CN1757644A - Method for recrystallizing lactide by using ethanol - Google Patents
Method for recrystallizing lactide by using ethanol Download PDFInfo
- Publication number
- CN1757644A CN1757644A CN200510094846.7A CN200510094846A CN1757644A CN 1757644 A CN1757644 A CN 1757644A CN 200510094846 A CN200510094846 A CN 200510094846A CN 1757644 A CN1757644 A CN 1757644A
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- CN
- China
- Prior art keywords
- lactide
- rac
- crystallization
- ethanol
- crystallization time
- Prior art date
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- JJTUDXZGHPGLLC-UHFFFAOYSA-N lactide Chemical compound CC1OC(=O)C(C)OC1=O JJTUDXZGHPGLLC-UHFFFAOYSA-N 0.000 title claims abstract description 41
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims abstract description 25
- 238000002425 crystallisation Methods 0.000 claims abstract description 25
- 230000008025 crystallization Effects 0.000 claims abstract description 25
- 238000001953 recrystallisation Methods 0.000 claims abstract description 13
- 239000013078 crystal Substances 0.000 claims description 10
- 239000002904 solvent Substances 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 2
- 238000001816 cooling Methods 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 12
- 235000019441 ethanol Nutrition 0.000 description 8
- -1 cyclic ester Chemical class 0.000 description 7
- 239000004310 lactic acid Substances 0.000 description 7
- 229920000747 poly(lactic acid) Polymers 0.000 description 7
- 235000014655 lactic acid Nutrition 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- 239000012535 impurity Substances 0.000 description 5
- 230000007062 hydrolysis Effects 0.000 description 4
- 238000006460 hydrolysis reaction Methods 0.000 description 4
- 239000004626 polylactic acid Substances 0.000 description 4
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- JVTAAEKCZFNVCJ-REOHCLBHSA-N L-lactic acid Chemical group C[C@H](O)C(O)=O JVTAAEKCZFNVCJ-REOHCLBHSA-N 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000001291 vacuum drying Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- JVTAAEKCZFNVCJ-UWTATZPHSA-N D-lactic acid Chemical group C[C@@H](O)C(O)=O JVTAAEKCZFNVCJ-UWTATZPHSA-N 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- JJTUDXZGHPGLLC-ZXZARUISSA-N (3r,6s)-3,6-dimethyl-1,4-dioxane-2,5-dione Chemical compound C[C@H]1OC(=O)[C@H](C)OC1=O JJTUDXZGHPGLLC-ZXZARUISSA-N 0.000 description 1
- RKDVKSZUMVYZHH-UHFFFAOYSA-N 1,4-dioxane-2,5-dione Chemical compound O=C1COC(=O)CO1 RKDVKSZUMVYZHH-UHFFFAOYSA-N 0.000 description 1
- MNKRTDOUBUSQHX-UHFFFAOYSA-N 2,4-dihydroxy-2-methyl-3-oxopentanoic acid Chemical compound CC(O)C(=O)C(C)(O)C(O)=O MNKRTDOUBUSQHX-UHFFFAOYSA-N 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- JYYOBHFYCIDXHH-UHFFFAOYSA-N carbonic acid;hydrate Chemical compound O.OC(O)=O JYYOBHFYCIDXHH-UHFFFAOYSA-N 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 239000000539 dimer Substances 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000002407 tissue scaffold Substances 0.000 description 1
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention relates to a method for recrystallizing lactide by using ethanol as a solvent, which comprises the following steps: dissolving lactide in ethanol under heating, cooling the solution for crystallization, and filtering to obtain a crystalline product. The invention is characterized in that: the concentration of the ethanolic solution of lactide, and the crystallization time of the solutions of different concentrations, were controlled. The invention can improve the quality of the crystallized product and improve the recrystallization efficiency.
Description
Technical field
The present invention relates to a kind of purification process of cyclic ester class organic compound.Specifically, a kind ofly exactly make impure rac-Lactide, reach the method for purifying by the crystallization control time being in the recrystallization process of solvent with ethanol.
Background technology
Rac-Lactide is a kind of cyclic ester that is generated by two molecule lactic acid, has four kinds of forms: the L-rac-Lactide that two molecule L-lactic acid forms; The D-rac-Lactide that two molecule D-lactic acid form; The Study of Meso-Lactide that a part L-lactic acid and a part D-lactic acid form; And the rac-lactide of L-rac-Lactide and the formation of D-rac-Lactide.Rac-Lactide is a kind of important compound that can be used for preparing poly(lactic acid) and multipolymer thereof.
As everyone knows, poly(lactic acid) and multipolymer thereof are as Biodegradable material, and have two big outstanding advantages: its raw material---lactic acid can be obtained by fermentation, belongs to renewable resources; Its finished product can be become carbonic acid gas and water by microbiological degradation, reach degraded fully, can not produce environment and pollute.Therefore, the research of relevant polylactic acid-based material causes extensive concern.
