WO2025229959A1 - Method for producing polycarbonate - Google Patents
Method for producing polycarbonateInfo
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- WO2025229959A1 WO2025229959A1 PCT/JP2025/016262 JP2025016262W WO2025229959A1 WO 2025229959 A1 WO2025229959 A1 WO 2025229959A1 JP 2025016262 W JP2025016262 W JP 2025016262W WO 2025229959 A1 WO2025229959 A1 WO 2025229959A1
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- polycarbonate
- producing
- epoxy compound
- inorganic metal
- oxide
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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
- This disclosure relates to a method for producing polycarbonate.
- Polycarbonates are used in many fields, such as ceramic binders, polyurethane raw materials, adhesives, and biocompatible materials. Polycarbonate is produced, for example, by alternating copolymerization of carbon dioxide and an epoxy compound. Various catalysts for use in the production of polycarbonate have been investigated.
- Patent Document 1 describes a catalyst for producing polycarbonate from epoxide and carbon dioxide, which is characterized by comprising a mixture of one or more scandium compounds (first catalyst) selected from scandium alkoxides, halides, and triflate compounds, and one or more metal compounds (second catalyst) selected from metal alkoxides, metal halides, and metal halide alkoxides of titanium, zirconium, hafnium, and cerium.
- first catalyst selected from scandium alkoxides, halides, and triflate compounds
- second catalyst selected from metal alkoxides, metal halides, and metal halide alkoxides of titanium, zirconium, hafnium, and cerium.
- the objective of one embodiment of the present disclosure is to provide a novel method for producing polycarbonate using an easy-to-handle catalyst.
- the means for solving the above problems include the following means.
- a method for producing polycarbonate comprising reacting carbon dioxide with an epoxy compound in the presence of an inorganic metal salt containing a rare earth element (excluding scandium halides and cerium halides).
- the inorganic metal salt is represented by the following formula (1): M( PO4 )...Formula (1)
- M is La, Ce, Pr, Nd, Sm, Gd, Tb, Dy, Ho, Er, Tm, Yb, or Lu.
- ⁇ 3> ⁇ 4> The method for producing a polycarbonate according to ⁇ 1> or ⁇ 2>, wherein the inorganic metal salt is cerium phosphate or lanthanum phosphate.
- the inorganic metal salt is cerium phosphate or lanthanum phosphate.
- the epoxy compound is an aliphatic epoxy compound.
- ⁇ 5> ⁇ 4> The method for producing a polycarbonate according to any one of ⁇ 1> to ⁇ 4>, wherein no solvent is used.
- One embodiment of the present disclosure provides a novel method for producing polycarbonate using an easy-to-handle catalyst.
- the upper or lower limit of one numerical range may be replaced with the upper or lower limit of another numerical range.
- the upper or lower limit of a numerical range may be replaced with a value shown in the examples.
- the word "to" is used to mean that the numerical values before and after it are included as the lower limit and upper limit.
- Each component may contain multiple types of the corresponding substance.
- the amount refers to the total amount of those multiple substances present in the composition, unless otherwise specified.
- the method for producing a polycarbonate according to the present disclosure includes reacting carbon dioxide with an epoxy compound in the presence of an inorganic metal salt containing a rare earth element (excluding scandium halides and cerium halides), to produce a polycarbonate.
- an inorganic metal salt containing a rare earth element excluding scandium halides and cerium halides
- metal complexes have been used as catalysts in the production of polycarbonate.
- the synthesis of metal complexes is extremely complicated.
- metal complexes are generally unstable in environments where oxygen, water, etc. are present, making them difficult to handle in air.
- the polycarbonate production method disclosed herein is a novel method for producing polycarbonate using an easy-to-handle catalyst.
- the inorganic metal salt preferably functions as a catalyst in the production method of polycarbonate.
- the inorganic metal salts may be used alone or in combination of two or more. In the method for producing a polycarbonate according to the present disclosure, it is preferable to use only one type of inorganic metal salt.
- Inorganic metal salts include rare earth elements. However, scandium halides and cerium halides are excluded from inorganic metal salts.
- rare earth elements include scandium (Sc), yttrium (Y), lanthanum (La), cerium (Ce), praseodymium (Pr), neodymium (Nd), promethium (Pm), samarium (Sm), europium (Eu), gadolinium (Gd), terbium (Tb), dysprosium (Dy), holmium (Ho), erbium (Er), thulium (Tm), ytterbium (Yb), and lutetium (Lu).
- the rare earth element is preferably La, Ce, Pr, Nd, Sm, Gd, Tb, Dy, Ho, Er, Tm, Yb, or Lu, and more preferably La, Ce, Nd, Sm, Gd, or Dy.
- Sals that make up inorganic metal salts include oxoacid salts such as phosphates, nitrates, nitrites, sulfates, sulfites, carbonates, bicarbonates, and silicates; halides such as chlorides, bromides, iodides, and fluorides; cyanides, thiocyanates, borates, chromates, manganates, and permanganates.
- the salt that constitutes the inorganic metal salt is preferably an oxoacid salt, and more preferably a phosphate salt.
- the inorganic metal salt is preferably represented by the following formula (1).
- M is La, Ce, Pr, Nd, Sm, Gd, Tb, Dy, Ho, Er, Tm, Yb, or Lu.
- M is preferably Ce, Nd, Sm, Gd, or Dy, and more preferably Ce.
