CN1385452A - Process for preparing copolymer of L-lactic acid and glycollic acid by direct polycondensation - Google Patents
Process for preparing copolymer of L-lactic acid and glycollic acid by direct polycondensation Download PDFInfo
- Publication number
- CN1385452A CN1385452A CN 02111794 CN02111794A CN1385452A CN 1385452 A CN1385452 A CN 1385452A CN 02111794 CN02111794 CN 02111794 CN 02111794 A CN02111794 A CN 02111794A CN 1385452 A CN1385452 A CN 1385452A
- Authority
- CN
- China
- Prior art keywords
- acid
- lactic acid
- molecular weight
- dehydration
- oxyacetic
- 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.)
- Granted
Links
Landscapes
- Polyesters Or Polycarbonates (AREA)
Abstract
The present invention discloses a method for preparing L-lactic acid and glycolic acid copolymer by means of direct polycondensation, and said method includes the following steps: dehydrating mixed aqueous solution of L-lactic acid/glycolic acid under the vacuum condition to obtain prepolymer with low molecular weight, adding additive and heating-melting under the vacuum condition and making condensation polymerization under the state of condensation back-flow so as to obtain the invented copolymer with high molecular weight. Said invented method is simple in process, low in cost and is suitable for large-scale production.
Description
Technical field:
The invention belongs to technical field of polymer materials.Be specifically related to a kind of direct condensation and prepare the method for the multipolymer of L-lactic acid and oxyacetic acid.
Background technology:
In recent years, the research day animando of biodegradable material, it is used and has related to fields such as medical material, food product pack, agricultural film and filamentary material.Especially the research of medical biodegradable material is paid attention to most, and succeeds in clinical application.Medical biodegradable material is the most important with polyglycolic acid (PGA), poly(lactic acid) (PLA) and polycaprolactone (PCL) and their multipolymer and blend.The product that they have good biocompatibility, degraded can participate in metabolism, the low toxin of human body, thereby is widely used.
Polyglycolic acid is to be used for the sutural polymkeric substance of absorbability the earliest, also is to be used to fracture one of absorbability polymkeric substance that internal fixing do not have the earliest.Mainly by the method preparation of ring-opening polymerization, promptly earlier by oxyacetic acid dehydration preparation glycollide, glycollide ring-opening polymerization again obtains PGA to high molecular PGA, as U.S.Pat3316557 and U.S.Pat3626948.Poly-lactic acid in high molecular weight also mainly adopts the method preparation of ring-opening polymerization.This technology prepares oligopolymer by acid by dehydrating lactic earlier, and the oligopolymer pyrolysis prepares rac-Lactide, and rac-Lactide ring-opening polymerization again obtains PLA.The research of the ring-opening polymerization of poly(lactic acid) is found in Brit1007347, Fr142533, EP261572, JP5813624, DE4412317, U.S.Pat5023349, USPAT5374743, CN1167776A, CN1325913A and U.S.Pat.6383161 etc.The CARGIL-DOW company of the U.S. has developed a kind of new ring-opening polymerization technology, sees U.S.Pat5142023, U.S.Pat5247058, U.S.Pat5247059, U.S.Pat5258488, U.S.Pat5274073, U.S.Pat5357035, U.S.Pat5484881 and U.S.Pat6326458.This technology prepares rac-Lactide under molten state, rac-Lactide is refining through vacuum distilling, is catalyzer then with the stannous octoate, and the melt polymerization process poly(lactic acid) can reduce the cost of poly(lactic acid) greatly.
In addition, people have also synthesized all kinds of lactic acid copolymers, with molecular weight, degradation rate, hydrophilic and hydrophobic and the mechanical property of regulating this base polymer, thereby satisfy the requirement of different field to the PLA biodegradable material.That current research is more is lactic acid/ethanol copolymer (PLGA).Lactic acid/ethanol copolymer adopts the ring-opening polymerization technology of glycollide/rac-Lactide to prepare usually.The preparation of this analog copolymer, purify and be applied in patent U.S.Pat6376643, U.S.Pat6007565, U.S.Pat6004573, U.S.Pat6004573, U.S.Pat5952405, U.S.Pat6255408, U.S.Pat4157437, U.S.Pat3839297, EP0275581 and EP0299730 have detailed report.1975, get permission listing by Vicryl participants in a bridge game's art suture line that 92% oxyacetic acid and 8% lactic acid copolymer are made.It is raw material that ring-opening polymerization needs rac-Lactide and glycollide, and the preparation of rac-Lactide and glycollide and purifying need consume a large amount of solvents, cause complex process, environmental pollution, product cost height, thereby has limited the Application Areas of polymkeric substance.
