enters in the water conduit (7) and participates in extraction process again, and making extracting operation is continuous operation.
Claims (3)
1. extraction element that is used to produce sea-buckthorn lycopene capsule, it is by water inlet pipe, oil-water decanter, the U-shaped pipe, first arm, second arm, the oil phase conduit, the water conduit, guide pin bushing, polytetrafluoroethylene sealing gasket, the rubber clamp pad, liquid conduits, conduit, auxilliary storage, outlet pipe and rubber hose are formed, it is characterized in that, the top of described extraction element is respectively with the water conduit, the oil phase conduit, the liquid conduits of auxilliary storage below links to each other, the below of extraction element links to each other with oil-water decanter by liquid conduits, the both sides of the liquid conduits in the oil-water decanter are respectively arranged with first arm, second arm, an arm links to each other with the oil phase conduit, and another arm links to each other with liquid conduits below U-shaped pipe; Oil-water decanter is provided with water inlet pipe, outlet pipe respectively; The same respectively oil-water decanter of rubber hose, extraction element, auxilliary storage link to each other.
2. the extraction element that is used to produce sea-buckthorn lycopene capsule as claimed in claim 1 is characterized in that, the junction between described water conduit, the oil phase conduit is a polytetrafluoroethylene sealing gasket.
3. the extraction element that is used to produce sea-buckthorn lycopene capsule as claimed in claim 1 is characterized in that, described pipe joint is outward the rubber clamp pad.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020546658XU CN201880396U (en) | 2010-09-29 | 2010-09-29 | Extraction equipment for producing sea buckthorn lycopene capsules |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020546658XU CN201880396U (en) | 2010-09-29 | 2010-09-29 | Extraction equipment for producing sea buckthorn lycopene capsules |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201880396U true CN201880396U (en) | 2011-06-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201020546658XU Expired - Fee Related CN201880396U (en) | 2010-09-29 | 2010-09-29 | Extraction equipment for producing sea buckthorn lycopene capsules |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201880396U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103961899A (en) * | 2013-02-06 | 2014-08-06 | 浙江大学 | Simultaneous distillation extraction device with controllable temperatures and using method thereof |
-
2010
- 2010-09-29 CN CN201020546658XU patent/CN201880396U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103961899A (en) * | 2013-02-06 | 2014-08-06 | 浙江大学 | Simultaneous distillation extraction device with controllable temperatures and using method thereof |
| CN103961899B (en) * | 2013-02-06 | 2015-08-19 | 浙江大学 | Extraction equipment and using method while controllable temperature |
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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: 20110629 Termination date: 20110929 |