- M is preferably La. That is, the inorganic metal salt is more preferably cerium phosphate or lanthanum phosphate. It should be noted that M may be Sc, Y, La, Ce, Pr, or Nd.
- the inorganic metal salt may have a crystalline structure or may be amorphous. If it has a crystalline structure, it is preferably a hexagonal structure.
- the crystal structure of the inorganic metal salt can be analyzed by X-ray diffraction.
- the amount of inorganic metal salt used is preferably 0.001 to 0.1 moles per mole of epoxy compound.
- epoxy compound used in the method for producing polycarbonate may be one kind or two or more kinds.
- the epoxy compound may be an aliphatic epoxy compound or an aromatic epoxy compound.
- the epoxy compound be an aliphatic epoxy compound.
- Examples of aliphatic epoxy compounds include ethylene oxide, propylene oxide, 1-butene oxide, 2-butene oxide, isobutylene oxide, 2,3-epoxy-2-methylbutane, 1-pentene oxide, 2-pentene oxide, 1-hexene oxide, 1-octene oxide, 1-decene oxide, 1-dodecene oxide, 3,3-dimethyl-1,2-epoxybutane, cyclopentene oxide, cyclohexene oxide, norbornene oxide, and adamantyl oxide.
- aromatic epoxy compounds include glycidyl compounds containing an aromatic ring such as a bisphenol skeleton, a fluorene skeleton, a biphenyl skeleton, a benzene ring, a naphthalene ring, an anthracene ring, etc.
- aromatic epoxy compounds include trans-styribene oxide, styrene oxide, 2,3-epoxypropylbenzene, and benzyl glycidyl ether.
- propylene oxide is preferred as the epoxy compound.
- a polymerization initiator In the method for producing a polycarbonate according to the present disclosure, a polymerization initiator may be used. Use of a polymerization initiator improves the yield. Examples of the polymerization initiator include methanol, water, and benzyl alcohol. The amount of the polymerization initiator used is preferably 0.001 to 0.01 moles per mole of the epoxy compound.
- reaction conditions In the method for producing a polycarbonate according to the present disclosure, the pressure of the carbon dioxide is preferably 1 MPa to 5 MPa.
- the reaction temperature is preferably 100 to 200°C.
- the reaction time is not particularly limited and is, for example, 2 to 24 hours.
- the reaction can proceed without using a solvent, which is industrially advantageous since no solvent is required.
- the solvent means a solvent used in an amount of 1 mol or more per mol of the epoxy compound, and is distinguished from the above-mentioned polymerization initiator.
- the number average molecular weight of the polycarbonate obtained by the method for producing a polycarbonate according to the present disclosure is preferably 1,000 to 30,000, and more preferably 1,000 to 10,000.
- number average molecular weight is measured using GPC (gel permeation chromatography).
- GPC gel permeation chromatography
- a high-performance liquid chromatograph product name "HLC8420GPC", manufactured by Tosoh Corporation
- a differential refractive index detector and a wavelength-tunable UV-visible detector is used, and measurements are performed at 40°C and a flow rate of 0.7 mL/min using tetrahydrofuran (THF) as an eluent and a calibration curve prepared using standard polystyrene (TSK standard polystyrene, Tosoh Corporation).
- THF tetrahydrofuran
- Example 1 The catalyst used was CePO 4 (manufactured by Thermo Fisher Scientific), which had a hexagonal crystal structure. An autoclave equipped with a magnetic stirrer and purged with nitrogen was charged with 0.4 mmol (100 mg) of CePO 4 , followed by 200 mmol (14 mL) of propylene oxide and 0.25 ⁇ mol (10 ⁇ L) of methanol as a polymerization initiator. Carbon dioxide was injected under pressure, and the total pressure was adjusted to 50 atmospheres (equivalent to 300 mmol of carbon dioxide). After reacting at 130°C for 24 hours, the reaction mixture was cooled to 0°C, and cold methylene chloride was added to dissolve the reaction mixture completely. A sample of this reaction mixture was analyzed by 1 H-NMR and 13 C-NMR.
- the number average molecular weight was measured using a high-performance liquid chromatograph (product name "HLC8420GPC", manufactured by Tosoh Corporation) equipped with a differential refractive index detector and a tunable UV-visible detector, at 40°C and a flow rate of 0.7 mL/min, using tetrahydrofuran (THF) as the eluent and a calibration curve prepared with standard polystyrene (TSK standard polystyrene, Tosoh Corporation).
- HLC8420GPC high-performance liquid chromatograph
- THF tetrahydrofuran
- the catalyst used was LaPO4 (manufactured by Aldrich Co.), which had a hexagonal crystal structure.
- the reaction was carried out in the same manner as in Example 1, except that LaPO4 was used instead of CePO4 .
- Example 5 The reaction was carried out in the same manner as in Example 1, except that the epoxy compounds shown in Table 2 were used instead of propylene oxide and the reaction temperature and reaction time were changed to those shown in Table 2.
- polycarbonate can be produced by reacting carbon dioxide with an epoxy compound in the presence of an inorganic metal salt containing a rare earth element. From Table 2, it can be seen that the method for producing polycarbonate according to the present disclosure can be applied to various epoxy compounds. In particular, although the epoxy compound used in Example 5 generally has low reactivity, it was found that polycarbonate can be obtained in good yield by the method for producing polycarbonate according to the present disclosure.