In view of the defective of ring-opening polymerization, people are devoted to the research of the direct method synthesis technique of poly(lactic acid), polyglycolic acid and lactic acid/ethanol copolymer always.Direct method be with lactic acid and oxyacetic acid under the situation that catalyzer or catalyst-free exist, direct heating and vacuum hydro-extraction, preparation poly(lactic acid), polyglycolic acid and lactic acid/ethanol copolymer.The direct method synthesis technique of poly(lactic acid) sees U.S.Pat5543494, U.S.Pat5075115, and U.S.Pat2396994, U.S.Pat2438208 and U.S.Pat2174491 etc., the polylactic acid molecule amount of gained is lower than 10,000.The polyglycolic acid that the direct method polymerization obtains, its polymerization degree are about several to tens, and mechanical strength can not satisfy service requirements.
The research that direct method prepares lactic acid/ethanol copolymer sees patent JP60-181029A, U.S.Pat4728721, U.S.Pat4011312, U.S.Pat5075115, U.S.Pat3736646, U.S.Pat4683288, US79-75296, FR2464973A1 and EP26599.These patents are under the situation that does not have organic solvent to exist, and by lactic acid/glycolic acid aqueous solution, crystallization or the polycondensation of pellet direct heating, the gained molecular weight of copolymer is lower than 10,000, can be used for drug delivery system.Nevin is in patent U.S.Pat4273920; with lactic acid and oxyacetic acid is raw material; in N2 protection, temperature 130-250 ℃, pressure 5-30 holder, to adopt strong-acid ion exchange resin be under the condition of catalyzer; reaction is more than 48 hours, and prepared lactic acid/ethanol copolymer molecular weight is 6000-35000.This technology is still needed sometimes and will be added N, dinethylformamide and dimethyl sulfoxide (DMSO) equal solvent, the molecular weight of copolymer of gained distributes wide (being about 3), and product colour is brown, and strong-acid ion exchange resin at high temperature is partially soluble in polymkeric substance, and polymkeric substance is polluted.Thereby Tanaka adopts the synthesis technique of catalyst-free in U.S.Pat4677191, under similar reaction conditions, prepared white lactic acid/ethanol copolymer.Its molecular weight increases with the prolongation of polymerization time, and 12 hours rear copolymer molecular weight of polyreaction are that 5200,24 hours molecular weight of copolymer are 9600, and 48 hours molecular weight of copolymer are 15800.Have only when the reaction times to be increased to about 100 hours, just can obtain the multipolymer of molecular weight 30000.In order to obtain the multipolymer of higher molecular weight, need add methyl alcohol and ethanol equal solvent in the reaction starting stage.
Mitsui company is at patent U.S.Pat5770683, U.S.Pat5310865, U.S.Pat5428126, reported the employing solution polymerization among U.S.Pat5440008 and the U.S.Pat5444143, direct method prepares high molecular weight polylactic acid, polyglycolic acid and other the hydroxyl carboxylic acid and the technology of multipolymer thereof.This technology is raw material with lactic acid, oxyacetic acid and other hydroxycarboxylic acids, make solvent with fragrant alkane and aryl oxide, metal and oxide compound, oxyhydroxide, halogenide, inorganic salt, carboxylate salt and organometallics with I, II, III, IV and V family are catalyzer, react under 130 ℃ of polymerization temperatures, condition of high vacuum degree and molecular sieve azeotropic reflux conditions, obtaining high molecular is the polymkeric substance of polyglycolic acid, poly(lactic acid), lactic acid/ethanol copolymer and other hydroxyl carboxylic acid.People such as Zhou Xinggui have reported direct method synthesizing polylactic acid technology in patent CN1326997A.This technology adopts the dewatering agent selectivity to deviate from moisture in the polycondensation at enclosed system, but not loss of rac-Lactide, thereby the preparation high molecular weight polylactic acid.The Kimura group of Japan makes prepolymer with the dehydration earlier of L-lactic acid or oxyacetic acid, adopt then fusion/solid phase polycondensation prepare poly-lactic acid in high molecular weight and polyglycolic acid (referring to Polymer, 2001,42,5059-5062 and Polymer, 2000,41,8725-8728).