High molecular weight polylactic acid is normally obtained by highly purified rac-Lactide ring-opening polymerization.Usually, rac-Lactide by aqueous lactic acid through low molecular weight as intermediate, obtain by the cracked method again.Patent CN1212343, CN1369490, AU2003231482, DE3232103, DE3708915, FR2843390, JP63101378, JP2004149418, US1095205, US5053522, US2002132967 etc. have introduced the building-up process of rac-Lactide.
In the rac-Lactide that above-mentioned patented method obtains, also contain impurity (rac-Lactide that hereinafter will contain these impurity is called impure rac-Lactide) such as a small amount of lactic acid monomer, lactic acid dipolymer (lactyllactic acid) and water.
Contained above-mentioned impurity can have a negative impact to the polyreaction of rac-Lactide: the existence of water can make the rac-Lactide hydrolysis obtain lactic acid, and can make polylactic acid molecule chain hydrolytic cleavage; The existence of acid such as lactic acid and dimer thereof can make the polylactic acid molecule chain be degraded etc. because of acidolysis.Therefore, impure rac-Lactide need be through purifying to remove the impurity that it contains.
The purification process of impure rac-Lactide generally has evaporation method of air aided, hydrolysis method and recrystallization method etc.
Evaporation method of air aided can make such as rac-Lactide or glycollide or and composition thereof cyclic ester be separated with impurity as the steam component in the air-flow.Relevant patent has AU2003295252, US5274073, US6277951 etc.But evaporation method of air aided sepn process complexity, and yield is generally not high.
Thereby hydrolysis method is a kind of method that mesoisomer obtains the high-optical-purity rac-Lactide of removing from impure rac-Lactide, and relevant patent has CN1112559, JP10025288, US5502215 etc.But after the hydrolysis treatment, generally still need recrystallization to be further purified.
And recrystallization method is few because of its operation steps, technology is used comparatively extensive than maturation.Patent CN1488628, FR2843390, WO9315069 etc. introduce recrystallization method purifying rac-Lactide.But the research for recrystallization method purifying rac-Lactide mostly is choice of Solvent greatly at present, adopt ethyl acetate, JP10279577 to adopt lower member ester class, US6313319 to use alcohols, JP6279435 application lower alcohol, ketone, ester class or its mixture etc. as patent US4727163, CN1583740, and the influence factor of lactide recrystallization technology is not studied.
This patent finds that rac-Lactide adopts different crystallization times when a certain solvent and a certain concentration, and the yield of its recrystallized product and purity have very big difference, and also influential to production efficiency, but this point does not cause people's attention.For example Japanese Patent JP7118259 is when describing the method for recrystallization, crystallizing system is cooled to the temperature that sets after, filter immediately and obtain crystal, its yield has only 50～52%, one of its reason may be crystallization time too short due to.Equally, document Bioresorbable Electrospun Tissue Scaffolds of Poly (ethylene glycol-b-lactide) Copolymers forBone Tissue Engineering one literary composition (Anand Shreyans Badami, Richmond:Virginia Polytechnic Instituteand State University, 2004) in crystallizing system placed that 1 hour after-filtration obtains the rac-Lactide crystal in the ice-water bath, also have the too short problem of crystallization time in this technology.And at document " the purification process research of the research of Biodegradable Polylactide (II) lactide monomer " (Heilongjiang University's natural science journal, 1998,15 (1): 110～113), crystallization time is decided to be 24 hours, this makes that again crystallization time is long, product purity and yield are descended, more prolonged the production cycle greatly.
The present invention particularly points out: crystallization time is too short, can cause product yield low; And crystallization time is long, can cause product purity poor, and productivity reduces.By control, can effectively improve the yield and the purity of crystallized product, and enhance productivity the crystallization time of different concns solution in the recrystallization process.
Summary of the invention
Purpose of the present invention promptly for the rac-Lactide ethanolic soln of different concns, by the control to crystallization time, makes product obtain better purity and crystallization yield.
Purpose of the present invention can reach by following measure:
A is dissolved in ethanol with impure rac-Lactide under 60 ℃～75 ℃, obtain solution;
B is under 0 ℃～30 ℃, and with solution left standstill, the crystallization of chien shih rac-Lactide is separated out during crystallization control;
C filters and obtains crystal and dry.
In further of the present invention, rac-Lactide ethanolic soln concentration is 30%～100%, best in quality concentration range 45%～70%.
The crystallization time of being controlled is 0.5～6 hour, optimum range 1～3 hour.
Advantage of the present invention: controlled by crystallization time, effectively improve the yield and the purity of crystallized product, and enhance productivity to the rac-Lactide ethanolic soln of different concns in the recrystallization process.
Embodiment
Embodiment 1
Add the impure rac-Lactide of 10.0g (through surveying 86 ℃～95 ℃ of melting ranges) in single neck flask, press mass ratio 30% and add ethanol 33.3g, be heated to 75 ℃ of dissolvings.After the dissolving fully, in 4 ℃ of refrigerators, left standstill crystallization 1 hour, filter and obtain crystal and vacuum-drying.Dry back crystal mass 8.4g, yield 84.0%, surveying its melting range is 94 ℃～96 ℃.
