KR20230146993A - Monomer composition for synthesising recycled plastic, prepration method thereof, and recycled plastic, molded product using the same - Google Patents

Abstract

The present invention relates to a monomer composition for synthesizing recycled plastics, which contains an aromatic diol compound, of which the impurity ratio of the aromatic diol compound derivative according to Formula 1 is 2% or less and the aromatic diol compound derivative according to Formula 2 has a yield of 80% or more, and which is recovered from a polycarbonate-based resin, a manufacturing method thereof, and recycled plastics using the same and molded products. The purpose of the present invention is to provide the monomer composition for synthesizing recycled plastics, capable of securing high-purity aromatic diol compounds recovered through recycling by chemical decomposition of the polycarbonate-based resin.

Description

Monomer composition for synthesizing recycled plastic, manufacturing method thereof, recycled plastic, and molded product using the same {MONOMER COMPOSITION FOR SYNTHESISING RECYCLED PLASTIC, PREPRATION METHOD THEREOF, AND RECYCLED PLASTIC, MOLDED PRODUCT USING THE SAME}

The present invention relates to a monomer composition for synthesizing recycled plastic containing a high-purity, high-yield aromatic diol compound recovered through recycling by chemical decomposition of polycarbonate resin, a manufacturing method thereof, and recycled plastic and molded products using the same. .

Polycarbonate is a thermoplastic polymer that has excellent properties such as excellent transparency, ductility, and relatively low manufacturing costs.

Although polycarbonate is widely used for various purposes, concerns about the environment and health have continuously been raised during waste disposal.

Currently, physical recycling methods are being implemented, but in this case, the problem of deterioration in quality occurs, so research on chemical recycling of polycarbonate is in progress.

Chemical decomposition of polycarbonate refers to the process of obtaining a monomeric aromatic diol compound (e.g., Bisphenol A (BPA)) through decomposition of polycarbonate and then using it for polymerization to obtain high purity polycarbonate. says

Representative examples of such chemical decomposition include thermal decomposition, hydrolysis, and alcohol decomposition. Among these, the most common method is alcohol decomposition, but methanol decomposition has the problem of using methanol, which is harmful to the human body. In the case of ethanol, high temperature and high pressure conditions are required and the yield is not high.

The present invention is to provide a monomer composition for recycling plastic synthesis that can secure high-purity, high-yield aromatic diol compounds recovered through recycling by chemical decomposition of polycarbonate resin.

In addition, the present invention is to provide a method for producing the monomer composition for synthesizing recycled plastic, recycled plastic, and molded articles using the monomer composition for synthesizing recycled plastic.

In order to solve the above problem, in the present specification, an aromatic diol compound is included, the impurity ratio of the aromatic diol compound derivative according to the following formula 1 is 2% or less, and the yield of the aromatic diol compound according to the following formula 2 is 80% or more, Provided is a monomer composition for synthesizing recycled plastic, which is recovered from polycarbonate-based resin.

[Equation 1]

Aromatic diol compound derivative impurity ratio (%) = (aromatic diol compound derivative peak area on HPLC / total peak area on HPLC)

[Equation 2]

Yield (%) = W1/W0

In Equation 2, W0 is the mass of the aromatic diol compound obtained upon 100% decomposition of the polycarbonate-based resin, and W1 is the mass of the aromatic diol compound actually obtained.

Also included in the present specification are the steps of preparing a mixed solution by adding polycarbonate to an organic solvent; Adding a glycol-based compound and an organic base catalyst to the mixed solution and stirring; and obtaining the aromatic diol compound formed in the stirring step. A method for producing the monomer composition for synthesizing recycled plastic of claim 1 is provided, including a step.

The present specification also provides a recycled plastic comprising a reaction product of the monomer composition for synthesizing recycled plastic and a comonomer.

Also provided herein is a molded article containing the recycled plastic.

Hereinafter, the monomer composition for synthesizing recycled plastic according to specific embodiments of the invention, its manufacturing method, and recycled plastic and molded products using the same will be described in more detail.

Unless explicitly stated herein, terminology is intended to refer only to specific embodiments and is not intended to limit the invention.

As used herein, singular forms include plural forms unless phrases clearly indicate the contrary.

As used herein, the meaning of 'comprise' is to specify a specific characteristic, area, integer, step, operation, element and/or component, and to specify another specific property, area, integer, step, operation, element, component and/or group. It does not exclude the existence or addition of .

Additionally, in this specification, terms including ordinal numbers such as 'first' and 'second' are used for the purpose of distinguishing one component from another component and are not limited by the ordinal numbers. For example, within the scope of the present invention, a first component may also be referred to as a second component, and similarly, the second component may be referred to as a first component.

As used herein, the term “substituted or unsubstituted” refers to deuterium; halogen group; Cyano group; nitro group; hydroxyl group; carbonyl group; ester group; imide group; amide group; Primary amino group; carboxyl group; sulfonic acid group; sulfonamide group; Phosphine oxide group; Alkoxy group; Aryloxy group; Alkylthioxy group; Arylthioxy group; Alkyl sulphoxy group; Aryl sulfoxy group; silyl group; boron group; Alkyl group; Cycloalkyl group; alkenyl group; Aryl group; Aralkyl group; Aralkenyl group; Alkylaryl group; Alkoxysilylalkyl group; Arylphosphine group; or substituted or unsubstituted with one or more substituents selected from the group consisting of heterocyclic groups containing one or more of N, O and S atoms, or substituted or unsubstituted with two or more of the above-exemplified substituents linked. . For example, “a substituent group in which two or more substituents are connected” may be a biphenyl group. That is, the biphenyl group may be an aryl group, or it may be interpreted as a substituent in which two phenyl groups are connected.

