Method for producing polyphenol derivative, polyphenol derivative, and polyphenol derivative-containing resin composition material

Abstract

A method for producing a polyphenol derivative, which comprises a step of reacting a polyphenol-containing composition with an aromatic compound having an ortho-para-directing group in a solvent; a polyphenol derivative produced by the method for producing a polyphenol derivative; and a polyphenol derivative-containing resin composition material containing the polyphenol derivative.

Description

[Technical field]

[0001] The present invention relates to a method for producing a polyphenol derivative, a polyphenol derivative, and a resin composition material containing a polyphenol derivative. [Background technology]

[0002] From the viewpoint of reducing greenhouse gas emissions, carbon-neutral plant-derived substances are expected to be used as plastic materials. Plant-derived substances mainly include cellulose and hemicellulose derived from sugar, and polyphenols such as lignin. Of these, polyphenols such as lignin have aromatic rings, aliphatic hydroxyl groups, and aromatic hydroxyl groups, and therefore it is desirable to use them as plastic materials. However, due to two problems (a) that a simple and economical method for separating and purifying polyphenols such as lignin has not been established, and (b) that polyphenols such as lignin are not easily biodegradable, are hardly soluble in solvents, and have a high softening point, making them difficult to handle, as well as poorly reactive with existing plastic materials, there are almost no applications of polyphenols such as lignin as plastic materials. Therefore, in order to make polyphenols such as lignin suitable as plastic materials, appropriate separation and purification, modification, and further technology for using the modified polyphenols such as lignin are being studied.

[0003] In the past, the separation of polyphenols such as lignin from biomass residues was done by separating polyphenols such as lignin from black liquor, which is a residue from the pulp industry. However, since black liquor contains a lot of impurities such as inorganic salts, it was used for products with low industrial value such as fuel. Recently, as shown in Patent Document 1, efforts have been made to improve the industrial value of black liquor by separating lignin by modifying it with PEG (polyethylene glycol) or the like. Furthermore, regarding the utilization of the separated lignin, for example, Patent Document 2 discloses a technology relating to modified lignin in which a benzoxazine skeleton is introduced into lignin to impart reactivity without lowering the molecular weight of the lignin, and a molding material containing the modified lignin to improve the mechanical strength, etc., of the molded product. Furthermore, Patent Document 3 discloses a technology in which lignin is reacted with phenols in the presence of a catalyst to form phenols, which are then heated together with an alkali to form alkalized lignin, and aldehydes are further added to the alkalized lignin to form hydroxymethylated lignin, thereby increasing the reactivity of the lignin, and a technology in which the lignin with increased reactivity is used in a binder composition. Furthermore, Patent Document 4 discloses a phenol-modified lignin resin having improved curability and resin strength, which is produced by reacting lignin, phenols, and aldehydes in the presence of an acid. [Prior art documents] [Patent documents]

[0004] [Patent Document 1] Special Publication No. 2015-519452 [Patent Document 2] Patent No. 5671430 [Patent Document 3] Special Publication No. 2016-540058 [Patent Document 4] International Publication No. 2015 / 147165 Summary of the Invention [Problem to be solved by the invention]

[0005] When aiming to reduce greenhouse gases as described above by using polyphenols such as lignin as plastic materials, there is a problem that the following four conditions must be satisfied: (i) cheap, (ii) can be prepared in large quantities, (iii) can be easily mixed with resin, and (iv) can easily react with resin. However, sulfite lignin, kraft lignin, and soda lignin obtained from black liquor discharged from the pulp industry, which are currently considered to be lignin raw materials, can satisfy the conditions (i) and (ii). However, since sulfite lignin contains a high sulfur concentration, it is difficult to achieve (iv), and since it is water-soluble, (iii) is not satisfactory. In addition, since kraft lignin and soda lignin have high molecular weights, they cannot achieve (iii) and (iv). Recently, organosolv lignin soluble in organic solvents (PEG lignin in Patent Document 1 is one example) has been reported, which is said to overcome the above problems, but there are problems in solving (i) and (ii).

[0006] Therefore, an object of the present invention is to provide a method for inexpensively producing a polyphenol derivative that has improved reactivity with existing plastic materials, good compatibility with resins, and can give molded articles with improved physical properties such as bending strength, as well as a lignin derivative and a lignin derivative-containing resin composition material that can give the above-mentioned molded articles. [Means for solving the problem]

[0007] As a result of intensive research to solve the above problems, the inventors have found that the above problems can be solved by reacting an aromatic compound having an ortho-para orienting group with a polyphenol-containing composition such as biomass in a solvent to separate polyphenols as polyphenol derivatives, while reducing the amount of light components derived from polyphenols and achieving a low molecular weight in a single reaction. That is, the present invention is as follows.

[0008] [1] A method for producing a polyphenol derivative, comprising the step of reacting a polyphenol-containing composition with an aromatic compound having ortho-para orientation in a solvent. [2] A lignin derivative having a weight-average molecular weight of less than 5,000 and a molecular weight LogM of 2.15 to 2.20 present in an amount of less than 0.7 mass%. [3] A lignin derivative produced by the method for producing a polyphenol derivative, or a lignin derivative-containing resin composition material containing the lignin derivative. Effect of the Invention

[0009] According to the present invention, it is possible to provide a method for inexpensively producing a polyphenol derivative which has improved reactivity with existing plastic materials, good compatibility with resins, and can give molded articles with improved physical properties such as bending strength, as well as a lignin derivative and a lignin derivative-containing resin composition material which can give the above-mentioned molded articles. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0010] [Method of producing polyphenol derivatives] The method for producing a polyphenol derivative of the present invention includes a step of reacting a polyphenol-containing composition with an aromatic compound having an ortho-para orienting group in a solvent. Here, in the present invention, the "polyphenol derivative" refers to a reaction product derived from polyphenol obtained by reacting a polyphenol contained in a polyphenol-containing composition with an aromatic compound. In the present invention, examples of the polyphenol in the polyphenol-containing composition include lignite, lignin, tannin, catechin, anthocyanin, rutin, isoflavone, lignan, curcumin, and chlorogenic acid.

[0011] In particular, in the method for producing a polyphenol derivative of the present invention, the polyphenol contained in the polyphenol-containing composition is preferably lignin from the viewpoint of its usefulness as a plastic material, and therefore the polyphenol derivative is preferably a lignin derivative. Hereinafter, in this specification, a specific example will be described in which the polyphenol contained in the polyphenol-containing composition is lignin and the polyphenol derivative is a lignin derivative, but the method for producing a polyphenol derivative of the present invention is not limited to these lignins and lignin derivatives.

[0012] Here, lignin is a polymer compound formed by polymerization of three types of lignin monomers, which are p-hydroxycinnamic alcohols, and has a basic skeleton represented by the following formula (2).

[0013] [ka]

[0014] In the above formula (2), the substituent R 3 and R 4 R represents a hydrogen atom or a methoxy group. 3 and R 4 When both are hydrogen atoms, it is a p-hydroxyphenyl nucleus (H-type skeleton), and R 3 and R 4 When either one of the above is a hydrogen atom, the guaiacyl nucleus (G-type skeleton) is formed, and R 3 and R 4 When neither of these is a hydrogen atom, it is called a syringyl nucleus (S-type skeleton). In the above formula (2), X represents a carbon atom, and Y represents a bond to a hydrogen atom or a carbon atom.

[0015] In the basic structure of lignin, R 3 and R 4 The carbon atom bonded to R is a highly reactive site (hereinafter, simply referred to as the "reactive site"). 3 and R 4 If R is a methoxy group, the reactivity of that carbon atom is poor. Therefore, in order to react with lignin, R 3 and R 4 is preferably a hydrogen atom. In addition, lignin contains not only the aromatic moieties but also aliphatic moieties, and the hydroxyl groups present in the aliphatic moieties have poor oxidation stability (aliphatic hydroxyl groups are converted to aldehydes or carboxylic acids by oxidation). Therefore, the fewer the hydroxyl groups present in the aliphatic moieties, the better the reactivity with existing plastic materials. Furthermore, the lignin derivative has a lower softening point without significantly decreasing the molecular weight, thereby improving the mixability and reactivity with existing plastic materials. That is, a lignin derivative is one that contains a large amount of two types of skeletons, the H-type skeleton and the G-type skeleton, which are highly reactive, has a small number of aliphatic hydroxyl groups, and preferably has a low softening point without significantly decreasing the molecular weight, and is therefore highly reactive and suitable as a plastic material. Therefore, in the production method of the present invention, a polyphenol-containing composition and an aromatic compound are mixed in a solvent, so that the substituent R 3 and R 4 The present invention utilizes a substitution reaction in which lignin is transferred to an aromatic compound to obtain a lignin derivative suitable for the above-mentioned plastic material.

