CN102875779A - Process method for synthesizing medical biodegradable polylactic acid by performing polycondensation on lactic acid through catalysis of 1,5,7-triazabicyclo[4.4.0]decane-5-ene (TBD) - Google Patents
Process method for synthesizing medical biodegradable polylactic acid by performing polycondensation on lactic acid through catalysis of 1,5,7-triazabicyclo[4.4.0]decane-5-ene (TBD) Download PDFInfo
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- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 title claims abstract description 62
- 229920000747 poly(lactic acid) Polymers 0.000 title claims abstract description 36
- 235000014655 lactic acid Nutrition 0.000 title claims abstract description 31
- 239000004310 lactic acid Substances 0.000 title claims abstract description 31
- 239000004626 polylactic acid Substances 0.000 title claims abstract description 31
- 238000000034 method Methods 0.000 title claims abstract description 20
- 238000006068 polycondensation reaction Methods 0.000 title claims description 7
- 238000006555 catalytic reaction Methods 0.000 title claims 2
- FVKFHMNJTHKMRX-UHFFFAOYSA-N 3,4,6,7,8,9-hexahydro-2H-pyrimido[1,2-a]pyrimidine Chemical compound C1CCN2CCCNC2=N1 FVKFHMNJTHKMRX-UHFFFAOYSA-N 0.000 title description 4
- 230000002194 synthesizing effect Effects 0.000 title description 3
- ZRALSGWEFCBTJO-UHFFFAOYSA-N Guanidine Chemical compound NC(N)=N ZRALSGWEFCBTJO-UHFFFAOYSA-N 0.000 claims abstract description 56
- CHJJGSNFBQVOTG-UHFFFAOYSA-N N-methyl-guanidine Natural products CNC(N)=N CHJJGSNFBQVOTG-UHFFFAOYSA-N 0.000 claims abstract description 30
- SWSQBOPZIKWTGO-UHFFFAOYSA-N dimethylaminoamidine Natural products CN(C)C(N)=N SWSQBOPZIKWTGO-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000003054 catalyst Substances 0.000 claims abstract description 25
- 239000000178 monomer Substances 0.000 claims abstract description 6
- 239000007864 aqueous solution Substances 0.000 claims abstract description 5
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 5
- 239000002994 raw material Substances 0.000 claims abstract description 4
- 238000006243 chemical reaction Methods 0.000 claims description 39
- JVTAAEKCZFNVCJ-REOHCLBHSA-N L-lactic acid Chemical compound C[C@H](O)C(O)=O JVTAAEKCZFNVCJ-REOHCLBHSA-N 0.000 claims description 24
- -1 poly(lactic acid) Polymers 0.000 claims description 24
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 16
- 241001024099 Olla Species 0.000 claims description 16
- 229910052786 argon Inorganic materials 0.000 claims description 11
- 238000006297 dehydration reaction Methods 0.000 claims description 11
- 230000015572 biosynthetic process Effects 0.000 claims description 9
- 238000003786 synthesis reaction Methods 0.000 claims description 9
- 229920001432 poly(L-lactide) Polymers 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims 1
- 238000012662 bulk polymerization Methods 0.000 claims 1
- 239000002131 composite material Substances 0.000 claims 1
- 230000006837 decompression Effects 0.000 claims 1
- 230000018044 dehydration Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 claims 1
- 238000010792 warming Methods 0.000 claims 1
- 125000002619 bicyclic group Chemical group 0.000 abstract description 19
- 231100000331 toxic Toxicity 0.000 abstract description 6
- 230000002588 toxic effect Effects 0.000 abstract description 6
- 238000009826 distribution Methods 0.000 abstract description 3
- 229910052751 metal Inorganic materials 0.000 abstract description 3
- 239000002184 metal Substances 0.000 abstract description 3
- 150000002739 metals Chemical class 0.000 abstract description 3
- 238000012643 polycondensation polymerization Methods 0.000 abstract description 3
- 239000003153 chemical reaction reagent Substances 0.000 abstract 1
- 231100000433 cytotoxic Toxicity 0.000 abstract 1
- 230000001472 cytotoxic effect Effects 0.000 abstract 1