In the present specification, the alkyl group is a monovalent functional group derived from an alkane and may be straight-chain or branched, and the number of carbon atoms of the straight-chain alkyl group is not particularly limited, but is preferably 1 to 20. Additionally, the branched chain alkyl group has 3 to 20 carbon atoms. Specific examples of alkyl groups include methyl, ethyl, propyl, n-propyl, isopropyl, butyl, n-butyl, isobutyl, tert-butyl, sec-butyl, 1-methyl-butyl, 1-ethyl-butyl, pentyl, n. -pentyl, isopentyl, neopentyl, tert-pentyl, hexyl, n-hexyl, 1-methylpentyl, 2-methylpentyl, 4-methyl-2-pentyl, 3,3-dimethylbutyl, 2-ethylbutyl, heptyl , n-heptyl, 1-methylhexyl, octyl, n-octyl, tert-octyl, 1-methylheptyl, 2-ethylhexyl, 2-propylpentyl, n-nonyl, 2,2-dimethylheptyl, 1-ethyl- Propyl, 1,1-dimethyl-propyl, isohexyl, 2-methylpentyl, 4-methylhexyl, 5-methylhexyl, 2,6-dimethylheptan-4-yl, etc., but are not limited to these. The alkyl group may be substituted or unsubstituted, and when substituted, examples of the substituent are as described above.

In this specification, the alkylene group is a divalent functional group derived from an alkane, and the description of the alkyl group described above can be applied except that it is a divalent functional group. For example, it may be straight-chain or branched, such as methylene group, ethylene group, propylene group, isobutylene group, sec-butylene group, tert-butylene group, pentylene group, hexylene group, etc. The alkylene group may be substituted or unsubstituted, and when substituted, examples of the substituent are as described above.

In this specification, a fused ring refers to a cyclic structure in which adjacent rings share only two atoms each in a polycyclic system composed of two or more carbon rings or heterocycles.

Throughout this specification, “one or more” means, for example, “1, 2, 3, 4 or 5, especially 1, 2, 3 or 4, more especially 1, 2 or 3, even more especially 1 or 2”. it means.

1. Monomer composition for recycling plastic synthesis

According to one embodiment of the invention, it contains an aromatic diol compound, the impurity ratio of the aromatic diol compound derivative according to the formula 1 is 2% or less, the yield of the aromatic diol compound according to the formula 2 is 80% or more, and the polycarbonate-based A monomer composition for synthesizing recycled plastics characterized in that it is recovered from resin can be provided.

The present inventors have found that the monomer composition for recycling plastic synthesis of the above embodiment has high purity and yield comparable to that of a newly synthesized aromatic diol compound even though it is recovered through recycling by chemical decomposition of polycarbonate resin, and impurities are significantly reduced. As it satisfies the requirements, it was confirmed through experiments that excellent physical properties can be achieved when synthesizing polycarbonate-based resin using this, and the invention was completed.

The present invention can have the technical advantage of being able to obtain a composition containing an aromatic diol compound with high purity by recycling polycarbonate-based resin by chemical decomposition.

Specifically, the monomer composition for recycling plastic synthesis of the above embodiment is characterized in that it is recovered from polycarbonate-based resin. That is, as a result of recovery from polycarbonate-based resin to obtain the monomer composition for recycled plastic synthesis of the above embodiment, a monomer composition for recycled plastic synthesis containing an aromatic diol compound is obtained.

The polycarbonate-based resin refers to all homopolymers or copolymers containing polycarbonate repeating units, and refers generically to reaction products obtained through polymerization or copolymerization of monomers including an aromatic diol compound and a carbonate precursor. A homopolymer can be synthesized if it contains one type of carbonate repeating unit obtained using only one type of aromatic diol compound and one type of carbonate precursor. In addition, as the monomer, one type of aromatic diol compound and two or more types of carbonate precursor may be used, two or more types of aromatic diol compound and one type of carbonate precursor may be used, or one type of other diol in addition to one type of aromatic diol compound and one type of carbonate precursor may be used. Using the above, a copolymer can be synthesized when two or more types of carbonate are contained. The homopolymer or copolymer may include low molecular weight compounds, oligomers, and polymers depending on the molecular weight range.

Additionally, the monomer composition for synthesizing recycled plastic of one embodiment may include an aromatic diol compound. Specific examples of the aromatic diol compound include bis (4-hydroxyphenyl) methane, bis (4-hydroxyphenyl) ether, bis (4-hydroxyphenyl) sulfone, bis (4-hydroxyphenyl) sulfoxide, bis (4-hydroxyphenyl) sulfide, bis (4-hydroxyphenyl) ketone, 1,1-bis (4-hydroxyphenyl) ethane, 2,2-bis (4-hydroxyphenyl) propane (bisphenol A) , 2,2-bis (4-hydroxyphenyl) butane, 1,1-bis (4-hydroxyphenyl) cyclohexane (bisphenol Z), 2,2-bis (4-hydroxy-3,5-di Bromophenyl) propane, 2,2-bis (4-hydroxy-3,5-dichlorophenyl) propane, 2,2-bis (4-hydroxy-3-bromophenyl) propane, 2,2-bis (4-hydroxy-3-chlorophenyl)propane, 2,2-bis(4-hydroxy-3-methylphenyl)propane, 2,2-bis(4-hydroxy-3,5-dimethylphenyl)propane, 1,1-bis(4-hydroxyphenyl)-1-phenylethane, or mixtures of two or more thereof. Preferably, the aromatic diol compound of the monomer composition for recycling plastic synthesis of the above embodiment may be 2,2-bis(4-hydroxyphenyl)propane (bisphenol A).

The aromatic diol compound is characterized in that it is recovered from the polycarbonate-based resin used to recover the monomer composition for synthesizing recycled plastic. That is, as a result of recovery from polycarbonate-based resin to obtain the monomer composition for recycling plastic synthesis of the above embodiment, this means that an aromatic diol compound is also obtained. Therefore, the case where a new aromatic diol compound is added externally, separately from recovery from the polycarbonate-based resin, to produce the monomer composition for recycled plastic synthesis of the above embodiment is not included in the scope of the aromatic diol compound of the present invention.

