JP2008266210A - Method for producing phenolized lignin - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a phenolized lignin containing little impurities and dryable rapidly, through enabling putting a solid fraction extracted by acid treatment to filtration. <P>SOLUTION: The method for producing the phenolized lignin comprises an acid reaction step of treating a grass-woody material by immersing it together with a phenol derivative in an acid solution, a step of neutralizing a solid fraction extracted by the above step with a volatile basic substance, and a step of putting the solid fraction after the neutralization step to filtration. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to a method for producing phenolized lignin for isolating and utilizing lignin from a vegetative material, and more particularly, to a solid component mainly composed of phenolized lignin extracted by immersing the vegetative material in an acid solution together with a phenol derivative. The present invention relates to a method for producing a phenolized lignin that can be filtered after neutralization of a phase component and can be quickly dried.

  Currently, petroleum-derived raw materials and products are widely used in various fields, and synthetic resins are one of them. However, since petroleum is a fossil resource, it is a depleted resource that cannot be reproduced, and the negative impact on the environment after disposal has become a problem. Against this background, attention has been focused on plant-derived raw materials that can be reproduced by being biomass resources and are also friendly to the global environment. For example, if a lignin plant material lignin mainly composed of carbohydrate (carbohydrate) cellulose and resin component lignin can be isolated, the lignin can be used as an environmentally friendly resin. Lignin accounts for 20 to 30% in wood, and is produced in tissues such as canal, temporary canal, and fiber as it grows in higher plants. It is known that this lignin can be used as a so-called biodegradable resin, and even if it is discarded, it is reduced in molecular weight by white rot fungi and further mineralized by being decomposed by bacteria such as Sphingomonas paucimobilis SYK-6. It has been. However, cellulose and lignin, which mainly constitute lignocellulosic substances (plants), have completely different structures and properties, and both exist in a complex and intertwined state at the molecular level. Therefore, in order to use plant-derived lignin alone, it is necessary to first separate cellulose and lignin.

  Therefore, there is a method of treating wood with concentrated sulfuric acid as a method of isolating lignin from vegetative materials. There is Patent Document 1 as a patent document adopting such a technique, and one of the present applicants has also proposed Patent Document 2. In Patent Document 1, cellulose is eluted in a sulfuric acid solution while preventing self-condensation (inactivation) of lignin by treating a woody material with concentrated sulfuric acid in the presence of phenol. Then, after solid-liquid separation, the solution is neutralized with sodium hydroxide and dried to obtain a phenolized lignin. In Patent Document 2, acetone is also interposed during concentrated sulfuric acid treatment to increase the meltability of cresol and sulfuric acid as a phenol derivative to acid-hydrolyze cellulose, and then neutralize with a weak base substance such as sodium carbonate. The solid phase is filtered off and then purified with acetone or ether.

JP 2004-210899A JP 2006-225325 A

  However, in Patent Document 1 and Patent Document 2, since neutralization is performed with sodium hydroxide or sodium carbonate, an unreacted sodium component remains as an impurity if an excessive basic substance is added to the acid. In order to remove this, it is conceivable to perform water washing, but it takes time and effort. Moreover, in patent document 1, since sodium hydroxide which is a strong base is used as a neutralizing agent, filtration of the solid phase after neutralization was extremely difficult. In Patent Document 2, since it is neutralized with sodium carbonate or the like which is a weak base, filtration is not impossible, but the filterability is not high due to the presence of sodium content. The reason for this is not necessarily clear, but it is thought that the water-solubility of the phenolized lignin increases due to the combination of lignin and sodium, and the particles of each phenolized lignin become finer and clog the filter paper.

  Therefore, an object of the present invention is to provide a method for producing a phenolized lignin that can filter a solid phase extracted by acid treatment and that can be quickly dried with less impurities.

  As a means for this, the method for producing a phenolized lignin of the present invention comprises an acid reaction step in which a vegetative material is soaked in an acid solution together with a phenol derivative, and a solid phase component extracted by the acid reaction step is converted into a volatile basic substance. And a neutralization step of neutralizing with a filtration step of filtering the solid phase after the neutralization step. Here, the vegetative material is a lignocellulosic material mainly composed of cellulose as a carbohydrate and lignin as a resin component, and typically corresponds to woody plants and herbaceous plants. . The phenolized lignin refers to a lignin in a state in which a phenol derivative is chemically bonded to a molecular chain in the lignin and stabilized (grafted) when the lignin and cellulose are separated by acid treatment of the woody material. . Hereinafter, the filter paper will be described as a concept including a filter cloth.