- 238000009776 industrial production Methods 0.000 abstract 1
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 239000012974 tin catalyst Substances 0.000 abstract 1
- 229920000642 polymer Polymers 0.000 description 22
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 20
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 20
- 239000007787 solid Substances 0.000 description 20
- 239000003814 drug Substances 0.000 description 5
- 239000003937 drug carrier Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 231100000252 nontoxic Toxicity 0.000 description 4
- 230000003000 nontoxic effect Effects 0.000 description 4
- 238000005086 pumping Methods 0.000 description 4
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical class [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 3
- 229910021626 Tin(II) chloride Inorganic materials 0.000 description 3
- 229940079593 drug Drugs 0.000 description 3
- TXUICONDJPYNPY-UHFFFAOYSA-N (1,10,13-trimethyl-3-oxo-4,5,6,7,8,9,11,12,14,15,16,17-dodecahydrocyclopenta[a]phenanthren-17-yl) heptanoate Chemical compound C1CC2CC(=O)C=C(C)C2(C)C2C1C1CCC(OC(=O)CCCCCC)C1(C)CC2 TXUICONDJPYNPY-UHFFFAOYSA-N 0.000 description 2
- 238000013270 controlled release Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 235000011150 stannous chloride Nutrition 0.000 description 2
- 239000001119 stannous chloride Substances 0.000 description 2
- KSBAEPSJVUENNK-UHFFFAOYSA-L tin(ii) 2-ethylhexanoate Chemical compound [Sn+2].CCCCC(CC)C([O-])=O.CCCCC(CC)C([O-])=O KSBAEPSJVUENNK-UHFFFAOYSA-L 0.000 description 2
- 208000030453 Drug-Related Side Effects and Adverse reaction Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000975 bioactive effect Effects 0.000 description 1
- 231100000135 cytotoxicity Toxicity 0.000 description 1
- 230000003013 cytotoxicity Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000007142 ring opening reaction Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000017423 tissue regeneration Effects 0.000 description 1
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- Polyesters Or Polycarbonates (AREA)
- Medicinal Preparation (AREA)
- Biological Depolymerization Polymers (AREA)
Abstract
一种双环胍催化乳酸直接缩聚合成医用生物降解性聚乳酸的方法。本发明以双环胍(TBD)为催化剂、工业级质量含量为90%的乳酸水溶液为单体、采用无溶剂(本体)、二阶缩合聚合,得到产品聚乳酸具有高度生物安全性。本发明避免了使用具有细胞毒性的锡类催化剂,所用催化剂具有生物相容性和生物安全性;所合成的聚乳酸不含任何金属以及其他毒性成分,适用于医用药用领域;采用绿色催化剂和绿色工艺(不使用任何试剂、无有毒产物生成),合成绿色生物降解聚乳酸;聚合反应方便易行,原料成本低廉,易于工业化生产;所合成产品分子量分布窄,分子量在1.0×104~4.0×104范围内调控。The invention discloses a method for the direct condensation polymerization of lactic acid catalyzed by bicyclic guanidine to synthesize medical biodegradable polylactic acid. The present invention uses bicyclic guanidine (TBD) as a catalyst, industrial-grade lactic acid aqueous solution with a mass content of 90% as a monomer, and adopts solvent-free (bulk) and second-stage condensation polymerization to obtain a product polylactic acid with high biological safety. The invention avoids the use of cytotoxic tin catalysts, and the catalysts used are biocompatible and biosafe; the synthesized polylactic acid does not contain any metals and other toxic components, and is suitable for medical applications; green catalysts and Green process (does not use any reagents, no toxic products are produced), and synthesizes green biodegradable polylactic acid; the polymerization reaction is convenient and easy, the cost of raw materials is low, and it is easy for industrial production; the molecular weight distribution of the synthesized product is narrow, and the molecular weight is 1.0×10 4 ~4.0 It can be regulated within the range of ×10 4 .
Description
技术领域: Technical field:
本发明属于药物降解材料技术领域,涉及用双环胍催化乳酸合成具有高度生物安全性聚乳酸的工艺方法。The invention belongs to the technical field of drug degradable materials, and relates to a process method for synthesizing polylactic acid with high biological safety by using bicyclic guanidine to catalyze lactic acid.
背景技术: Background technique:
近年来,医药及生物医学发展迅猛,对能够应用于控释及靶向药物载体、硬组织修复材料、生物组织工程中的生物活性支架材料的降解材料需求急剧增加。生物降解聚乳酸具有良好的生物相容性,作为药物载体可以提高药效、降低给药量以及药物的毒副作用等,使其在药物科学及生物医学方面取得许多重要应用。目前商品化聚乳酸生产主要采用辛酸亚锡开环缩聚方法合成以及氯化亚锡催化乳酸直接缩聚方法合成。但是作为药物载体时,要求聚合物中不含有任何有毒金属及具有毒性的其他成分。以上两种方法能够达到药物载体所需分子量(1.0×104~4.0×104)要求,但是所用的重金属锡盐类催化剂很难从聚合物中去除,研究证明辛酸亚锡及氯化亚锡具有细胞毒性,用锡类催化剂合成的工程材料的安全性已经引起了广泛关注,使其在药物领域的应用得到限制。因而开发高效、无毒催化剂用于聚乳酸的合成是现在研究重点。In recent years, with the rapid development of medicine and biomedicine, the demand for degradable materials that can be applied to controlled release and targeted drug carriers, hard tissue repair materials, and bioactive scaffold materials in biological tissue engineering has increased dramatically. Biodegradable polylactic acid has good biocompatibility. As a drug carrier, it can improve drug efficacy, reduce dosage and drug side effects, etc., making it have many important applications in pharmaceutical science and biomedicine. At present, the production of commercialized polylactic acid is mainly synthesized by the ring-opening polycondensation method of stannous octoate and the direct polycondensation method of lactic acid catalyzed by stannous chloride. However, when used as a drug carrier, it is required that the polymer does not contain any toxic metals and other toxic components. The above two methods can meet the molecular weight (1.0×10 4 ~4.0×10 4 ) required by the drug carrier, but the heavy metal tin salt catalyst used is difficult to remove from the polymer. Studies have shown that stannous octoate and stannous chloride With cytotoxicity, the safety of engineering materials synthesized with tin-based catalysts has aroused widespread concern, limiting their application in the field of medicine. Therefore, the development of high-efficiency, non-toxic catalysts for the synthesis of polylactic acid is the focus of current research.
发明内容: Invention content:
本发明的目的是解决采用锡类催化剂合成的聚乳酸,用于人类药物载体上具有潜在的安全隐患问题,提供一种无毒、无金属的双环胍化合物为催化剂直接催化乳酸聚合生成具有高度生物安全性医用生物降解聚乳酸的工艺方法。The purpose of the present invention is to solve the problem of potential safety hazards of polylactic acid synthesized by tin-based catalysts when used as human drug carriers, and to provide a non-toxic, metal-free bicyclic guanidine compound as a catalyst to directly catalyze the polymerization of lactic acid to generate a highly biological A safe medical biodegradable polylactic acid process.
本发明首次研发出一种利用无毒、无金属的有机胍化合物(双环胍)为催化剂,质量含量90%的乳酸水溶液为单体,经本体缩合聚合法合成高度生物安全性聚乳酸的新工艺。For the first time, the present invention has developed a new process for synthesizing polylactic acid with high biological safety by bulk condensation polymerization using non-toxic, metal-free organic guanidine compound (bicyclic guanidine) as catalyst, and 90% lactic acid aqueous solution as monomer. .
本发明所使用的无毒、无金属有机胍化合物——双环胍,其化学名为:1,5,7-三氮杂二环[4.4.0]癸-5-烯(1,5,7-Triazabicyclo[4.4.0]dec-5-ene,英文缩写为:TBD),其分子结构式如下:The nontoxic, metal-free organic guanidine compound used in the present invention——bicyclic guanidine, its chemical name is: 1,5,7-triazabicyclo[4.4.0]dec-5-ene (1,5,7 -Triazabicyclo[4.4.0]dec-5-ene, English abbreviation: TBD), its molecular structure is as follows:
本发明提供的双环胍催化乳酸直接缩聚合成具有高度生物安全性、可降解聚乳酸的工艺方法是,利用有机胍化合物(双环胍)作为催化剂,质量含量为90%乳酸水溶液为单体,经本体聚合合成高度生物安全性聚乳酸,具体包括:The process method of bicyclic guanidine catalyzed direct polycondensation of lactic acid to synthesize highly biosafety and degradable polylactic acid provided by the present invention is to use organic guanidine compound (bicyclic guanidine) as a catalyst, and the mass content is 90% lactic acid aqueous solution as a monomer. Polymerization and synthesis of polylactic acid with high biological safety, including:
合成路线:synthetic route:
合成步骤:Synthetic steps:
第1、寡聚乳酸OLLA的合成1. Synthesis of oligomeric lactic acid OLLA
以工业级质量含量为90%乳酸水溶液为单体,首先合成数均分子量Mn 400~600的寡聚乳酸OLLA,合成条件:在反应釜中加入乳酸,重复抽真空充氩气操作三次后;在200Torr下加热至100~120℃,脱水1h;将反应釜减压至100Torr在130~150℃继续反应1h;然后将反应釜减压至30Torr在150~170℃继续反应1h。Using industrial-grade lactic acid aqueous solution with a mass content of 90% as a monomer, first synthesize oligomeric lactic acid OLLA with a number-average molecular weight Mn of 400-600. Heat to 100~120°C at 200 Torr, dehydrate for 1 hour; depressurize the reactor to 100 Torr and continue the reaction at 130~150°C for 1 hour; then reduce the pressure of the reactor to 30 Torr and continue the reaction at 150~170°C for 1 hour.
第2、聚乳酸PLLA的合成2. Synthesis of polylactic acid PLLA
以第1步合成的寡聚乳酸OLLA为原料、以商品化双环胍为催化剂,控制双环胍与乳酸质量比为1:300~1:6500,在减压及一定温度下进行本体熔融缩聚,合成得到高度生物安全性药用聚乳酸,合成条件:向反应釜中加入催化剂双环胍,将反应釜减压至10Torr,升温至180~230℃反应10~20h,得到聚乳酸PLLA。Using the oligomeric lactic acid OLLA synthesized in the first step as a raw material, using commercial bicyclic guanidine as a catalyst, controlling the mass ratio of bicyclic guanidine to lactic acid at 1:300~1:6500, performing bulk melt polycondensation under reduced pressure and a certain temperature to synthesize High biosafety pharmaceutical polylactic acid was obtained. Synthesis conditions: add catalyst bicyclic guanidine to the reactor, depressurize the reactor to 10Torr, raise the temperature to 180~230℃ for 10~20h, and obtain polylactic acid PLLA.
本发明方法所合成的聚乳酸分子量为1.0×104~4.0×104,分子量分布指数(PDI)为1.7-2.0。The molecular weight of the polylactic acid synthesized by the method of the invention is 1.0×10 4 to 4.0×10 4 , and the molecular weight distribution index (PDI) is 1.7-2.0.
本发明的优点和有益效果:Advantages and beneficial effects of the present invention:
1.所用催化剂具有高度生物相容性、生物安全性;1. The catalyst used has high biocompatibility and biosafety;
2.所合成聚乳酸不含有任何金属及其他毒性成分,因此适合用于控释和靶向药物的载体;2. The synthesized polylactic acid does not contain any metals and other toxic components, so it is suitable for the carrier of controlled release and targeted drugs;
3.采用绿色催化剂和绿色工艺(不使用任何溶剂、无有毒产物生成),合成绿色(高度生物安全性)生物降解性聚乳酸;3. Synthesize green (highly biologically safe) biodegradable polylactic acid by using green catalysts and green processes (no solvents are used, no toxic products are produced);
4.所合成产品分子量分布窄,分子量可实现在1.0×104~4.0×104范围可控。4. The molecular weight distribution of the synthesized product is narrow, and the molecular weight can be controlled within the range of 1.0×10 4 ~4.0×10 4 .
5.反应所用时间短(10~20h);5. The reaction time is short (10~20h);
6.聚合反应工艺简便,原料成本低廉,易于工业化实施。6. The polymerization process is simple, the cost of raw materials is low, and it is easy to implement industrially.
具体实施方式: Detailed ways:
实施例1Example 1
在反应釜中装入80g的L-乳酸(质量含量90%),重复抽真空—充氩气操作三次。在200Torr下加热至100℃,脱水反应1h。然后将反应釜减压至100Torr,在130℃下继续反应1h。然后将反应釜减压至30Torr在160℃继续反应1h,得到寡聚乳酸OLLA。80g of L-lactic acid (mass content 90%) was charged into the reactor, and the vacuuming-argon filling operation was repeated three times. Heating to 100°C under 200 Torr, dehydration reaction for 1h. Then the reactor was depressurized to 100 Torr, and the reaction was continued at 130° C. for 1 h. Then the reactor was depressurized to 30 Torr and the reaction was continued at 160° C. for 1 h to obtain oligomeric lactic acid OLLA.
向反应釜加入催化剂双环胍240mg,将反应釜减压至10Torr,升温至180℃反应10h。停止反应后,将反应釜冷至室温,将聚合物用丙酮溶解,然后倒入0℃的乙醇中,减压过滤,固体在50℃及真空下干燥36h,得到白色固体,即高度生物安全性药用聚乳酸,产率75.6%,聚合物分子量1.5×104,PDI 1.87。Add 240 mg of catalyst bicyclic guanidine to the reactor, depressurize the reactor to 10 Torr, and raise the temperature to 180° C. for 10 h. After stopping the reaction, cool the reactor to room temperature, dissolve the polymer with acetone, then pour it into ethanol at 0°C, filter under reduced pressure, and dry the solid at 50°C under vacuum for 36 hours to obtain a white solid, which is highly biosafety Pharmaceutical polylactic acid, yield 75.6%, polymer molecular weight 1.5×10 4 , PDI 1.87.
实施例2Example 2
在反应釜中装入80g的L-乳酸(质量含量90%),重复抽真空充氩气操作三次。在200Torr下加热至110℃,脱水反应1h。然后将反应釜减压至100Torr在130℃继续反应1h。然后将反应釜减压至30Torr在150℃继续反应1h,得到寡聚乳酸OLLA。80 g of L-lactic acid (mass content 90%) was charged into the reaction kettle, and the vacuum pumping and argon filling operations were repeated three times. Heated to 110°C under 200 Torr, dehydration reaction for 1h. Then the reactor was depressurized to 100 Torr and the reaction was continued at 130° C. for 1 h. Then the reactor was depressurized to 30 Torr and the reaction was continued at 150° C. for 1 h to obtain oligomeric lactic acid OLLA.
向反应釜加入催化剂双环胍240mg,将反应釜减压至10Torr,升温至190℃反应16h。停止反应后,将反应釜冷至室温,将聚合物用丙酮溶解,然后倒入0℃的乙醇中,减压过滤,固体在50℃及真空下干燥36h,得到白色固体,即高度生物安全性药用聚乳酸,产率73.1%,聚合物分子量2.3×104,PDI 1.70。Add 240 mg of catalyst bicyclic guanidine to the reactor, depressurize the reactor to 10 Torr, and raise the temperature to 190° C. for 16 hours. After stopping the reaction, cool the reactor to room temperature, dissolve the polymer with acetone, then pour it into ethanol at 0°C, filter under reduced pressure, and dry the solid at 50°C under vacuum for 36 hours to obtain a white solid, which is highly biosafety Pharmaceutical polylactic acid, yield 73.1%, polymer molecular weight 2.3×10 4 , PDI 1.70.
实施例3Example 3
在反应釜中装入80g的L-乳酸(质量含量90%),重复抽真空—充氩气操作三次。在200Torr下加热至120℃,脱水反应1h。然后将反应釜减压至100Torr在130℃继续反应1h。然后将反应釜减压至30Torr在150℃继续反应1h,得到寡聚乳酸OLLA。80g of L-lactic acid (mass content 90%) was charged into the reactor, and the vacuuming-argon filling operation was repeated three times. Heated to 120°C under 200 Torr, dehydration reaction for 1h. Then the reactor was depressurized to 100 Torr and the reaction was continued at 130° C. for 1 h. Then the reactor was depressurized to 30 Torr and the reaction was continued at 150° C. for 1 h to obtain oligomeric lactic acid OLLA.
向反应釜加入催化剂双环胍120mg,将反应釜减压至10Torr,升温至200℃反应20h。停止反应后,将反应釜冷至室温,将聚合物用丙酮溶解,然后倒入0℃的乙醇中,减压过滤,固体在50℃及真空下干燥36h,得到白色固体,即高度生物安全性药用聚乳酸,产率70.1%,聚合物分子量3.6×104,PDI 1.90。Add 120 mg of catalyst bicyclic guanidine to the reactor, depressurize the reactor to 10 Torr, and raise the temperature to 200° C. for 20 h. After stopping the reaction, cool the reactor to room temperature, dissolve the polymer with acetone, then pour it into ethanol at 0°C, filter under reduced pressure, and dry the solid at 50°C under vacuum for 36 hours to obtain a white solid, which is highly biosafety Pharmaceutical polylactic acid, yield 70.1%, polymer molecular weight 3.6×10 4 , PDI 1.90.
实施例4Example 4
在反应釜中装入80g的L-乳酸(质量含量90%),重复抽真空—充氩气操作三次。在200Torr下加热至110℃,脱水反应1h。然后将反应釜减压至100Torr在140℃继续反应1h。然后将反应釜减压至30Torr在150℃继续反应1h,得到寡聚乳酸OLLA。80g of L-lactic acid (mass content 90%) was charged into the reactor, and the vacuuming-argon filling operation was repeated three times. Heated to 110°C under 200 Torr, dehydration reaction for 1h. Then the reactor was depressurized to 100 Torr and the reaction was continued at 140° C. for 1 h. Then the reactor was depressurized to 30 Torr and the reaction was continued at 150° C. for 1 h to obtain oligomeric lactic acid OLLA.
向反应釜加入催化剂双环胍120mg,将反应釜减压至10Torr,升温至210℃反应13h。停止反应后,将反应釜冷至室温,将聚合物用丙酮溶解,然后倒入0℃的乙醇中,减压过滤,固体在50℃及真空下干燥36h,得到白色固体,即高度生物安全性药用聚乳酸,产率69.2%,聚合物分子量4.0×104,PDI 1.85。Add 120 mg of catalyst bicyclic guanidine to the reactor, reduce the pressure of the reactor to 10 Torr, and raise the temperature to 210° C. for 13 hours. After stopping the reaction, cool the reactor to room temperature, dissolve the polymer with acetone, then pour it into ethanol at 0°C, filter under reduced pressure, and dry the solid at 50°C under vacuum for 36 hours to obtain a white solid, which is highly biosafety Pharmaceutical polylactic acid, yield 69.2%, polymer molecular weight 4.0×10 4 , PDI 1.85.
实施例5Example 5
在反应釜中装入80g的L-乳酸(质量含量90%),重复抽真空充氩气操作三次。在200Torr下加热至100℃,脱水反应1h。然后将反应釜减压至100Torr在150℃继续反应1h。然后将反应釜减压至30Torr在150℃继续反应1h,得到寡聚乳酸OLLA。80 g of L-lactic acid (mass content 90%) was charged into the reaction kettle, and the vacuum pumping and argon filling operations were repeated three times. Heating to 100°C under 200 Torr, dehydration reaction for 1h. Then the reactor was depressurized to 100 Torr and the reaction was continued at 150° C. for 1 h. Then the reactor was depressurized to 30 Torr and the reaction was continued at 150° C. for 1 h to obtain oligomeric lactic acid OLLA.
向反应釜加入催化剂双环胍72mg,将反应釜减压至10Torr,升温至220℃反应10h。停止反应后,将反应釜冷至室温,将聚合物用丙酮溶解,然后倒入0℃的乙醇中,减压过滤,固体在50℃及真空下干燥36h,得到白色固体,即高度生物安全性药用聚乳酸,产率67.4%,聚合物分子量2.9×104,PDI 2.00。Add 72 mg of catalyst bicyclic guanidine to the reactor, reduce the pressure of the reactor to 10 Torr, and raise the temperature to 220° C. for 10 h. After stopping the reaction, cool the reactor to room temperature, dissolve the polymer with acetone, then pour it into ethanol at 0°C, filter under reduced pressure, and dry the solid at 50°C under vacuum for 36 hours to obtain a white solid, which is highly biosafety Pharmaceutical polylactic acid, yield 67.4%, polymer molecular weight 2.9×10 4 , PDI 2.00.
实施例6Example 6
在反应釜中装入80g的L-乳酸(质量含量90%),重复抽真空充氩气操作三次。在200Torr下加热至120℃,脱水反应1h。然后将反应釜减压至100Torr在140℃继续反应1h。然后将反应釜减压至30Torr在160℃继续反应1h,得到寡聚乳酸OLLA。80 g of L-lactic acid (mass content 90%) was charged into the reaction kettle, and the vacuum pumping and argon filling operations were repeated three times. Heating to 120°C under 200 Torr, dehydration reaction for 1h. Then the reactor was depressurized to 100 Torr and the reaction was continued at 140° C. for 1 h. Then the reactor was depressurized to 30 Torr and the reaction was continued at 160° C. for 1 h to obtain oligomeric lactic acid OLLA.
向反应釜加入催化剂双环胍136mg,将反应釜减压至10Torr,升温至220℃反应15h。停止反应后,将反应釜冷至室温,将聚合物用丙酮溶解,然后倒入0℃的乙醇中,减压过滤,固体在50℃及真空下干燥36h,得到白色固体,即高度生物安全性药用聚乳酸,产率48.5%,聚合物分子量3.4×104,PDI 1.85。Add 136 mg of catalyst bicyclic guanidine to the reactor, reduce the pressure of the reactor to 10 Torr, and raise the temperature to 220° C. for 15 hours. After stopping the reaction, cool the reactor to room temperature, dissolve the polymer with acetone, then pour it into ethanol at 0°C, filter under reduced pressure, and dry the solid at 50°C under vacuum for 36 hours to obtain a white solid, which is highly biosafety Pharmaceutical polylactic acid, yield 48.5%, polymer molecular weight 3.4×10 4 , PDI 1.85.
实施例7Example 7
在反应釜中装入80g的L-乳酸(质量含量90%),重复抽真空—充氩气操作三次。在200Torr下加热至100℃,脱水反应1h。然后将反应釜减压至100Torr在140℃继续反应1h。然后将反应釜减压至30Torr在170℃继续反应1h,得到寡聚乳酸OLLA。80g of L-lactic acid (mass content 90%) was charged into the reactor, and the vacuuming-argon filling operation was repeated three times. Heating to 100°C under 200 Torr, dehydration reaction for 1h. Then the reactor was depressurized to 100 Torr and the reaction was continued at 140° C. for 1 h. Then the reactor was depressurized to 30 Torr and the reaction was continued at 170° C. for 1 h to obtain oligomeric lactic acid OLLA.
向反应釜加入催化剂双环胍72mg,将反应釜减压至10Torr,升温至230℃反应16h。停止反应后,将反应釜冷至室温,将聚合物用丙酮溶解,然后倒入0℃的乙醇中,减压过滤,固体在50℃及真空下干燥36h,得到白色固体,即高度生物安全性药用聚乳酸,产率66.3%,聚合物分子量3.9×104,PDI 1.78。Add 72 mg of catalyst bicyclic guanidine to the reactor, reduce the pressure of the reactor to 10 Torr, and raise the temperature to 230° C. for 16 hours. After stopping the reaction, cool the reactor to room temperature, dissolve the polymer with acetone, then pour it into ethanol at 0°C, filter under reduced pressure, and dry the solid at 50°C under vacuum for 36 hours to obtain a white solid, which is highly biosafety Pharmaceutical polylactic acid, yield 66.3%, polymer molecular weight 3.9×10 4 , PDI 1.78.
实施例8Example 8
在反应釜中装入80g的L-乳酸(质量含量90%),重复抽真空—充氩气操作三次。在200Torr下加热至110℃,脱水反应1h。然后将反应釜减压至100Torr在150℃继续反应1h。然后将反应釜减压至30Torr在160℃继续反应1h,得到寡聚乳酸OLLA。80g of L-lactic acid (mass content 90%) was charged into the reactor, and the vacuuming-argon filling operation was repeated three times. Heated to 110°C at 200 Torr, dehydration reaction for 1h. Then the reactor was depressurized to 100 Torr and the reaction was continued at 150° C. for 1 h. Then the reactor was depressurized to 30 Torr and the reaction was continued at 160° C. for 1 h to obtain oligomeric lactic acid OLLA.
向反应釜加入催化剂双环胍36mg,将反应釜减压至10Torr,升温至200℃反应15h。停止反应后,将反应釜冷至室温,将聚合物用丙酮溶解,然后倒入0℃的乙醇中,减压过滤,固体在50℃及真空下干燥36h,得到白色固体,即高度生物安全性药用聚乳酸,产率74.6%,聚合物分子量2.4×104,PDI 1.92。Add 36 mg of catalyst bicyclic guanidine to the reactor, reduce the pressure of the reactor to 10 Torr, and raise the temperature to 200° C. for 15 hours. After stopping the reaction, cool the reactor to room temperature, dissolve the polymer with acetone, then pour it into ethanol at 0°C, filter under reduced pressure, and dry the solid at 50°C under vacuum for 36 hours to obtain a white solid, which is highly biosafety Pharmaceutical polylactic acid, yield 74.6%, polymer molecular weight 2.4×10 4 , PDI 1.92.
实施例9Example 9
在反应釜中装入80g的L-乳酸(质量含量90%),重复抽真空充氩气操作三次。在200Torr下加热至120℃,脱水反应1h。然后将反应釜减压至100Torr在150℃继续反应1h。然后将反应釜减压至30Torr在150℃继续反应1h,得到寡聚乳酸OLLA。80 g of L-lactic acid (mass content 90%) was charged into the reaction kettle, and the vacuum pumping and argon filling operations were repeated three times. Heating to 120°C under 200 Torr, dehydration reaction for 1h. Then the reactor was depressurized to 100 Torr and the reaction was continued at 150° C. for 1 h. Then the reactor was depressurized to 30 Torr and the reaction was continued at 150° C. for 1 h to obtain oligomeric lactic acid OLLA.
向反应釜加入催化剂双环胍36mg,将反应釜减压至10Torr,升温至200℃反应16h。停止反应后,将反应釜冷至室温,将聚合物用丙酮溶解,然后倒入0℃的乙醇中,减压过滤,固体在50℃及真空下干燥36h,得到白色固体,即高度生物安全性药用聚乳酸,产率71.3%,聚合物分子量3.2×104,PDI 1.75。Add 36 mg of catalyst bicyclic guanidine to the reactor, reduce the pressure of the reactor to 10 Torr, and raise the temperature to 200° C. for 16 hours. After stopping the reaction, cool the reactor to room temperature, dissolve the polymer with acetone, then pour it into ethanol at 0°C, filter under reduced pressure, and dry the solid at 50°C under vacuum for 36 hours to obtain a white solid, which is highly biosafety Pharmaceutical polylactic acid, yield 71.3%, polymer molecular weight 3.2×10 4 , PDI 1.75.
实施例10Example 10
在反应釜中装入80g的L-乳酸(质量含量90%),重复抽真空—充氩气操作三次。在200Torr下加热至120℃,脱水反应1h。然后将反应釜减压至100Torr在150℃继续反应1h。然后将反应釜减压至30Torr在170℃继续反应1h,得到寡聚乳酸OLLA。80g of L-lactic acid (mass content 90%) was charged into the reactor, and the vacuuming-argon filling operation was repeated three times. Heated to 120°C under 200 Torr, dehydration reaction for 1h. Then the reactor was depressurized to 100 Torr and the reaction was continued at 150° C. for 1 h. Then the reactor was depressurized to 30 Torr and the reaction was continued at 170° C. for 1 h to obtain oligomeric lactic acid OLLA.
向反应釜加入催化剂双环胍11.1mg,将反应釜减压至10Torr,升温至210℃反应20h。停止反应后,将反应釜冷至室温,将聚合物用丙酮溶解,然后倒入0℃的乙醇中,减压过滤,固体在50℃及真空下干燥36h,得到白色固体,即高度生物安全性药用聚乳酸,产率68.4%,聚合物分子量4.0×104,PDI 1.91。Add 11.1 mg of catalyst bicyclic guanidine to the reactor, depressurize the reactor to 10 Torr, and raise the temperature to 210° C. for 20 h. After stopping the reaction, cool the reactor to room temperature, dissolve the polymer with acetone, then pour it into ethanol at 0°C, filter under reduced pressure, and dry the solid at 50°C under vacuum for 36 hours to obtain a white solid, which is highly biosafety Pharmaceutical polylactic acid, yield 68.4%, polymer molecular weight 4.0×10 4 , PDI 1.91.
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CN104892916A (en) * | 2015-06-11 | 2015-09-09 | 南京大学 | Technology for controlled synthesis of polylactic acid through lactide activity ring-opening polymerization under catalytic action of organic guanidine-nontoxic alcohol |
CN112094407A (en) * | 2020-09-27 | 2020-12-18 | 江南大学 | Biguanide group covalent organic framework material and preparation method and application thereof |
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CN102408553A (en) * | 2011-09-15 | 2012-04-11 | 南开大学 | Synthetic process of medical biodegradable polylactic acid-glutamic acid |
CN102504227A (en) * | 2011-10-14 | 2012-06-20 | 南开大学 | Process method for synthesizing lactic acid-lysine copolymer by catalytically opening loop and copolymerizing with acetic bicyclo-guanidine |
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CN102408553A (en) * | 2011-09-15 | 2012-04-11 | 南开大学 | Synthetic process of medical biodegradable polylactic acid-glutamic acid |
CN102504227A (en) * | 2011-10-14 | 2012-06-20 | 南开大学 | Process method for synthesizing lactic acid-lysine copolymer by catalytically opening loop and copolymerizing with acetic bicyclo-guanidine |
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CN104725616B (en) * | 2015-04-13 | 2017-01-11 | 南京大学 | Novel process for using organic guanidine catalysis melt-solid polycondensation to synthesize poly (butylene adipate-co-terephthalate) |
CN104892916A (en) * | 2015-06-11 | 2015-09-09 | 南京大学 | Technology for controlled synthesis of polylactic acid through lactide activity ring-opening polymerization under catalytic action of organic guanidine-nontoxic alcohol |
CN104892916B (en) * | 2015-06-11 | 2017-01-11 | 南京大学 | Technology for controlled synthesis of polylactic acid through lactide activity ring-opening polymerization under catalytic action of organic guanidine-nontoxic alcohol |
CN112094407A (en) * | 2020-09-27 | 2020-12-18 | 江南大学 | Biguanide group covalent organic framework material and preparation method and application thereof |
CN112094407B (en) * | 2020-09-27 | 2021-10-08 | 江南大学 | A kind of biguanide-based covalent organic framework material and preparation method and application thereof |
CN114685772A (en) * | 2022-04-20 | 2022-07-01 | 深圳光华伟业股份有限公司 | Novel biomedical polylactic acid synthesis method |
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