[0016] <Reaction process> Polyphenol-containing composition In the method for producing a polyphenol derivative of the present invention, at least one of biomass and biomass residues can be used as the polyphenol-containing composition used as a raw material. Biomass residues include those derived from plant biomass, such as woody biomass and herbaceous biomass. Examples of biomass residues include saccharification residues and fermentation residues of lignocellulosic biomass (second-generation ethanol saccharification residues and second-generation ethanol fermentation residues), black liquor (sulfite lignin, kraft lignin, soda lignin, etc.), and tannins, and any one or more of these can be used. Among these, from the viewpoints of availability, quality of polyphenol derivatives, and economic efficiency, any one or more of second-generation ethanol saccharification residues and second-generation ethanol fermentation residues can be used as the polyphenol-containing composition.

[0017] (Lignocellulosic biomass) Examples of non-edible plant biomass include woody biomass and herbaceous biomass. Woody biomass includes coniferous and broadleaf trees such as cedar, cypress, Japanese cypress, cherry blossom, eucalyptus, beech, and bamboo. Examples of herbaceous biomass include palm trunks and empty bunches, palm fruit fiber and seeds, bagasse (sugar cane and high-biomass sugar cane residue), cane tops (sugar cane tops and leaves), energy cane, rice straw, wheat straw, corn cobs, stems and leaves, and residues (corn stover, corn cobs, corn hulls), sorghum residues (including sweet sorghum), jatropha seed husks and shells, cashew husks, switchgrass, erianthus, high-biomass yield crops, and energy crops. Among these, from the viewpoints of availability and compatibility with the production method applied in the present invention, herbaceous biomass is preferred, with palm empty bunches, wheat straw, corn cobs, stems and leaves, residues (corn stover, corn cob, corn hull), bagasse, cane tops, energy cane, and residues thereof after useful component extraction being more preferred, with corn cobs, stems and leaves, residues (corn stover, corn cob, corn hull), bagasse, cane tops, and energy cane being even more preferred. The above useful components include, for example, hemicellulose, carbohydrates, minerals, moisture, etc. Bagasse contains about 5 to 30 mass % of lignin, and the lignin in bagasse contains all of the H, G and S nuclei as basic skeletons. The plant biomass may be in the form of a pulverized material, or may be in the form of a block, chip, powder, or a water-containing material.

[0018] Bagasse, corn stover, or the like is treated with an organosolv method, a compressed hot water method, ammonia treatment, ammonia explosion, acid treatment, alkali treatment, oxidative decomposition, thermal decomposition, microwave heating, or the like, preferably with acid treatment, ammonia explosion, steam explosion, or the like, to separate hemicellulose into the solution side, and then the cellulose is converted into glucose by an enzyme and separated into the solution side, or the hemicellulose is not separated but is saccharified together with the cellulose and separated into the solution side, and the remaining solid is the second-generation ethanol saccharification residue, or the sugars are not separated but are separated into the solution side as ethanol by fermentation, and the remaining solid is the second-generation ethanol fermentation residue. Second-generation ethanol saccharification residue is composed mainly of lignin and contains decomposed organic matter, catalysts, enzymes, ash, cellulose, etc. Second-generation ethanol fermentation residue is composed mainly of lignin and contains decomposed organic matter, catalysts, enzymes, yeast, ash, cellulose, etc.

[0019] More specific examples of the embodiment of the production method of the present invention are shown in the examples described later, but for example, they are as follows. One or more of second-generation ethanol saccharification residue and second-generation ethanol fermentation residue are used as raw materials, and a solvent and an aromatic compound are added. After continuing heating for about 2 to 4 hours, the heated liquid contains insoluble matter, so it is filtered while hot using No. 2 filter paper. The filtered solid is unreacted matter and inorganic impurities. The filtrate is distilled under reduced pressure to remove the solvent and unreacted aromatic compounds. Aromatic compounds that cannot be completely removed by distillation are removed by vacuum drying, or by dissolving them in acetone as necessary and repeating reprecipitation with water, which is a poor solvent. The separated solid is a lignin derivative that has already been modified. If the aromatic compounds remaining during distillation do not cause problems in subsequent reactions, they can be used as plastic materials as they are.

[0020] Furthermore, as the polyphenol-containing composition used as the raw material, lignin separated from non-edible plant biomass by treatment such as organosolv method, hot water pressurization method, steam explosion method, ammonia treatment method, ammonia explosion method, acid treatment method, alkali treatment method, oxidative decomposition method, thermal decomposition, microwave heating method, etc. can also be used. Specifically, for example, lignin contained in non-edible plant biomass can be dissolved in a solvent by treatment at high temperature using an organic solvent or a solvent containing an organic solvent and water, and the lignin-containing solution can be filtered to remove cellulose, etc., and then the solution can be concentrated and dried to obtain separated lignin.

[0021] <Aromatic compounds> The aromatic compound having an ortho-para orienting group (hereinafter, sometimes simply referred to as "aromatic compound") may be any aromatic compound having one or more ortho-para orienting groups. The ortho-para directing group is an electron donating substituent, and examples of the functional group include a hydroxyl group, a methoxy group, an aliphatic hydrocarbon group, an amino group, a halogen group, etc., and is preferably a hydroxyl group. That is, the aromatic compound is preferably a phenol compound. In addition, the aromatic compound has a hydrogen atom at least in one of the 2-, 4- and 6-positions, which are the positions of the substituents relative to the ortho-para directing group, and preferably includes those represented by the following formula (A).

[0022] [ka]

[0023] In the above formula (A), W is an ortho-para directing group, and R 1 and R 2 each independently represents a hydrogen atom, a hydroxyl group, or an alkyl group having 1 to 15 carbon atoms; R 1 and R 2 may be the same or different. The alkyl group having 1 to 15 carbon atoms may be linear or branched. The alkyl group having 1 to 15 carbon atoms is preferably a linear or branched alkyl group having 1 to 15 carbon atoms, more preferably a linear or branched alkyl group having 1 to 5 carbon atoms, and further preferably a linear alkyl group having 1 to 3 carbon atoms. Examples of the aromatic compound represented by the above formula (A) include phenol, anisole, toluene, ethylbenzene, n-propylbenzene, isopropylbenzene, n-butylbenzene, isobutylbenzene, t-butylbenzene, aniline, -methylaniline, N,N-dimethylaniline, chlorobenzene, m-cresol, p-cresol, o-cresol, m-methoxyphenol, m-xylene, 1,3-diethylbenzene, 3-methylaniline, 3-methyl-N-methylaniline, 3-methyl-N,N-dimethylaniline, m-dichlorobenzene, m-chlorotoluene, 3,5-dimethylphenol, 3,5-dimethylanisole, mesitylene, 3,5-dimethylaniline, 3,5-dimethyl-N-methylaniline, 3,5-dimethyl-N,N-dimethylaniline, 3-chloro-m-xylene, and 3,5-dichlorotoluene.

[0024] [Phenol compounds] As described above, the aromatic compound is preferably a phenol compound in which the ortho-para directing group is a hydroxyl group. The phenol compound is preferably a phenol compound in which at least one of the 2-, 4- and 6-positions, which are the positions of the substituents relative to the hydroxyl group, is a hydrogen atom. The phenolic compound having hydrogen atoms at the 2-, 4-, and 6-positions (i.e., ortho- and para-positions) is particularly suitable as a recipient of a substituent in a substitution reaction with lignin due to its orientation. The reason for this is that by mixing a polyphenol-containing composition and a phenolic compound in a solvent, the R 3 and R 4This is because the substituent of R of the lignin is transferred to the 2-position, 4-position, or 6-position of the phenol compound. 3 or R 4 Alternatively, both may be hydrogen atoms, resulting in a lignin derivative having an increased number of the above-mentioned reaction sites. Therefore, the substitution reaction reduces the S-type skeleton in lignin and increases the G-type and H-type skeletons, improving reactivity. As described above, the substitution reaction also modifies the molecular chain of lignin, reducing the molecular weight and improving the mixability of the lignin derivative. The phenol compounds may be used alone or in combination of two or more.