  When the vegetative material is treated with an acid solution, saccharide cellulose is hydrolyzed and eluted, and lignin can be extracted as a solid phase component. At this time, self-polymerization of lignin is prevented by the presence of the phenol derivative. The specific treatment method in this acid reaction step is not particularly limited, and may be carried out by a known method. In order to increase the purity of the solid phase component comprising the phenolized lignin obtained as a main component, the acid is neutralized with a volatile basic substance, and this is filtered to remove excess moisture and impurities. The filtered phenolized lignin (solid phase) has a cake shape and may be used as a product as it is, or may be dried to obtain a flaky phenolized lignin.

  At this time, the boiling point of the volatile basic substance used in the neutralization step is preferably 150 ° C. or lower. Volatile base materials may include those containing substituted alkylamines, alkanolamines, and cyclic amines, and amines such as ammonia, of which only one may be used. Two or more kinds can be mixed and used.

  According to the present invention, since the solid phase extracted by the acid treatment step is neutralized by the volatile base substance, it can be filtered well. The reason for this is not necessarily clear, but when neutralized with a volatile basic substance, even if the phenolized lignin dissolves, it is only on the surface, and the phenolized lignin particles are relatively large particles that maintain a certain amount of mass. Therefore, it is considered that the filter paper is not clogged. Thereby, impurities in the phenolized lignin can be effectively removed to increase the purity, and the yield can also be increased.

  If neutralized with a non-volatile basic substance, the basic substance remaining after neutralization causes deterioration of the characteristics of the phenolized lignin, such as an increase in ash and an increase in electrical conductivity. On the other hand, if a volatile basic substance is used, even if an excessive basic substance is added to the acid, the basic component remaining as an impurity in the dehydrated cake after filtration is reduced by volatilization over time. To go. Thereby, the purity of the obtained phenolized lignin can be further improved and the drying time can be shortened without requiring a step of washing the remaining basic substance.

  Even if the boiling point of the volatile basic substance is 150 ° C. or higher, it cannot be used, but if the boiling point of the volatile basic substance is 150 ° C. or lower, the volatile basic substance has good volatility and can significantly reduce the drying time. It becomes possible. Amines such as substituted alkylamines, alkanolamines, and cyclic amines, particularly ammonia, are advantageous in terms of cost and handling.

  In the present invention, as shown in the flow of FIG. 1, first, in the acid reaction step, the vegetative material is treated with an acid to elute saccharides (cellulose), and phenolized lignin is extracted as a solid phase. Next, the solid phase obtained in the neutralization step is neutralized to remove the acid, and finally the solid phase is filtered in the filtration step to further remove extra impurities.

  As the vegetative material used as a raw material, woody plants and herbaceous plants mainly composed of cellulose and lignin can be used. For example, coniferous trees such as cedar and cypress, and broad-leaved trees such as shii, oak, and cherry as well as tropical trees can be used as trees. In addition, kenaf, ramie (flax), linen (flax), abaca (Manila hemp), Heneken (sisal hemp), jute (cannabis), hemp (palm), palm, palm, mulberry, straw and bagasse are used as herbs. can do. When processing as a raw material, the vegetative material can be used in various forms such as powder, chips, waste, and mill ends.

[Acid reaction step]
The acid reaction step is a step of hydrolyzing cellulose with an acid while preventing self-polymerization of lignin with a phenol derivative, and the specific method thereof is not particularly limited. For example, Patent Document 1 and Patent Document 2 described above are used. It may be performed according to a known method disclosed in the above. Specifically, the vegetation material is mixed with a phenol derivative in advance and then immersed in an acid solution, the vegetation material and the phenol derivative are immersed in an acid solution at the same time, or the phenol derivative is mixed with an acid solution in advance. For example, a case of immersing a vegetation-like material in this. As the acid used here, a strong acid aqueous solution such as sulfuric acid, hydrochloric acid, phosphoric acid, nitric acid, hydrobromic acid and hydroiodic acid can be used, and the acid concentration thereof is as high as about 60% to 80%. It is adjusted to. This is because if the acid concentration is lower than 60%, the molecular structure of the vegetation material cannot be reliably destroyed, and it may be insufficient to hydrolyze and elute cellulose. On the other hand, when the acid concentration is higher than 80%, the molecular structure can be reliably destroyed, but the cellulose that has been hydrolyzed and eluted in the acid solution is precipitated as sugar, and the carbonization of the sugar proceeds, so that impurities are wasted. This is because there is a risk of increasing it.

