Patent Application
20240368347
The present disclosure relates to a double metal cyanide catalyst which has high catalyst activity and is capable of increasing the ratio of a repeating unit including carbon dioxide in polyalkylene carbonate prepared, a method for preparing same and a method for preparing polyalkylene carbonate using the catalyst.
After industrial revolution, humanity consumes a large amount of fossil fuels to build a modern society but increases the concentration of carbon dioxide in the air by environmental destruction including deforestation. In the way that the increase of the concentration of carbon dioxide becomes a factor of increasing the greenhouse effect, it is important to reduce the concentration in the air of carbon dioxide which has high contribution to global warming, and various researches on the emission regulation and immobilization of carbon dioxide are being conducted.
Recently, a polyalkylene carbonate resin from the polymerization of carbon dioxide and epoxide is in the spotlight as a biodegradable resin. Particularly, a process for preparing a polyalkylene carbonate resin using carbon dioxide may reduce the global warming problems in terms of immobilizing the carbon dioxide in the air and is also actively studied in terms of using as a carbon source.
In order to prepare a polyalkylene carbonate resin, a catalyst is surely required as well as carbon dioxide and epoxide, and as a typical heterogeneous catalyst, a double metal cyanide catalyst composed of a zinc dicarboxylate-based catalyst such as a zinc glutarate catalyst combined with dicarboxylic acid, and a complex of Co, Zn, Al, or the like, is being used.
In the case of the zinc glutarate catalyst, there are advantages of easy synthesis and treatment, but the activity of the catalyst is very low to increase the amount used of the catalyst, and the removal of the catalyst after polymerization reaction is difficult. On the contrary, in the case of the double metal cyanide catalyst, there are problems in that the activity is high, but the ratio of a repeating unit including carbon dioxide in a polyalkylene carbonate resin polymerized is low.
Accordingly, the development of a catalyst showing high catalyst activity and improved immobilizing efficiency of carbon dioxide, simultaneously, and being capable of polymerizing polyalkylene carbonate stably and improving the ratio of a repeating unit including carbon dioxide in polyalkylene carbonate polymerized, is required.
The background description provided herein is for the purpose of generally presenting context of the disclosure. Unless otherwise indicated herein, the materials described in this section are not prior art to the claims in this application and are not admitted to be prior art, or suggestions of the prior art, by inclusion in this section.
The present disclosure is to solve the above-described problems and provides a double metal cyanide catalyst that may improve the activity of a catalyst to stably polymerize polyalkylene carbonate and may improve the ratio of a repeating unit including carbon dioxide in polyalkylene carbonate polymerized, a method for preparing same and a method for preparing polyalkylene carbonate using the catalyst.
In order to solve the above-described tasks, the present disclosure provides a double metal cyanide catalyst, a method for preparing same and a method for preparing polyalkylene carbonate using the catalyst.
R1 and R2 are each independently a single bond or an alkylene group having 1 to 5 carbon atoms, where at least one among R1 and R2 is an alkylene group having 1 to 5 carbon atoms, R3 and R4 are each independently a hydrogen atom or an alkyl group having 1 to 6 carbon atoms, and n is an integer of 0 to 2.
R1 and R2 are each independently a single bond or an alkylene group having 1 to 5 carbon atoms, where at least one among R1 and R2 is an alkylene group having 1 to 5 carbon atoms,
R3 and R4 are each independently a hydrogen atom or an alkyl group having 1 to 6 carbon atoms, and
The present disclosure utilizes a compound represented by Formula 1 as a complexing agent to show higher immobilizing effects of carbon dioxide in contrast to the conventional double metal cyanide catalyst. As a result, the ratio of a repeating unit including carbon dioxide in polyalkylene carbonate polymerized may be markedly improved, and it may be useful to apply to a technical field on reducing carbon dioxide. In addition, the equal level or higher activity may be shown in contrast to the conventional double metal cyanide catalyst, and polyalkylene carbonate may be stably polymerized.
