CN201923970U - Lentinan separating, purifying and concentrating device - Google Patents
Lentinan separating, purifying and concentrating device Download PDFInfo
- Publication number
- CN201923970U CN201923970U CN2011200453075U CN201120045307U CN201923970U CN 201923970 U CN201923970 U CN 201923970U CN 2011200453075 U CN2011200453075 U CN 2011200453075U CN 201120045307 U CN201120045307 U CN 201120045307U CN 201923970 U CN201923970 U CN 201923970U
- Authority
- CN
- China
- Prior art keywords
- lentinan
- reverse osmosis
- separation
- pipeline
- purification
- 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 - Lifetime
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a lentinan separating, purifying and concentrating device, comprising a ceramic membrane filter system and a reverse osmosis system. In the utility model, the separation, purification and concentration of lentinan can be realized by adopting a way of ceramic membrane filtration and reverse osmosis concentration; the ceramic membrane can realize the aim of solid and liquid separation and can be used for filtering large-molecular impurities and the like, thus achieving the aim of filtering and removing impurities; the reverse osmosis system can be used for concentrating the lentinan solution effectively, thus achieving the aims of reducing consumption of ethanol, reducing energy consumption, and further reducing production cost and improving product purity.
Description
Technical field
The utility model relates to the plant extract device, particularly relates to a kind of separation and purification device of lentinan.
Background technology
Lentinan is extraction from the Mycophyta mushroom fruiting body of cultivation, separation, the resulting single polysaccharide of purifying.Has special advantage as antitumor drug: can regulate immunologic function, and make that dosage is low, curative effect is better, toxic side effect is little etc.Mainly do the treatment of malignant tumours such as Digestive tract.Usually be used, exempt the untoward reaction that curative effect produced with chemotherapeutics.Be particularly suitable for the Patients with Gastric Cancer that to perform the operation or to recur, improve patient's life treatment, prolong patient's life.
Wu Siling, Wang Xiaolin disclose a kind of separation purification method of lentinan on CN1978467A, its mainly with the lentinan extracting solution, through concentrate, alcohol precipitation, alkali molten after alcohol precipitation again, precipitation is with the molten after pre-treatment of alkali, desalination, through DEAE column chromatography, ultrafiltration, permeation parts concentrates, through precipitations such as freeze-drying or acetone, get lentinan, the inventive method has yield height, characteristics such as good product quality.But the present invention also has following shortcoming: the present invention need pass through ethanol precipitation twice, will consume a large amount of ethanol, and concentrated energy consumption height of the present invention.
Summary of the invention
In above-mentioned lentinan leaching process, the ethanol consumption is big, problems such as energy consumption height, the purpose of this utility model is, based on the membrane sepn modern technique, designs a kind of separation and purification and concentrating unit of lentinan, reach and reduce ethanol consumption, cut down the consumption of energy, and then reduce production costs, improve the purpose of product purity.
For achieving the above object, the technical scheme that the utility model proposed is: a kind of separation and purification of lentinan and concentrating unit, comprise ceramic membrane filter system and reverse osmosis system, it is characterized in that: described ceramic membrane filter system comprises that the head tank, dehvery pump, ceramic film component, the ceramic film component concentrated solution outlet that link to each other successively by feed pipe link to each other with head tank by reflux line, are equipped with a under meter on the reflux line; Described reverse osmosis system comprises concentration tank, dehvery pump, security personnel's strainer, high-pressure pump, the reverse osmosis membrane assembly that connects successively by feed pipe; Described reverse osmosis membrane assembly dialyzate outlet links to each other with dialysate tank by the dialysis pipeline, and concentrated solution outlet links to each other with concentration tank by concentrating pipeline, concentrates on the pipeline under meter is installed; Described ceramic film component dialyzate outlet links to each other with concentration tank by the dialysis pipeline.
Further, the ceramic membrane filter aperture in the described ceramic film component is 0.05 μ m-0.5 μ m.
Further,, on described reflux line and the concentrated pipeline interchanger is installed all, can realizes feed liquid is heated or lowers the temperature as a kind of optimal way of the present utility model.
In sum, the utility model is realized the separation and purification of lentinan by the mode that adopts ceramic membrane filter+reverse osmosis concentration and concentrates that ceramic membrane can be realized solid-liquid separation, and filtrations such as macromole impurity can be reached the purpose of filtering and impurity removing; Reverse osmosis then can concentrate the lentinan feed liquid efficiently, reaches and reduces ethanol consumption, cuts down the consumption of energy, and then reduces production costs, and improves the purpose of product purity.