[0025] The phenol compound is preferably a compound represented by the following formula (1) in which W in the above formula (A) is a hydroxyl group. By using such a phenol compound, there are at least three places to accept the above-mentioned substituents, so that the substitution reaction can proceed smoothly.

[0026] [ka]

[0027] In the above formula (1), R 1 and R 2 is R in the above formula (A). 1 and R 2 is synonymous with. Examples of the phenol compound represented by the above formula (1) include 3-alkylphenols such as phenol, resorcinol, phloroglucinol, m-cresol, 3-ethylphenol, and 3-propylphenol; 5-alkylresorcinols such as 5-methylresorcinol, 5-ethylresorcinol, and 5-propylresorcinol; and 3,5-dialkylphenols such as 3,5-dimethylphenol, 3-methyl-5-ethyl-phenol, and 3,5-diethylphenol.

[0028] In addition, since the phenolic compound has multiple hydroxyl groups, the acidity of the compound increases, and it is expected that the reaction will proceed without the need for a catalyst. 1 and R 2 A phenol compound in which at least one of the groups is a hydroxyl group can be used. Specific examples of such a phenol compound include resorcinol, phloroglucinol, and 5-alkylresorcinol (5-methylresorcinol, 5-ethylresorcinol, etc.).

[0029] <solvent> The reaction of the polyphenol-containing composition with the aromatic compound is carried out in a solvent. The polyphenol in the polyphenol-containing composition reacts with aromatic compounds, and if no solvent is used in the reaction, the reaction proceeds, but the amount of aromatic compounds used is greater than that of the reaction using a solvent.In addition, the solubility of polyphenol is increased by using a solvent, so the reaction proceeds favorably, and even if the amount of aromatic compounds used is relatively small, there is no risk of extremely decreasing the yield, and a certain yield or more can be achieved, which is also preferable from the viewpoint of economic efficiency.

[0030] The solvent preferably contains a polar solvent from the viewpoint of increasing the solubility of polyphenols such as lignin in the raw material. In addition, the solvent preferably contains at least one of alcohols, ketones, ethers, aromatics, and water from the viewpoint of the solubility of polyphenols such as lignin in the raw material and economic efficiency. Specifically, these solvents are at least one of alcohols such as methanol, ethanol, and isopropyl alcohol, ketones such as acetone and methyl ethyl ketone, ethers such as tetrahydrofuran, organic solvents such as aromatics, and water. The organic solvent preferably has 1 to 6 carbon atoms, more preferably 1 to 4 carbon atoms, and even more preferably 1 to 3 carbon atoms, so that the softening point is not too high and can be easily adjusted to a suitable range, and from the viewpoints of solubility of polyphenols such as lignin and economic efficiency.

[0031] Among the above solvents, from the viewpoints of low softening point, high yield and economic efficiency of polyphenol derivatives such as lignin derivatives, it is preferable to use at least one of ethanol, acetone and water, more preferably at least one of ethanol and water, and even more preferably to use ethanol or a combination of ethanol and water. In particular, a high yield can be expected by using water and an organic solvent in combination as a solvent. When an organic solvent and water are used in combination, from the viewpoints of a low softening point, high yield, and economic efficiency of a polyphenol derivative such as a lignin derivative, the mass ratio [organic solvent:water] is preferably 95:5 to 5:95, more preferably 95:5 to 20:80, even more preferably 95:5 to 30:70, even more preferably 95:5 to 40:60, even more preferably 95:5 to 50:50, and even more preferably 90:10 to 50:50.

[0032] In addition, the aromatic compound can be used in an amount of 4 to 95% by mass based on the total amount of the aromatic compound and the solvent. If the amount of the aromatic compound used exceeds 95% by mass, the molecular weight decreases, the strength decreases, and the economic efficiency decreases. If the amount of the aromatic compound used is 4% by mass or more, the softening point of the polyphenol derivative such as a lignin derivative does not become too high, and the compatibility with the resin becomes good, so there is no risk of causing a decrease in yield. Furthermore, if the amount of the aromatic compound used is 4% by mass or more, it is expected that the reaction between the polyphenol-containing composition and the aromatic compound having an ortho-para orientation group in the solvent will proceed effectively. From the viewpoint of economic efficiency, the amount of the aromatic compound used is preferably 10 to 70% by mass, more preferably 10 to 50% by mass, and even more preferably 20 to 40% by mass.

[0033] Mass ratio [aromatic compounds / lignin] In the production method of the present invention, the mass ratio of aromatic compounds to polyphenols such as lignin in the polyphenol-containing composition [aromatic compounds / polyphenols such as lignin] may usually be about 0.1 to 15. From the viewpoints of economic efficiency and of smoothly proceeding with the above-mentioned substitution reaction, the above mass ratio is preferably 0.1 to 10, more preferably 0.1 to 5, even more preferably 0.1 to 4, even more preferably 0.1 to 3, even more preferably 0.1 to 2, even more preferably 0.1 to 1, even more preferably 0.1 to 0.7, and even more preferably 0.1 to 0.5.

[0034] <Acid catalyst> In the production method of the present invention, the reaction between the polyphenol-containing composition and the aromatic compound is preferably carried out without a catalyst or in the presence of an acid catalyst, preferably from more than 0 to 5.0 mass%, and more preferably from 0.1 to 3.0 mass%, of the total amount of polyphenols such as lignin and aromatic compounds in the polyphenol-containing composition. As described above, the reaction can proceed without a catalyst depending on the aromatic compound used in the reaction. By proceeding without a catalyst, for example, it is possible to omit post-treatment (purification process) after the reaction process, and it is expected that the physical properties such as bending strength of molded products using the obtained polyphenol derivative as a plastic material will be improved.

[0035] Examples of the acid catalyst include inorganic acids such as phosphoric acid, phosphoric acid esters, hydrochloric acid, sulfuric acid, and sulfuric acid esters, and organic acids such as acetic acid, formic acid, oxalic acid, and p-toluenesulfonic acid. One or more types of acid catalysts may be used in combination. When an acid catalyst is used in the above reaction, the amount of the acid catalyst used is not particularly limited as long as it is more than 0 relative to the total amount of polyphenols such as lignin and aromatic compounds in the polyphenol-containing composition, but the effect of adding the acid catalyst can be exhibited well, and the reaction is usually carried out in the presence of 0.01 to 5.0 mass% of the acid catalyst from the viewpoint of impurities remaining in the polyphenol derivative, preferably 0.1 to 3.0 mass%, more preferably 0.2 to 3.0 mass%, and even more preferably 0.2 to 2.6 mass%. If the amount of the acid catalyst used is within the above range, the above reaction can be smoothly promoted. If the amount of the acid catalyst used exceeds the above range, the hydrolysis of cellulose, hemicellulose, etc. contained in the biomass and biomass residue as the polyphenol-containing composition proceeds, and the concentration of sulfate radicals increases, and the cost of purification may increase due to the increase in impurities.

[0036] <Reaction temperature and time> The reaction temperature is not particularly limited as long as it is usually 100° C. or higher, but is usually about 140° C. or higher and 350° C. or lower, preferably 140° C. or higher and 300° C. or lower, more preferably 140° C. or higher and 270° C. or lower, even more preferably 140° C. or higher and 250° C. or lower, even more preferably 150 to 230° C., and even more preferably 180 to 230° C. If it is above 140° C., the lignin derivative can be dissolved to allow the reaction to proceed, and if it is 300° C. or lower, the progress of the reverse reaction can be prevented. The reaction time is usually about 0.1 to 15 hours, but from the viewpoint of allowing the reaction to proceed sufficiently and modifying the polyphenols, it is preferably 0.5 hours or more, and more preferably 1 hour or more. Also, from the viewpoint that the reaction cannot be expected to proceed if the reaction time is too long, the upper limit is preferably 10 hours or less, more preferably 1 hour or more and 8 hours or less, and even more preferably 2 hours or more and 8 hours or less.

[0037] <Reaction pressure> The reaction pressure is not particularly limited as long as it is usually 0.05 MPa or more, but is usually preferably about 0.1 MPa or more and 30 MPa or less. However, the preferred range of the pressure of the reaction system may be appropriately set since it is affected by the amount of the solvent and the temperature. The reaction may be carried out under ambient atmosphere. It is particularly preferable to carry out the reaction under an atmosphere in which oxygen has been reduced by nitrogen purging in order to suppress polymerization due to oxidation reaction. The reaction method in the reaction is not particularly limited, but examples include stationary or stirring treatment. For example, a general batch reactor or semi-batch reactor can be used. In addition, a method in which a slurry consisting of biomass, biomass residue, and a solvent is extruded with a screw or pump can also be applied.

