WO2008150033A1 - エポキシドと二酸化炭素との立体選択的交互共重合 - Google Patents
エポキシドと二酸化炭素との立体選択的交互共重合 Download PDFInfo
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- WO2008150033A1 WO2008150033A1 PCT/JP2008/060813 JP2008060813W WO2008150033A1 WO 2008150033 A1 WO2008150033 A1 WO 2008150033A1 JP 2008060813 W JP2008060813 W JP 2008060813W WO 2008150033 A1 WO2008150033 A1 WO 2008150033A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G64/00—Macromolecular compounds obtained by reactions forming a carbonic ester link in the main chain of the macromolecule
- C08G64/20—General preparatory processes
- C08G64/32—General preparatory processes using carbon dioxide
- C08G64/34—General preparatory processes using carbon dioxide and cyclic ethers
Definitions
- the present invention relates to a method for producing a polystrength by alternating copolymerization of epoxide and carbon dioxide, and a catalyst used for the production method.
- the present invention relates to a method for producing a polycarbonate having high stereoregularity and a catalyst used in the production method.
- Optically active polycarbonate obtained by alternately polymerizing one kind of chiral epoxide isomer and carbon dioxide has a highly stereoregular polymer structure, and has excellent mechanical and physical chemistry. It is expected to be applied to chromatographies, separation media such as separation membranes, biodegradable materials, ferroelectric materials, and piezoelectric pyroelectric materials. .
- optically active polycarbonate is a force that can be produced by using one optical isomer of chiral epoxide. Since chiral epoxide is usually obtained as a racemic mixture, Must prepare one of the very expensive optical isomers. On the other hand, the optically active polycarbonate can be synthesized by selectively polymerizing one kind of optical isomer with carbon dioxide from a racemic mixture of readily available epoxides. For this reason, research aimed at developing enantioselective alternating copolymerization reactions using racemic mixtures is underway.
- the second epoxy raw material (1 -Butenoxide) is introduced to form a different polymer chain at the end of the polymer chain to produce a block copolymer. Disclosure of the invention
- the present invention is a method for producing a polycarbonate copolymer by copolymerizing with carbon dioxide using an epoxide compound as a monomer raw material in the presence of a planar four-coordinate type cobalt mono-Schiff base complex,
- the Schiff base ligand is N, N'-bis (2-hydroxybenzylidene) ethylenediamine (sal en, salen) or N, N'-bis (2-hydroxybenzylidene) phenylenediamine (sal ph) Or a derivative thereof, in which a methyl group substituted with an asymmetric carbon atom or an amino group having an asymmetric axis at the 3-position and / or 3'-position of the benzene ring derived from the salicyl group is introduced. It is a method characterized by
- Another aspect of the present invention is a cobalt-Schiff base complex that can be used as a polymerization catalyst for the production of polycarbonate, wherein an asymmetric carbon atom or asymmetric group is present at the 3rd and / or 3 'position of the salicyl group.
- the cobalt complex used as a catalyst in the present invention contains a Schiff base that is a planar four-coordinate multidentate ligand.
- the typical Schiff base ligand used in the present invention is a salen ligand ( ⁇ , ⁇ '-bis (salicylidene) ethylenediamine) and its derivatives (hereinafter referred to as "salen ligands"). ”).
- a salen-based ligand is obtained by a dehydration condensation reaction between salicylaldehyde and ethylenediamine.
- ethylenediamine By using a different diamine instead of ethylenediamine, or by introducing a substituent into the aromatic ring portion of salicylic acid.
- a large number of derivatives can be obtained.
- the particularly preferred compound is the sa I cy ligand (N, N '—bis (salicylidene) _ 1 obtained by changing the ethylenediamine moiety of the salen ligand to cyclohexanediamine.
- a methyl group (hereinafter referred to as “arm”) substituted with an amino having an asymmetric carbon center or an asymmetric axis is introduced at the 3-position (—and out).