Specifically, recovered from the polycarbonate-based resin means obtained through a depolymerization reaction of the polycarbonate-based resin. The depolymerization reaction can be performed under acidic, neutral, or basic conditions. In particular, the depolymerization reaction can be performed under basic (alkaline) conditions. In particular, the depolymerization reaction is preferably carried out in the presence of a glycol-based compound, as described later.

Meanwhile, the monomer composition for synthesizing recycled plastic may further include impurities other than aromatic diol compounds. The impurities refer to aromatic diol compound derivative compounds excluding aromatic diol compounds, which are the main recovery targets of the present invention.

The derivative of the aromatic diol compound may include one or more compounds selected from the group consisting of monohydroxyethyl-bisphenol A and bishydroxyethyl-bisphenol A.

That is, the derivative of the aromatic diol compound may include one type of monohydroxyethyl-bisphenol A, one type of bishydroxyethyl-bisphenol A, or a mixture of two types thereof.

As the method for producing a monomer composition for recycling plastic synthesis described later involves introducing an organic solvent and an organic salt catalyst to proceed with chemical decomposition of polycarbonate by a glycol-based compound under mild reaction conditions, the production of impurities derived from aromatic diol compounds is significantly increased. It can be reduced.

Specifically, the monomer composition for synthesizing recycled plastic may have an upper limit numerical range of the aromatic diol compound derivative impurity ratio according to Formula 1 of 2% or less, or 1.5% or less, or 1% or less, or 0.5% or less, or 0.19% or less. and the lower numerical range may be greater than 0.01%, or greater than 0.05%, or greater than 0.06%, or greater than 0.08%, or greater than 0.1%, or greater than 0.12%, or greater than 0.14%, or greater than 0.16%, or greater than 0.18%. there is. By combining the upper and lower numerical ranges, the lower to upper numerical ranges can also be satisfied. As an example of the numerical range between the lower limit and the upper limit, the impurity ratio of the aromatic diol compound derivative according to Equation 1 may be 0.01% to 2%.

According to Equation 1, %, the unit of impurity ratio of the aromatic diol compound derivative, is the peak area ratio on HPLC and means area %.

In Equation 1, the peak area of the aromatic diol compound derivative on HPLC may be the sum of the peak areas of one or more aromatic diol compound derivatives. For example, when the aromatic diol compound derivative is a mixture of two types of monohydroxyethyl-bisphenol A and bishydroxyethyl-bisphenol A, monohydroxyethyl-bisphenol A and bishydroxyethyl-bisphenol A, respectively It means the sum of the peak areas.

More specifically, the monohydroxyethyl-bisphenol A [MHE-BPA] may exhibit a peak with an HPLC retention time of 2.84 minutes, and bishydroxyethyl-bisphenol A [BHE-BPA] may exhibit a peak with an HPLC retention time of 2.61 minutes. .

The example of the method for measuring the weight ratio of the derivative impurity of the aromatic diol compound in the monomer composition for recycling plastic synthesis of the above embodiment is not greatly limited, and for example, high performance liquid chromatography (HPLC) analysis may be used. You can. The specific methods, conditions, equipment, etc. of the HPLC can be applied to various previously known contents without limitation. However, to explain as an example, the recycled bisphenol A monomer composition was dissolved in Acetonitrile (ACN) solvent at 1w% under normal pressure and 20 ~ 30 ℃ conditions, and then subjected to Waters HPLC using UG 120 (4.6mm I.DX 50mm). It can be measured through the system (e2695 separation module, 2998 PDA detector). More specifically, ① Column: UG 120 (4.6mm I.DX 50mm), ② Column Temp: 40 ℃, ③ Injection volume: 10㎕, ④ Flow: THF:ACN:water=15:15:70, volume=1.23 ml/min (total=10min), ⑤ Detector: Can be measured under 245nm conditions.

In this way, in the monomer composition for recycling plastic synthesis of the above embodiment, the ratio of impurities of aromatic diol compound derivatives other than the aromatic diol compound, which is the main recovery target material, is extremely reduced, making it possible to realize excellent physical properties when synthesizing polycarbonate-based resin. do.

Meanwhile, the monomer composition for recycling plastic synthesis of the above embodiment may have a color coordinate b* value of 0.01 to 2, or 0.1 to 1.5, or 0.5 to 1.2, or 0.8 to 1.2, or 0.88 to 1.17. That is, the monomer composition for recycling plastic synthesis of the embodiment has a lower limit numerical range of the color coordinate b* value of 0.01 or more, or 0.1 or more, or 0.5 or more, or 0.6 or more, or 0.7 or more, or 0.8 or more, or 0.9 or more, or It may be 1.0 or more, or 1.1 or more, and the upper numerical range may be 2 or less, or 1.2 or less, or 1.17 or less. By combining the upper and lower numerical ranges, the lower to upper numerical ranges can also be satisfied.

Additionally, the monomer composition for recycling plastic synthesis of the above embodiment may have a color coordinate L* value of 94 to 99, or 95 to 98, or 96 to 98, or 96.64 to 97.79. That is, the monomer composition for recycling plastic synthesis of the embodiment has a lower limit numerical range of the color coordinate L* value of 94 or more, or 95 or more, or 96 or more, or 96.3 or more, or 96.6 or more, or 96.9 or more, or 97.2 or more, or It may be 97.4 or higher, or 97.7 or higher, and the upper numerical range may be 99 or lower, or 98 or lower, or 97.79 or lower. By combining the upper and lower numerical ranges, the lower to upper numerical ranges can also be satisfied.

Additionally, the monomer composition for synthesizing recycled plastic of the above embodiment may have a color coordinate a* of 0.01 to 1.5, 0.1 to 1, or 0.13 to 0.23. That is, the monomer composition for recycling plastic synthesis of the embodiment has a lower limit numerical range of the color coordinate a* value of 0.01 or more, or 0.1 or more, or 0.12 or more, or 0.14 or more, or 0.16 or more, or 0.18 or more, or 0.2 or more, or It may be 0.22 or more, and the upper limit numerical range may be 1.5 or less, or 1 or less, or 0.23 or less. By combining the upper and lower numerical ranges, the lower to upper numerical ranges can also be satisfied.