[0038] ≪Refining process≫ The polyphenol derivative of the present invention is produced by carrying out the above-mentioned reaction process. Therefore, the lignin derivative produced by the method for producing a polyphenol derivative through the reaction process can be used as a plastic material as it is, but a purification process may be carried out after the reaction process. For example, the method for producing a polyphenol derivative preferably further includes a solid-liquid separation process in addition to the above-mentioned reaction process. <Solid-liquid separation> After the above reaction, the polyphenol derivative is dissolved in the solvent and aromatic compound, but unreacted substances and inorganic residues are present in the liquid as solids. These are preferably removed by filtration (hot). For example, the reaction liquid is placed in a pressure (hot) filter equipped with filter paper such as No. 5C or No. 2, and pressure-filtered at about 20 to 100°C, about 20 to 70°C, usually about 20 to 50°C, and about 0.1 to 0.99 MPa, usually about 0.1 to 0.4 MPa. The filtered solid may be diluted and / or washed with a suitable solvent and filtered. In this filtration, the polyphenol derivative is contained in the filtrate. In addition, for example, the reaction product liquid may be diluted and / or washed with any one or more of low-boiling point general-purpose solvents such as water, ketones such as acetone and methyl ethyl ketone, alcohols such as methanol, ethanol, and isopropyl alcohol, and ethers such as tetrahydrofuran, and separated into solid and liquid. In this solid-liquid separation, the polyphenol derivative is contained in the solution. The method for performing solid-liquid separation is not particularly limited, but examples thereof include filtration, a filter press, centrifugation, and a dehydrator. <distillation> The distillation can be carried out, for example, by distilling the solution containing the polyphenol derivative under reduced pressure at a temperature of about 40 to 200°C, usually about 50 to 150°C, and a reduced pressure of about 3 to 20 kPa, usually about 5 to 10 kPa, to remove the solvent and aromatic compounds. In this distillation, the polyphenol derivative is obtained as a solid. In addition, for example, when using other dilution solvents, the distillation can be carried out by removing the low-boiling point general-purpose solvent by reduced pressure distillation at an appropriate temperature taking into account the boiling point of the solvent, and then removing the aromatic compounds by the same method as above. In this distillation, the polyphenol derivative is obtained as a solid. <Drying under reduced pressure> The polyphenol derivative obtained by distillation may be purified by removing the aromatic compounds after the reaction by heating it to usually 50 to 200° C. and drying it in a solid or molten state under vacuum. Alternatively, the polyphenol derivative in a heated fluid state after distillation may be similarly dried under vacuum to remove the aromatic compounds after the reaction. <Reprecipitation> When aromatic compounds remain in the polyphenol derivative obtained by distillation or drying under reduced pressure, the polyphenol derivative obtained by the distillation may be further dissolved in a solvent such as acetone, and reprecipitated by adding ion-exchanged water, which is a poor solvent for the polyphenol derivative, to remove the aromatic compounds after the reaction and purify the polyphenol derivative. In the purification step, the above-mentioned filtration, distillation, evaporation to dryness under reduced pressure, and reprecipitation may be repeated, or any one or two or more of them may be combined. The amount of aromatic compounds remaining in the polyphenol derivative is not particularly limited, but is usually less than 30%, preferably less than 10%, more preferably less than 5%, and even more preferably less than 1%.

[0039] [Polyphenol derivatives] The polyphenol derivative of the present invention is not limited in its production method as long as the effects of the present invention are not impaired, but it is preferable that the polyphenol derivative is produced by the above-mentioned production method of a polyphenol derivative. As described above, lignin may have an H-type skeleton, a G-type skeleton, or an S-type skeleton. 31 The ratio of the sum of the relative abundance rate H (%) of the H-type skeleton to the relative abundance rate S (%) of the S-type skeleton determined from the integral value measured by P-NMR and the relative abundance rate G (%) of the G-type skeleton [(2H+G) / S] can be 2.3 or more, 31 The ratio of aliphatic hydroxyl groups to the total ratio of aliphatic hydroxyl groups and aromatic hydroxyl groups determined from the integral value measured by P-NMR can be less than 27%. If the ratio [(2H+G) / S] is 2.3 or more, the reactivity with existing plastic materials tends to be good. Similarly, if the ratio of aliphatic hydroxyl groups is less than 27%, the reactivity with existing plastic materials tends to be good.

[0040] In addition, from the viewpoint of further improving the reactivity of the polyphenol derivative and expecting to give a molded product with improved physical properties such as bending strength, the above ratio [(2H+G) / S] is preferably 2.4 or more, more preferably 2.5 or more, and even more preferably 2.6 or more. The upper limit of the above ratio [(2H+G) / S] is not limited as long as it does not impair the effects of the present invention, but from the viewpoint of productivity, it is preferably 10.0 or less, more preferably 7.0 or less, and even more preferably 5.0 or less. In addition, from the same viewpoint, the above abundance ratio of aliphatic hydroxyl groups is preferably less than 25%, more preferably less than 23%, even more preferably less than 20%, and the closer to 0%, the more preferable.

[0041] The relative abundance of S-type skeleton, H-type skeleton, and G-type skeleton and the amount of aliphatic hydroxyl groups are as follows: 31 This is a value calculated from the integral value measured by P-NMR. 31 More details about the P-NMR measurement are as described in MAGNETIC RESONANCE IN CHEMISTRY, VOL. 33, 375-382 (1995). In the present invention, more specifically, the measurement can be performed by the method described in the examples below.

[0042] <Molecular weight and softening point> The polyphenol derivative of the present invention can be obtained by the above-mentioned substitution reaction. 3 and R 4 In this way, by reducing the molecular weight of lignin, it is possible to efficiently extract polyphenol derivatives, improve the mixability (kneadability or stirrability) with other resin materials, and provide molded products with improved physical properties such as bending strength. Furthermore, since the polyphenol derivative of the present invention has an aromatic compound inserted at the substitution site, the softening point does not decrease significantly even if the molecular weight is reduced. Therefore, the polyphenol derivative of the present invention can have a softening point of preferably 90° C. or higher, more preferably 130° C. or higher, and even more preferably 150° C. or higher. If the softening point is 90° C. or higher, defects such as swelling are unlikely to occur during molding and post-curing of the resin composition material containing the polyphenol derivative. In addition, the softening point of the polyphenol derivative is preferably 210° C. or lower, more preferably 200° C. or lower, even more preferably 190° C. or lower, even more preferably 180° C. or lower, and even more preferably 160° C. or lower. If the softening point is 210° C. or lower, the resin composition material containing the polyphenol derivative becomes easier to handle.

[0043] Moreover, the polyphenol derivative of the present invention has a weight average molecular weight of less than 5000, and the abundance ratio of molecular weights LogM of 2.15 to 2.20 is less than 0.7% by mass. If the weight-average molecular weight of the polyphenol derivative is 5,000 or more, it becomes difficult to improve the physical properties such as bending strength of the molded article. The weight average molecular weight of the polyphenol derivative is preferably 3,000 or more and 4,000 or less, the weight average molecular weight is preferably 2,000 or more and less than 3,000, the weight average molecular weight is preferably 1,000 or more and less than 2,000, and the weight average molecular weight is preferably 600 or more and less than 1,000. Furthermore, if the proportion of polyphenol derivatives with a molecular weight LogM of 2.15 to 2.20 is 0.7% by mass or more, problems such as blistering may occur during molding and post-curing of a resin composition material containing the polyphenol derivative. The proportion of polyphenol derivatives with a molecular weight LogM of 2.15 to 2.20 is preferably 0.5% by mass or less, more preferably 0.25% by mass or less, and the lower the proportion, the better.

[0044] The polyphenol derivative of the present invention can also be used, for example, If the weight average molecular weight is 3,000 or more and 4,000 or less, the softening point is preferably 140° C. or more and 210° C. or less. If the weight average molecular weight is 2,000 or more and less than 3,000, the softening point is preferably 120° C. or more and 190° C. or less. If the weight average molecular weight is 1,000 or more and less than 2,000, the softening point is preferably 100° C. or more and 170° C. or less. If the weight average molecular weight is 600 or more and less than 1,000, the softening point is preferably 90°C or more and 170°C or less. These can be used depending on the properties of the existing plastic material to be reacted, and it is expected that improving the mixability will increase the reactivity of the polyphenol derivatives, resulting in molded products with improved physical properties such as bending strength. The weight average molecular weight can be measured by the method described in the Examples section below.