- Example 11 to 22 Catalyst synthesis -
- a solution of (NH 4 )HPO 4 (15 mmol) dissolved in 50 mL of water was added to a solution of a metal nitrate (6 mmol) corresponding to the target catalyst in 50 mL of water while stirring.
- Aqueous ammonia was added to adjust the pH to 9.5, and the mixture was left to stand overnight.
- the precipitate was washed with water and ethanol and centrifuged. This procedure was repeated three times.
- the mixture was dried overnight at 80°C to obtain the inorganic metal salts shown in Table 3.
- the inorganic metal salts had the crystalline structures shown in Table 3. Note that the crystalline structure could not be analyzed in Example 12. Furthermore, when no crystalline structure was present, the material was classified as "amorphous.”
- Table 3 shows that polycarbonate can be produced in high yields by reacting carbon dioxide with an epoxy compound in the presence of an inorganic metal salt containing a rare earth element.
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Abstract
Description
本開示は、ポリカーボネートの製造方法に関する。 This disclosure relates to a method for producing polycarbonate.
ポリカーボネートは、セラミックバインダー、ポリウレタン原料、接着剤、生体適合性材料などの多くの分野で用いられている。
ポリカーボネートは、例えば、二酸化炭素とエポキシ化合物との交互共重合によって製造される。ポリカーボネートの製造に用いられる触媒は、種々検討されている。
Polycarbonates are used in many fields, such as ceramic binders, polyurethane raw materials, adhesives, and biocompatible materials.
Polycarbonate is produced, for example, by alternating copolymerization of carbon dioxide and an epoxy compound. Various catalysts for use in the production of polycarbonate have been investigated.
例えば、特許文献1には、エポキシドと二酸化炭素からポリカーボネートを製造する際に用いられる触媒であって、スカンジウムのアルコキシド、ハロゲン化物及びトリフラート化合物から選ばれる一種又は二種以上のスカンジウム化合物(第1の触媒)と、チタン、ジルコニウム、ハフニウム及びセリウムの金属アルコキシド、金属ハロゲン化物、及び金属ハロゲン化物アルコキシドから選ばれる一種又は二種以上の金属化合物(第2の触媒)が混合されてなることを特徴とするポリカーボネート製造用触媒が記載されている。 For example, Patent Document 1 describes a catalyst for producing polycarbonate from epoxide and carbon dioxide, which is characterized by comprising a mixture of one or more scandium compounds (first catalyst) selected from scandium alkoxides, halides, and triflate compounds, and one or more metal compounds (second catalyst) selected from metal alkoxides, metal halides, and metal halide alkoxides of titanium, zirconium, hafnium, and cerium.
本開示の一実施形態における課題は、取り扱い容易な触媒を用いた新規なポリカーボネートの製造方法を提供することである。 The objective of one embodiment of the present disclosure is to provide a novel method for producing polycarbonate using an easy-to-handle catalyst.
上記課題を解決するための手段には、以下の手段が含まれる。
<1>
希土類元素を含む無機金属塩(ただし、スカンジウムのハロゲン化物、及び、セリウムのハロゲン化物を除く)の存在下、二酸化炭素とエポキシ化合物とを反応させて、ポリカーボネートを製造することを含む、ポリカーボネートの製造方法。
<2>
前記無機金属塩は、下記式(1)で表される、<1>に記載のポリカーボネートの製造方法。
M(PO4) …式(1)
式(1)中、
Mは、La、Ce、Pr、Nd、Sm、Gd、Tb、Dy、Ho、Er、Tm、Yb、又はLuである。
<3>
無機金属塩は、リン酸セリウム又はリン酸ランタンである、<1>又は<2>に記載のポリカーボネートの製造方法。<4>
エポキシ化合物は、脂肪族エポキシ化合物である、<1>~<3>のいずれか1つに記載のポリカーボネートの製造方法。
<5>
溶媒を使用しない、<1>~<4>のいずれか1つに記載のポリカーボネートの製造方法。
The means for solving the above problems include the following means.
<1>
A method for producing polycarbonate, comprising reacting carbon dioxide with an epoxy compound in the presence of an inorganic metal salt containing a rare earth element (excluding scandium halides and cerium halides).
<2>
The method for producing a polycarbonate according to <1>, wherein the inorganic metal salt is represented by the following formula (1):
M( PO4 )...Formula (1)
In formula (1),
M is La, Ce, Pr, Nd, Sm, Gd, Tb, Dy, Ho, Er, Tm, Yb, or Lu.
<3>
<4> The method for producing a polycarbonate according to <1> or <2>, wherein the inorganic metal salt is cerium phosphate or lanthanum phosphate.
<3> The method for producing a polycarbonate according to any one of <1> to <3>, wherein the epoxy compound is an aliphatic epoxy compound.
<5>
<4> The method for producing a polycarbonate according to any one of <1> to <4>, wherein no solvent is used.
本開示の一実施形態によれば、取り扱い容易な触媒を用いた新規なポリカーボネートの製造方法が提供される。 One embodiment of the present disclosure provides a novel method for producing polycarbonate using an easy-to-handle catalyst.