- the two substituents may be the same or different.
- the amino group constituting the arm may be a tertiary amino group, preferably a pyrrolidinyl group.
- a pyrrolidinyl group preferably a pyrrolidinyl group, so that, for example, when the amino group constituting the arm is a pyrrolidinyl group,
- the carbon of the 5-membered ring to which the substituent is bonded shows optical activity as an asymmetric center. Not limited to substituents).
- the absolute configuration around the asymmetric carbon center or the asymmetric axis that characterizes the structure of the amino group that constitutes the arm has two types (R) and (S). Select the arm that has either absolute configuration. Whether or not to be introduced can be determined in consideration of the absolute configuration of the polycarbonate ⁇ having the desired optical activity.
- the central metal of the cobalt complex is involved in the polymerization reaction of the present invention, it is easy to substitute one or two in the axial direction of the central metal so that the cobalt metal can easily act on the substrate.
- the ligand can be coordinated. Most typical ligands are carboxylate, halogen, etc., preferably acetate (A c O—).
- a preferred cobalt-Schiff base complex of the present invention has the following formula:
- X, H, C, _ 2 alkyl, ⁇ 2 alkoxy, C 6 -.. 20 ⁇ reel, F any one type of group selected from the group consisting of C 1, B r and I
- Y is one kind of anion ligand selected from the group consisting of aliphatic carboxylate, aromatic carboxylate, Cl—, Br— and I—.
- a particularly preferred cobalt mono-Schiff base complex of the present invention is a compound represented by the following formula.
- the catalyst system used in the present invention alone exhibits sufficient catalytic activity and exhibits excellent enantioselectivity without using a nucleophile or other promoter.
- a composite catalyst system in which a cobalt mono-Schiff base complex and a co-catalyst such as a nucleophilic reagent are combined is used in the same manner as a conventional catalyst system used for the production of a polycarbonate copolymer. May be.
- the catalyst of the present invention is characterized in that the substrate conversion rate can be 100% (that is, the substrate can be completely consumed).
- the present invention has the following preferred embodiments.
- the catalyst of the present invention when a racemic mixture of chiral epoxide is used as a monomer raw material and alternating copolymerization with carbon dioxide is carried out, one of the optical isomers contained in the monomer raw material first. Is selectively consumed, and until the optical isomer is completely consumed, the absolute configuration of the asymmetric carbon center contained in the polymer chain is given preference to either S or R. An optically active polymer is produced.
- one kind of optical isomer contained in the monomer raw material is selectively consumed, and the polymerization reaction is stopped by the reaction terminator before the optical isomer becomes complete.
- an optically active polycarbonate in which the absolute configuration of the asymmetric carbon center contained in the polymer chain preferentially contains either S or R can be produced.
- one optical isomer is completely consumed in the polymerization reaction in the presence of the catalyst of the present invention and then the polymerization reaction is continued, the other optical isomer remaining without being selected. Is bonded to the polymer chain, and a chain structure having a different absolute configuration from the previous polymer chain is added.
- the absolute configuration of the asymmetric carbon center in the high molecular chain is S by continuing the polymerization reaction after one type of optical isomer is completely consumed.
- Polycarbonates can be manufactured, consisting of blocks that preferentially contain some and blocks that preferentially contain R whose absolute configuration is R.
- the absolute configuration of the asymmetric carbon center in the polymer chain is highly stereoregular (only optical (R, R) or (S, S)). It is also possible to produce polycarbonates having activity.
- the substrate can be completely consumed, the same as the first epoxide after the first epoxide is completely consumed.
- a block polymer with high stereoregularity can be synthesized by introducing a different second epoxide.
- the composition ratio of the optical isomers contained in the monomer raw material not only the composition ratio of the optical isomers contained in the monomer raw material, but also the variety of epoxides and the order in which they are added are appropriately adjusted so that the stereoregularity is controlled.
- a polycarbonate copolymer can be produced.