[0045] Furthermore, by the method for producing a polyphenol derivative of the present invention, of the lignin content contained in the second-generation ethanol fermentation residue or the second-generation ethanol saccharification residue, it is preferable that 50 mass% or more is extracted as a polyphenol derivative, more preferably 60 mass% or more is extracted as a polyphenol derivative, even more preferably 70 mass% or more is extracted as a polyphenol derivative, even more preferably 80 mass% or more is extracted as a polyphenol derivative, and even more preferably 90 mass% or more is extracted as a polyphenol derivative. The method for calculating the polyphenol content in the second-generation ethanol fermentation residue and the second-generation ethanol saccharification residue will be specifically explained in the Examples below.

[0046] [Polyphenol derivative-containing resin composition materials and molded products] The present invention also provides a polyphenol derivative-containing material, particularly a polyphenol derivative-containing resin composition material, containing one or more of the polyphenol derivatives produced by the above-mentioned polyphenol derivative production method and the above-mentioned polyphenol derivatives, and a molded product using the same. The polyphenol derivative-containing resin composition material may contain one or more resin components such as thermosetting resins and thermoplastic resins, aldehydes, etc., in addition to the polyphenol derivative obtained by the above-mentioned production method. The components other than the polyphenol derivative are described below. (thermosetting resin) The polyphenol derivative-containing resin composition material may further contain a thermosetting resin. Examples of the thermosetting resin include other general thermosetting resins such as phenolic resins, epoxy resins, polyurethane resins, melamine resins, urea resins, unsaturated polyester resins, silicone resins, and alkyd resins. Among these, phenolic resins are preferred because they have a phenolic hydroxyl group like polyphenol derivatives, can react with polyphenol derivatives, and can be used as a diluent for polyphenol derivatives. Among phenolic resins, novolac-based phenolic resins and resol-based phenolic resins are more preferred. These thermosetting resins may be used alone or in combination of two or more.

[0047] The content of the thermosetting resin in the polyphenol derivative-containing plastic material may be determined according to the purpose, but from the viewpoint of obtaining good physical properties and moldability, it is preferably 100 to 300 parts by mass, more preferably 150 to 250 parts by mass, per 100 parts by mass of the polyphenol derivative.

[0048] (Aldehydes) The polyphenol derivative-containing resin composition material may further contain aldehydes. A polyphenol derivative-containing resin composition material containing a polyphenol derivative and an aldehyde can be used to form a self-curing molding material. Examples of aldehydes include formaldehyde, paraformaldehyde, acetaldehyde, propionaldehyde, furfural, benzaldehyde, phenylacetaldehyde, salicylaldehyde, and the like, and among these, formaldehyde is preferred.

[0049] The molar ratio of the phenol group to formaldehyde contained in the polyphenol derivative [formaldehyde / phenol group] is preferably 1.0 to 2.5, more preferably 1.2 to 2.0. If the molar ratio is within the above range, there is no risk of a decrease in the curing rate during the reaction. From the viewpoint of accelerating the curing reaction between the polyphenol derivative and the aldehyde, it is preferable to use an alkali, such as sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, ammonia, tetramethylammonium hydroxide, or an alkylamine. There are no limitations on the temperature and reaction time during the curing reaction of the polyphenol derivative and the aldehydes, but the temperature is usually about 60 to 130° C., and the reaction time is usually about 0.5 to 5 hours. The polyphenol derivative-containing resin composition material may further contain one or more selected from the group consisting of thermosetting resins and aldehydes.

[0050] (Filler) The polyphenol derivative-containing resin composition material may further contain a filler, which may be an inorganic filler or an organic filler. Examples of inorganic fillers include spherical or crushed fused silica, silica powder such as crystalline silica, alumina powder, glass powder, glass fiber, glass flake, mica, talc, calcium carbonate, alumina, hydrated alumina, boron nitride, aluminum nitride, silicon nitride, silicon carbide, titanium nitride, zinc oxide, tungsten carbide, magnesium oxide, and the like. Examples of organic fillers include carbon fiber, aramid fiber, paper powder, wood powder, cellulose fiber, cellulose powder, rice husk powder, fruit shell / nut powder, chitin powder, and starch.

[0051] The inorganic filler and the organic filler may be used alone or in combination of two or more, and the content is determined according to the purpose. When the inorganic filler and / or the organic filler are contained, it is desirable that the content of the inorganic filler and / or the organic filler is appropriate in order to obtain good physical properties and moldability. From this viewpoint, the content of the inorganic filler and / or the organic filler is preferably 50 to 200 parts by mass, more preferably 80 to 150 parts by mass, based on 100 parts by mass of the polyphenol derivative.

[0052] (hardening agent) The polyphenol derivative-containing resin composition material may further contain a hardener. Examples of the curing agent include hexamethylenetetramine, hexaformaldehyde, paraformaldehyde, etc. These may be used alone or in combination of two or more kinds. In addition to the curing agent, in order to further increase the curing speed and degree of curing, inorganic bases such as calcium hydroxide, sodium hydroxide, potassium hydroxide, calcium oxide, and magnesium oxide, Lewis acids such as zinc chloride and zinc acetate, and catalysts such as triethylamine may be used. These may be used alone or in combination of two or more.

[0053] (Other additives) Various additives can be added to the polyphenol derivative-containing resin composition according to the present embodiment within the range that does not impair the properties of the molded product obtained from the resin composition. In addition, a compatibilizer, a surfactant, etc. can be further added depending on the purpose. As the compatibilizer, a resin obtained by adding maleic anhydride or epoxy to a thermoplastic resin to introduce a polar group, such as a maleic anhydride-modified polyethylene resin or a maleic anhydride-modified polypropylene resin, or various commercially available compatibilizers may be used in combination. Examples of surfactants include, but are not limited to, straight-chain fatty acids such as stearic acid, palmitic acid, and oleic acid, and branched or cyclic fatty acids with rosins. In addition to the above, other additives that can be added include flexibilizers, heat stabilizers, ultraviolet absorbers, flame retardants, antistatic agents, antifoaming agents, thixotropic agents, release agents, antioxidants, plasticizers, stress reducing agents, coupling agents, dyes, light scattering agents, small amounts of thermoplastic resins, etc. These may be used alone or in combination of two or more.

[0054] (thermoplastic resin) Thermoplastic resins that can be blended into the polyphenol derivative-containing resin composition material are preferably amorphous thermoplastic resins having a glass transition temperature of 200°C or lower, or crystalline thermoplastic resins having a melting point of 200°C or lower. Examples of thermoplastic resins include polycarbonate resins, styrene resins, polystyrene elastomers, polyethylene resins, polypropylene resins, polyacrylic resins (polymethyl methacrylate resin, etc.), polyvinyl chloride resins, cellulose acetate resins, polyamide resins, low-melting-point polyester resins (PET, PBT, etc.) typified by polyesters formed from combinations of terephthalic acid and ethylene glycol, and terephthalic acid and 1,4-butanediol, polylactic acid and / or copolymers containing polylactic acid, acrylonitrile-butadiene-styrene resins (ABS resins), polyphenylene oxide resins (PPO), polyketone resins, polysulfone resins, polyphenylene sulfide resins (PPS), fluororesins, silicone resins, polyimide resins, polybenzimidazole resins, polyamide elastomers, and copolymers of these with other monomers.

[0055] When using a polyphenol derivative as an additive for a thermoplastic resin, for example, a conventionally known method such as those described in JP 2014-15579 A, ​​WO 2016 / 104634 A, etc. can be used. From the viewpoint of obtaining remarkable fluidity and strength, the content of the thermoplastic resin in the polyphenol derivative resin composition material is preferably 30% by mass or more and 99.9% by mass or less, more preferably 40% by mass or more and 99.9% by mass or less, even more preferably 45% by mass or more and 99.9% by mass or less, and particularly preferably 50% by mass or more and 99.9% by mass or less, based on the total amount of the resin composition material. The polyphenol derivative-containing resin composition material may contain, in addition to the above-mentioned thermoplastic resin, a resin, an additive, and a filler that are compatible with the resin composition material.