  As the phenol derivative, a monovalent phenol derivative, a divalent phenol derivative, a trivalent phenol derivative, and the like can be used, but those that are easily dissolved in the acid solution to be used are desirable. For example, when a sulfuric acid solution is used, phenol derivatives such as phenol, cresol, xylenol, catechol, resorcinol can be used. Furthermore, when heated at a high temperature in a concentrated sulfuric acid solution, sugars eluted in the acid solution are precipitated and carbonization proceeds, and from the viewpoint of energy cost, relatively low melting point phenol derivatives such as phenol, xylenol and cresol are used. It is desirable to use it. In particular, phenol that can be obtained at low cost is desirable.

  The treatment solution used in the acid reaction step is obtained by adding about 5% to 25% of a phenol derivative to the concentrated acid solution with respect to the weight of the vegetative material. Then, the vegetative material is mixed in the treatment solution heated to room temperature or a temperature around the melting point of the phenol derivative and stirred for a predetermined time. As a result, cellulose present in the vegetation material is hydrolyzed and eluted into the treatment solution. At that time, the lignin present in the vegetation wood material can be partially decondensed, but since the phenol derivative in the treatment solution is always present in the vicinity of the lignin, the phenol derivative is immediately chemically attached to the side chain of the separated lignin. It can be bound (grafted) and stabilized by suppressing the self-condensation of lignin. Thereby, since the heat fluidity of the phenolic lignin finally obtained can be lowered, it is effective when used as an adhesive, for example. In addition, if the treatment solution is heated to a predetermined temperature and the phenol derivative is uniformly dissolved in the concentrated acid solution, the phenol derivative penetrates well into the inside of the vegetative material, and the lignin inside and outside the vegetative material is absorbed. Variations in the degree of inhibition of self-condensation can be reduced. Thus, in the acid reaction step, cellulose in the vegetative material is hydrolyzed and eluted into the treatment solution, and other metal elements and the like are also eluted into the treatment solution. The lignin phenolized with the phenol derivative is solidified. Extracted as a phase fraction.

[Solid-liquid separation]
After the acid reaction step, it is preferable to perform solid-liquid separation in order to remove excess acid and eluted saccharides and metal elements. Solid-liquid separation at this timing is not always necessary, but it is useful in that the amount of neutralizing agent added in the subsequent neutralization step can be reduced if a certain amount of acid or solution is eliminated by solid-liquid separation. is there. As the solid-liquid separation method, in addition to decantation and centrifugation, a filter press is also suitable, and ordinary filtration may be used. At this timing, there is no problem with filterability.

[Washing]
It is also preferable to wash with water if necessary after removing impurities such as acids to some extent by solid-liquid separation or prior to solid-liquid separation. For example, even if the liquid phase component and the solid phase component are separated by solid-liquid separation, the obtained solid phase component still contains many treatment solutions. In this treatment solution, unreacted phenol and acid are dissolved in addition to the eluted carbohydrates and metal elements. Therefore, by washing with water, these impurities can be further removed to increase the purity of lignin. In the water washing, the obtained solid phase can be mixed and dispersed in a sufficiently larger amount of water, followed by filtration or the like for dehydration or water washing.

[Neutralization process]
The solid phase is then neutralized with a volatile base material to ensure removal of the acid. Typically, the solid phase component is mixed and dispersed in a solution in which a volatile basic substance is dissolved. The solid phase before the neutralization step is in a strongly acidic region of pH 2 or less unless washed with water, and if washed with water, depending on the number of times and treatment time, the pH is close to a weakly acidic region. It has become. And in a neutralization process, it is preferable to adjust the pH of a solid-phase part to the range of 4-8, Preferably it is 5-6. If the pH is less than 4, acid may remain. On the other hand, if the pH exceeds 8, the phenolized lignin dissolves and the filterability may deteriorate, or the yield may decrease. Since lignin has the property of changing from pink to brown at a pH exceeding pH 8, it can be taken as a guide that it does not change to brown at least.