- a preferred embodiment of the present invention includes a polycarbonate having a novel block copolymer structure. That is, the polycarbonate of the present invention Is a block copolymer consisting of blocks that preferentially contain those whose absolute configuration at the asymmetric carbon center in the polymer chain is S and blocks that preferentially contain those whose absolute self-position is R. .
- the polycarbonate of the present invention is a block comprising a block containing those in which the absolute configuration of the asymmetric carbon center in the polymer chain is only S and a block containing those in which the absolute configuration is only R. It is a copolymer.
- the molar ratio of one epoxide optically different substance preferentially contained in the block is 60% or more, preferably 70% or more, based on the total amount of epoxide monomers contained in the block. Preferably, it can take a value of 75% or more.
- the epoxide compound that can be used as a monomer raw material for the production method of the present invention includes both chiral epoxides and meso epoxides. Specifically, an epoxide represented by the following formula may be included.
- R 1 and R 2 may be the same or different, provided that they are not hydrogen atoms at the same time. Furthermore, R 1 and R 2 are independently a hydrogen atom or a halogen atom.
- Substituted amino group one NR 3 R 4 ), cyano, linear or branched C, ⁇ C 2 Q alkyl, C 2 ⁇ C 2 alkenyl or C ;: ⁇ C 2 () alkynyl, C 4 ⁇ C 1 () cycloalkyl, C 6 ⁇ C 4 Q Ariru or C 7 ⁇ C 4 Q ⁇ reel alkyl, there have, R 1 and R 2 are together in a connexion saturated or unsaturated C 4 ⁇ C, may form an alicyclic group; the aryl moiety in the allyl and allyl alkyl and the alicyclic group are a halogen atom, a linear or branched C i C ⁇ alkyl, C 2 ⁇ C 2.
- alkenyl Wakashi Ku is selected from the group consisting of C 2 ⁇ C 2 0 alkynyl, C 4 ⁇ C 2 0 cycloalkyl Bale May be substituted with one or more substituents, or may be saturated or unsaturated C 4 to C 1 Q when the two substituents bonded to two adjacent carbons constituting the aryl ring are joined together.
- An alicyclic group may be formed; the alkyl, alkenyl, alkynyl and cycloalkyl, aryl and alicyclic group may contain one or more heteroatoms, wherein the heteroatoms are One or more atoms selected from nitrogen, oxygen, sulfur, phosphorus and silicon; the halogen is one or more atoms selected from fluorine, chlorine, bromine and iodine;
- R 3 and R 4 are linear or branched C, ⁇ C 2 0 alkyl, C 2 ⁇ C 20 alkenyl Wakashi Ku is C 2 ⁇ C 2.
- Alkynyl, C 4 -C I () cycloalkyl, C 6 -C 40 aryl or C 7 -C 4 Q arylalkyl, or R 3 and R 4 together are saturated or unsaturated. May form saturated C 4 -C 1 () alicyclic groups,
- heteroatom can be present, for example, in the form:
- Oxygen atoms can be included in the alkyl chains of alkyl and arylalkyl to produce ether linkages and form aryloxy groups.
- a more preferred epoxide compound that can be used in the production method of the present invention is a chiral epoxide or meso epoxide represented by the following formula:
- the shaku 2 shaku 2 may be the same or different, provided that they are not simultaneously hydrogen atoms, and R 1 and R 2 are independently hydrogen atoms, Linear or branched C 1, C 8 alkyl, C 2 C 8 alkenyl or C 2 C 8 alkynyl, 4 8 cycloalkyl, C 6 C 6 aryl, or C 7 C 2 .
- R 1 and R 2 together may form a saturated or unsaturated C 4 to C 8 alicyclic group;
- Two adjacent may have both substituents attached to the carbon to form a C 4 ⁇ C 8 alicyclic group together such connexion saturated or unsaturated constituting a;
- the Al kill, alkenyl, alkynyl and cycloalkyl Alkyl, aryl and alicyclic groups may contain one or more heteroatoms, wherein the halogen is one or more atoms selected from fluorine, chlorine, bromine and iodine.