[0056] (Mixing and molding) The components used in the polyphenol derivative-containing resin composition material can be blended and kneaded by premixing them in a commonly used device, such as a ribbon blender or drum tumbler, and then using a Henschel mixer, Banbury mixer, single screw extruder, twin screw extruder, multi-screw extruder, roll kneader, co-kneader, etc. The heating temperature during kneading is usually appropriately selected within the range of 100 to 300°C. The method of molding the polyphenol derivative-containing resin composition material is not particularly limited. For example, press molding, injection molding, transfer molding, medium-sized molding, FRP molding, etc. can be mentioned. In addition, when the resin composition material is a thermoplastic resin composition material, the method of molding into a predetermined shape can be extrusion molding, injection molding, etc.

[0057] Examples of molded products using polyphenol derivative-containing resin compositions include those obtained by curing resin compositions containing polyphenol derivatives and curing agents, those further containing various fillers or industrially obtained general phenol resins as necessary, and molding them into a predetermined shape and then curing them, or those molded after curing, and those molded resin compositions obtained by mixing polyphenol derivatives with thermoplastic resins, etc. Examples of molded products using such polyphenol derivative-containing resin compositions include insulation materials for housing, electronic parts, resins for frac sand, resins for coated sand, resins for impregnation, resins for lamination, resins for FRP molding, automobile parts, reinforcing materials for automobile tires, office automation equipment, machinery, information and communication equipment, industrial materials, etc.

[0058] Polyphenol derivatives can be used in polyphenol derivative-containing materials other than resin composition materials. Examples of polyphenol derivative-containing materials other than resin composition materials include carbon materials such as carbon black and carbon fiber, lubricants such as grease base materials, foods and cosmetics with antioxidant and antibacterial properties, cement additives, concrete additives, binders, rubber compositions, packaging materials such as gas barrier films, agricultural materials such as plant activators and soil conditioners, inks and toners, adhesives, surfactants, ultraviolet absorbers, storage battery electrode materials, growth promoters for marine organisms, and food discoloration inhibitors. EXAMPLES

[0059] The present invention will be specifically described below with reference to examples and comparative examples, but the present invention is not limited to these.

[0060] <Calculation of lignin content in second-generation ethanol saccharification residue (raw material)> The lignin content in the biomass residue used in the examples was calculated by analyzing the constituent sugars after pretreatment as described below. [Preprocessing] As a pretreatment, the raw material was pulverized using a Willey mill and dried at 105°C to prepare samples. [Constituent sugar analysis] An appropriate amount of the above sample was weighed out, 72% by mass sulfuric acid was added, and the mixture was left at 30°C for 1 hour while stirring from time to time. The reaction solution was transferred completely to a pressure bottle while being mixed with pure water, and treated in an autoclave at 120°C for 1 hour, after which the filtrate and the residue were separated by filtration. The monosaccharides in the filtrate were quantified by high performance liquid chromatography. C6 polysaccharides (mainly glucan) were defined as cellulose, and C5 polysaccharides (mainly xylan) were defined as hemicellulose. [Lignin] The residue obtained by filtration during the sugar content analysis was dried at 105°C and weighed to calculate the decomposition residue rate. Furthermore, the lignin content was calculated by correcting for the ash content.

[0061] <Properties of lignin derivatives and lignin in raw materials> In addition, the lignin derivatives obtained in each example or the lignin in the raw material were subjected to various measurements by the following methods. [Molecular weight measurement] The weight average molecular weight (Mw) of the lignin derivatives obtained in each example and the lignin in the raw material was determined in terms of standard polystyrene by GPC (gel permeation chromatography) using the following measuring device and conditions. Separation column: 2 columns of TSKgel SuperMultiporeHZ-M manufactured by Tosoh Corporation Eluent: Tetrahydrofuran ·Eluent flow rate: 1.0mL / min Detector: Index of Refraction (RI) ·Measurement temperature: 40℃

[0062] [Ratio of molecular weight LogM2.15~2.20 components] From the chart of the molecular weight of lignin obtained by GPC (gel permeation chromatography) (y-axis is plotted as dw / dLogM, x-axis is plotted as LogM), the positions where the existence of peaks was predicted (LogM) were found for peak tops or shoulder peaks, and each was taken as the average (A) of the Gaussian function. In addition, the variance (S) value and an arbitrary number (X) were set as the probability of existence for each Gaussian function. The number of Gaussian functions prepared was the number of predicted peaks or shoulders (N), and three variables, A, S, and X, were given to each. The correlation coefficient R was calculated from the composite function (linear sum) of N Gaussian functions and the y-axis of the GPC chart: dw / dLogM. 2 Calculate R 2 The three variables A, S, and X of each Gaussian function were manipulated so that the maximum value was set. Specifically, this was done using a spreadsheet software such as Excel. Here, R 2 It is necessary to manipulate A, S, and X of each function appropriately so that the value is at least 0.9999 or more. By performing this manipulation, the ratio of the composite function of multiple Gaussian functions present in the molecular weight range of LogM2.15 to 2.20 to the composite of all Gaussian functions was determined as the abundance ratio of the molecular weight LogM2.15 to 2.20 component.

[0063] [Softening point (℃)] The lignin derivative or raw material (solid sample) obtained in each example was crushed in a mortar and sieved (40 mesh) to remove large particles, and the crushed sample was placed in an aluminum cup (circular upper φ60, lower φ53 × depth 15 mm) in an amount of 10 to 20 mg. The aluminum cup containing the sample was placed on a hot plate (ASONE ND-2A) and covered with a glass plate (thickness 0.5 mm). After heating to 80 °C, the temperature was increased in 10 °C increments, and visual observation was made through the glass. The temperature at which the sample melted was taken as the softening point.

[0064] [Relative abundance of basic structure (%) and hydroxyl group ratio (%)] (1) A mixture of deuterated chloroform, pyridine, and cyclohexanol (internal standard) was added to the lignin derivative or raw material (solid sample) obtained in each example, and 2-chloro-4,4,5,5-tetramethyl-1,3,2-dioxaphospholane was added as a derivatization reagent, followed by heating at 50°C for 1 hour. 31 P-NMR measurements were carried out. In addition, since the comparative raw material lignin 2 does not dissolve completely in the solvent, only the soluble portion was measured. The measurement apparatus and conditions are as follows. Pulse width: 30° Repeat time: 2 seconds Measurement range: -60~200ppm -Number of times: 200 The signal derived from cyclohexanol, the internal standard, was set at 145.2 ppm, 144.0 to 142.0 ppm was identified as the S-type skeleton, and 141.0 to 136.6 ppm was identified as the G-type skeleton, and the relative abundance percentage of each basic skeleton was calculated from the integral value. The relative abundance percentage of the H-type skeleton was calculated by subtracting the relative abundance percentages of the S-type skeleton and the G-type skeleton from the total amount of aromatic hydroxyl groups. Furthermore, 150.0 to 145.5 ppm was identified as aliphatic hydroxyl groups, and 144.7 to 136.6 ppm as aromatic hydroxyl groups. The amount of aliphatic hydroxyl groups (mol / g) and the amount of aromatic hydroxyl groups (mol / g) were calculated from the integral curve to determine the percentage of each hydroxyl group. (2) Abundance ratio and reaction point Based on the relative abundance percentage of each basic skeleton above, The ratio of the sum of twice the relative abundance of the H-type skeleton H (%) and the relative abundance of the G-type skeleton G (%) to the relative abundance of the S-type skeleton S (%) [(2H+G) / S], The sum of reaction sites based on the relative abundance of H-type skeletons (H) (%) and the relative abundance of G-type skeletons (G) (2H+G), was calculated.

[0065] [Lignin Derivatives] [Example 1] (1) Reaction process 100.1 parts by mass (100.1 g, 55.0 g as lignin) of second-generation ethanol saccharification residue (lignin content: 55% by mass), 20 parts by mass of phenol, and 200 parts by mass of ethanol were placed in a 1.0 L pressure-resistant vessel capable of stirring, and heated and stirred at 2.6 MPa and 200°C for 4 hours. (2) Purification process (2-1) Filtration A pressure filter incorporating No. 2 filter paper was assembled, and the reaction liquid obtained in the above reaction step was placed in it, pressurized to 0.1 to 0.4 MPa with compressed air or nitrogen, and filtered. (2-2) Distillation The filtrate obtained by filtration was distilled under reduced pressure (5 to 10 kPa) and heated (40 to 60° C.) using an evaporator to remove ethanol and phenol. (2-3) Drying under reduced pressure In order to remove the phenol remaining after the above distillation, the mixture was vacuum-dried under reduced pressure (1.0 to 5.0 kPa) and heating (120 to 150° C.) to remove the phenol, thereby obtaining a lignin derivative 1 (52.9 g). The yield was calculated as the amount of the lignin derivative (30.0 g) relative to the amount of the charged lignin (calculated value 55.0 g) according to the following formula, and was found to be 54%. Yield (%) = [(amount of lignin derivative) / (amount of lignin charged)] x 100

[0066] [Example 2] The same procedure as in Example 1 was carried out except that the amount of phenol was 37 parts by mass and the amount of ethanol was 183 parts by mass, to obtain lignin derivative 2 (amount of lignin derivative: 52.9 g, yield: 96%).

