CN103864958A - Method of preparing high-purity heparin sodium - Google Patents
Method of preparing high-purity heparin sodium Download PDFInfo
- Publication number
- CN103864958A CN103864958A CN201310625500.XA CN201310625500A CN103864958A CN 103864958 A CN103864958 A CN 103864958A CN 201310625500 A CN201310625500 A CN 201310625500A CN 103864958 A CN103864958 A CN 103864958A
- Authority
- CN
- China
- Prior art keywords
- heparin sodium
- organic solvent
- high purity
- preparing high
- purity heparin
- 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.)
- Pending
Links
Images
Landscapes
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Abstract
The invention discloses a method of preparing high-purity heparin sodium. The method is characterized in that under a room temperature of 298K, an organic precipitation method is adopted to remove heparin sodium-like impurities dermatan sulfate and chondroitin sulfate in the heparin sodium to prepare high-purity heparin sodium, so that the heparin sodium and similar substances thereof are separated according to solubility difference in different polar solvents. The method is suitable for purifying and separating the sodium-like impurities dermatan sulfate, chondroitin sulfate and the like in the heparin sodium to prepare the high-purity heparin sodium, and has remarkable social and beneficial benefits.
Description
Technical field
The present invention relates to biological technical field, relate in particular to a kind of method of preparing high purity heparin sodium.
Background technology
Heparin sodium and quasi-heparin substance chondroitin sulfate (CS), dermatan sulfate (DS) all belong to the mixture of mucopolysaccharide family macromolecule, the extraction of polysaccharide separates the technique of great majority employing water extract-alcohol precipitation, alcohol precipitation is different according to the molecular size range of polysaccharide, and carry out separation and purification, so when organic solvent deposit, the product difference that volume fraction difference obtains, according to the molecular weight difference of heparin sodium, CS, DS, precipitate to separate impurity CS, the DS in heparin sodium by distribution with organic solvent.
In existing isolation technique, the ion-exchange-resin process that separated to heparin sodium with similar substance CS, DS, its weak point is: take time and effort, expend reagent, complicated operation, yield are low.
For the deficiency of above-mentioned isolation technique, expend reagent in order to solve existing ion-exchange-resin process, take time and effort, the problems such as complicated operation, the invention provides one can sharp separation heparin sodium and similar substance thereof, prepares the method for high purity heparin sodium, method green non-pollution of the present invention, simple, can effectively separate heparin sodium and similar substance thereof, prepare high purity heparin sodium.
Summary of the invention
The present invention is achieved by the following technical solutions:
Prepare a method for high purity heparin sodium, according to heparin sodium and similar substance thereof, the different solubility in the organic solvent of opposed polarity reaches the separation and purification of heparin sodium and its impurity, thereby prepares highly purified heparin sodium:
Described experimental procedure is as follows:
1, take 5g heparin industry crude product (containing DS, the CS impurity of different amounts),
2, add the salt solution that contains certain percentage ratio to be uniformly dissolved,
3, be V1-V2 (Volume) to adding organic solvent volume multiple in solution,
4, evenly, normal temperature leaves standstill to be preserved for some time in vibration,
5, centrifugal, collecting precipitation, then supernatant liquor is regulated to organic solvent volume multiple is V3-V4, evenly, normal temperature leaves standstill to be preserved in vibration,
6, centrifugal, collecting precipitation, then regulate alcohol volume multiple to be V5-V6 supernatant liquor, centrifugal, collecting precipitation, dries the throw out of every part, weighs.
The concentration of the salt in described step 2 is 2%; Organic solvent in described step 3 is ethanol; Organic solvent volume fraction V1 in described step 3 is that 9.1%, V2 is 28.6%; Time of repose in described step 4 is 2 hours; Organic solvent volume fraction V3 in described step 5 is that 33.3%, V4 is 44.4%; Organic solvent volume fraction V5 in described step 6 is that 47.4%, V6 is 66.7%.
The inventive method is simple, is suitable for heparin sodium and similar substance chondroitin sulfate thereof, dermatan sulfate to carry out the free of contamination separation of quick nondestructive, provides technical support for preparing highly purified heparin sodium.
Brief description of the drawings
Fig. 1 is that percent by volume taking ethanol is as X-coordinate, to precipitate the experimental result picture of quality for the substep ethanol precipitation that ordinate zou was done
Embodiment
Below in conjunction with embodiment, the present invention is further illustrated.