以下、本開示の一例である実施形態について説明する。これらの説明および実施例は、実施形態を例示するものであり、発明の範囲を制限するものではない。
本明細書中に段階的に記載されている数値範囲において、一つの数値範囲で記載された上限値又は下限値は、他の段階的な記載の数値範囲の上限値又は下限値に置き換えてもよい。また、本明細書中に記載されている数値範囲において、その数値範囲の上限値又は下限値は、実施例に示されている値に置き換えてもよい。
なお、本願明細書において「~」とはその前後に記載される数値を下限値及び上限値として含む意味で使用される。
Hereinafter, an embodiment of the present disclosure will be described. These descriptions and examples are intended to illustrate the embodiment and are not intended to limit the scope of the invention.
In the present specification, the upper or lower limit of one numerical range may be replaced with the upper or lower limit of another numerical range. In addition, in the present specification, the upper or lower limit of a numerical range may be replaced with a value shown in the examples.
In the present specification, the word "to" is used to mean that the numerical values before and after it are included as the lower limit and upper limit.
各成分は該当する物質を複数種含んでいてもよい。
組成物中の各成分の量について言及する場合、組成物中に各成分に該当する物質が複数種存在する場合には、特に断らない限り、組成物中に存在する当該複数種の物質の合計量を意味する。
Each component may contain multiple types of the corresponding substance.
When referring to the amount of each component in a composition, if there are multiple substances corresponding to each component in the composition, the amount refers to the total amount of those multiple substances present in the composition, unless otherwise specified.
[ポリカーボネートの製造方法]
本開示に係るポリカーボネートの製造方法は、希土類元素を含む無機金属塩(ただし、スカンジウムのハロゲン化物、及び、セリウムのハロゲン化物を除く)の存在下、二酸化炭素とエポキシ化合物とを反応させて、ポリカーボネートを製造することを含む。
[Method for producing polycarbonate]
The method for producing a polycarbonate according to the present disclosure includes reacting carbon dioxide with an epoxy compound in the presence of an inorganic metal salt containing a rare earth element (excluding scandium halides and cerium halides), to produce a polycarbonate.
従来、ポリカーボネートの製造方法においては、金属錯体が触媒として用いられていた。しかし、金属錯体は、合成が非常に煩雑である。また、金属錯体は、一般に、酸素、水等が存在する環境下で不安定なため、空気中での取り扱いが困難である。 Conventionally, metal complexes have been used as catalysts in the production of polycarbonate. However, the synthesis of metal complexes is extremely complicated. Furthermore, metal complexes are generally unstable in environments where oxygen, water, etc. are present, making them difficult to handle in air.
これに対して、本開示に係るポリカーボネートの製造方法は、取り扱い容易な触媒を用いた新規なポリカーボネートの製造方法である。 In contrast, the polycarbonate production method disclosed herein is a novel method for producing polycarbonate using an easy-to-handle catalyst.
(無機金属塩)
無機金属塩は、ポリカーボネートの製造方法において、触媒として機能することが好ましい。
(inorganic metal salts)
The inorganic metal salt preferably functions as a catalyst in the production method of polycarbonate.
無機金属塩は、1種のみを用いてもよく、2種以上を組み合わせて用いてもよい。
本開示に係るポリカーボネートの製造方法では、無機金属塩を1種のみ用いることが好ましい。
The inorganic metal salts may be used alone or in combination of two or more.
In the method for producing a polycarbonate according to the present disclosure, it is preferable to use only one type of inorganic metal salt.
無機金属塩は、希土類元素を含む。ただし、無機金属塩において、スカンジウムのハロゲン化物、及び、セリウムのハロゲン化物を除く。 Inorganic metal salts include rare earth elements. However, scandium halides and cerium halides are excluded from inorganic metal salts.
希土類元素としては、例えば、スカンジウム(Sc)、イットリウム(Y)、ランタン(La)、セリウム(Ce)、プラセオジム(Pr)、ネオジム(Nd)、プロメチウム(Pm)、サマリウム(Sm)、ユウロピウム(Eu)、ガドリニウム(Gd)、テルビウム(Tb)、ジスプロシウム(Dy)、ホルミウム(Ho)、エルビウム(Er)、ツリウム(Tm)、イッテルビウム(Yb)、及びルテチウム(Lu)が挙げられる。 Examples of rare earth elements include scandium (Sc), yttrium (Y), lanthanum (La), cerium (Ce), praseodymium (Pr), neodymium (Nd), promethium (Pm), samarium (Sm), europium (Eu), gadolinium (Gd), terbium (Tb), dysprosium (Dy), holmium (Ho), erbium (Er), thulium (Tm), ytterbium (Yb), and lutetium (Lu).
中でも、希土類元素は、La、Ce、Pr、Nd、Sm、Gd、Tb、Dy、Ho、Er、Tm、Yb、又はLuであることが好ましく、La、Ce、Nd、Sm、Gd、又はDyであることがより好ましい。 Among these, the rare earth element is preferably La, Ce, Pr, Nd, Sm, Gd, Tb, Dy, Ho, Er, Tm, Yb, or Lu, and more preferably La, Ce, Nd, Sm, Gd, or Dy.
無機金属塩を構成する塩としては、リン酸塩、硝酸塩、亜硝酸塩、硫酸塩、亜硫酸塩、炭酸塩、重炭酸塩、ケイ酸塩等のオキソ酸塩;塩化物、臭化物、ヨウ化物、フッ化物等のハロゲン化物;シアン化物、チオシアン酸塩、ホウ酸塩、クロム酸塩、マンガン酸塩、過マンガン酸塩などが挙げられる。 Sals that make up inorganic metal salts include oxoacid salts such as phosphates, nitrates, nitrites, sulfates, sulfites, carbonates, bicarbonates, and silicates; halides such as chlorides, bromides, iodides, and fluorides; cyanides, thiocyanates, borates, chromates, manganates, and permanganates.