- chiral epoxides that are particularly preferred as monomer raw materials for the production method of the present invention include propylene oxide, 1-butene oxide, 1-pentenoxide, 2-penteneoxide, 1-hexene oxide, and 1-octenoxide.
- Examples include dimethylsilyloxypropyleneoxy, and propyleneoxide is preferable.
- These chiral epoxides can be used as racemic mixtures (but are not limited to these).
- mesoepoxy particularly preferable as a monomer raw material include 2-butene thioside, cyclite P pentene oxy, and hexene oxide (but not limited to them).
- carbon dioxide to be copolymerized with the chiral epoxide is introduced into the reaction vessel in the form of gas and used for the reaction.
- the alternating copolymerization reaction in the present invention is preferably carried out in an inert atmosphere in order to eliminate the influence of oxygen and the like, and carbon dioxide coexists in the reaction vessel together with the inert gas.
- the pressure of carbon dioxide in the reaction vessel is 0.16 M
- P a preferably 1.0 3. O M Pa.
- the molar ratio of epoxide to carbon dioxide used in the reaction is typically 1 • 0.1 L
- a force that is 10 is preferably 10.5 and more preferably 13.0
- the copolymerization reaction of the present invention may be carried out in a solvent or without using a solvent.
- a solvent is used, toluene, methylene chloride, 1,2-dimethoxetane, or the like may be used.
- 1,2-dimethoxetane is used.
- the alternating copolymerization in the present invention can be carried out in a temperature range of about 0 60 but is usually carried out at room temperature.
- the alternating copolymerization reaction can continue until the epoxide is completely consumed in the presence of an excess of carbon dioxide, but it can be adequate after the reaction has proceeded sufficiently for several hours to several tens of hours.
- the reaction may be stopped with a reaction stopper.
- the reaction stopper is a conventional reagent that stops the polymerization reaction of polycarbonate ⁇ .
- compounds having active protons such as alcohol (for example, methanol), water, and acid (for example, hydrochloric acid) can be used.
- the molecular weight of the polycarbonate produced according to the present invention has a typical number average molecular weight Mn measured by gel permeation chromatography (GPC; converted to polystyrene) of 10,000 or more, preferably 2 , 0 0 0 to 1, 0 0 0, 0 0 0, and more preferably 3, 0 0 0 to 1 0 0, 0 0 0.
- GPC gel permeation chromatography
- the optically active polycarbonate obtained by the production method of the present invention can have a relatively narrow molecular weight distribution (M w / M n ). Specifically, it is less than 4, preferably less than 2.5, and most preferably from about 1.0 to about 1.6.
- M w / M n relatively narrow molecular weight distribution
- the 1 H NMR spectrum of the compound obtained in this example was measured using JNM-ECP500 (500 MHz) manufactured by JE0L.
- the molecular weight of the optically active polycarbonate is measured using a high-performance liquid chromatography system (DG660B ⁇ PU713 ⁇ UV702 • RI704 ⁇ C0631A) manufactured by GL Sciences and two KF-804F force rams manufactured by SH0DEX.
- the eluate 40 ° C, 1.0 mL / min
- the optical purity of the unreacted optically active epoxide is measured.
- the enantiomeric excess rate (% ee ) calculated by converting the epoxide into a corresponding cyclic carbonate ⁇ was evaluated.
- helium was measured as a carrier gas using a Shimadzu gas chromatograph system (GC-2010) and an analytical column (Chemopack CHIRASIL-DEX CB).
- Enantiomeric excess the peak area of each of the optical isomers obtained by Gasukuroma Bok graph was evaluated by the following formulas (R body, the peak area of S-form and A R, A s respectively).
- index (k rel ) was evaluated by the following equation to show the selectivity indicating whether one kind of enantiomer was preferentially incorporated into the polymer from the racemate.