Description of drawings
Fig. 1 is the separation and purification and the concentrating unit of lentinan described in the utility model;
Wherein: 1. the ceramic membrane filter system, 2. reverse osmosis system, 101. head tanks, 102. dehvery pumps, 103. feed pipes, 104. ceramic film components, 105. reflux lines, 106. under meters, 107. interchanger, 108. dialysis pipelines, 201. concentration tanks, 202. feed pipes, 203. dehvery pumps, 204. security personnel's strainers, 205. high-pressure pump, 206. reverse osmosis membrane assemblies, 207. concentration tanks dialysis pipeline, 208. concentrate pipelines, 209. under meters, 210. interchanger.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described further.
Shown in the separation and purification and concentrating unit of Fig. 1 lentinan described in the utility model, a kind of separation and purification of lentinan and concentrating unit, comprise ceramic membrane filter system 1 and reverse osmosis system 2, described ceramic membrane filter system 1 comprises that the head tank 101, dehvery pump 102, ceramic film component 104, ceramic film component 104 concentrated solution outlets that link to each other successively by feed pipe 103 link to each other with head tank 101 by reflux line 105, are equipped with a under meter 106 on the reflux line 105; Reverse osmosis system 2 comprises concentration tank 201, dehvery pump 203, security personnel's strainer 204, high-pressure pump 205, the reverse osmosis membrane assembly 206 that connects successively by feed pipe 202; The outlet of reverse osmosis membrane assembly 206 dialyzates links to each other with dialysate tank 211 by dialysis pipeline 207, and concentrated solution outlet links to each other with concentration tank 201 by concentrating pipeline 208, concentrates on the pipeline 208 under meter 209 is installed; Described ceramic film component 104 dialyzates outlet links to each other with concentration tank 201 by dialysis pipeline 108.Ceramic membrane filter aperture in the described ceramic film component 104 is 0.05 μ m-0.5 μ m.One interchanger 107,210 is installed on described reflux line 105 and the concentrated pipeline 208.
During concrete the use, lentinan precipitation solution in the head tank 101 pumps in the ceramic film component 104 by dehvery pump 102 through feed pipe 103, ceramic membrane filter aperture in the ceramic film component is 0.05 μ m-0.5 μ m, is back to through reflux line 105 by the isolated solid of ceramic membrane and macromole impurity and carries out circulating filtration in the head tank 101; The dialyzate of permeation ceramic membrane then enters in the concentration tank 201 through dialysis pipeline 108, and pump into security personnel's strainer 204 after pump in the reverse osmosis system 201 after high-pressure pump 205 pressurization through dehvery pump 203 by feed pipe 202, the dialyzate that sees through reverse osmosis membrane enters in the dialysate tank 211 through dialysis pipeline 207, the lentinan concentrated solution is back in the concentration tank 201 by concentrating pipeline 208, the circulation that reaches lentinan concentrates, if feed temperature is too high, then can realize feed liquid is heated or lowers the temperature by interchanger 107,210
Although specifically show and introduced the utility model in conjunction with preferred embodiment; but the those skilled in the art should be understood that; in the spirit and scope of the present utility model that do not break away from appended claims and limited; in the form and details the utility model is made various variations, be protection domain of the present utility model.
Claims (4)
1. the separation and purification of a lentinan and concentrating unit, comprise ceramic membrane filter system (1) and reverse osmosis system (2), it is characterized in that: described ceramic membrane filter system (1) comprises that the head tank (101), dehvery pump (102), ceramic film component (104), ceramic film component (104) concentrated solution outlet that link to each other successively by feed pipe (103) link to each other with head tank (101) by reflux line (105), are equipped with a under meter (106) on the reflux line (105); Described reverse osmosis system (2) comprises concentration tank (201), dehvery pump (203), security personnel's strainer (204), high-pressure pump (205), the reverse osmosis membrane assembly (206) that connects successively by feed pipe (202); The outlet of described reverse osmosis membrane assembly (206) dialyzate links to each other with dialysate tank (211) by dialysis pipeline (207), concentrated solution outlet links to each other with concentration tank (201) by concentrating pipeline (208), concentrates on the pipeline (208) under meter (209) is installed; The outlet of described ceramic film component (104) dialyzate links to each other with concentration tank (201) by dialysis pipeline (108).