In a word, direct method prepares lactic acid/ethanol copolymer by lactic acid/oxyacetic acid direct condensation, does not need to prepare rac-Lactide and glycollide.Compare with ring-opening polymerization, direct method technology is simple, and environmental pollution is lower, but the molecular weight of product is difficult to further raising.The technology that the direct method polycondensation prepares lactic acid/ethanol copolymer can be divided into two kinds of solution polycondensation and body polycondensations.The technology of the body polycondensation of lactic acid/ethanol copolymer is simple, but it is long to exist the cycle, the defective that the molecular weight of polymkeric substance is lower, performance can not satisfy application requiring.Solution polymerization then causes the polymerization technique complexity owing to the existence of solvent, and the cycle is long, and removing of solvent also causes its cost to increase in the polymkeric substance.
Summary of the invention:
Technical problem to be solved by this invention is the existing defective of technology that overcomes direct method synthesizing lactic acid/ethanol copolymer, seeks that a kind of technology is simple, with short production cycle, cost is low, pollution-free, high-molecular weight PLGA synthesis technique.
A kind of direct condensation prepares the method for L-lactic acid and ethanol copolymer, and this method comprises the following steps:
(1) L-lactic acid and oxyacetic acid mixed aqueous solution dehydration prepolymerization: with the aquo compound crystallization of 90% aqueous solution and the oxyacetic acid of L-lactic acid, add the reactor that has condensation reflux unit, the mol ratio of L-lactic acid and oxyacetic acid is 100/0--0/100, the temperature of dehydration is 140-180 ℃, under constant temperature, at first mix monomer was dewatered 1-2 hour under normal pressure, and then be depressurized to 200-100 mmhg continuation dehydration 1-3 hour, continue dehydration 1-5 hour at the 20-50 mmhg at last.The aquifer yield that weighing obtains, and the output of the blend after calculating is dewatered according to this;
(2) melt polymerization: in L-lactic acid and oxyacetic acid mixture after the catalyzer adding dehydration, catalyst consumption is the 0.01-3.0% of dehydration back lactic acid/oxyacetic acid blend gross weight, the pressure of system progressively is reduced to the 2-30 mmhg, temperature of reaction is 140-200 ℃, reaction times is 10-40 hour, the by product rac-Lactide and the glycollide that produce in the polymerization process turn back to reactor by the condensation reflux unit that molecular sieve and water trap are housed, and the temperature of condensation reflux unit is controlled at 20-90 ℃.
Polymerization is dissolved in ethyl acetate with the multipolymer that obtains after finishing, and filtration is also used ether sedimentation, and the throw out that leaches obtained the lactic acid/ethanol copolymer of purifying at 65 ℃ of following vacuum-drying 10-16 hours.
The prepolymerized main purpose of dewatering is the moisture of removing in lactic acid/oxyacetic acid mixture, can form the oligopolymer of lactic acid/oxyacetic acid in thermal dehydration.The molecular weight control of oligopolymer is advisable at 500-2000.Can select relatively mild dehydration temperaturre and short dewatering time like this.
When melt phase polycondensation, can select different catalyst systems for use, the microstructure of control multipolymer, synthetic multipolymer with different molecular weight and molecular weight distribution.The catalyzer that the present invention uses is selected the compound system of metallic compound and protonic acid or the compound system of metallic compound and alkylating reagent for use.The metallic compound that can select for use comprises the hydrate of oxide compound, halogenide, oxyhydroxide, organometallics, carboxylate salt and these metallic compounds of the metal of I, II, III, IV, V family and transition metal.
The metallic compound that can select for use such as SnCl
2, SnCl
22H
2O, SnCl
4, SnCl
42H
2O, ZnCl
2H
2O, SbF
3, TiCl
4, MgCl
2, Sb
2O
3, MgO, PbO, diethoxy aluminium, aluminium isopropoxide, stannous octoate and tributyl methoxyl group tin etc.Protonic acid can be selected mineral acids such as hydrochloric acid, phosphoric acid and phosphorous acid for use, also can select organic acids such as acetate, sad and halogenated carboxylic acid for use.Alkylating reagent can be selected fluosulfonic acid, Phenylsulfonic acid, tosic acid for use and contain other substituent Phenylsulfonic acids etc.