[0067] [Example 3] The same procedure as in Example 1 was carried out except that the amount of phenol was 10 parts by mass and the amount of ethanol was 210 parts by mass, to obtain lignin derivative 3 (amount of lignin derivative: 26.4 g, yield: 48%). [Example 4] The same procedure as in Example 1 was carried out except that the amount of phenol was 51 parts by mass and the amount of ethanol was 169 parts by mass, to obtain lignin derivative 4 (amount of lignin derivative: 52.1 g, yield: 95%). [Example 5] The same procedure as in Example 1 was carried out except that the amount of phenol was 20 parts by mass, the amount of ethanol was 100 parts by mass, and the amount of water was 100 parts by mass, to obtain lignin derivative 5 (amount of lignin derivative: 47.6 g, yield: 86%). [Example 6] The same procedure as in Example 3 was carried out except that the amount of ethanol was 180 parts by mass and the amount of water was 20 parts by mass, to obtain lignin derivative 6 (amount of lignin derivative: 37.3 g, yield: 68%). [Example 7] The same procedure as in Example 3 was carried out except that the amount of ethanol was 160 parts by mass and the amount of water was 40 parts by mass, to obtain lignin derivative 7 (amount of lignin derivative: 39.8 g, yield: 72%). [Example 8] The same procedure as in Example 1 was carried out except that 0.2 parts by mass of sulfuric acid was added and the reaction time was set to 2 hours, to obtain lignin derivative 8 (amount of lignin derivative: 37.8 g, yield: 69%). [Example 9] The same procedure as in Example 1 was repeated except that the amount of phenol was 44 parts by mass, the amount of ethanol was 154 parts by mass, the amount of water was 22 parts by mass, the reaction temperature was 220°C, and the reaction time was 2 hours, to obtain lignin derivative 9 (amount of lignin derivative: 42.4 g, yield: 77%). [Example 10] The same procedure as in Example 9 was carried out except that the reaction temperature was 200° C. and the reaction time was 4 hours, to obtain lignin derivative 10 (amount of lignin derivative: 37.8 g, yield: 69%). [Example 11] The same procedure as in Example 10 was carried out except that 0.2 parts by mass of sulfuric acid was added, to obtain lignin derivative 11 (amount of lignin derivative: 43.6 g, yield: 79%). [Example 12] The same procedure as in Example 10 was carried out except that anisole was used instead of phenol, and lignin derivative 12 (amount of lignin derivative: 36.8 g, yield: 67%) was obtained. [Example 13] The same procedure as in Example 11 was carried out except that anisole was used instead of phenol, and lignin derivative 13 was obtained (amount of lignin derivative: 39.7 g, yield: 72%). [Example 14] The same procedure as in Example 11 was carried out except that phenol was replaced with toluene, and lignin derivative 14 (amount of lignin derivative: 35.1 g, yield: 64%) was obtained. [Example 15] The same procedure as in Example 10 was carried out except that the amount of phenol was 66 parts by mass and the amount of ethanol was 132 parts by mass, to obtain lignin derivative 14 (amount of lignin derivative: 46.3 g, yield: 84%).

[0068] The properties of the lignin derivatives 1 to 15 obtained in the above Examples 1 to 15 were measured by the above-mentioned methods, and the results are shown in Tables 1 and 2. In addition, since a part of the lignin derivative 5 was insoluble in the eluent in the molecular weight measurement, the molecular weight measurement (Mw) of Example 5 was not possible.

[0069] [Comparative Example 1] In Comparative Example 1, the properties of lignin in the raw material, second-generation ethanol saccharification residue, were analyzed. However, since the lignin in the second-generation ethanol saccharification residue is only slightly soluble in various organic solvents, it was not possible to analyze it using the above-mentioned method. [Comparative Example 2] Kraft lignin (Lignin,alkali (product number 370959) manufactured by SIGMA-ALDRICH) was used as Comparative Example 2. The properties of the kraft lignin were analyzed, but since the kraft lignin contains many components that are insoluble in various organic solvents, the analysis by the above-mentioned method was only partial. [Comparative Example 3] The same procedure as in Example 8 was carried out except that phenol was not added and the amount of ethanol was 220 parts by mass, to obtain comparative lignin 1 (amount of lignin derivative: 25.9 g, yield: 47%). [Comparative Example 4] The same procedure as in Example 1 was carried out except that phenol was not added, and the amount of ethanol and water were 110 parts by mass, to obtain comparative lignin 2 (amount of lignin derivative: 43.3 g, yield: 79%).

[0070] [Table 1]

[0071] [Table 2]

[0072] As mentioned above, the lower the softening point of the lignin derivative, the easier it tends to be to mix with resin. Furthermore, the lower the amount of aliphatic hydroxyl groups in the lignin derivative, and the higher the ratio [(2H+G) / S], which is an index of reactivity, the easier it tends to react with resin. Furthermore, by having a molecular weight of the lignin derivative that is not too small and has a certain degree of size, the physical properties such as bending strength tend to be good when it is made into a molded product. Considering Tables 1 and 2 from the above viewpoint, a comparison of Examples 1 to 15 with Comparative Examples 3 and 4 shows that the manufacturing method of the present invention can obtain a lignin derivative with a certain yield that has a good compatibility with resins and good reactivity because the molecular weight is not too small and the softening point is 210°C or less. In particular, it can be seen that by adjusting the proportion of aromatic compound used and the selection and proportion of solvent used, it is possible to achieve both a lower softening point and a higher yield. In Comparative Examples 3 and 4, which do not use aromatic compounds, the proportions of components with molecular weights of 50 to 300 are 0.70% by mass and 0.26% by mass, respectively, and it can be seen that there is a risk of problems such as swelling occurring when used as a resin composition material. Therefore, as can be seen from Tables 1 and 2, the lignin derivatives of the Examples were modified in molecular weight and composition, and thus demonstrated to be usable as lignin derivative-containing materials, particularly as resin composition materials. Furthermore, the raw materials, the second-generation ethanol saccharification residue in Comparative Example 1 and the kraft lignin in Comparative Example 2, cannot be used as they are as resin composition materials, whereas the production method of the present invention produces lignin derivatives that can actually be used as resin composition materials.

[0073] [Cured product] Next, using lignin derivatives 2, 6, and 8 of Examples 2, 6, and 8, the second-generation ethanol saccharification residue (comparative raw material lignin 1) of Comparative Example 1, the kraft lignin (comparative raw material lignin 2) of Comparative Example 2, comparative lignin 1 of Comparative Example 3, and comparative lignin 2 of Comparative Example 4, resin composition materials and molded bodies using the same were produced in the following examples. The resin composition and the molded article were evaluated by the following methods. (Easy to mix) In Examples 16 to 18 and Comparative Examples 5 to 8, the ease of kneading was evaluated based on the following index. A: Easy to mix B: Difficult but possible to knead C: Unable to knead

[0074] (stirrability) In Examples 19 to 21 and Comparative Examples 9 to 12, the ease of stirring during the reaction was evaluated based on the following index. A: Easy to stir B: Difficult but possible to mix C: Stirring not possible

[0075] (Bending strength) A sample of 5 mm x 50 mm x 1 mm was cut out from the molded body obtained in each example, and the bending strength was measured using an Instron 5566 manufactured by Instron Japan under conditions of a three-point bending mode, a span of 30 mm, and a speed of 2 mm / min, and evaluated based on the index. A: The sample was less likely to break. B: The sample was broken. C: The sample broke immediately. -:Poor molding

[0076] [Examples 16 to 18] 35 parts by mass of novolac-type phenolic resin (PR-53195, manufactured by Sumitomo Bakelite Co., Ltd.), 50 parts by mass of wood flour, 15 parts by mass of each of the lignin derivatives 2, 6 and 8 of Examples 2, 6 and 8 described above, 7 parts by mass of hexamethylenetetramine as a curing agent, and 1 part by mass of zinc stearate as an internal mold release agent were mixed and kneaded in a two-roll kneader at 110 to 120°C for 3 minutes to obtain a lignin derivative-containing resin composition material. The lignin derivative-containing resin composition material obtained above was pressed into a heated mold cavity and molded by transfer molding at 175°C for 3 minutes, and then cured in an oven at 180°C for 8 hours to obtain a molded product. The results of the evaluation of the resin composition and the molded article are shown in Table 3.

[0077] [Comparative Example 5] A resin composition material and a molded body were obtained in the same manner as in Example 16, except that a second-generation ethanol saccharification residue (comparative raw material lignin 1) was used instead of the lignin derivative. The results of the evaluation of the resin composition and the molded article are shown in Table 3. [Comparative Example 6] A resin composition material and a molded product were obtained in the same manner as in Example 16, except that kraft lignin (comparative raw material lignin 2) was used instead of the lignin derivative. The results of the evaluation of the resin composition and the molded article are shown in Table 3. [Comparative Example 7] A resin composition material and a molded product were obtained in the same manner as in Example 16, except that comparative lignin 1 was used instead of the lignin derivative. [Comparative Example 8] A resin composition material and a molded product were obtained in the same manner as in Example 16, except that comparative lignin 2 was used instead of the lignin derivative. The results of the evaluation of the resin composition and the molded article are shown in Table 3.

[0078] [Table 3]

[0079] [Examples 19 to 21] In a 0.5 L separable flask equipped with a reflux device and a stirring blade, 50 parts by mass (50.0 g) of each of the lignin derivatives 2, 6, and 8 of Examples 2, 6, and 8 above, and 30 parts by mass of a 40% by mass aqueous formaldehyde solution were added and stirred. The molar ratio of formaldehyde to phenol in the lignin derivative was 1.5. While gradually dropping 35 parts by mass of a 50% by mass aqueous sodium carbonate solution, the mixture was heated at 100°C for 2 hours to obtain a liquid composition. Further, 54 parts by mass of wood flour was added and stirred until homogenized to obtain a lignin derivative-containing resin composition material. The lignin derivative-containing resin composition material obtained above was decompressed to remove moisture, and press molded at a surface pressure of 0.2 MPa, 180° C. for 10 minutes, and then cured in an oven at 200° C. for 4 hours to obtain a molded product. The results of the evaluation of the resin composition and the molded article are shown in Table 4.

[0080] [Comparative Example 9] A resin composition material and a molded body were obtained in the same manner as in Example 19, except that a second-generation ethanol saccharification residue (comparative raw material lignin 1) was used instead of the lignin derivative. The results of the evaluation of the resin composition and the molded article are shown in Table 4. [Comparative Example 10] A molded body was obtained in the same manner as in Example 19, except that kraft lignin (comparative raw material lignin 2) was used instead of the lignin derivative. The results of the evaluation of the resin composition and the molded article are shown in Table 4. [Comparative Example 11] A molded body was obtained in the same manner as in Example 19, except that Comparative Lignin 1 was used instead of the lignin derivative. [Comparative Example 12] A molded body was obtained in the same manner as in Example 19, except that comparative lignin 2 was used instead of the lignin derivative. The results of the evaluation of the resin composition and the molded article are shown in Table 4.

[0081] [Table 4]

[0082] In Comparative Examples 7, 8, 11, and 12, which used Comparative Lignin 1 or 2 obtained without reacting with an aromatic compound, the results showed that all of the kneading property, stirrability, and bending strength were not excellent. In contrast, as shown in Tables 3 and 4, the lignin derivative obtained in the present invention has excellent kneading property and stirrability during reaction, which shows that the mixability is improved. In addition, the bending properties of the molded bodies obtained in the examples show that molded bodies with good properties were obtained. It is noted that Comparative Examples 5, 6, 9, and 10 show that it is difficult to use the second generation ethanol saccharification residue and kraft lignin as raw materials as they are as resin composition materials.

[0083] Therefore, as can be seen from Tables 1 to 4, the polyphenol derivative obtained by the production method of the present invention has a low softening point and is excellent in kneading and stirring properties, so that it can be easily mixed with resins, and also has highly reactive reaction sites and excellent bending strength, so that it can easily react with resins. Furthermore, by adjusting the proportion of the aromatic compound used and the selection and proportion of the solvent used, it is possible to achieve both an even lower softening point, high yield, and good economic efficiency. In other words, the polyphenol derivatives obtained by the manufacturing method of the present invention are useful as plastic materials that satisfy the following four conditions: (i) they are inexpensive, (ii) they can be prepared in large quantities, (iii) they can be easily mixed with resins, and (iv) they can easily react with resins. [Industrial Applicability]

[0084] The polyphenol derivative of the present invention has a low molecular weight, which improves its mixability with other plastic materials and increases the number of reaction sites. The improved mixability and increased reaction sites are expected to improve the physical properties of molded products, and the ease of mixing makes it possible to eliminate the need for large-scale equipment that is costly when producing hardened parts. In addition, lignin, which has been almost entirely discarded until now, can be effectively utilized, which is also effective in protecting the environment.

Claims

1. A method for producing a lignin derivative, comprising the steps of reacting a lignin-containing composition with a phenolic compound represented by the following formula (1) in a solvent at a reaction temperature of more than 140° C. and not more than 300° C., for a reaction time of 0.5 hours to 10 hours, and at a reaction pressure of 0.1 MPa to 5.8 MPa: The lignin-containing composition is at least one of a second-generation ethanol saccharification residue and a second-generation ethanol fermentation residue, a mass ratio of the phenol compound to the lignin in the lignin-containing composition [phenol compound / lignin] is 0.1 to 2; the solvent comprises an organic solvent and water; The organic solvent includes one or more selected from methanol, ethanol, and isopropyl alcohol; The method for producing a lignin derivative, wherein the mass ratio of the organic solvent to the water [organic solvent:water] is 95:5 to 50:

50. 【Chemistry 1】 In the formula (1), R １ and R ２ each independently represents a hydrogen atom, a hydroxyl group, or an alkyl group having 1 to 15 carbon atoms, which may be the same or different.

2. The method for producing a lignin derivative according to claim 1, wherein the phenol compound is used in an amount of 10 to 50% by mass based on the total amount of the phenol compound and the solvent.

3. The method for producing a lignin derivative according to claim 1 or 2, wherein a mass ratio of the phenol compound to the lignin in the lignin-containing composition [phenol compound / lignin] is 0.1 to 1.

2.

4. The method for producing a lignin derivative according to any one of claims 1 to 3, wherein the reaction is carried out without a catalyst or in the presence of an acid catalyst in an amount of more than 0 to 5.0 mass% based on the total amount of lignin and the phenolic compound in the lignin-containing composition.

5. The method for producing a lignin derivative according to any one of claims 1 to 4, wherein the reaction is carried out without a catalyst or in the presence of 0.1 to 3.0 mass% of an acid catalyst relative to the total amount of lignin and the phenol compound in the lignin-containing composition.

6. The method for producing a lignin derivative according to any one of claims 1 to 5, wherein the reaction is carried out at a reaction pressure of 0.1 MPa or more and 2.6 MPa or less.

7. The method for producing a lignin derivative according to any one of claims 1 to 6, wherein the reaction is carried out at a reaction temperature of more than 140°C and not more than 250°C.

8. The method for producing a lignin derivative according to any one of claims 1 to 7, wherein the reaction is carried out for a reaction time of 1 hour or more and 8 hours or less.

9. The method for producing a lignin derivative according to any one of claims 1 to 8, further comprising a solid-liquid separation step.

10. A lignin derivative produced by the method for producing a lignin derivative according to any one of claims 1 to 9, The lignin derivative has a weight average molecular weight of less than 5000 and a molecular weight LogM content of 2.15 to 2.20 of less than 0.7% by mass.

11. A lignin derivative-containing material comprising at least one of the lignin derivatives produced by the method for producing a lignin derivative according to any one of claims 1 to 9 and the lignin derivatives according to claim 10.

12. A lignin derivative-containing resin composition material comprising at least one of the lignin derivatives produced by the method for producing a lignin derivative according to any one of claims 1 to 9 and the lignin derivatives according to claim 10.

13. The lignin derivative-containing resin composition material according to claim 12, further comprising at least one of a thermosetting resin and an aldehyde.

14. A molded article comprising at least one of the lignin derivative-containing resin composition materials according to claim 12 and claim 13.

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