Embodiment 1:
(1) take 5g heparin industry crude product (containing DS, the CS impurity of different amounts);
(2) add and contain 2% salt solution and be uniformly dissolved;
(3) be 9.1%-28.6% (Volume) to adding organic solvent volume multiple in solution;
(4) evenly, normal temperature leaves standstill 2 hours in vibration;
(5) centrifugal, collecting precipitation, then supernatant liquor is regulated to organic solvent volume multiple is 33.3%-44.4%, evenly, normal temperature leaves standstill to be preserved in vibration;
(6) centrifugal, collecting precipitation, then regulate alcohol volume multiple to be 47.4%-66.7% supernatant liquor, centrifugal, collecting precipitation, dries the throw out of every part, weighs.
(7) experimental result of ethanol substep alcohol precipitation is in table 1.
Table 1 ethanol substep alcohol precipitation experimental result
Can find out from Fig. 1 (seeing Figure of description) and associative list 1, the quality product of ethanol fractional precipitation heparin industry crude product gained has three sections: the first section volume fraction of ethanol 10% to 33%, this section precipitation quality maximum, its yield accounts for approximately 62.3% of total mass; The second section volume fraction of ethanol 35% to 47%, the quality of this section precipitation is taken second place, and its yield accounts for 24.2% of total mass; Mass ratio two sections of the 3rd section volume fraction of ethanol from 50% to 62% this section precipitation reduce, and its yield accounts for 12.3%.
From
1the qualitative analysis of H-NMR result is known: HP concentrates on the first section, be that ethanol volume multiple 0.1V-0.4V (9.1%-28.6%) is settled out HP, DS concentrates on the second section, be that ethanol volume multiple 0.5V-0.8V (33.3%-44.4%) is settled out DS, CS concentrates on the 3rd section, and ethanol volume multiple 0.9V-2.0V (47.4%-66.7%) is settled out CS.
Claims (7)
1. prepare the method for high purity heparin sodium for one kind, it is characterized in that, step is as follows: according to heparin sodium and similar substance thereof, the different solubility in the organic solvent of opposed polarity reaches the separation and purification of heparin sodium and its impurity, thereby prepares highly purified heparin sodium:
Described experimental procedure is as follows:
(1) take 5g heparin industry crude product (containing DS, the CS impurity of different amounts),
(2) add the salt solution that contains certain percentage ratio to be uniformly dissolved,
(3) be V1-V2 (Volume) to adding organic solvent volume multiple in solution,
(4) evenly, normal temperature leaves standstill to be preserved for some time in vibration,
(5) centrifugal, collecting precipitation, then supernatant liquor is regulated to organic solvent volume multiple is V3-V4, evenly, normal temperature leaves standstill to be preserved in vibration,
(6) centrifugal, collecting precipitation, then regulate alcohol volume multiple to be V5-V6 supernatant liquor, centrifugal, collecting precipitation, dries the throw out of every part, weighs.
2. a kind of method of preparing high purity heparin sodium according to claim 1, is characterized in that: the concentration of salt solution used is 2%.
3. a kind of method of preparing high purity heparin sodium according to claim 1, is characterized in that: organic solvent used is ethanol.
4. a kind of method of preparing high purity heparin sodium according to claim 1, is characterized in that: organic solvent volume fraction V1 used is that 9.1%, V2 is 28.6%.
5. a kind of method of preparing high purity heparin sodium according to claim 1, is characterized in that: organic solvent volume fraction V3 used is that 33.3%, V4 is 44.4%.
6. a kind of method of preparing high purity heparin sodium according to claim 1, is characterized in that: the standing time of normal temperature is 2 hours.
7. a kind of method of preparing high purity heparin sodium according to claim 1, is characterized in that: organic solvent volume fraction V5 used is that 47.4%, V6 is 66.7%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310625500.XA CN103864958A (en) | 2013-11-24 | 2013-11-24 | Method of preparing high-purity heparin sodium |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310625500.XA CN103864958A (en) | 2013-11-24 | 2013-11-24 | Method of preparing high-purity heparin sodium |
Publications (1)
Publication Number | Publication Date |
---|---|
CN103864958A true CN103864958A (en) | 2014-06-18 |
Family
ID=50904013
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310625500.XA Pending CN103864958A (en) | 2013-11-24 | 2013-11-24 | Method of preparing high-purity heparin sodium |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103864958A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104163878A (en) * | 2014-08-13 | 2014-11-26 | 南京健友生化制药股份有限公司 | Method for producing nadroparin calcium from heparin sodium crude product |