The compound system of metallic compound and protonic acid can be selected SnCl for use
2/ acetate, SnCl
22H
2Sad, the MgCl of O/
2/ Mono Chloro Acetic Acid and stannous octoate/sad etc.The compound system of metallic compound and alkylating reagent such as SnCl
2/ Phenylsulfonic acid, SnCl
4/ Phenylsulfonic acid, SnCl
2/ p-methyl benzenesulfonic acid and SnCl
2/ carboxylic acid etc.In complex catalyst system, the molar content of metallic compound is 90-30%.
The present invention adopts the direct polymerization method, and the multipolymer of body melt polymerization process L-lactic acid and oxyacetic acid does not use solvent in synthesis technique, thereby technology is simple, and product cost is low.The present invention can prepare the L-lactic acid and the ethanol copolymer of different number-average molecular weights, and molecular weight is 2-10 ten thousand.The present invention is by changing the proportioning of oxyacetic acid and L-lactic acid, and the PLGA multipolymer that preparation has different degradation rates and mechanical property satisfies different purposes.The molecular weight of multipolymer, fusing point, second-order transition temperature, degree of crystallinity and degradation rate are all along with two kinds of monomeric ratios change and change.When the lactic acid/oxyacetic acid of raw material greater than 80/20 the time, PLGA is the crystal form polymkeric substance, and crystallization is formed by the LLA segment.When lactic acid/oxyacetic acid was 80/30 to 30/70, PLGA was the polymkeric substance of unformed shape.When lactic acid/oxyacetic acid less than 30/70 the time, can obtain crystal form PLGA again, and crystallization is formed by the GA segment.Molecular weight is lower than 30000 PLGA can be used for pharmaceutical auxiliary agent, pharmaceutical carrier, protein release vehicle and vaccine adjuvant etc., and high-molecular weight PLGA multipolymer (molecular weight is greater than 70,000) then can be used to prepare film and wet-spinning.
Embodiment:
The present invention will be further described with following example, but scope of the present invention is not limited to the content of these examples.
Example 1
The aqueous solution (not adding oxyacetic acid) of L-lactic acid 90% is added reactor, 150 ℃ of dehydrations down.At first dewatered 2 hours under normal pressure, and then be depressurized to 150 mmhg continuation dehydration 2 hours, the last continuation under the pressure of 30 mmhg dewatered 4-6 hour.After dehydration finishes, 0.5wt% glass putty catalyzer is added in the reactor, the pressure of system progressively is reduced to 10 mmhg, temperature of reaction rises to 160 ℃, carries out polyreaction.Along with the carrying out of reaction, begin to occur lactide monomer and reflux, the reactant thickness that becomes gradually.React and stop polymerization after 30 hours, obtain poly (l-lactic acid).Be yellow powder behind this polymer purification, yield is 55%, and molecular weight is 10000,134 ℃ of fusing points.Under drying regime, preserve after 6 months the molecular weight and molecular weight 15% of this polymkeric substance.
Example 2
90% aqueous solution of L-lactic acid and the aquo compound of oxyacetic acid (two kinds of monomeric mol ratios of L-lactic acid and oxyacetic acid are 90/10) are added reactor, under 180 ℃ of temperature, dewater.At first the normal pressure dehydration is 2 hours, is depressurized to 150 mmhg dehydration 2 hours then, at last 30 mmhg dehydration 4-6 hour.After dehydration finishes, with 0.4wt%SnCl
22H
2The O catalyzer adds in the L prepolymer.The pressure of system progressively is reduced to 10 mmhg, and temperature of reaction rises to 190 ℃, carries out polyreaction.Along with the carrying out of reaction, begin to occur rac-Lactide and/or glycolide monomer and reflux, the reactant thickness that becomes gradually, and rod climbing phenomenon finally appears.Polyreaction stopped after 20 hours, obtained L-lactic acid/ethanol copolymer.Be buff powder behind this multipolymer purifying, molecular weight 40,000, yield are 59%, and fusing point is 110 ℃.At room temperature kept dry is after 6 months, the molecular weight and molecular weight 40% of this polymkeric substance.