It will be understood that words or terms used in the description and claims of the present disclosure shall not be interpreted as the meaning defined in commonly used dictionaries. It will be understood that the words or terms should be interpreted as having a meaning that is consistent with their meaning in the technical idea of the invention, based on the principle that an inventor may properly define the meaning of the words to best explain the invention.
The inventors of the present disclosure repeated research on a catalyst showing the equal or higher activity in contrast to the conventional double metal cyanide catalyst and improving the ratio of a repeating unit including carbon dioxide in polyalkylene carbonate, and found that high catalyst activity may be shown, and at the same time, the ratio of a repeating unit including carbon dioxide in polyalkylene carbonate prepared by using the catalyst may be improved in the case of using a compound represented by Formula 1 instead of tert-butanol that has been used as the conventional complexing agent, to complete the present disclosure.
Hereinafter, the present disclosure will be explained in detail.
The present disclosure provides a double metal cyanide catalyst having excellent catalyst activity and being capable of preparing polyalkylene carbonate having high immobilizing efficiency of carbon dioxide.
The double metal cyanide catalyst according to an embodiment of the present disclosure comprises a double metal cyanide compound and a complexing agent, wherein the complexing agent is characterized in being a compound represented by Formula 1.
R1 and R2 are each independently a single bond or an alkylene group of 1 to 5 carbon atoms, where at least one among R1 and R2 is an alkylene group of 1 to 5 carbon atoms, R3 and R4 are each independently a hydrogen atom or an alkyl group of 1 to 6 carbon atoms, and n is an integer of 0 to 2.
Particularly, in Formula 1, R1 and R2 may be each independently a single bond or an alkylene group of 1 to 3 carbon atoms, where at least one among R1 and R2 is an alkylene group of 1 to 3 carbon atoms, R3 and R4 may be each independently a hydrogen atom or an alkyl group of 1 to 4 carbon atoms, and n may be an integer of 0 to 2.
In another embodiment, in Formula 1, R1 and R2 may be each independently a single bond or an alkylene group of 1 to 3 carbon atoms, where at least one among R1 and R2 is an alkylene group of 1 to 3 carbon atoms, R3 may be a hydrogen atom, and n may be 0.
In another embodiment, the complexing agent may be a cycloalkyl alcohol of 3 to 12 carbon atoms, particularly, a cycloalkyl alcohol of 4 to 10 carbon atoms or 5 to 7 carbon atoms.
In another embodiment, the compound represented by Formula 1 may be any one or more selected from the group consisting of cyclobutanol, cyclopentanol, cyclohexanol, cycloheptanol, cyclooctanol, 1-methyl cyclopentanol, 2-methyl cyclopentanol, 3-methyl cyclopentanol, 1-ethyl cyclopentanol, 2-ethyl cyclopentanol, 3-ethyl cyclopentanol, 1-propyl cylopentanol, 2-propyl cyclopentanol, 3-propyl cyclopentanol, 1-butyl cyclopentanol, 2-butyl cyclopentanol, 3-butyl cyclopentanol, 1-isopropyl cyclopentanol, 2-isopropyl cyclopentanol, 3-isopropyl cyclopentanol, 1-(propan-2-yl) cyclopentanol, 2,2-dimethyl cyclopentanol, 2,3-dimethyl cyclopentanol, 3,3-dimethyl cyclopentanol, 1,2-dimethyl cyclopentanol, 1,3-dimethyl cyclopentanol, 1-methyl cyclohexanol, 1-ethyl cyclohexanol, 1-propyl cyclohexanol, 1-butyl cylohexanol, 2-methyl-1-cyclohexanol, 2-ethyl-1-cyclohexanol, 3-ethyl-1-cyclohexanol, 4-ethyl-1-cyclohexanol, 2-propy-1-cyclohexanol, 3-propyl-1-cyclohexanol, 4-propyl-1-cyclohexanol, 2-butyl-1-cyclohexanol, 3-butyl-1-cyclohexanol, 4-butyl-1-cyclohexanol, 2-isopropyl-1-cyclohexanol, 3-isopropyl-1-cyclohexanol, 4-isopropyl-1-cyclohexanol, 2-tert-butyl-1-cyclohexanol, 3-tert-butyl-1-cyclohexanol, 4-tert-butyl-1-cyclohexanol, 2,3-dimethyl-1-cyclohexanol, 2,4-dimethyl-1-cyclohexanol, 3,4-dimethyl-1-cyclohexanol, 1-methyl cycloheptanol, 2-methyl cycloheptanol, 3-mehtyl cycloheptanol and 4-methy cycloheptanol.