CN104448044A (en) * | 2014-12-24 | 2015-03-25 | 南京健友生化制药股份有限公司 | Method for decolorizing heparin sodium and lowering dermatan sulfate content |
CN104479048A (en) * | 2014-12-24 | 2015-04-01 | 青岛九龙生物医药有限公司 | Method for removing heparinoid impurities such as DS (dermatan sulfate) and the like in heparin sodium |
CN104530257A (en) * | 2014-12-24 | 2015-04-22 | 青岛九龙生物医药有限公司 | Method for separating dermatan sulfate in heparin sodium |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080318328A1 (en) * | 2004-03-24 | 2008-12-25 | Aventis Pharma S.A. | Process for oxidizing unfractionated heparins and detecting presence or absence of glycoserine in heparin and heparin products |
CN101824098A (en) * | 2010-02-12 | 2010-09-08 | 淮安麦德森化学有限公司 | Method for quickly precipitating and separating oversulfated chondroitin sulfate in sodium heparin |
CN102633906A (en) * | 2011-04-11 | 2012-08-15 | 南通天龙畜产品有限公司 | Method for removing oversulfated chondroitin sulfate in production process of crude product heparin sodium |
-
2013
- 2013-11-24 CN CN201310625500.XA patent/CN103864958A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080318328A1 (en) * | 2004-03-24 | 2008-12-25 | Aventis Pharma S.A. | Process for oxidizing unfractionated heparins and detecting presence or absence of glycoserine in heparin and heparin products |
CN101824098A (en) * | 2010-02-12 | 2010-09-08 | 淮安麦德森化学有限公司 | Method for quickly precipitating and separating oversulfated chondroitin sulfate in sodium heparin |
CN102633906A (en) * | 2011-04-11 | 2012-08-15 | 南通天龙畜产品有限公司 | Method for removing oversulfated chondroitin sulfate in production process of crude product heparin sodium |
Non-Patent Citations (1)
Title |
---|
高晓明: "肝素钠中主要杂质的NMR定量分析方法及污染肝素的分离技术研究", 《中国优秀硕士学位论文全文数据库》 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104163878A (en) * | 2014-08-13 | 2014-11-26 | 南京健友生化制药股份有限公司 | Method for producing nadroparin calcium from heparin sodium crude product |
CN104448044A (en) * | 2014-12-24 | 2015-03-25 | 南京健友生化制药股份有限公司 | Method for decolorizing heparin sodium and lowering dermatan sulfate content |
CN104479048A (en) * | 2014-12-24 | 2015-04-01 | 青岛九龙生物医药有限公司 | Method for removing heparinoid impurities such as DS (dermatan sulfate) and the like in heparin sodium |
CN104530257A (en) * | 2014-12-24 | 2015-04-22 | 青岛九龙生物医药有限公司 | Method for separating dermatan sulfate in heparin sodium |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107011125B (en) | Method for enriching cannabidiol | |
CN110283048B (en) | Preparation method of cannabidiol crystal | |
CN103864958A (en) | Method of preparing high-purity heparin sodium | |
CN105316107B (en) | Method for separating oleic acid and linoleic acid from tea seed oil | |
RU2015120458A (en) | CLEANING POLYPEPTIDES USING TWO-STAGE ULTRAFILTRATION IN A TANGENTIAL FLOW | |
CN102952187A (en) | Preparation method of high-purity bovine serum albumin | |
CN104447666B (en) | A kind of method that Aronia melanocarpa anthocyanidin extracts | |
CN105002160B (en) | The DNA of Chinese patent drug or the health products containing Chinese medicine extracting method | |
Rajendran et al. | Design of aqueous two‐phase systems for purification of hyaluronic acid produced by metabolically engineered Lactococcus lactis | |
CN104558229A (en) | Separating and purifying method for Chinese wolfberry polyose | |
Sharma et al. | Studies on pectin extraction from kinnow peel and pomace | |
CN102408318B (en) | Method for extracting and purifying sequoyitol | |
CN104356227A (en) | Efficient method for concentration and extraction of lipids, lipoprotein and apolipoprotein in serum | |
MY194118A (en) | Method for efficiently removing or recovering extractable components from biomass | |
CN107556156B (en) | Method for extracting palmitoleic acid from natural vegetable oil | |
CN107266521B (en) | Method for extracting cotton mitochondria and protein thereof | |
CN104479040A (en) | Process for extracting bamboo fungus polysaccharide | |
WO2014194362A8 (en) | Process for preparing apolipoprotein a-i (apo a-i) | |
CN105777938B (en) | A method of removing keratan sulfate from chondroitin sulfate crude extract | |
Schwerdtner et al. | The separation of male and female: A comparison of seven protocols (P) | |
CN101367728B (en) | Method for purifying chicoric acid and monocaffeyltartaric acid from echinacea purpurea extract | |
CN103642794A (en) | Large-scale preparation method of BCG-CpG-DNA | |
CN103789092A (en) | Essential oil separating and purifying method of oat bran | |
CN104557520B (en) | A kind of method of separation and purification coffic acid, forulic acid and isoferulic acid from Chinese Water extracts of propolis | |
CN104530257A (en) | Method for separating dermatan sulfate in heparin sodium |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20140618 |