Example 3
90% aqueous solution of L-lactic acid and the monohydrate of oxyacetic acid (two kinds of monomeric mol ratios of L-lactic acid and oxyacetic acid are 90/10) are added reactor, under 155 ℃ of temperature, dewater.At first mix monomer was dewatered 2 hours under normal pressure, and then be depressurized to 50-200 mmhg continuation dehydration 2 hours, continue dehydration 4-6 hour at the 10-60 mmhg at last.After dehydration finishes, with 1.0wt%SnCl
22H
2O and Catalyzed by p-Toluenesulfonic Acid agent system (mol ratio of two kinds of catalyzer is 50/50) add L-lactic acid and oxyacetic acid mixture.The pressure of system progressively is reduced to the 1-30 mmhg, and temperature of reaction rises to 180 ℃, and the condensing reflux temperature is 20-90 ℃, carries out polyreaction.Along with the carrying out of reaction, rac-Lactide and/or glycolide monomer produce and also begin to reflux, the reactant thickness that becomes gradually.Wait to occur to stop polymerization behind the rod climbing phenomenon, the reaction times is 15-20 hour.Be white fiber shaped polymer, yield 70%, molecular weight 100,000,120 ℃ of fusing points behind L-lactic acid that obtains and the ethanol copolymer purifying.Kept dry is after 6 months under the room temperature, the molecular weight and molecular weight 50% of this sample.
Example 4
90% aqueous solution of L-lactic acid and the monohydrate of oxyacetic acid (two kinds of monomeric mol ratios of L-lactic acid and oxyacetic acid are 80/20) are added reactor, under 150 ℃ of temperature, dewater.At first mix monomer was dewatered 2 hours under normal pressure, and then be depressurized to 50-200 mmhg continuation dehydration 2 hours, continue dehydration 4-6 hour at the 10-60 mmhg at last.After dehydration finishes, with 0.8wt%SnCl
22H
2O/ Phenylsulfonic acid complex catalyst system (mol ratio of two kinds of catalyzer is 60/40) adds L-lactic acid and oxyacetic acid mixture.The pressure of system progressively is reduced to the 10-30 mmhg, and temperature of reaction is 160-180 ℃.Along with the carrying out of reaction, begin to occur rac-Lactide and/or glycolide monomer and reflux, the reactant thickness that becomes gradually.React and stop after 25 hours.Obtain being brown ceramic powder behind L-lactic acid and the ethanol copolymer purifying, yield is 60%, and molecular weight is 35000.This multipolymer amorphous polymer.Kept dry at room temperature, molecular weight and molecular weight 55% after 6 months.
Example 5
The aqueous solution of L-lactic acid 90% and the hydrate of oxyacetic acid (two kinds of monomeric mol ratios 70/30) are added reactor, under 150 ℃ of temperature, dewater.At first under normal pressure, dewatered 2-4 hour, be depressurized to 50-200 mmhg dehydration 2-4 hour then, at last 10-60 mmhg dehydration 4-6 hour.After dehydration finishes, with 0.5wt%SnCl
22H
2O/ Mono Chloro Acetic Acid acid catalysis system adds in the prepolymer.The pressure of system progressively is reduced to the 10-30 mmhg, and temperature of reaction is 180 ℃.Rac-Lactide that produces in the polymerization process and/or glycolide monomer condensing reflux are to reactor.Along with the carrying out of reaction, the reactant thickness that becomes gradually react end after 30 hours.The purified back of this L-lactic acid and ethanol copolymer yield is 60%, and molecular weight is 30000, belongs to amorphous polymer.At room temperature kept dry is after 6 months, and this molecular weight analyte descends 65%.