In another embodiment, the compound represented by Formula 1 may be any one or more selected from the group consisting of cyclobutanol, cyclopentanol, cyclohexanol, cycloheptanol and cyclooctanol.
Generally, a double metal cyanide catalyst is prepared using a complexing agent, and in this case, the complexing agent is required to react with a metal cyanide complex easily, and the complexing agent is mostly an organic compound including a heteroatom and easily dissolved in water. Examples of such a complexing agent include alcohols, aldehydes, ketones, ethers, esters, amides, urea, nitriles, sulfates, or the like. Among them, ethanol, isopropanol, n-butanol, iso-butanol, sec-butanol, tert-butanol, or the like are alcohols easily dissolved in water and are widely used as complexing agents. Among them, tert-butanol is the most widely used one for preparing a double metal cyanide catalyst.
However, a double metal cyanide catalyst prepared using tert-butanol as a complexing agent generally has an amorphous crystal structure, and in case of polymerizing a polyalkylene carbonate resin under such a catalyst, there are problems in that the ring-opening reaction of an epoxide compound may be excessively carried out, and the ratio of a repeating unit including carbon dioxide in polyalkylene carbonate resin thus polymerized is low.
In another embodiment, in order to increase the ratio of a repeating unit including carbon dioxide in a polymer obtained by the copolymerization of alkylene oxide and carbon dioxide, a double metal cyanide catalyst including an unsaturated alcohol of C2 to C20, that may have a cycloalkyl group as a complexing ligand, has been developed and used as the copolymerization catalyst, but the improvement of the ratio of the repeating unit including carbon dioxide in the polymer thus prepared was insignificant. In another embodiment, a double metal cyanide catalyst including a cyclic polyol as a complexing agent in the copolymerization has been used, but in this case, due to the high melting point of the cyclic polyol, the double metal cyanide catalyst has a solid state at room temperature and could not be used as a sole complexing agent. Accordingly, there are problems of essentially requiring another complexing agent such as tert-butanediol, and there are problems in that the ratio of the repeating unit including carbon dioxide in the polymer thus prepared is still not high.
However, the double metal cyanide catalyst of the present disclosure is prepared by using a cycloalkane-type alcohol having a bulky structure as the complexing agent, and the crystal structure of the catalyst may be diverse including cubic, amorphous and monoclinic, and accordingly, effects of suitably controlling the reaction rate of an epoxide compound and carbon dioxide could be shown.
Particularly, the double metal cyanide compound according to an embodiment of the present disclosure may be derived from a metal cyanide complex and a metal salt.
The metal cyanide complex may show water-soluble properties. Particularly, the metal cyanide complex may be represented by Formula 2.
YaM′(CN)b(A)c [Formula 2]
In Formula 2, M′ may be one or more selected from the group consisting of Fe(II), Fe(III), Co(II), Co(III), Cr(II), Cr(III), Mn(II), Mn(III), Ir(III), Ni(II), Rh(III), Ru(II), V(V) and V(IV), preferably, one or more selected from the group consisting of Co(II), Co(III), Fe(II), Fe(III), Cr(III), Ir(III) and Ni(II). Y may be an alkali metal ion or an alkaline earth metal ion, A may be an anion selected from halide, hydroxide, sulfate, carbonate, cyanide, oxalate, thiocyanate, isocyanate, isothiocyanate, carboxylate and nitrate. a and b are integers of 1 or more, and the sum of the charges of a, b and c may make balance with the charge of M′.