In the present invention, “color coordinates” refer to coordinates in the CIE Lab color space, which are color values defined by CIE (Commission International de l'Eclairage), and any position in the CIE color space is L*, It can be expressed as three coordinate values: a*, b*.

Here, the L* value represents brightness. If L*=0, it represents black, and if L*=100, it represents white. In addition, the a* value indicates whether the color with the corresponding color coordinate is biased toward pure red or pure green, and the b* value indicates whether the color with the corresponding color coordinate is biased toward pure yellow or pure green. It indicates which direction the color is biased towards pure blue.

Specifically, the a* value ranges from -a to +a. The maximum value of a* (a* max) represents pure red, and the minimum value of a* (a* min) represents pure green. Additionally, the b* value ranges from -b to +b. The maximum value of b* (b* max) represents pure yellow, and the minimum value of b* (b* min) represents pure blue. For example, a negative b* value means a color biased toward pure blue, and a positive value means a color biased toward pure yellow. When comparing b*=50 and b*=80, it means that b*=80 is closer to pure yellow than b*=50.

If the color coordinate b* value of the monomer composition for synthesizing recycled plastic of one embodiment is excessively increased beyond 2, the color of the monomer composition for synthesizing recycled plastic of one embodiment is excessively biased toward yellow, resulting in poor color characteristics. In addition, if the color coordinate b* value of the monomer composition for synthesizing recycled plastic of one embodiment is excessively reduced to less than 0.01, the color of the monomer composition for synthesizing recycled plastic of one embodiment is excessively biased toward blue, resulting in poor color characteristics.

If the color coordinate L* value of the monomer composition for synthesizing recycled plastic of the embodiment is excessively reduced to less than 94, the color characteristics of the monomer composition for synthesizing recycled plastic of the embodiment will be poor.

Meanwhile, if the color coordinate a* value of the monomer composition for synthesizing recycled plastic of one embodiment is excessively increased to more than 1.5, the color of the monomer composition for synthesizing recycled plastic of one embodiment is excessively biased toward red, resulting in poor color characteristics. In addition, if the color coordinate a* value of the monomer composition for synthesizing recycled plastic of one embodiment is excessively reduced to less than 0.01, the color of the monomer composition for synthesizing recycled plastic of one embodiment is excessively biased toward green, resulting in poor color characteristics.

The example of the method for measuring the color coordinates L*, a*, and b* values of the monomer composition for recycling plastic synthesis of the above embodiment is not greatly limited, and various color characteristic measurement methods in the plastics field can be applied without limitation.

However, as an example of a method of measuring the color coordinates L*, a*, and b* values of the monomer composition for recycled plastic synthesis of the above embodiment, they can be measured in reflection mode using HunterLab UltraScan PRO Spectrophotometer equipment.

Meanwhile, the monomer composition for recycling plastic synthesis according to the above embodiment may have an aromatic diol compound yield of 80% or more, or 88% or more, or 90% or more, or 92% or more, or 94% or more, and an upper limit value. The range may be 100% or less, or 98% or less, or 96% or less, or 94.1% or less. By combining the upper and lower numerical ranges, the lower to upper numerical ranges can also be satisfied. The increase in the yield of the aromatic diol compound to more than 80% appears to be due to the method of producing a monomer composition for synthesizing recycled plastic, which will be described later.

The example of the method for measuring the aromatic diol compound yield of the monomer composition for recycling plastic synthesis of the above embodiment is not greatly limited, and for example, it can be calculated using Equation 2 below.

[Equation 2]

Yield (%) = W ₁ /W ₀

In Equation 2, W ₀ is the mass of the aromatic diol compound obtained upon 100% decomposition, and W ₁ is the mass of the aromatic diol compound actually obtained.

In Equation 2, the mass of the aromatic diol compound can be determined without limitation using various commonly known mass measurement methods, for example, a scale can be used.

In this way, the yield of the aromatic diol compound, which is the main recovery target material, in the monomer composition for recycling plastic synthesis of the above embodiment is greatly increased to 80% or more, and the efficiency of the recycling process for polycarbonate-based resin can be improved.

The monomer composition for synthesizing recycled plastic of one embodiment can be used as a raw material for manufacturing various recycled plastics (eg, polycarbonate (PC)), which will be described later.

The monomer composition for recycling plastic synthesis of the above embodiment may further include a small amount of other additives and solvents, and the type of specific additives or solvents is not greatly limited, and may include an aromatic diol compound recovery process by depolymerization of polycarbonate-based resin. A variety of widely used materials can be applied without limitation.

The monomer composition for synthesizing recycled plastic of the above embodiment may be obtained by the method for producing a monomer composition for synthesizing recycled plastic, which will be described later. That is, the monomer composition for recycling plastic synthesis of the above embodiment is obtained by going through various filtration, purification, washing, and drying processes to secure only the aromatic diol compound, which is the main recovery target material, in high purity after the depolymerization reaction of the polycarbonate-based resin. It applies.

2. Manufacturing method of monomer composition for recycled plastic synthesis

According to another embodiment of the invention, preparing a mixed solution by adding polycarbonate to an organic solvent; Adding a glycol-based compound and an organic base catalyst to the mixed solution and stirring; and obtaining the aromatic diol compound formed in the stirring step. A method for producing the monomer composition for synthesizing recycled plastic of claim 1 may be provided.

Specifically, the present invention can stably obtain bisphenol A, a highly pure monomer, by decomposing polycarbonate into a glycol-based compound under mild conditions.

The polycarbonate includes all homopolymers or copolymers containing carbonate repeating units, and refers to a general term for reaction products obtained through polymerization or copolymerization of monomers including an aromatic diol compound and a carbonate precursor. A homopolymer can be synthesized if it contains one type of carbonate repeating unit obtained using only one type of aromatic diol compound and one type of carbonate precursor. In addition, as the monomer, one type of aromatic diol compound and two or more types of carbonate precursor may be used, two or more types of aromatic diol compound and one type of carbonate precursor may be used, or one type of other diol in addition to one type of aromatic diol compound and one type of carbonate precursor may be used. Using the above, a copolymer can be synthesized when two or more types of carbonate are contained. The homopolymer or copolymer may include low molecular weight compounds, oligomers, and polymers depending on the molecular weight range.