Claims (5)
1, a kind of direct condensation prepares the method for the multipolymer of L-lactic acid and oxyacetic acid, it is characterized in that this method comprises the following steps:
(1) .L-lactic acid and oxyacetic acid mixed aqueous solution dehydration prepolymerization:
With 90% aqueous solution and the alcoholic acid mol ratio of L-lactic acid is 100/0-0/100, dehydration temperaturre is 140-180 ℃, under constant temperature, at first mix monomer was dewatered 1-2 hour under normal pressure, and then be depressurized to the 200-100 mmhg and continue dehydration 1-3 hour, continue dehydration 1-5 hour at the 20-50 mmhg at last, the aquifer yield that weighing obtains, and the output of the blend after calculating is dewatered according to this;
(2). melt polymerization: in L-lactic acid and oxyacetic acid mixture after the catalyzer adding dehydration, catalyst consumption is the 0.01-3.0% of dehydration back lactic acid/oxyacetic acid blend gross weight, the pressure of system progressively is reduced to the undoubted mercury column of 20-30, temperature of reaction is 140-200 ℃, reaction times is 10-40 hour, the by product rac-Lactide and the glycollide that produce in the polymerization process turn back to reactor by the condensation reflux unit that molecular sieve and water trap are housed, the temperature of condensation reflux unit is controlled at 20-90 ℃, after polymerization finishes, the multipolymer that obtains is dissolved in ethyl acetate, filters and use ether sedimentation.The throw out that leaches obtained the lactic acid/ethanol copolymer of purifying at 65 ℃ of following vacuum-drying 10-16 hours.
2, a kind of direct condensation according to claim 1 prepares the method for the multipolymer of L-lactic acid and oxyacetic acid, it is characterized in that the prepolymer molecular weight that wherein said step (1) obtains is 500-2000; The molecular weight of copolymer that step (2) obtains is 30000-120000, and when the mol ratio of the lactic acid/oxyacetic acid of raw material greater than 90/10 the time, the molecular weight of copolymer of gained is greater than 100,000.
3, a kind of direct condensation according to claim 1 prepares the method for the multipolymer of L-lactic acid and oxyacetic acid, it is characterized in that when the mol ratio of the lactic acid/oxyacetic acid of raw material greater than 80/20 or less than 30/70 the time, obtain crystalline copolymer, when the lactic acid/oxyacetic acid mol ratio of raw material during, obtain the amorphous state polymkeric substance at 80/20-30/70.
4, a kind of direct condensation according to claim 1 prepares the method for the multipolymer of L-lactic acid and oxyacetic acid, it is characterized in that catalyzer used in the wherein said step (2) is metallic compound and protonic acid compound system or metallic compound and alkylating reagent compound system, wherein the molar content of metallic compound is 90-30%.
5, catalyzer according to claim 4 is characterized in that wherein said composite catalyst system is Sncl
2/ Mono Chloro Acetic Acid, Sncl
2/ Phenylsulfonic acid, Sncl
4/ Phenylsulfonic acid, Sncl
2/ p-methyl benzenesulfonic acid or Sncl
2/ carboxylic acid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021117942A CN1166718C (en) | 2002-05-23 | 2002-05-23 | Process for preparing copolymer of L-lactic acid and glycollic acid by direct polycondensation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021117942A CN1166718C (en) | 2002-05-23 | 2002-05-23 | Process for preparing copolymer of L-lactic acid and glycollic acid by direct polycondensation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1385452A true CN1385452A (en) | 2002-12-18 |
| CN1166718C CN1166718C (en) | 2004-09-15 |
Family
ID=4741747
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB021117942A Expired - Fee Related CN1166718C (en) | 2002-05-23 | 2002-05-23 | Process for preparing copolymer of L-lactic acid and glycollic acid by direct polycondensation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1166718C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102532501A (en) * | 2010-12-29 | 2012-07-04 | 安徽生建可降解聚乳酸新材料有限公司 | Refining method for poly(L-lactic acid) and poly(L-lactic acid-glycolic acid) |
| CN105111417A (en) * | 2015-08-25 | 2015-12-02 | 杭州铭众生物科技有限公司 | Preparing method for glycolic acid-hydracrylic acid random copolymer |
| CN112280021A (en) * | 2020-09-25 | 2021-01-29 | 内蒙古久泰新材料有限公司 | Method for preparing polyglycolic acid |
| CN114381229A (en) * | 2022-01-14 | 2022-04-22 | 湖北拓盈新材料有限公司 | PLGA glue for environment-friendly fly glue and preparation method thereof |