For example, the metal cyanide complex represented by Formula 2 may be potassium hexacyanocobaltate(III), potassium hexacyanoferrate(II), potassium hexacyanoferrate(III), calcium hexacyanoferrate(III) or lithium hexacyanoiridate(III), preferably, potassium hexacyanocobaltate(III). The metal salt may show water-soluble properties.
Particularly, the metal salt may be represented by Formula 3.
M(X)n [Formula 3]
In Formula 3, M is a transition metal, preferably, one or more selected from the group consisting of Zn(II), Fe(II), Ni(II), Mn(II), Co(II), Sn(II), Pb(II), Fe(III), Mo(IV), Mo(VI), Al(III), V(V), V(IV), Sr(II), W(IV), W(VI), Cu(II) and Cr(III), more preferably, one or more selected from the group consisting of Zn(II), Fe(II), Co(II) and Ni(II). X is an anion selected from halide, hydroxide, sulfate, carbonate, cyanide, oxalate, thiocyanate, isocyanate, isothiocyanate, carboxylate and nitrate. The value of N satisfies the valence state of M. For example, the metal salt represented by Formula 2 may be zinc(II) chloride, zinc(III) chloride, zinc bromide, zinc iodide, zinc acetate, zinc acetylacetonate, zinc benzoate, zinc nitrate, iron(II) sulfate, iron(II) bromide, cobalt(II) chloride, cobalt(II) thiocyanate, nickel(II) formate, nickel(II) nitrate and mixtures thereof, preferably, zinc(II) chloride, zinc(III) chloride, zinc bromide or zinc iodide.
The double metal cyanide catalyst according to the present disclosure may be represented by Formula 4.
M2 [M1(CN)p]q·dM2(X)r·eL·fH2O [Formula 4]
In Formula 4, M1 and M2 are each independently a transition metal, X is an anion, and L is cyclobutanol, cyclopentanol, cyclohexanol, cycloheptanol, or cyclooctanol. d, e, f, p, q and r are positive numbers.
More particularly, the double metal cyanide catalyst according to the present disclosure may be represented by Formula 5.
Zn3[Co(CN)6]2·gZnCl2·hL·iH2O [Formula 5]
In Formula 5, L is cyclobutanol, cyclopentanol, cyclohexanol, cycloheptanol, or cyclooctanol, and g, h and i are positive numbers.
The double metal cyanide catalyst of the present disclosure may further include an auxiliary complexing agent, and the auxiliary complexing agent may be a compound having a hydroxyl group, an amine group, an ester group, or an ether group at a terminal.
The auxiliary complexing agent may play the role of improving the activity of the double metal cyanide catalyst even further. The auxiliary complexing agent may be a compound prepared by the ring-opening polymerization of a cyclic ether compound, an epoxy polymer or an oxetane polymer, for example, one or more selected from the group consisting of polyether, polyester, polycarbonate, polyalkylene glycol, polyalkylene glycol sorbitan ester, polyalkylene glycol glycidyl ether, polyacrylamide, poly (acrylamide-co-acrylic acid), polyacrylic acid, poly (acrylic acid-co-maleic acid), polyacrylonitrile, polyalkyl acrylate, polyalkyl methacrylate, polyvinyl methyl ether, polyvinyl ethyl ether, polyvinyl acetate, polyvinyl alcohol, poly-N-vinylpyrrolidone, poly (N-vinylpyrrolidone-co-acrylic acid), polyvinyl methyl ketone, poly (4-vinylphenol), poly (acrylic acid-co-styrene), an oxazoline polymer, polyalkyleneimine, maleic acid, a maleic anhydride copolymer, hydroxyethyl cellulose, polyacetal, glycidyl ether, glycoside, carboxylic ester of polyhydric alcohols, gallic acid, ester and amide.