- ee is the enantiomeric excess of unreacted epoxide obtained by the above method
- c is the conversion of epoxide
- Dichloromethane and tetrahydrofuran used as solvents in the following synthesis examples were obtained by passing a dehydrated grade reagent obtained from Kanto Chemical Co., Ltd. through a solvent purifier manufactured by Glass Contour. Further, ethanol was used as it was without purifying a reagent obtained from Kanto Chemical.
- Cobalt acetate was available from Kanto Chemical. Glacial acetic acid was used without purification from a reagent obtained from Aldrich. For (1 R, 2 R) -1, 2 -diaminocyclohexane, the reagent obtained from Tokyo Chemical Industry Co., Ltd. was used as it was.
- (S)-2-(Diphenylmethyoxymethyl) pyrrolidine has been reported in the literature [(1) Enders, D .; Kipphardt, H .; Gerdes, P .; Brena-Val le, LJ; Bhushan, V. Bull. im, Belg. 1988, 8— 9, 691-704. (2) Ho, CY; Chen, YC; Wong, MK; Yang, DJ Org. Chem. 2005, 70, 898-906.] The one prepared according to the method was used.
- the salicylaldehyde derivative 3 used as a raw material in the following ligand synthesis was prepared according to the literature (DiMauro, EF; Kozlowski, M. Org. Lett. 20 01, 3, 3053-3056).
- the propylene oxide used in the following polymerization experiments was obtained by dehydrating a reagent obtained from Tokyo Chemical Industry with calcium hydride and then distilling in an argon atmosphere.
- the complex 6 used for the production of the following polycarbonate is the same as K. Nakano, et al., Angew. Chem., Int. Ed, 2006, 45, 7274-7. The one prepared according to 277 was used.
- the substrate conversion rate was calculated as follows. That is, after the polymerization was completed, phenanthrene was added to the reaction mixture as an internal standard, and a part of the resulting mixture was extracted and subjected to NMR measurement. The amounts of PPC and PC were calculated from the peak areas of phenanthrene, polypropylene carbonate (PPC), and propylene carbonate (PC), and the sum was used as the substrate conversion rate.
- Copolymer selectivity > 99%
- Spider body excess rate 13.3% [(A) holiday]
- Example 2 Production of polypropylene carbonate using cobalt complex 2b of the present invention
- Enantiomeric excess 15.4% [(A) body]
- Enantiomeric excess 0%
- the recovered unreacted epoxide, sodium iodide (21 mg, 0.143 mmol), triphenylphosphine (38 mg, 0.143 mmol), and phenol (14 mg, 0.143 mmol) are placed in a pressure-resistant reaction vessel.
- Carbon dioxide (4.0 MPa) was injected and stirred at 120 for 5 hours.
- the carbon dioxide pressure was removed and a portion of the reaction mixture was taken to determine the enantiomeric excess of propylene carbonate produced by gas chromatography (0% ee).
- K re 1.0 was calculated from the above equation.
- Example 3 Production of polypropylene carbonate ⁇ using cobalt complex 2a of the present invention (when high substrate conversion rate is achieved)
- Copolymer selectivity > 99%
- cobalt complex 2a (12 mg, 0.014 mmol) and propylene oxide (2.0 mL, 28.6 mmol) were placed in a pressure-resistant reactor, carbon dioxide (1.4 MPa) was injected, and the mixture was stirred at 25 at 78 hours. did. The carbon dioxide pressure was released, most of the unreacted propylene oxide was recovered under reduced pressure, and the solid composition organism remaining in the reaction vessel was transferred to a round-bottomed flask using a black mouth form.