2. the separation and purification of a kind of lentinan according to claim 1 and concentrating unit is characterized in that the ceramic membrane filter aperture in the described ceramic film component (104) is 0.05 μ m-0.5 μ m.
3. the separation and purification of a kind of lentinan according to claim 1 and 2 and concentrating unit is characterized in that being equipped with on the described reflux line (105) interchanger (107).
4. the separation and purification of a kind of lentinan according to claim 1 and 2 and concentrating unit is characterized in that being equipped with on the described concentrated pipeline (208) interchanger (210).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200453075U CN201923970U (en) | 2011-02-23 | 2011-02-23 | Lentinan separating, purifying and concentrating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200453075U CN201923970U (en) | 2011-02-23 | 2011-02-23 | Lentinan separating, purifying and concentrating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201923970U true CN201923970U (en) | 2011-08-10 |
Family
ID=44427834
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200453075U Expired - Lifetime CN201923970U (en) | 2011-02-23 | 2011-02-23 | Lentinan separating, purifying and concentrating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201923970U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103084066A (en) * | 2013-01-23 | 2013-05-08 | 余苟 | Membrane filtration gelatin dehydration preconcentration system |
| CN112898448A (en) * | 2021-03-15 | 2021-06-04 | 贵州省工程复合材料中心 | Lentinan extraction system and extraction method |
-
2011
- 2011-02-23 CN CN2011200453075U patent/CN201923970U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103084066A (en) * | 2013-01-23 | 2013-05-08 | 余苟 | Membrane filtration gelatin dehydration preconcentration system |
| CN112898448A (en) * | 2021-03-15 | 2021-06-04 | 贵州省工程复合材料中心 | Lentinan extraction system and extraction method |
| CN112898448B (en) * | 2021-03-15 | 2022-08-02 | 贵州省工程复合材料中心有限公司 | Lentinan extraction system and extraction method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201990619U (en) | Lentinan extraction, separation, purification and concentration device | |
| CN203866137U (en) | Direct drinking water purification system for building pipeline | |
| CN103772523B (en) | A kind of membrane separation and purification technology prepares Pachymose extract novel process | |
| CN104163849A (en) | Separation and purification method of N(2)-L-alanyl-L-glutamine | |
| CN201923970U (en) | Lentinan separating, purifying and concentrating device | |
| CN202465570U (en) | Device for comprehensively extracting active substances in asparagus through multi-level membrane separation and purification | |
| CN102603478A (en) | Method for separating and purifying erythritol from mother liquid obtained after repeated crystallization of erythritol | |
| CN103815405B (en) | The production system of cistanche extracts | |
| CN202080964U (en) | Multi-purpose water-treatment facility | |
| CN205556296U (en) | Water treatment system | |
| CN210261597U (en) | Device for extracting cannabidiol from cannabis sativa | |
| CN104788515B (en) | Method for preparing high-purity water-soluble oleuropein by reduced pressure ultrasonic-assisted extraction | |
| CN101921343A (en) | Method for extracting polysaccharide from fresh hedgehog hydnum | |
| CN103860626A (en) | Method for preparing total flavonoids in eucommia ulmoides leaves | |
| CN210560185U (en) | Device for purifying and recovering protein peptide by membrane method | |
| CN116239132A (en) | Method for recovering carbonate in process of preparing battery-grade lithium carbonate from salt lake brine | |
| CN102372788A (en) | Mactra veneriformis glycosaminoglycan extraction method | |
| CN201512490U (en) | Integrated device for extracting, separating and concentrating anthocyanin of vaccinium vitis-idaea | |
| CN207525085U (en) | A kind of water for pharmaceutical purposes purifying processing device | |
| CN102584611A (en) | Production method for medical grade valine | |
| CN202909639U (en) | Separation, purification and concentration device for glycyrrhizic acid extract | |
| CN208949005U (en) | Primary reverse osmosis water system for preparing ergothioneine through biological fermentation synthesis | |
| CN106565813B (en) | The processing method that a kind of Tea Saponin continuously purifies | |
| CN101735135A (en) | Method for concentrating 5-hydroxyl tryptophan | |
| CN202705273U (en) | D-ribose extraction and purification production line |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180718 Address after: 068350 Fengning Economic Development Zone, Chengde, Hebei Patentee after: Fengning Ping'an High-Tech Industrial Co., Ltd. Address before: 361009 two software park, Siming District, Xiamen, Fujian, 10, 601 Patentee before: Sepatec Environmental Protection Technology (Xiamen) Co., Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110810 |