The polycarbonate can be applied in various forms and types, such as new polycarbonate produced through synthesis, recycled polycarbonate produced through a recycling process, or polycarbonate waste.

In the present invention, the glycol-based compound may include both a glycol compound or a derivative thereof, and specifically, the glycol-based compound may include alkylene glycol. Specific examples of the alkylene glycol are not greatly limited, and various known alkylene glycols can be used without limitation. Examples include ethylene glycol or propylene glycol.

Meanwhile, the organic solvent may include one or more solvents selected from the group consisting of tetrahydrofuran, toluene, methylene chloride, chloroform, dimethyl carbonate, ethylmethyl carbonate, diethyl carbonate, and dipropyl carbonate. That is, the organic solvent may include tetrahydrofuran, toluene, methylene chloride, chloroform, dimethyl carbonate, ethylmethyl carbonate, diethyl carbonate, dipropyl carbonate, or a mixture of two or more thereof.

Specifically, when methylene chloride is used as the organic solvent, there is an advantage in that the dissolution characteristics for polycarbonate are improved and reactivity can be improved.

The weight ratio of the glycol-based compound, organic solvent, and polycarbonate is not greatly limited, but for example, the weight ratio between the glycol-based compound and polycarbonate is 10:1 to 1:10, or 1:1 to 1:10, or 1:1 to 1:5, or 1:1 to 1:2, or 1:1.2 to 1:2.

In addition, the weight ratio between the organic solvent and polycarbonate is 10:1 to 1:10, or 10:1 to 1:1, or 10:1 to 2:1, or 2:1 to 5:1, or 2:1. to 3:1, or 2.5:1 to 3:1.

In addition, the weight ratio between organic solvent and glycol-based compound is 10:1 to 1:10, or 1:1 to 10:1, or 2:1 to 10:1, or 2:1 to 5:1, or 3:1. It may be 4:1.

Specifically, there is an advantage that the depolymerization reaction of the polymer can proceed at the required level by mixing the glycol-based compound and the organic solvent within the above range.

The organic base catalyst is used in an amount of 0.1 to 10 parts by weight, or 0.1 to 5 parts by weight, or 0.1 to 4 parts by weight, or 0.1 to 3 parts by weight, or 0.1 parts by weight, based on 100 parts by weight of polycarbonate. It may be added in an amount of from 0.1 to 2 parts by weight, or from 0.1 to 1 part by weight. Specifically, there is an advantage in that an economical catalytic reaction can be performed by including an organic base catalyst in the above content range.

Meanwhile, the organic base catalyst refers to a nonionic organic compound with basic properties, and may specifically include an amidine-based compound or a guanidine-based compound. The amidine-based compound may include all amidine compounds or derivative compounds thereof. The guanidine-based compound may include a guanidine compound or a derivative thereof.

The amidine-based compound or guanidine-based compound may have a bonded ring. The bonded ring may include a 6-membered ring and a bonded ring between 6-membered rings. Additionally, the bonded ring may include a bonded ring between a 7-membered ring and a 6-membered ring. Additionally, the bonded ring may include a bonded ring between a 5-membered ring and a 6-membered ring. The 7-membered ring refers to a case where the ring has 7 elements, the 6-membered ring refers to a case where the ring has 6 elements, and the 5-membered ring refers to a case where the ring has 5 elements.

The 6-membered ring may contain a C=N double bond of amidine or guanidine. The 5-membered ring or 7-membered ring may contain a C-C single bond of amidine or a C-N single bond of guanidine. Additionally, a C-N single bond of amidine or guanidine may be included in the area where two rings overlap.

Specifically, the amidine-based compound may include an amidine-based compound having a bonded ring.

Detailed examples of the amidine-based compounds include 1,8-diazabicyclo[5.4.0]undec-7-ene, or 1,5-diazabicyclo[4.3.0]non-5. -N, etc. may be mentioned, but are not limited thereto.

Additionally, the guanidine-based compound may include a guanidine-based compound having a bonded ring.

Detailed examples of the guanidine-based compounds include 1,5,7-triazabicyclo[4.4.0]dec-5-ene, 7-methyl-1,5,7-triazabicyclo[4.4] .0]dec-5-ene, 1,2,3,5,6,7-hexahydroimidazo[1,2-a]pyrimidine, or 1-methyl-1,2,3,5,6, Examples include, but are not limited to, 7-hexahydroimidazo[1,2-a]pyrimidine.

Meanwhile, the step of adding and stirring the glycol-based compound and the organic base catalyst to the mixed solution is performed at 20 ℃ to 100 ℃, or 50 ℃ to 100 ℃, or 60 ℃ to 100 ℃, or 70 ℃ to 100 ℃, or 70 ℃ It may be stirred at 90° C. for 1 hour to 24 hours, or 1 hour to 12 hours, or 1 hour to 8 hours.

Specifically, the above conditions are mild process conditions compared to the existing pressurization/high temperature process, and by performing stirring under the above conditions, the process can be performed in a mild process compared to the pressurization/high temperature process, especially at temperatures ranging from 70°C to 70°C. There is an advantage in obtaining the most efficient results in terms of reproducibility and acceptability when stirred at 90°C for 1 to 12 hours.

Meanwhile, the step of obtaining the aromatic diol compound formed in the stirring step includes adding the product obtained in the stirring step to a crystallization solvent to form an aromatic diol compound crystal; and filtering the aromatic diol compound crystals. The specific equipment and conditions for adding the crystallization solvent and forming aromatic diol compound crystals are not limited, and various recrystallization processes that have been widely used in the field of technology for recovering aromatic diol compounds (bisphenol A) can be applied without limitation. As an example of the crystallization solvent, water can be used.