| CN114716655A (en) * | 2020-12-22 | 2022-07-08 | 上海丽珠制药有限公司 | Preparation method of lactide-glycolide copolymer |
| CN115725060A (en) * | 2021-08-31 | 2023-03-03 | 华润化学材料科技股份有限公司 | Block copolyester and preparation method and application thereof |
-
2002
- 2002-05-23 CN CNB021117942A patent/CN1166718C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102532501A (en) * | 2010-12-29 | 2012-07-04 | 安徽生建可降解聚乳酸新材料有限公司 | Refining method for poly(L-lactic acid) and poly(L-lactic acid-glycolic acid) |
| CN102532501B (en) * | 2010-12-29 | 2014-07-09 | 安徽生建可降解聚乳酸新材料有限公司 | Refining method for poly(L-lactic acid) and poly(L-lactic acid-glycolic acid) |
| CN105111417A (en) * | 2015-08-25 | 2015-12-02 | 杭州铭众生物科技有限公司 | Preparing method for glycolic acid-hydracrylic acid random copolymer |
| CN112280021A (en) * | 2020-09-25 | 2021-01-29 | 内蒙古久泰新材料有限公司 | Method for preparing polyglycolic acid |
| CN114716655A (en) * | 2020-12-22 | 2022-07-08 | 上海丽珠制药有限公司 | Preparation method of lactide-glycolide copolymer |
| CN114716655B (en) * | 2020-12-22 | 2023-12-22 | 上海丽珠制药有限公司 | Process for preparing lactide-glycolide copolymer |
| CN115725060A (en) * | 2021-08-31 | 2023-03-03 | 华润化学材料科技股份有限公司 | Block copolyester and preparation method and application thereof |
| CN115725060B (en) * | 2021-08-31 | 2024-04-09 | 华润化学材料科技股份有限公司 | Block copolyesters, and preparation method and application thereof |
| CN114381229A (en) * | 2022-01-14 | 2022-04-22 | 湖北拓盈新材料有限公司 | PLGA glue for environment-friendly fly glue and preparation method thereof |
| CN114381229B (en) * | 2022-01-14 | 2023-08-15 | 湖北拓盈新材料有限公司 | PLGA glue for environment-friendly fly glue and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1166718C (en) | 2004-09-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR101234538B1 (en) | Biodegradable linear random copolyester and process for preparing it and use of the same | |
| KR100520279B1 (en) | Catalysts for polyester production, process for producing polyester, and polyester | |
| CN100429256C (en) | Biodegradable linear random copolyester and its preparation method and uses | |
| CN110283305B (en) | Preparation method of biodegradable high polymer material poly (glycolide-lactide) for medical use | |
| LV13428B (en) | Polymerization catalyst for preparing polyesters, preparation of polyethylene terephthalate and use of polymerization catalyst | |
| CN1166718C (en) | Process for preparing copolymer of L-lactic acid and glycollic acid by direct polycondensation | |
| CN115785427B (en) | Composite catalyst and method for preparing aliphatic polycarbonate by using composite catalyst | |
| CN111087596A (en) | Method for preparing polyglycolide by continuous ring opening, catalyst and preparation method | |
| TW561163B (en) | Process for preparing polypropylene terephthalate/polyethylene terephthalate copolymers | |
| CN113429762A (en) | Starch/polylactic acid/PBAT nano composite material and preparation method thereof | |
| CN116375996A (en) | Preparation method of medical polycaprolactone | |
| CN1168756C (en) | Method for preparing macromolecular weight branched polycaprolactone | |
| EP0907338A1 (en) | Crystalline copolymers and methods of producing such copolymers | |
| AU2013280006A1 (en) | Preparation method for polyester/polyvinyl glyoxal hot melt adhesive having a semi-interpenetrating network structure | |
| JP4794096B2 (en) | Method for producing glycolic acid copolymer | |
| JP4090299B2 (en) | Method for producing glycolic acid copolymer | |
| CN101302281B (en) | Polylactic acid and preparation thereof | |
| KR100212968B1 (en) | Process for preparing polylactic acid and polyglycolic acid copolymer | |
| CN115073417B (en) | Method for preparing lactide by catalyzing lactic acid with ternary composite catalyst | |
| CN1231516C (en) | Process for preparing poly-(L-lactic acid) | |
| CN1203107C (en) | Prepn process of poly (L-lactic acid-glycolic acid) | |
| CN111548481B (en) | Biodegradable polyester material, preparation method and application thereof, carrier material and preparation method thereof | |
| CN102333810B (en) | Ethylene terephthalate-based polyester resin for molding container and process for producing same | |
| KR101817348B1 (en) | Preparation method of polylactic acid by one-pot direct polycondensation | |
| CN111154089A (en) | Metal-free non-toxic catalyst for ring-opening polymerization reaction of glycolide and application method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| 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 | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |