CN100999569A - Chemical synthesizing process of beta-butyrolactone with propyl lactide copolymer - Google Patents
Chemical synthesizing process of beta-butyrolactone with propyl lactide copolymer Download PDFInfo
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- CN100999569A CN100999569A CN 200610130757 CN200610130757A CN100999569A CN 100999569 A CN100999569 A CN 100999569A CN 200610130757 CN200610130757 CN 200610130757 CN 200610130757 A CN200610130757 A CN 200610130757A CN 100999569 A CN100999569 A CN 100999569A
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Abstract
The present invention is chemical process of synthesizing poly-3-hydroxy butyrate with beta-butyrolactone and lactide. The synthesizing process includes the following steps: preparing material including beta-butyrolactone in 1-100 weight portions and lactide in 1-100 weight portions; preparing polymerization catalyst in 0.01-1 wt% of the total material; drying the catalyst in the reaction container for up to 48 hr; sealing the material in the reaction container and stirring at 40-150 deg.c to react for 24-720 hr to obtain colorless solid product; dissolving the product in organic solvent and dropping excessive precipitant to obtain poly-3-hydroxy butyrate as the precipitate. Thus obtained beta-butyrolactone and lactide copolymer has molecular weight of 1,000-40,000 and relatively narrow molecular weight distribution.
Description
Technical field
The invention belongs to synthetic method of polymers, particularly synthesize the chemical synthesis process of poly 3-hydroxy butyrate with the technology of beta-butyrolactone and lactide copolymer.
Background technology
Poly 3-hydroxy butyrate (PHB) is a kind of fully biodegradable plastics.Because PHB excellent biological compatibility, PHB is at electronics, optics, particularly be subjected to people's great attention in the application of high-tech sectors such as biomedicine, PHB is at the absorbability suture so far, tissue and bone guided regeneration membrane, band medicine controlled release preparation, adsorbable bone folding maintenance clamping plate and retention pin, compound bone is subjected to broad research for aspects such as materials.
PHB is fermentation using bacteria and a kind of intracellular product of producing, and it is present in the cell with graininess.In order to use PHB, at first must fermentative production, separation and Extraction PHB in the cell afterwards.The molecular weight that extracts gained PHB and the polymerization degree are different and different with the kind of the kind of microorganism, restricted carbon source and concentration, culture condition, fermentation time, extracting method etc.In addition, because aspects such as bacterial classification, fermentative production and separation and Extraction exist because of difficulty, cause the PHB cost higher.It is reported, be that the synthetic plastics price of raw material is about 1～6.6 dollar/kg at present with the oil, and the cost of PHB obtains to use widely in order to make PHB up to 16～22 dollars/kg, must the new low-cost route of synthesis of exploitation.Chemical synthesis has be easy to relative with product quality of reaction and controls, the characteristics that can be mass-produced, the synthetic PHB of chemical method generally is to be that monomer obtains by ring-opening polymerization with the beta-butyrolactone, and synthetic PHB has become the parallel important method of biological process with chemical synthesis.
Purified PHB is the hard and crisp material of a kind of height isotactic, bad mechanical property, be easy to decomposes, solvent resistance is poor, (the PHB work range is narrow to be difficult to shortcomings such as processing, can only carry out about 190 ℃, fusing point 170-180 ℃ approaching with 205 ℃ of decomposition temperatures; Resistance to impact shock is low, and its elongation at break is 6%; And the PHB vivo degradation is also very slow).Therefore single PHB is subjected to certain restriction in medical use.The modification of PHB becomes one of key of PHB successful Application, the existing so far report that contains beta-lactam end group PHB, PHB-PHBV, PHB-PPVL and PHB grafting polymethyl acrylic acid.
This patent adopts the method for beta-butyrolactone and rac-Lactide copolymerization to improve the performance of PHB homopolymer, improves its mechanical property, processing characteristics to reach, and reduces its production cost.
Summary of the invention
The chemical synthesis process that the purpose of this invention is to provide a kind of beta-butyrolactone and lactide copolymer.
The chemical synthesis process of beta-butyrolactone of the present invention and lactide copolymer is the ring-opening polymerization by beta-butyrolactone and rac-Lactide, and its step is as follows:
(1) preparation reactant: the rac-Lactide of the beta-butyrolactone of 1 ~ 100 weight part and 1 ~ 100 weight part;
(2) polycoordination class catalyzer or anionoid polymerization class catalyzer are gross weight 0.01 ~ 1%; With catalyzer in reaction vessel dry 0 ~ 48 hour;
(3) reactant is gone in reaction vessel and with reaction vessel to seal, stirring down, 40 ~ 150 ℃ of reactions obtained beta-butyrolactone and lactide copolymer in 24 ~ 720 hours.
Can also step (1) and (2) is constant, and step (3) is that reactant is gone in reaction vessel, and 10 ~ 200 parts by weight solvent are joined in the reaction vessel; Step (4) is: 40 ~ 140 ℃ were reacted 24 ~ 144 hours under argon filling stirred, and obtaining thing is beta-butyrolactone and lactide copolymer.
Catalyzer of the present invention is a kind of in coordination polymerization catalysts dibutyl tin dichloride, Dibutyltin oxide, dioctyl tin oxide, dimethyl tin oxide, triethyl aluminum/water, zinc ethyl/water, porphyrin aluminium or the tetrabutylammonium acetate amine.
The chemical synthesis process of described poly 3-hydroxy butyrate is characterized in that described rac-Lactide is L-rac-Lactide or D, the L-rac-Lactide.
Described dry solvent is a tetrahydrofuran (THF), trichloromethane, any of methylene dichloride or toluene.
Stirring of the present invention is to stir at machinery or electric power.
Effect of the present invention is by beta-butyrolactone and rac-Lactide copolymerization, has realized the chemical modification to PHB, and its crystallinity and processing characteristics are all improved.
Utilize the preparation method of beta-butyrolactone of the present invention and lactide copolymer, can make the number average relative molecular mass of beta-butyrolactone and lactide copolymer reach 1000～40000, and the relative molecular mass narrowly distributing.
Description of drawings
Fig. 1 is the prepared multipolymer of embodiment 1
1The HNMR spectrogram;
Fig. 2 is the prepared multipolymer of embodiment 1
13The CNMR spectrogram.
Embodiment
(1) the catalyzer dibutyl tin dichloride of 0.0033g was loaded in the reaction vessel vacuum-drying 48 hours, (2) add the beta-butyrolactone of 0.33g in reaction vessel, and (3) join the L-rac-Lactide of 33g in the reaction vessel and with reaction vessel and seal.(4) the magnetic force condition stirs following 120 ℃ of reactions and obtained the water white transparency solid in 48 hours.(5) product that step (4) is obtained is dissolved in the methylene dichloride, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, its
1H-NMR spectrogram such as accompanying drawing 1,1.25ppm, 2.47ppm, 2.59ppm, 5.23ppm belong to the characteristic peak of poly 3-hydroxy butyrate section, and 1.56ppm and 5.15ppm belong to the characteristic peak of poly(lactic acid) section.
13C-NMR such as accompanying drawing 2,19.8ppm, 40.7ppm, 67.7ppm and 169.1ppm be the characteristic absorbance of poly 3-hydroxy butyrate section, and 16.6ppm, 69.4ppm and 169.6ppm are the characteristic absorbance of poly(lactic acid) section, illustrate that product is beta-butyrolactone and L-lactide copolymer.The number average relative molecular mass of multipolymer is 20000.
Catalyzer can also be a kind of in Dibutyltin oxide, dioctyl tin oxide and dimethyl tin oxide, triethyl aluminum/water, zinc ethyl/water, the porphyrin aluminium in this example.
Embodiment 2
(1) the catalyzer dibutyl tin dichloride with 0.33g is loaded in the reaction vessel, and (2) add the beta-butyrolactone of 33g in the reaction vessel, and with the D of 0.33g, the L-rac-Lactide joins in the reaction vessel and with reaction vessel to be sealed (3).(4) stir following 40 ℃ of reactions and obtained the water white transparency solid in 48 hours.(5) product that step (4) is obtained is dissolved in the methylene dichloride, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 3000.
Catalyzer can also be a kind of in Dibutyltin oxide, dioctyl tin oxide and dimethyl tin oxide, triethyl aluminum/water, zinc ethyl/water, the porphyrin aluminium in this example.
Embodiment 3
(1) the catalyzer dibutyl tin dichloride of 0.0033g was loaded in the reaction vessel vacuum-drying 24 hours, (2) add the beta-butyrolactone of 0.33g in reaction vessel, and (3) join the L-rac-Lactide of 0.55g in the reaction vessel and with reaction vessel and seal.(4) stir following 40 ℃ of reactions and obtained the water white transparency solid in 720 hours.(5) product that step (4) is obtained is dissolved in the methylene dichloride, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 12000.
Catalyzer can also be a kind of in Dibutyltin oxide, dioctyl tin oxide and dimethyl tin oxide, triethyl aluminum/water, zinc ethyl/water, the porphyrin aluminium in this example.
Embodiment 4
(1) the catalyzer tetrabutylammonium acetate ammonium of 0.0033g was loaded in the reaction vessel vacuum-drying 48 hours, (2) add the beta-butyrolactone of 0.33g in reaction vessel, and with the D of 33g, the L-rac-Lactide joins in the reaction vessel and with reaction vessel to be sealed (3).(4) stir following 80 ℃ of reactions and obtained the water white transparency solid in 48 hours.(5) product that step (4) is obtained is dissolved in the methylene dichloride, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 18000.
Embodiment 5
(1) the catalyzer tetrabutylammonium acetate ammonium of 0.33g was loaded in the reaction vessel vacuum-drying 48 hours, (2) add the beta-butyrolactone of 33g in reaction vessel, and (3) join the L-rac-Lactide of 0.33g in the sealed reaction vessel.(4) the following 40 ℃ of reactions of mechanical stirring obtained the water white transparency solid in 144 hours.(5) product that step (4) is obtained is dissolved in the methylene dichloride, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 4500.
Embodiment 6
(1) the catalyzer tetrabutylammonium acetate ammonium with 0.0033g is loaded in the reaction vessel, and (2) add the beta-butyrolactone of 0.33g in the reaction vessel, and with the D of 0.55g, the L-rac-Lactide joins in the reaction vessel and with reaction vessel to be sealed (3).(4) stir following 120 ℃ of reactions and obtained the water white transparency solid in 48 hours.(5) product that step (4) is obtained is dissolved in the methylene dichloride, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 8900.
Embodiment 7
(1) the catalyzer dioctyl tin oxide of 0.0047g was loaded in the reaction vessel vacuum-drying 48 hours, (2) beta-butyrolactone with 0.12g adds in the reaction vessel, (3) the L-rac-Lactide with 12g joins in the reaction vessel, (4) drying is good 50mL tetrahydrofuran (THF) joins in the reaction vessel, (5) argon filling stirs following 40 ℃ of reactions 48 hours, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 19800.
Catalyzer can also be a kind of in Dibutyltin oxide, dibutyl tin dichloride and dimethyl tin oxide, triethyl aluminum/water, zinc ethyl/water, the porphyrin aluminium in this example.
Dry solvent can also be a trichloromethane in this example, methylene dichloride, any in the toluene.
Embodiment 8
(1) the catalyzer dioctyl tin oxide of 0.012g was loaded in the reaction vessel vacuum-drying 48 hours, (2) beta-butyrolactone with 12g adds in the reaction vessel, (3) the L-rac-Lactide with 0.12g joins in the reaction vessel, (4) drying is good 10mL tetrahydrofuran (THF) joins in the reaction vessel, (5) argon filling stirs following 40 ℃ of reactions 144 hours, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 8000.
Catalyzer can also be a kind of in Dibutyltin oxide, dibutyl tin dichloride and dimethyl tin oxide, triethyl aluminum/water, zinc ethyl/water, the porphyrin aluminium in this example.
Dry solvent can also be a trichloromethane in this example, methylene dichloride, any in the toluene.
Embodiment 9
(1) the catalyzer dioctyl tin oxide of 0.0033g was loaded in the reaction vessel vacuum-drying 48 hours, (2) beta-butyrolactone with 0.3g adds in the reaction vessel, (3) the L-rac-Lactide with 1.2g joins in the reaction vessel, (4) drying is good 10mL tetrahydrofuran (THF) joins in the reaction vessel, (5) argon filling stirs following 40 ℃ of reactions 72 hours, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 10000.
Catalyzer can also be a kind of in Dibutyltin oxide, dibutyl tin dichloride and dimethyl tin oxide, triethyl aluminum/water, zinc ethyl/water, the porphyrin aluminium in this example.
Dry solvent can also be a trichloromethane in this example, methylene dichloride, any in the toluene.
Embodiment 10
(1) the catalyzer tetrabutylammonium acetate ammonium of 0.0047g was loaded in the reaction vessel vacuum-drying 48 hours, (2) beta-butyrolactone with 0.12g adds in the reaction vessel, (3) the L-rac-Lactide with 12g joins in the reaction vessel, (4) drying is good 50mL tetrahydrofuran (THF) joins in the reaction vessel, (5) argon filling stirs following 40 ℃ of reactions 48 hours, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 17000.
Dry solvent can also be a trichloromethane in this example, methylene dichloride, any in the toluene.
(1) the catalyzer tetrabutylammonium acetate ammonium of 0.012g was loaded in the reaction vessel vacuum-drying 48 hours, (2) beta-butyrolactone with 12g adds in the reaction vessel, (3) with the D of 0.12g, the L-rac-Lactide joins in the reaction vessel, (4) drying is good 10mL tetrahydrofuran (THF) joins in the reaction vessel, (5) argon filling stirs following 40 ℃ of reactions 144 hours, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 6000.
Dry solvent can also be a trichloromethane in this example, methylene dichloride, any in the toluene.
Embodiment 12
(1) the catalyzer tetrabutylammonium acetate ammonium of 0.0033g was loaded in the reaction vessel vacuum-drying 48 hours, (2) beta-butyrolactone with 0.3g adds in the reaction vessel, (3) the L-rac-Lactide with 1.2g joins in the reaction vessel, (4) drying is good 10mL tetrahydrofuran (THF) joins in the reaction vessel, (5) argon filling stirs following 40 ℃ of reactions 72 hours, gets solution A.A is added drop-wise in the excessive anhydrous methanol, obtains white precipitate B, will promptly get the multipolymer of beta-butyrolactone and L-rac-Lactide after the gained deposit B washing drying, the number average relative molecular mass of multipolymer is 11000.
Dry solvent can also be a trichloromethane in this example, methylene dichloride, any in the toluene.
The present invention proposes the chemical synthesis process of beta-butyrolactone and lactide copolymer, be described by embodiment, person skilled obviously can be changed or suitably change and combination content as herein described in not breaking away from content of the present invention, spirit and scope, realizes the present invention.Special needs to be pointed out is, the replacement that all are similar and change apparent to those skilled in the artly, they are regarded as being included in spirit of the present invention, scope and the content.
Claims (7)
1. the chemical synthesis process of the multipolymer of beta-butyrolactone and rac-Lactide is by the polyreaction of beta-butyrolactone and rac-Lactide, it is characterized in that:
(1) preparation reactant: the rac-Lactide of the beta-butyrolactone of 1 ~ 100 weight part and 1 ~ 100 weight part;
(2) polycoordination class catalyzer or anionoid polymerization class catalyzer are gross weight 0.01 ~ 1%; With catalyzer in reaction vessel dry 0 ~ 48 hour;
(3) reactant is gone in reaction vessel and with reaction vessel to seal, stirring down, 40 ~ 150 ℃ of reactions obtained beta-butyrolactone and lactide copolymer in 24 ~ 720 hours.
2. the chemical synthesis process of the multipolymer of beta-butyrolactone as claimed in claim 1 and rac-Lactide is characterized in that described step (3) is that reactant is gone in reaction vessel, joins 10 ~ 200 parts by weight solvent in the reaction vessel; (4) 40 ~ 15 ℃ were reacted 144 hours under argon filling stirred, and obtaining thing is the multipolymer of beta-butyrolactone and rac-Lactide.
3. the chemical synthesis process of the multipolymer of beta-butyrolactone as claimed in claim 1 or 2 and rac-Lactide is characterized in that described catalyzer is a kind of in coordination polymerization catalysts dibutyl tin dichloride, Dibutyltin oxide, dioctyl tin oxide, dimethyl tin oxide, triethyl aluminum/water, zinc ethyl/water, porphyrin aluminium or the tetrabutylammonium acetate amine.
4. the chemical synthesis process of the multipolymer of beta-butyrolactone as claimed in claim 1 or 2 and rac-Lactide is characterized in that described rac-Lactide is L-rac-Lactide or D, the L-rac-Lactide.
5. the chemical synthesis process of the multipolymer of beta-butyrolactone as claimed in claim 1 or 2 and rac-Lactide is characterized in that described dry solvent is a tetrahydrofuran (THF), trichloromethane, any of methylene dichloride or toluene.
6. the chemical synthesis process of the multipolymer of beta-butyrolactone as claimed in claim 1 or 2 and rac-Lactide is characterized in that described stirring is in machinery or induction stirring.
7. the chemical synthesis process of the multipolymer of beta-butyrolactone as claimed in claim 1 or 2 and rac-Lactide is characterized in that described drying is vacuum-drying.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101134808B (en) * | 2007-10-18 | 2010-05-19 | 吉林大学 | Method for catalyzing polymerization of cyclic lactone |
| CN102643301A (en) * | 2011-02-22 | 2012-08-22 | 中国石油天然气股份有限公司 | Alkoxy aluminum complex, and preparation and application thereof |
| CN115340673A (en) * | 2022-10-17 | 2022-11-15 | 富海(东营)新材料科技有限公司 | Light-stable type polyphenylsulfone resin and preparation method thereof |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP4092067A1 (en) * | 2021-05-21 | 2022-11-23 | TotalEnergies OneTech | Process for preparing tailor-made lactide copolymers and lactide copolymers thereby obtained |
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2006
- 2006-12-31 CN CNB2006101307578A patent/CN100506878C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101134808B (en) * | 2007-10-18 | 2010-05-19 | 吉林大学 | Method for catalyzing polymerization of cyclic lactone |
| CN102643301A (en) * | 2011-02-22 | 2012-08-22 | 中国石油天然气股份有限公司 | Alkoxy aluminum complex, and preparation and application thereof |
| CN102643301B (en) * | 2011-02-22 | 2014-12-24 | 中国石油天然气股份有限公司 | Alkoxy aluminum complex, and preparation and application thereof |
| CN115340673A (en) * | 2022-10-17 | 2022-11-15 | 富海(东营)新材料科技有限公司 | Light-stable type polyphenylsulfone resin and preparation method thereof |
| CN115340673B (en) * | 2022-10-17 | 2022-12-20 | 富海(东营)新材料科技有限公司 | Light-stable type polyphenylsulfone resin and preparation method thereof |
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