In addition, in the step of filtering the aromatic diol compound crystals, specific filtration equipment and conditions are not limited, and various filtration processes that have been widely used in the field of technology for recovering aromatic diol compounds (bisphenol A) can be applied without limitation. . As an example of the filtration, reduced pressure filtration can be used.

3. Recycled plastic

According to another embodiment of the invention, a recycled plastic containing a reaction product of the monomer composition for synthesizing recycled plastic of the above embodiment and a comonomer may be provided.

The content of the monomer composition for synthesizing recycled plastic of the one embodiment includes all of the content described above in the one embodiment and other embodiments.

Examples of the above recycled plastics are not greatly limited, and various plastics synthesized using aromatic diol compounds such as bisphenol A and carbonate precursors such as dimethyl carbonate, diethyl carbonate, or ethylmethyl carbonate as monomers can be applied without limitation, A more specific example may include polycarbonate-based resin.

The polycarbonate-based resin refers to all homopolymers or copolymers containing polycarbonate repeating units, and refers to reaction products obtained through polymerization or copolymerization of monomers including aromatic diol compounds and carbonate precursors. A homopolymer can be synthesized if it contains one type of carbonate repeating unit obtained using only one type of aromatic diol compound and one type of carbonate precursor. In addition, as the monomer, one type of aromatic diol compound and two or more types of carbonate precursors may be used, two or more types of aromatic diol compounds and one type of carbonate precursor may be used, or one type of other diol in addition to one type of aromatic diol compound and one type of carbonate precursor may be used. Using the above, a copolymer can be synthesized when two or more types of carbonate are contained. The homopolymer or copolymer may include all low molecular weight compounds, oligomers, and polymers depending on the molecular weight range.

More specifically, in the recycled plastic containing the reaction product of the monomer composition for recycling plastic synthesis and the comonomer of the above embodiment, a carbonate precursor may be used as the comonomer. Specific examples of the carbonate precursor include phosgene, triphosgene, diphosgene, bromophosgene, dimethyl carbonate, diethyl carbonate, dibutyl carbonate, dicyclohexyl carbonate, diphenyl carbonate, ditoryl carbonate, bis(chlorophenyl) carbonate, m -Cresyl carbonate, dinaphthyl carbonate, bis(diphenyl) carbonate, or bishaloformate may be mentioned.

Examples of the reaction process of the monomer composition and comonomer for synthesizing recycled plastics for synthesizing the polycarbonate-based resin are not greatly limited, and various previously known polycarbonate production methods can be applied without limitation.

However, as an example of the polycarbonate production method, a polycarbonate production method including the step of polymerizing a monomer composition for synthesizing recycled plastic and a composition containing a comonomer can be used. At this time, the polymerization can be performed by interfacial polymerization. During interfacial polymerization, the polymerization reaction is possible at normal pressure and low temperature, and molecular weight control is easy.

The polymerization temperature may be 0°C to 40°C, and the reaction time may be 10 minutes to 5 hours. Additionally, the pH during the reaction can be maintained at 9 or higher or 11 or higher.

The solvent that can be used in the polymerization is not particularly limited as long as it is a solvent used in the polymerization of polycarbonate in the art. For example, halogenated hydrocarbons such as methylene chloride and chlorobenzene can be used.

Additionally, the polymerization can be performed in the presence of an acid binder, and the acid binder can be an alkali metal hydroxide such as sodium hydroxide or potassium hydroxide, or an amine compound such as pyridine.

Additionally, in order to control the molecular weight of polycarbonate during the polymerization, the polymerization may be performed in the presence of a molecular weight regulator. The molecular weight regulator may be an alkylphenol having 1 to 20 carbon atoms, and specific examples thereof include p-tert-butylphenol, p-cumylphenol, decylphenol, dodecylphenol, tetradecylphenol, hexadecylphenol, octadecylphenol, Examples include eicosylphenol, docosylphenol, or triacontylphenol. The molecular weight regulator may be added before the start of polymerization, during the start of polymerization, or after the start of polymerization. The molecular weight regulator can be used in an amount of 0.01 to 10 parts by weight, or 0.1 to 6 parts by weight, based on 100 parts by weight of the aromatic diol compound, and the desired molecular weight can be obtained within this range.

In addition, in order to promote the polymerization reaction, reactions such as tertiary amine compounds such as triethylamine, tetra-n-butylammonium bromide, tetra-n-butylphosphonium bromide, quaternary ammonium compounds, quaternary phosphonium compounds, etc. Additional accelerators may be used.

4. Molded product

According to another embodiment of the invention, a molded article containing the recycled plastic of the other embodiment can be provided. The content regarding the recycled plastic includes all the content described in detail in the other embodiments.

The molded product may be obtained by applying various known plastic molding methods to the recycled plastic without limitation, and examples of the molding methods include injection molding, foam injection molding, blow molding, or extrusion molding.

Examples of the above molded products are not greatly limited, and can be applied to various molded products using plastic without limitation. Examples of the molded products include automobile parts, electrical and electronic products, communication products, household goods, building materials, optical parts, and exterior materials.

In addition to the recycled plastic of the other embodiments, the molded article may optionally contain one or more additives selected from the group consisting of antioxidants, plasticizers, antistatic agents, nucleating agents, flame retardants, lubricants, impact modifiers, fluorescent whitening agents, ultraviolet absorbers, pigments, and dyes. may additionally be included.

As an example of a method of manufacturing the molded product, the recycled plastic and additives of the other embodiments are mixed well using a mixer, then extruded with an extruder to produce pellets, dried, and then injected with an injection molding machine. It can be included.

According to the present invention, a monomer composition for synthesizing recycled plastic containing a high-purity, high-yield aromatic diol compound recovered through recycling by chemical decomposition of polycarbonate resin, a method for manufacturing the same, and recycled plastic and molded products using the same are provided. can be provided.

The invention is explained in more detail in the following examples. However, the following examples only illustrate the present invention, and the content of the present invention is not limited by the following examples.

<Example: Preparation of recycled bisphenol A monomer composition>

Examples 1 to 8

80 g of methylene chloride and 30 g of polycarbonate were added to a 250 ml 3-neck flask and stirred.

Afterwards, 22 g of ethylene glycol and the catalyst shown in Table 1 below were added and stirred for 24 hours at the reaction temperature shown in Table 1 below.

When the reaction was completed, the reaction product was added to water, and the crystallized bisphenol A was filtered under reduced pressure to obtain bisphenol A to prepare a recycled bisphenol A monomer composition.

division catalyst Catalyst input amount (g) Reaction temperature (℃) Example 1 Compound 1 0.17 70 Example 2 Compound 2 0.17 70 Example 3 Compound 3 0.17 70 Example 4 Compound 4 0.17 70 Example 5 Compound 5 0.17 70 Example 6 Compound 6 0.17 70 Example 7 Compound 1 0.3 80 Example 8 Compound 1 0.3 90

- Compound 1: 1,5,7-triazabicyclo[4.4.0]dec-5-ene

- Compound 2: 7-methyl-1,5,7-triazabicyclo[4.4.0]dec-5-ene

- Compound 3: 1,8-diazabicyclo[5.4.0]undec-7-ene

- Compound 4: 1,5-diazabicyclo[4.3.0]non-5-ene

- Compound 5: 1,2,3,5,6,7-hexahydroimidazo[1,2-a]pyrimidine

- Compound 6: 1-methyl-1,2,3,5,6,7-hexahydroimidazo[1,2-a]pyrimidine

<Comparative example: Preparation of recycled bisphenol A monomer composition>

Comparative Example 1

20 g of polycarbonate was added to a 250 ml 3-neck flask and stirred.

Afterwards, 22 g of ethylene glycol and 0.17 g of Compound 1 as a catalyst were added and stirred at 130° C. for 24 hours.

When the reaction was completed, the reaction product was added to water, and the crystallized bisphenol A was filtered under reduced pressure to obtain bisphenol A to prepare a recycled bisphenol A monomer composition.

Comparative example 2

60 ml of toluene, 30 ml of ethanol, and 1.5 g of Compound 1 as a catalyst were added to a 250 ml 3-neck flask and stirred.

Afterwards, 30 g of waste polycarbonate was added and stirred at 80°C for 36 hours.

When the reaction was completed, the reaction product was added to water, and the crystallized bisphenol A was filtered under reduced pressure to obtain bisphenol A to prepare a recycled bisphenol A monomer composition.

<Experimental example>

The physical properties of the recycled bisphenol A monomer composition or by-product obtained in the above Examples and Comparative Examples were measured by the following method, and the results are shown in Table 2.

1. BPA purity

The recycled bisphenol A monomer composition was dissolved in Acetonitrile (ACN) solvent at 1w% under normal pressure and 20 to 30°C conditions, and then analyzed using a Waters HPLC system (e2695 separation module, 2998 PDA) using UG 120 (4.6mm I.DX 50mm). The purity of bisphenol A (BPA) was analyzed using a detector.

<HPLC conditions>

① Column: UG 120 (4.6mm I.DX 50mm)

② Column Temp: 40℃

③ Injection volume: 10㎕

④ Flow: THF:ACN:water=15:15:70, volume=1.23ml/min (total=10min)

⑤ Detector: 245nm

2. Color coordinates (L*, a*, b*)

The recycled bisphenol A monomer composition was analyzed in reflection mode using HunterLab UltraScan PRO Spectrophotometer equipment.

3. BPA derivative (MHE-BPA, BHE-BPA) impurity ratio

1 ml of the recycled bisphenol A monomer composition was collected as a sample and subjected to High Performance Liquid Chromatography (HPLC) analysis using the same method as the method for measuring 1.BPA purity. For 100% of the total HPLC peak area, The peak area ratio (unit: %) of impurities of BPA derivatives (monohydroxyethyl-bisphenol A [MHE-BPA], bishydroxyethyl-bisphenol A [BHE-BPA]) was measured according to Equation 1 below.

[Equation 1]

BPA derivative impurity ratio (%) = (Bisphenol A derivative peak area on HPLC / total peak area on HPLC)

In Equation 1, the peak area of the bisphenol A derivative on HPLC is specifically as follows, and in Equation 1, the peak area of the bisphenol A derivative on HPLC is the sum of the peak areas of MHE-BPA and BHE-BPA.

Monohydroxyethyl-bisphenol A [MHE-BPA]: peak retention time 2.84 minutes

Bishydroxyethyl-bisphenol A [BHE-BPA]: peak retention time 2.61 minutes

4. BPA yield

The weight of BPA produced when the polycarbonate used in the reaction was 100% decomposed was measured, the weight of the obtained BPA was measured, and the yield of BPA was calculated as shown in Equation 2 below.

[Equation 2]

Yield (%) = W ₁ /W ₀

In Equation 2, W ₀ is the mass of BPA obtained upon 100% decomposition, and W ₁ is the mass of BPA actually obtained. Specifically, when about 100 g of polycarbonate is decomposed, the theoretical mass of BPA obtained upon 100% decomposition is 89 g. If the mass of BPA actually obtained is 80 g, the yield is 80/89 * 100 = 90%.

Experimental example measurement results division BPA purity (%) L* a* b* BPA derivative impurity rate (%) BPA yield (%) Example 1 99.9 97.79 0.13 1.08 0.06 93.5 Example 2 99.7 97.19 0.18 1.17 0.10 93.2 Example 3 99.8 96.86 0.20 0.88 0.13 92.7 Example 4 99.6 97.23 0.23 1.01 0.14 94.1 Example 5 99.6 96.98 0.19 0.95 0.19 92.8 Example 6 99.5 97.59 0.22 0.96 0.14 90.6 Example 7 99.7 97.54 0.16 1.02 0.17 91.3 Example 8 99.5 96.64 0.22 0.97 0.16 88.5 Comparative Example 1 72.6 - - - 25.32 - Comparative example 2 95.2 92.08 2.112 2.547 - 75.0

As shown in Table 1, the recycled bisphenol A monomer compositions obtained in Examples 1 to 8 showed high purity of 99.5% to 99.9%. In addition, the recycled bisphenol A monomer compositions obtained in Examples 1 to 8 showed color coordinates L* of 96.64 to 97.79, a* of 0.13 to 0.23, and b* of 0.88 to 1.17, showing excellent optical properties. In addition, the recycled bisphenol A monomer compositions obtained in Examples 1 to 8 were measured to have a high bisphenol A yield of 88.5% to 94.1%. In addition, the recycled bisphenol A monomer composition obtained in Examples 1 to 8 had a low BPA derivative impurity ratio of 0.06% to 0.19%.

On the other hand, the purity of the recycled bisphenol A monomer composition obtained in Comparative Example 1 was reduced to 72.6% compared to the Example, and the BPA derivative impurity ratio was measured to be 25.32%, which was higher than that of the Example.

In addition, the purity of the recycled bisphenol A monomer composition obtained in Comparative Example 2 was reduced to 95.2% compared to the example, and the bisphenol A yield was measured to be 75%, which was lower than that of the example. In addition, the recycled bisphenol A monomer composition obtained in Comparative Example 2 showed poor optical properties compared to the Example, with color coordinates L* of 92.08, a* of 2.112, and b* of 2.547.

Claims (20)

Contains an aromatic diol compound,
The impurity ratio of the aromatic diol compound derivative according to the following formula 1 is 2% or less,
The aromatic diol compound yield according to the following formula 2 is 80% or more,
Monomer composition for recycling plastic synthesis, characterized in that recovered from polycarbonate-based resin:
[Equation 1]
Aromatic diol compound derivative impurity ratio (%) = (aromatic diol compound derivative peak area on HPLC / total peak area on HPLC)
[Equation 2]
Yield (%) = W1/W0
In Equation 2, W0 is the mass of the aromatic diol compound obtained upon 100% decomposition of the polycarbonate-based resin, and W1 is the mass of the aromatic diol compound actually obtained.
According to paragraph 1,
In Equation 1, the peak area of the aromatic diol compound derivative on HPLC is the sum of the peak areas of one or more aromatic diol compound derivatives. Monomer composition for synthesizing recycled plastic.
According to paragraph 1,
A monomer composition for synthesizing recycled plastic, wherein the derivative of the aromatic diol compound includes at least one compound selected from the group consisting of monohydroxyethyl-bisphenol A and bishydroxyethyl-bisphenol A.
According to paragraph 1,
The monomer composition for synthesizing recycled plastic has a color coordinate L* of 94 to 99.
According to paragraph 1,
The monomer composition for synthesizing recycled plastic has a color coordinate b* of 0.01 to 2.
According to paragraph 1,
The monomer composition for synthesizing recycled plastic has a color coordinate a* of 0.01 to 1.5.
Preparing a mixed solution by adding polycarbonate to an organic solvent;
Adding a glycol-based compound and an organic base catalyst to the mixed solution and stirring; and
A method for producing the monomer composition for recycling plastic synthesis of claim 1, comprising: obtaining the aromatic diol compound formed in the stirring step.
In clause 7,
A method of producing a monomer composition for synthesizing recycled plastic, wherein the glycol-based compound includes alkylene glycol.
In clause 7,
The organic solvent is a method of producing a monomer composition for recycling plastic synthesis, wherein the organic solvent includes at least one solvent selected from the group consisting of tetrahydrofuran, toluene, methylene chloride, chloroform, dimethyl carbonate, ethylmethyl carbonate, diethyl carbonate, and dipropyl carbonate. .
In clause 7,
A method for producing a monomer composition for synthesizing recycled plastic wherein the organic solvent:glycol-based compound weight ratio is 10:1 to 1:10.
In clause 7,
A method for producing a monomer composition for synthesizing recycled plastic, wherein the organic base catalyst is added in an amount of 0.1 to 10 parts by weight based on 100 parts by weight of polycarbonate.
In clause 7,
A method of producing a monomer composition for synthesizing recycled plastic, wherein the organic base catalyst includes an amidine-based compound or a guanidine-based compound.
According to clause 12,
A method of producing a monomer composition for synthesizing recycled plastic, wherein the amidine-based compound or guanidine-based compound has a bonded ring.
According to clause 13,
A method of producing a monomer composition for recycling plastic synthesis, wherein the bonded ring includes a bonded ring between a 5- to 7-membered ring and a 6-membered ring.
According to clause 12,
The amidine-based compound is a recycled plastic, including 1,8-diazabicyclo[5.4.0]undec-7-ene or 1,5-diazabicyclo[4.3.0]non-5-ene. Method for producing monomer composition for synthesis.
According to clause 12,
The guanidine-based compound is 1,5,7-triazabicyclo[4.4.0]dec-5-ene, 7-methyl-1,5,7-triazabicyclo[4.4.0]dec-5-ene , 1,2,3,5,6,7-hexahydroimidazo [1,2-a] pyrimidine, or 1-methyl-1,2,3,5,6,7-hexahydroimidazo [1 ,2-a] Method for producing a monomer composition for recycling plastic synthesis containing pyrimidine.
In clause 7,
The step of adding a glycol-based compound and an organic base catalyst to the mixed solution and stirring,
A method for producing a monomer composition for synthesizing recycled plastic, which involves stirring at 20°C to 100°C for 1 hour to 30 hours.
In clause 7,
The step of obtaining the aromatic diol compound formed in the stirring step is,
Adding the product obtained in the stirring step to a crystallization solvent to form an aromatic diol compound crystal; and
A method of producing a monomer composition for synthesizing recycled plastic, comprising: filtering the aromatic diol compound crystals.
A recycled plastic comprising a reaction product of the monomer composition for recycling plastic synthesis of claim 1 and a comonomer.
A molded article comprising the recycled plastic of claim 19.