無機金属塩を構成する塩は、収率の観点から、オキソ酸塩であることが好ましく、リン酸塩であることがより好ましい。 From the standpoint of yield, the salt that constitutes the inorganic metal salt is preferably an oxoacid salt, and more preferably a phosphate salt.
中でも、無機金属塩は、下記式(1)で表されることが好ましい。
M(PO4) …式(1)
Among these, the inorganic metal salt is preferably represented by the following formula (1).
M( PO4 )...Formula (1)
式(1)中、Mは、La、Ce、Pr、Nd、Sm、Gd、Tb、Dy、Ho、Er、Tm、Yb、又はLuである。
収率の観点から、Mは、Ce、Nd、Sm、Gd、又はDyであることが好ましく、Ceであることがより好ましい。また、実用化の観点から、Mは、Laであることが好ましい。すなわち、無機金属塩は、リン酸セリウム又はリン酸ランタンであることがより好ましい。
なお、Mは、Sc、Y、La、Ce、Pr、又はNdであってもよい。
In formula (1), M is La, Ce, Pr, Nd, Sm, Gd, Tb, Dy, Ho, Er, Tm, Yb, or Lu.
From the viewpoint of yield, M is preferably Ce, Nd, Sm, Gd, or Dy, and more preferably Ce. From the viewpoint of practical application, M is preferably La. That is, the inorganic metal salt is more preferably cerium phosphate or lanthanum phosphate.
It should be noted that M may be Sc, Y, La, Ce, Pr, or Nd.
無機金属塩の結晶構造を有していてもよく、非晶質であってもよい。結晶構造を有する場合には、六方晶であることが好ましい。
無機金属塩が有する結晶構造は、X線回折法によって解析することができる。
The inorganic metal salt may have a crystalline structure or may be amorphous. If it has a crystalline structure, it is preferably a hexagonal structure.
The crystal structure of the inorganic metal salt can be analyzed by X-ray diffraction.
無機金属塩の使用量は、エポキシ化合物1モルに対して、0.001モル~0.1モルであることが好ましい。 The amount of inorganic metal salt used is preferably 0.001 to 0.1 moles per mole of epoxy compound.
(エポキシ化合物)
ポリカーボネートの製造方法に用いられるエポキシ化合物は、1種のみであってもよく、2種以上であってもよい。
(epoxy compound)
The epoxy compound used in the method for producing polycarbonate may be one kind or two or more kinds.
エポキシ化合物は、脂肪族エポキシ化合物であってもよく、芳香族エポキシ化合物であってもよい。 The epoxy compound may be an aliphatic epoxy compound or an aromatic epoxy compound.
エポキシ化合物の反応性の観点から、エポキシ化合物は、脂肪族エポキシ化合物であることが好ましい。 In view of the reactivity of the epoxy compound, it is preferable that the epoxy compound be an aliphatic epoxy compound.
脂肪族エポキシ化合物としては、例えば、エチレンオキシド、プロピレンオキシド、1-ブテンオキシド、2-ブテンオキシド、イソブチレンオキシド、2,3-エポキシ-2-メチルブタン、1-ペンテンオキシド、2-ペンテンオキシド、1-ヘキセンオキシド、1-オクテンオキシド、1-デセンオキシド、1-ドデセンオキシド、3,3-ジメチル-1,2-エポキシブタン、シクロペンテンオキシド、シクロヘキセンオキシド、ノルボルネンオキシド、アダマンチルオキシド、3,4-エポキシテトラヒドロフラン、3,4-エポキシシクロペンテン、1,4-シクロヘキサジエン-1,2-オキシド、t-ブチルエチレンオキシド、シクロヘキシルエチレンオキシド、2-ノルボルニルエチレンオキシド、1-アダマンチルエチレンオキシド、リモネンオキシド、インデンオキシド、4,4-ジメチルー3,5,8-トリオキサビシクロ[5.1.0]オクタン、1,4-ジヒドロナフタレンオキシド、グリシドール、及びエピクロロヒドリンが挙げられる。
芳香族エポキシ化合物としては、例えば、ビスフェノール骨格、フルオレン骨格、ビフェニル骨格、ベンゼン環、ナフタレン環、アントラセン環等の芳香環を含むグリシジル化合物が挙げられる。芳香族エポキシ化合物としては、例えば、トランス-スチリベンオキシド、スチレンオキシド、2,3-エポキシプロピルベンゼン、及びベンジルグリシジルエーテルが挙げられる。
Examples of aliphatic epoxy compounds include ethylene oxide, propylene oxide, 1-butene oxide, 2-butene oxide, isobutylene oxide, 2,3-epoxy-2-methylbutane, 1-pentene oxide, 2-pentene oxide, 1-hexene oxide, 1-octene oxide, 1-decene oxide, 1-dodecene oxide, 3,3-dimethyl-1,2-epoxybutane, cyclopentene oxide, cyclohexene oxide, norbornene oxide, and adamantyl oxide. , 3,4-epoxytetrahydrofuran, 3,4-epoxycyclopentene, 1,4-cyclohexadiene-1,2-oxide, t-butylethylene oxide, cyclohexylethylene oxide, 2-norbornylethylene oxide, 1-adamantylethylene oxide, limonene oxide, indene oxide, 4,4-dimethyl-3,5,8-trioxabicyclo[5.1.0]octane, 1,4-dihydronaphthalene oxide, glycidol, and epichlorohydrin.