Embodiment 2
Add the impure rac-Lactide of 10.0g (through surveying 89 ℃～95 ℃ of melting ranges) in single neck flask, press mass ratio 45% and add ethanol 22.2g, be heated to 75 ℃ of dissolvings.After the dissolving fully, in 4 ℃ of refrigerators, left standstill crystallization 4 hours, filter and obtain crystal and vacuum-drying.Dry back crystal mass 8.8g, yield 88.0%, surveying its melting range is 93 ℃～96 ℃.
Embodiment 3
Add the impure rac-Lactide of 10.0g (through surveying 85 ℃～95 ℃ of melting ranges) in single neck flask, press mass ratio 70% and add ethanol 14.3g, be heated to 75 ℃ of dissolvings.After the dissolving fully, in 4 ℃ of refrigerators, left standstill crystallization 6 hours, filter and obtain crystal and vacuum-drying.Dry back crystal mass 9.0g, yield 90.0%, surveying its melting range is 91 ℃～95 ℃.
Claims (5)
1. the present invention is the method for a kind of crystallization or recrystallization purifying rac-Lactide, and this method comprises:
A is dissolved in ethanol with impure rac-Lactide under 60 ℃～75 ℃, obtain solution;
B is under 0 ℃～30 ℃, and with solution left standstill, the crystallization of chien shih rac-Lactide is separated out during crystallization control;
C filters and obtains crystal and dry.
2. according to the process of claim 1 wherein that the described rac-Lactide solution quality of steps A concentration is 30%～100%.
3. according to the method for claim 2, wherein rac-Lactide solution quality concentration is 45%～70%.
4. according to the method for claim 1, it is characterized in that the described crystallization time of controlling of step B is 0.5～6 hour.
5. according to the method for claim 4, it is characterized in that the described crystallization time of controlling of step B is 1～3 hour.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100948467A CN100343247C (en) | 2005-10-17 | 2005-10-17 | Method for recrystallizing lactide by using ethanol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100948467A CN100343247C (en) | 2005-10-17 | 2005-10-17 | Method for recrystallizing lactide by using ethanol |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1757644A true CN1757644A (en) | 2006-04-12 |
| CN100343247C CN100343247C (en) | 2007-10-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100948467A Expired - Fee Related CN100343247C (en) | 2005-10-17 | 2005-10-17 | Method for recrystallizing lactide by using ethanol |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100343247C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101157680B (en) * | 2007-11-16 | 2010-12-29 | 南京工业大学 | Method for recrystallizing lactide by using double solvents |
| US8431725B2 (en) | 2007-03-14 | 2013-04-30 | Niro Process Technology B.V. | Purification of lactide rich streams |
| CN103145691A (en) * | 2013-04-03 | 2013-06-12 | 天津科技大学 | Coupling refining method of high-purity L-lactide |
| CN111285840A (en) * | 2020-03-04 | 2020-06-16 | 东北林业大学 | Method for extracting lactide from waste polylactic acid through co-pyrolysis |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2809069B2 (en) * | 1993-10-26 | 1998-10-08 | 株式会社島津製作所 | Lactide purification and polymerization |
| JPH10279577A (en) * | 1997-04-04 | 1998-10-20 | Shimadzu Corp | Lactide for food additive and purification of lactide |
| JP2001157552A (en) * | 1998-09-25 | 2001-06-12 | Shimadzu Corp | Food additive lactide |
-
2005
- 2005-10-17 CN CNB2005100948467A patent/CN100343247C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8431725B2 (en) | 2007-03-14 | 2013-04-30 | Niro Process Technology B.V. | Purification of lactide rich streams |
| CN101157680B (en) * | 2007-11-16 | 2010-12-29 | 南京工业大学 | Method for recrystallizing lactide by using double solvents |
| CN103145691A (en) * | 2013-04-03 | 2013-06-12 | 天津科技大学 | Coupling refining method of high-purity L-lactide |
| CN111285840A (en) * | 2020-03-04 | 2020-06-16 | 东北林业大学 | Method for extracting lactide from waste polylactic acid through co-pyrolysis |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100343247C (en) | 2007-10-17 |
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Legal Events
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent of invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Liu Xiaoning Inventor after: Wei Rongqing Inventor after: Liu Ying Inventor after: Wei Jun Inventor after: Zheng Tao Inventor before: Liu Xiaoning Inventor before: Wei Rongqing Inventor before: Liu Ying Inventor before: Wei Jun |
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| COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: LIU XIAONING WEI RONGQING LIU YING WEI JUN TO: LIU XIAONING WEI RONGQING LIU YING WEI JUN ZHENG TAO |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071017 Termination date: 20151017 |
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| EXPY | Termination of patent right or utility model |