The present disclosure provides a method for preparing the double metal cyanide catalyst.
The method for preparing the double metal cyanide catalyst according to an embodiment of the present disclosure is characterized in including: (a) a step of reacting a metal salt aqueous solution comprising a complexing agent and a metal cyanide complex aqueous solution; (b) a step of separating a precipitate from a suspension obtained in step (a); (c) a step of washing the precipitate with the complexing agent; and (d) a step of drying the precipitate obtained in step (C) at a temperature of 20° C. to 180° C., wherein the complexing agent is a compound represented by Formula 1.
Here, the complexing agent, the metal salt, and the metal cyanide complex are the same as described above.
Hereinafter, each step will be explained in particular.
Step (a) is a step of preparing a suspension containing a metal salt, a metal cyanide complex and a double metal cyanide compound, and may be performed by reacting a metal salt aqueous solution containing a complexing agent and a metal cyanide complex aqueous solution. Particularly, step (a) may be performed by adding a metal cyanide complex aqueous solution to a mixture of a complexing agent and a metal salt aqueous solution, and then, reacting.
In addition, the reaction in step (a) may be carried out by further using an auxiliary complexing agent, and in this case, a metal salt aqueous solution including a complexing agent and a metal cyanide complex aqueous solution may be injected together with the auxiliary complexing agent, or a metal cyanide complex aqueous solution may be injected to a metal salt aqueous solution including a complexing agent and then, the complexing agent may be injected.
Step (b) is a step of obtaining the double metal cyanide compound of a solid from the suspension prepared in step (a), and a double metal cyanide compound of a solid could be obtained by separating a precipitate by centrifuging or filtering the suspension obtained in step (a).
Step (c) is a step of washing the precipitate obtained in step (b), and the precipitate may be washed with an aqueous solution containing a complexing agent to remove secondary products (by-products) attached to the precipitate. The washing process of step (c) may be performed once, but may preferably be performed three times or more to increase the removing efficiency of the secondary products attached to the precipitate.
Step (d) is a step of preparing a double metal cyanide catalyst and may be performed by drying the precipitate washed in step (c) at a temperature of 20° C. to 180° C. More particularly, in step (d), a double metal cyanide catalyst may be obtained by drying in a vacuum oven of a temperature of 40° C. to 160° C. under pressure conditions of 0.1 mbar to 1013 mbar.
The present disclosure provides a method for preparing polyalkylene carbonate, including a step of polymerizing an epoxide compound with carbon dioxide in the presence of the above-described double metal cyanide catalyst.
The polymerization method is not specifically limited, but may preferably be performed by solution polymerization. By the solution polymerization, the heat of reaction may be suitably controlled, and the weight average molecular weight or viscosity of polyalkylene carbonate to be obtained may be easily controlled. More particularly, by the solution polymerization, polymerization reaction may be performed at a temperature of 50° C. to 120° C., preferably, at a temperature of 60° C. to 120° C., in conditions of 15 bar to 50 bar for 1 hour to 40 hours.
The epoxide compound may use one or more compounds selected from the group consisting of alkylene oxide of 2 to 20 carbon atoms unsubstituted or substituted with halogen or an alkyl group of 1 to 5 carbon atoms; cycloalkylene oxide of 4 to 20 carbon atoms unsubstituted or substituted with halogen or an alkyl group of 1 to 5 carbon atoms; and styrene oxide of 8 to 20 carbon atoms unsubstituted or substituted with halogen or an alkyl group of 1 to 5 carbon atoms, for example, one or more compounds selected from the group consisting of ethylene oxide, propylene oxide, butene oxide, pentene oxide, hexene oxide, octene oxide, decene oxide, dodecane oxide, tetradecane oxide, hexadecane oxide, octadecene oxide, butadiene monoxide, 1,2-epoxy-7-octene, epifluorohydrin, epichlorohydrin, epibromohydrin, isopropyl glycidyl ether, butyl glycidyl ether, t-butyl glycidyl ether, 2-ethylhexyl glycidyl ether, allyl glycidyl ether, cyclopentene oxide, cyclohexene oxide, cyclooctene oxide, cyclododecene oxide, alpha-pinene oxide, 2,3-epoxynorbornene, limonene oxide, dieldrin, 2,3-epoxypropylbenzene, styrene oxide, phenylpropylene oxide, stilbene oxide, chlorostilbene oxide, dichlorostilbene oxide, 1,2-epoxy-3-phenoxypropane, benzyloxymethyl oxirane, glycidyl-methylphenyl ether, chlorophenyl-2,3-epoxypropyl ether, epoxypropyl methoxyphenyl ether, biphenyl glycidyl ether and glycidyl naphthyl ether.
As the solvent, one or more selected from the group consisting of methylene chloride, ethylene dichloride, trichloroethane, tetrachloroethane, chloroform, acetonitrile, propionitrile, dimethylformamide, N-methyl-2-pyrrolidone, dimethylsulfoxide, nitromethane, 1,4-dioxane, hexane, toluene, tetrahydrofuran, methyl ethyl ketone, methyl amine ketone, methyl isobutyl ketone, acetone, cyclohexanone, trichloroethylene, methyl acetate, vinyl acetate, ethyl acetate, propyl acetate, butyrolactone, caprolactone, nitropropane, benzene, styrene, xylene, and methyl propasol, may be used, and preferably, polymerization reaction may be more effectively carried out by using methylene chloride as the solvent.
The solvent and the epoxide compound may be used in a weight ratio of 1:0.1 to 1:100, preferably, a weight ratio of 1:1 to 1:10. Within this range, the solvent may suitably act as a reaction medium, and accordingly, the productivity of polyalkylene carbonate may be improved, and effects of minimizing by-products produced during a preparation process may be achieved.
In addition, the double metal cyanide catalyst and the epoxide compound may be used in a weight ratio of 1:100 to 1:8000, preferably, 1:300 to 1:6000, more preferably, 1:1000 to 1:4000. Within this range, high catalyst activity may be shown while minimizing by-products, and effects of minimizing the back-biting phenomenon of polyalkylene carbonate prepared by heating may be achieved.
Hereinafter, the present disclosure will be explained in particular through particular embodiments. However, the embodiments below are only for illustrating the present disclosure, and the scope of the present disclosure is not limited thereby.
In a first beaker with a volume of 500 ml, 11.45 g of zinc chloride, 30 ml of distilled water and 39 g of cyclohexanol were mixed to prepare a first mixture solution. In a second beaker with a volume of 250 ml, 4 g of potassium hexacyanocobaltate was dissolved in 100 ml of distilled water to prepare a second mixture solution. By using a mechanical stirrer, the second mixture solution was added dropwisely to the first mixture solution at 25° C. for 1 hour. Then, a mixture product was separated by using a high-speed centrifuge, and a precipitate separated was washed twice using a mixture of 70 ml of distilled water and 54 g of cyclohexanol. Then, additional washing was performed using 109 g of cyclohexanol, and the precipitate thus washed was dried in a vacuum oven of 80° C. for 12 hours to finally obtained 5.9 g of a double metal cyanide catalyst.
The same method as in Example 1 was performed except for using cycloheptanol instead of cyclohexanol as a complexing agent in Example 1 to finally obtain 5.3 g of a double metal cyanide catalyst.
The same method as in Example 1 was performed except for using cyclopentanol instead of cyclohexanol as a complexing agent in Example 1 to finally obtain 5.7 g of a double metal cyanide catalyst.
In a first beaker with a volume of 500 ml, 11.45 g of zinc chloride, 30 ml of distilled water and 39 g of cyclohexanol were mixed to prepare a first mixture solution. In a second beaker with a volume of 250 ml, 4 g of potassium hexacyanocobaltate was dissolved in 100 ml of distilled water to prepare a second mixture solution. In a third beaker with a volume of 100 ml, 5 g of polypropylene glycol (Mw=3,000) and 23 g of cyclohexanol were dissolved in 2 ml of distilled water to prepare a third mixture solution. By using a mechanical stirrer, the second mixture solution was added dropwisely to the first mixture solution at 25° C. for 1 hour, and the third mixture solution was injected at one time, followed by reacting for 1 hour. Then, a mixture product was separated by using a high-speed centrifuge, and a precipitate separated was washed twice using a mixture of 70 ml of distilled water and 54 g of cyclohexanol. Then, additional washing was performed using 109 g of cyclohexanol, and the precipitate thus washed was dried in a vacuum oven of 80° C. for 12 hours to finally obtained 6.2 g of a double metal cyanide catalyst.
The same method as in Example 4 was performed except for using cycloheptanol instead of cyclohexanol as a complexing agent in Example 4 to finally obtain 6.3 g of a double metal cyanide catalyst.
The same method as in Example 4 was performed except for using cyclopentanol instead of cyclohexanol as a complexing agent in Example 4 to finally obtain 6.0 g of a double metal cyanide catalyst.
The same method as in Example 1 was performed except for using tert-butanol instead of cyclohexanol as a complexing agent in Example 1 to finally obtain 6.1 g of a double metal cyanide catalyst.
The same method as in Example 4 was performed except for using tert-butanol instead of cyclohexanol as a complexing agent in Example 4 to finally obtain 6.5 g of a double metal cyanide catalyst.
The same method as in Example 4 was performed except for using 2-methyl-3-buten-2-ol instead of cyclohexanol as a complexing agent in Example 4 to finally obtain 6.5 g of a double metal cyanide catalyst.
The same method as in Example 4 was performed except for using 1,5-cyclooctanediol instead of cyclohexanol as a complexing agent in Example 4 to finally obtain 6.5 g of a double metal cyanide catalyst.
To a high-pressure reactor, 10 mg of the double metal cyanide catalyst prepared in Example 1, 20 g of propylene oxide and the same amount of a methylene chloride solvent as the propylene oxide were added. Then, carbon dioxide was injected into the reactor and a pressure of 30 bar was applied. Polymerization reaction was carried out at 105° C. for 5 hours, and unreacted carbon dioxide was removed after finishing the reaction. Then, the product was diluted in 200 ml of a methylene chloride solvent, unreacted propylene oxide was removed using a vacuum evaporation method, and drying was performed in a vacuum oven of 40° C. for 12 hours to finally obtain 25.5 g of polypropylene carbonate.
The same method as in Example 7 was performed except for using the double metal cyanide catalyst prepared in Example 4 instead of the double metal cyanide catalyst prepared in Example 1, in Example 7 to finally obtain 23.2 g of polypropylene carbonate.
The same method as in Example 7 was performed except for performing the polymerization reaction at 85° C. instead of 105° C., in Example 7 to finally obtain 32.7 g of polypropylene carbonate.
The same method as in Example 8 was performed except for performing the polymerization reaction at 85° C. instead of 105° C., in Example 8 to finally obtain 30.5 g of polypropylene carbonate.
The same method as in Example 9 was performed except for using the double metal cyanide catalyst prepared in Example 2 instead of the double metal cyanide catalyst prepared in Example 1, in Example 9 to finally obtain 31.3 g of polypropylene carbonate.
The same method as in Example 9 was performed except for using the double metal cyanide catalyst prepared in Example 5 instead of the double metal cyanide catalyst prepared in Example 1, in Example 9 to finally obtain 32.1 g of polypropylene carbonate.
The same method as in Example 9 was performed except for using the double metal cyanide catalyst prepared in Example 3 instead of the double metal cyanide catalyst prepared in Example 1, in Example 9 to finally obtain 30.9 g of polypropylene carbonate.
The same method as in Example 9 was performed except for using the double metal cyanide catalyst prepared in Example 6 instead of the double metal cyanide catalyst prepared in Example 1, in Example 9 to finally obtain 30.7 g of polypropylene carbonate.
The same method as in Example 7 was performed except for using the double metal cyanide catalyst prepared in Comparative Example 1 instead of the double metal cyanide catalyst prepared in Example 1, in Example 7 to finally obtain 24.7 g of polypropylene carbonate.
The same method as in Example 7 was performed except for using the double metal cyanide catalyst prepared in Comparative Example 2 instead of the double metal cyanide catalyst prepared in Example 1, in Example 7 to finally obtain 23.2 g of polypropylene carbonate.
The same method as in Comparative Example 5 was performed except for performing the polymerization reaction at 85° C. instead of 105° C., in Comparative Example 5 to finally obtain 26.0 g of polypropylene carbonate.
The same method as in Comparative Example 6 was performed except for performing the polymerization reaction at 85° C. instead of 105° C., in Comparative Example 6 to finally obtain 23.6 g of polypropylene carbonate.
The same method as in Comparative Example 8 was performed except for using the double metal cyanide catalyst prepared in Comparative Example 3 instead of the double metal cyanide catalyst prepared in Comparative Example 2, in Comparative Example 8 to finally obtain 24.1 g of polypropylene carbonate.
The same method as in Comparative Example 9 was performed except for using the double metal cyanide catalyst prepared in Comparative Example 4 instead of the double metal cyanide catalyst prepared in Comparative Example 3, in Comparative Example 9. However, catalyst activity was not shown, and polypropylene carbonate was not obtained.
Catalyst activity for Examples 7 to 14 and Comparative
Examples 5 to 10 was measured and shown in Table 1 below. In addition, the mole % of each carbonate unit and the weight average molecular weight of each polypropylene carbonate obtained in Examples 7 to 14 and Comparative Examples 5 to 10 were measured and shown in Table 1 below.
Catalyst activity (g-polymer/g-catalyst)=weight of polypropylene carbonate polymerized (g)/amount used of catalyst (g) [Equation 1]
Mole % of carbonate unit=[(area of carbonate peak)/(area of carbonate peak+area of ether peak)]×100 [Equation 2]
1)PPG: polypropylene glycol
As shown in Table 1, in the cases of Examples 7 to 14, using catalysts including the cycloalkane alcohol represented by Formula 1 of the present disclosure as a complexing agent, showed the equal or better catalyst activity in contrast to Comparative Examples 5 to 10, and it could be confirmed that the ratio of a repeating unit including carbon dioxide in polyalkylene carbonate polymerized was markedly increased.
Particularly, in the cases of Examples 7 to 14, using the catalysts of Example 1 to Example 6, prepared using cyclopentanol, cyclohexanol, or cycloheptanol as a complexing agent, showed better catalyst activity in contrast to Comparative Examples 5 to 8, using the catalysts of Comparative Examples 1 and 2, prepared using tert-butanol as a complexing agent and Comparative Example using the catalyst of Comparative Example 3 prepared using 2-methyl-3-buten-2-ol as a complexing agent, and showed increased results of the molar ratio of a carbonate unit to 1.20 times to 2.85 times.
Through this, the catalyst according to the present disclosure is used for the preparation of polyalkylene carbonate, and it could be confirmed that high catalyst activity is shown, high immobilizing efficiency of carbon dioxide is achieved and effects of markedly increasing the ratio of a repeating unit including carbon dioxide in the polyalkylene carbonate prepared are achieved. In addition, because of the effects, it could be confirmed that the present disclosure could be more suitably used in a technical field of reducing carbon dioxide.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2021-0119702 | Sep 2021 | KR | national |
The present application is a National Phase entry pursuant to 35 U.S.C. § 371 of International Application No. PCT/KR2022/013375, filed on Sep. 6, 2022, and claims the benefit of and priority to Korean Patent Application No. 10-2021-0119702, filed on Sep. 8, 2021, the entire contents of which are hereby incorporated by reference in their entirety.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/KR2022/013375 | 9/6/2022 | WO |