Examples of aromatic epoxy compounds include glycidyl compounds containing an aromatic ring such as a bisphenol skeleton, a fluorene skeleton, a biphenyl skeleton, a benzene ring, a naphthalene ring, an anthracene ring, etc. Examples of aromatic epoxy compounds include trans-styribene oxide, styrene oxide, 2,3-epoxypropylbenzene, and benzyl glycidyl ether.
中でも、エポキシ化合物は、プロピレンオキシドであることが好ましい。 Among these, propylene oxide is preferred as the epoxy compound.
(重合開始剤)
本開示に係るポリカーボネートの製造方法では、重合開始剤を用いてもよい。重合開始剤を用いることにより、収率が向上する。
重合開始剤としては、例えば、メタノール、水、ベンジルアルコールが挙げられる。
重合開始剤の使用量は、エポキシ化合物1モルに対して、0.001モル~0.01モルであることが好ましい。
(Polymerization initiator)
In the method for producing a polycarbonate according to the present disclosure, a polymerization initiator may be used. Use of a polymerization initiator improves the yield.
Examples of the polymerization initiator include methanol, water, and benzyl alcohol.
The amount of the polymerization initiator used is preferably 0.001 to 0.01 moles per mole of the epoxy compound.
(反応条件)
本開示に係るポリカーボネートの製造方法において、二酸化炭素の圧力は、1MPa~5MPaであることが好ましい。
反応温度は、100℃~200℃であることが好ましい。
反応時間は特に限定されず、例えば、2時間~24時間である。
(Reaction conditions)
In the method for producing a polycarbonate according to the present disclosure, the pressure of the carbon dioxide is preferably 1 MPa to 5 MPa.
The reaction temperature is preferably 100 to 200°C.
The reaction time is not particularly limited and is, for example, 2 to 24 hours.
本開示に係るポリカーボネートの製造方法では、溶媒を使用せずに、反応を進行させることができる。溶媒が不要であり、工業的に優れている。
なお、本開示において、溶媒とは、エポキシ化合物1モルに対して1モル以上の量で用いられる溶媒を意味し、上記重合開始剤とは区別される。
In the method for producing polycarbonate according to the present disclosure, the reaction can proceed without using a solvent, which is industrially advantageous since no solvent is required.
In the present disclosure, the solvent means a solvent used in an amount of 1 mol or more per mol of the epoxy compound, and is distinguished from the above-mentioned polymerization initiator.
(ポリカーボネート)
本開示に係るポリカーボネートの製造方法で得られるポリカーボネートの数平均分子量は、1000~30000であることが好ましく、1000~10000であることがより好ましい。
(Polycarbonate)
The number average molecular weight of the polycarbonate obtained by the method for producing a polycarbonate according to the present disclosure is preferably 1,000 to 30,000, and more preferably 1,000 to 10,000.
本開示において、数平均分子量は、GPC(ゲル浸透クロマトグラフィー)を用いて測定される。
具体的には、示差屈折率検出器及び波長可変UV-可視光検出器を備えた高速液体クロマトグラフ(製品名「HLC8420GPC」、東ソー社製)において、溶出剤としてテトラヒドロフラン(THF)を用い、標準ポリスチレン(TSK標準ポリスチレン、東ソー)で作成した校正曲線を用い、40℃、流量0.7mL/分で測定を行う。
In this disclosure, number average molecular weight is measured using GPC (gel permeation chromatography).
Specifically, a high-performance liquid chromatograph (product name "HLC8420GPC", manufactured by Tosoh Corporation) equipped with a differential refractive index detector and a wavelength-tunable UV-visible detector is used, and measurements are performed at 40°C and a flow rate of 0.7 mL/min using tetrahydrofuran (THF) as an eluent and a calibration curve prepared using standard polystyrene (TSK standard polystyrene, Tosoh Corporation).
以下に実施例によりさらに具体的に説明するが、本開示は以下の実施例に限定されるものではない。 The following examples provide a more detailed explanation, but the present disclosure is not limited to these examples.
(実施例1)
触媒として、CePO4(Thermo Fisher Scientific社製)を用いた。CePO4は、六方晶の結晶構造を有していた。
マグネチックスターラーを入れ、内部を窒素パージしたオートクレーブに、CePO40.4mmol(100mg)を加えた後、プロピレンオキシド200mmol(14mL)と、重合開始剤としてメタノール0.25μmol(10μL)を入れた。圧力をかけて二酸化炭素を注入し、全圧が50気圧(二酸化炭素300mmol相当)となるように調節した。130℃で24時間反応を行った後、反応混合物を0℃まで冷却し、冷塩化メチレンを加えて反応混合物をすべて溶解させた。この反応混合物をサンプリングして1H-NMR及び13C-NMRにより分析した。
Example 1
The catalyst used was CePO 4 (manufactured by Thermo Fisher Scientific), which had a hexagonal crystal structure.
An autoclave equipped with a magnetic stirrer and purged with nitrogen was charged with 0.4 mmol (100 mg) of CePO 4 , followed by 200 mmol (14 mL) of propylene oxide and 0.25 μmol (10 μL) of methanol as a polymerization initiator. Carbon dioxide was injected under pressure, and the total pressure was adjusted to 50 atmospheres (equivalent to 300 mmol of carbon dioxide). After reacting at 130°C for 24 hours, the reaction mixture was cooled to 0°C, and cold methylene chloride was added to dissolve the reaction mixture completely. A sample of this reaction mixture was analyzed by 1 H-NMR and 13 C-NMR.
1H-NMR及び13C-NMR測定は、Bruker DPX-400 分光測定装置において、溶媒としてCDCl3、内部標準としてテトラメチルシラン(δ=0.00ppm)を用いて27℃で行った。 1 H-NMR and 13 C-NMR measurements were carried out at 27° C. on a Bruker DPX-400 spectrometer using CDCl 3 as the solvent and tetramethylsilane (δ=0.00 ppm) as the internal standard.
1H-NMRスペクトルにおいて、残存するプロピレンオキシドのメチン水素のシグナル(2.9ppm~3.1ppm)の積分値より、プロピレンオキシドの反応転化率は約73%であった。
環状カーボネートのメチン水素のシグナルは4.8ppm~4.9ppmに検出された。
また、開環したプロピレンオキシドの連続したポリエーテル結合由来のシグナルは3.5ppmに検出された。
1H-NMRスペクトルにより、ポリ(プロピレンカーボネート)、環状カーボネート、及びポリエーテルの生成割合(モル比)を算出した。
表1中、ポリ(プロピレンカーボネート)を「PC」、環状カーボネートを「CC」、ポリエーテルを「PE」と記載した。
In the 1 H-NMR spectrum, the integral value of the signal (2.9 ppm to 3.1 ppm) of the methine hydrogen of the remaining propylene oxide indicated that the reaction conversion of propylene oxide was about 73%.
The signal of methine hydrogen of cyclic carbonate was detected at 4.8 ppm to 4.9 ppm.
Furthermore, a signal derived from the continuous polyether bond of ring-opened propylene oxide was detected at 3.5 ppm.
The molar ratios of poly(propylene carbonate), cyclic carbonate, and polyether produced were calculated from the 1 H-NMR spectrum.
In Table 1, poly(propylene carbonate) is abbreviated as "PC," cyclic carbonate as "CC," and polyether as "PE."
示差屈折率検出器及び波長可変UV-可視光検出器を備えた高速液体クロマトグラフ(製品名「HLC8420GPC」、東ソー社製)において、溶出剤としてテトラヒドロフラン(THF)を用い、標準ポリスチレン(TSK標準ポリスチレン、東ソー)で作成した校正曲線を用い、40℃、流量0.7mL/分で、数平均分子量を測定した。 The number average molecular weight was measured using a high-performance liquid chromatograph (product name "HLC8420GPC", manufactured by Tosoh Corporation) equipped with a differential refractive index detector and a tunable UV-visible detector, at 40°C and a flow rate of 0.7 mL/min, using tetrahydrofuran (THF) as the eluent and a calibration curve prepared with standard polystyrene (TSK standard polystyrene, Tosoh Corporation).
GPCスペクトルより、生成したポリ(プロピレンカーボネート)の数平均分子量は16,000、分子量分布は14.7であった。 GPC spectrum showed that the number average molecular weight of the resulting poly(propylene carbonate) was 16,000 and the molecular weight distribution was 14.7.
触媒として、LaPO4(アルドリッチ社製)を用いた。LaPO4は、六方晶の結晶構造を有していた。
CePO4の代わりに、LaPO4を用いたこと以外は、実施例1と同様の方法で反応を行った。
The catalyst used was LaPO4 (manufactured by Aldrich Co.), which had a hexagonal crystal structure.
The reaction was carried out in the same manner as in Example 1, except that LaPO4 was used instead of CePO4 .
(実施例3~実施例5)
プロピレンオキシドの代わりに表2に示すエポキシ化合物を用い、表2に示す反応温度及び反応時間に変更したこと以外は、実施例1と同様の方法で反応を行った。
(Examples 3 to 5)
The reaction was carried out in the same manner as in Example 1, except that the epoxy compounds shown in Table 2 were used instead of propylene oxide and the reaction temperature and reaction time were changed to those shown in Table 2.
表1より、希土類元素を含む無機金属塩の存在下、二酸化炭素とエポキシ化合物とを反応させることで、ポリカーボネートを製造できることが分かった。
表2より、本開示に係るポリカーボネートの製造方法は、種々のエポキシ化合物に対して適用できることが分かった。
特に、実施例5で用いられているエポキシ化合物は一般に反応性が低いものであるが、本開示に係るポリカーボネートの製造方法によれば、収率良く、ポリカーボネートが得られることが分かった。
From Table 1, it was found that polycarbonate can be produced by reacting carbon dioxide with an epoxy compound in the presence of an inorganic metal salt containing a rare earth element.
From Table 2, it can be seen that the method for producing polycarbonate according to the present disclosure can be applied to various epoxy compounds.
In particular, although the epoxy compound used in Example 5 generally has low reactivity, it was found that polycarbonate can be obtained in good yield by the method for producing polycarbonate according to the present disclosure.
(実施例11~実施例22)
-触媒の合成-
目的とする触媒に対応する金属硝酸塩(6mmol)が水50mLに溶解した溶液に、(NH4)HPO4(15mmol)が水50mLに溶解した溶液を撹拌しながら加えた。アンモニア水を加えてpHを9.5に調整し、一晩静置した。沈殿物を、水及びエタノールで洗浄し、遠心分離を行った。この操作を3回繰り返した。80℃で一晩乾燥させて、表3に記載の無機金属塩を得た。無機金属塩は、表3に記載の結晶構造を有していた。なお、実施例12では、結晶構造を解析できなかった。また、結晶構造を有しない場合には、「非晶質」とした。
(Examples 11 to 22)
- Catalyst synthesis -
A solution of (NH 4 )HPO 4 (15 mmol) dissolved in 50 mL of water was added to a solution of a metal nitrate (6 mmol) corresponding to the target catalyst in 50 mL of water while stirring. Aqueous ammonia was added to adjust the pH to 9.5, and the mixture was left to stand overnight. The precipitate was washed with water and ethanol and centrifuged. This procedure was repeated three times. The mixture was dried overnight at 80°C to obtain the inorganic metal salts shown in Table 3. The inorganic metal salts had the crystalline structures shown in Table 3. Note that the crystalline structure could not be analyzed in Example 12. Furthermore, when no crystalline structure was present, the material was classified as "amorphous."
-プロピレンオキシドの反応-
表3に記載の無機金属塩を用いたこと以外は、実施例1と同様の方法で反応を行った。
- Reaction of propylene oxide -
The reaction was carried out in the same manner as in Example 1, except that the inorganic metal salts shown in Table 3 were used.
表3より、希土類元素を含む無機金属塩の存在下、二酸化炭素とエポキシ化合物とを反応させることで、高収率でポリカーボネートを製造できることが分かった。 Table 3 shows that polycarbonate can be produced in high yields by reacting carbon dioxide with an epoxy compound in the presence of an inorganic metal salt containing a rare earth element.
なお、2024年4月30日に出願された日本国特許出願2024-074004号の開示は、その全体が参照により本明細書に取り込まれる。また、本明細書に記載された全ての文献、特許出願及び技術規格は、個々の文献、特許出願、及び技術規格が参照により取り込まれることが具体的かつ個々に記された場合と同程度に、本明細書中に参照により取り込まれる。 The disclosure of Japanese Patent Application No. 2024-074004, filed on April 30, 2024, is incorporated herein by reference in its entirety. Furthermore, all documents, patent applications, and technical standards described herein are incorporated herein by reference to the same extent as if each individual document, patent application, and technical standard were specifically and individually indicated to be incorporated by reference.
Claims (5)
M(PO4) …式(1)
式(1)中、
Mは、La、Ce、Pr、Nd、Sm、Gd、Tb、Dy、Ho、Er、Tm、Yb、又はLuである。 The method for producing a polycarbonate according to claim 1 , wherein the inorganic metal salt is represented by the following formula (1):
M( PO4 )...Formula (1)
In formula (1),
M is La, Ce, Pr, Nd, Sm, Gd, Tb, Dy, Ho, Er, Tm, Yb, or Lu.
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001011170A (en) * | 1999-06-28 | 2001-01-16 | Kao Corp | Polycarbonate manufacturing method |
| US20020082363A1 (en) * | 2000-12-27 | 2002-06-27 | Xiaojiang Zhao | Catalyst for producing aliphatic polycarbonate and the preparation thereof |
| JP2004263168A (en) * | 2003-03-03 | 2004-09-24 | Changchun Inst Of Applied Chemistry Chinese Academy Of Science | Three-component catalyst used for producing high molecular aliphatic polycarbonate |
| WO2009113716A1 (en) * | 2008-03-11 | 2009-09-17 | 国立大学法人東京大学 | Catalyst for polycarbonate production and method for producing polycarbonate |
| JP2011213982A (en) * | 2010-03-17 | 2011-10-27 | Univ Of Tokyo | Method for producing polycarbonate using metal complex, the metal complex, and catalyst system including the metal complex |
| CN113683765A (en) * | 2021-09-03 | 2021-11-23 | 中国科学院长春应用化学研究所 | Carbon dioxide-epoxide copolymer and preparation method thereof |
-
2025
- 2025-04-28 WO PCT/JP2025/016262 patent/WO2025229959A1/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001011170A (en) * | 1999-06-28 | 2001-01-16 | Kao Corp | Polycarbonate manufacturing method |
| US20020082363A1 (en) * | 2000-12-27 | 2002-06-27 | Xiaojiang Zhao | Catalyst for producing aliphatic polycarbonate and the preparation thereof |
| JP2004263168A (en) * | 2003-03-03 | 2004-09-24 | Changchun Inst Of Applied Chemistry Chinese Academy Of Science | Three-component catalyst used for producing high molecular aliphatic polycarbonate |
| WO2009113716A1 (en) * | 2008-03-11 | 2009-09-17 | 国立大学法人東京大学 | Catalyst for polycarbonate production and method for producing polycarbonate |
| JP2011213982A (en) * | 2010-03-17 | 2011-10-27 | Univ Of Tokyo | Method for producing polycarbonate using metal complex, the metal complex, and catalyst system including the metal complex |
| CN113683765A (en) * | 2021-09-03 | 2021-11-23 | 中国科学院长春应用化学研究所 | Carbon dioxide-epoxide copolymer and preparation method thereof |
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