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Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
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US12/663,639 US20100256329A1 (en) | 2007-06-08 | 2008-06-06 | Stereoselective alternating copolymerization of epoxide with carbon dioxide |
EP08765554A EP2157116A4 (en) | 2007-06-08 | 2008-06-06 | ALTERNATED STEREOSELECTIVE EPOXY-CARBON DIOXIDE COPOLYMER |
CN200880019263A CN101715465A (zh) | 2007-06-08 | 2008-06-06 | 环氧化物和二氧化碳的立体选择***替共聚 |
JP2009517933A JPWO2008150033A1 (ja) | 2007-06-08 | 2008-06-06 | エポキシドと二酸化炭素との立体選択的交互共重合 |
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JP2007153322 | 2007-06-08 | ||
JP2007-153322 | 2007-06-08 |
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EP (1) | EP2157116A4 (ja) |
JP (1) | JPWO2008150033A1 (ja) |
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WO (1) | WO2008150033A1 (ja) |
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US11634539B2 (en) | 2018-09-24 | 2023-04-25 | Saudi Aramco Technologies Company | Polycarbonate block copolymers and methods thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0597276A1 (de) * | 1992-11-11 | 1994-05-18 | Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. | N,N'-2.2-3.3-Tetramethylethylen-bis(5-NO2-salicyliden-iminato)colbalt(II) und dessen Verwendung als Trägersubstanz für Sauerstoff |
CN1560111A (zh) * | 2004-02-27 | 2005-01-05 | 大连理工大学 | 一种高分子量完全交替结构聚碳酸酯的制备方法 |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3869229D1 (de) * | 1987-06-10 | 1992-04-23 | Siemens Ag | Generatorschaltung. |
DE19914953A1 (de) * | 1999-04-01 | 2000-10-05 | Basf Ag | Verfahren der radikalisch initiierten wässrigen Emulsionspolymerisation |
-
2008
- 2008-06-06 EP EP08765554A patent/EP2157116A4/en not_active Withdrawn
- 2008-06-06 JP JP2009517933A patent/JPWO2008150033A1/ja active Pending
- 2008-06-06 WO PCT/JP2008/060813 patent/WO2008150033A1/ja active Application Filing
- 2008-06-06 US US12/663,639 patent/US20100256329A1/en not_active Abandoned
- 2008-06-06 CN CN200880019263A patent/CN101715465A/zh active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0597276A1 (de) * | 1992-11-11 | 1994-05-18 | Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. | N,N'-2.2-3.3-Tetramethylethylen-bis(5-NO2-salicyliden-iminato)colbalt(II) und dessen Verwendung als Trägersubstanz für Sauerstoff |
CN1560111A (zh) * | 2004-02-27 | 2005-01-05 | 大连理工大学 | 一种高分子量完全交替结构聚碳酸酯的制备方法 |
Non-Patent Citations (4)
Title |
---|
LU X.-B. AND YI WANG: "Highly Active, Binary Catalyst Systems for the Alternating Copolymerization of CO2 and Epoxides under Mild Conditions", ANGEWANDTE CHEMIE, INTERNATIONAL EDITION, vol. 43, no. 27, 2004, pages 3574 - 3577, XP003024214 * |
NIU Y. ET AL.: "Alternative Copolymerization of Carbon Dioxide and Propylene Oxide Catalyzed by (R,R)-SalencoIII-(2,4-dinitrophenoxy) and Lewis-Basic Cocatalyst", JOURNAL OF POLYMER SCIENCE, PART A: POLYMER CHEMISTRY, vol. 45, no. 22, 2007, pages 5050 - 5056, XP003024215 * |
See also references of EP2157116A4 * |
SHI L. ET AL.: "Asymmetric Alternating Copolymerization and Terpolymerization of Epoxides with Carbon Dioxide at Mild Conditions", MACROMOLECULES, vol. 39, no. 17, 2006, pages 5679 - 5685, XP003024216 * |
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Also Published As
Publication number | Publication date |
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US20100256329A1 (en) | 2010-10-07 |
CN101715465A (zh) | 2010-05-26 |
JPWO2008150033A1 (ja) | 2010-08-26 |
EP2157116A4 (en) | 2010-11-03 |
EP2157116A1 (en) | 2010-02-24 |
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