  The concentration of the volatile base substance in the neutralization solution may be appropriately adjusted according to the amount of acid remaining in the solid phase based on the above pH conditions. For example, for the solid phase after solid-liquid separation and water washing Or about 0.2 to 2.0% by weight based on the dry weight of the phenolized lignin. If the amount is less than 0.2% by weight based on the dry weight of the phenolized lignin, the acid cannot be reliably neutralized. There is a possibility that the filterability may deteriorate due to excessive increase in pH or pH. Examples of the volatile base substance include those containing amines such as substituted alkylamines, alkanolamines, and cyclic amines, and ammonia. Examples of the substituted alkylamine include primary alkylamines having an alkyl group having 1 to 6 carbon atoms and secondary or tertiary alkylamines having an alkyl group having 1 to 4 carbon atoms. The alkyl groups in the secondary or tertiary alkylamines may each have a different carbon number. Specifically, methylamine, dimethylamine, trimethylamine, ethylamine, diethylamine, triethylamine, propylamine, dipropylamine, butylamine, isobutylamine, tertiary butylamine, pentylamine, neopentylamine, hexylamine, cyclohexylamine, methylethylamine And methyldiethylamine. Examples of the alkanolamine include alkanolamines such as mono, di or triethanolamine, and β-aminoalkanols such as 2-amino-2-methyl-1-propanol. Examples of cyclic amines include morpholine and piperidine. These volatile basic substances may be used alone or in combination of two or more. Among these, ammonia is preferable from the viewpoints of cost and handleability. In addition, if a weak base substance such as ammonia is used, the pH does not increase rapidly even if an excessive amount is added to the acid in the solid phase. Therefore, the adverse effect on the filterability can be reduced, and it is advantageous in that it is not necessary to adjust the addition amount strictly.

[Filtering process]
If the neutralization step is carried out by dispersing the solid phase in the basic substance solution, if it is dried as it is, it will be excessively watery, requiring a lot of time and energy cost for drying, or by neutralization reaction such as ammonium sulfate. The produced impurities remain. Therefore, the solid phase after the neutralization step is filtered to remove impurities such as sulfate and excess water. At this time, since it is neutralized with a volatile basic substance, phenolic lignin can be filtered without clogging the filter paper. The phenolized lignin thus obtained has a cake-like shape, and may be used as it is for various applications, or may be dried to obtain a flaky phenolized lignin. At this time, even if an excess of the basic substance remains in the solid phase, the basic substance disappears spontaneously because it has volatility, so that the purity can be improved and the drying time can be shortened.

[Drying process]
As described above, when impurities can be removed by the filtration step, drying is performed to remove excess moisture as necessary. The drying method may be natural drying or blow drying with a fan. In the case of blow drying, cold air drying or hot air drying may be used, but it is better to avoid hot air drying because of the risk of denaturation of lignin.

Example 1
Kenaf, known as a fast-growing plant, was used as a vegetative material. In the acid reaction step, 15 kg of a core material (kenaf core) from which kenaf bast was removed was pulverized to a size of a major axis of 2 mm or less was prepared. Further, sulfuric acid was used as the acid, and phenol was used as the phenol derivative.

  First, 1.8 kg of phenol equivalent to 12% by weight with respect to kenaf core was added to 75 kg of 70% sulfuric acid solution and stirred for 30 minutes while heating to 45 ° C. to prepare a treatment solution in which phenol was completely dissolved in sulfuric acid solution. It was adjusted. Then, 15 kg of kenaf core as a raw material was mixed in the treatment solution in a tank made of acid resistant material (Ni-Mo alloy), and stirred for 30 minutes while keeping the temperature at 45 ° C. to perform an acid reaction step. Next, the solid phase after the acid reaction step (phenolic lignin) was subjected to solid-liquid separation with a filter press to obtain a solid phase. The obtained solid phase was mixed and dispersed in water about 4 times by weight, washed, and again solid-liquid separated by a filter press. This solid phase content was 3.6 kg in terms of dry weight. Subsequently, the neutralization process was performed by mixing and dispersing in a sufficient amount of an aqueous solution containing 1% by weight of ammonia relative to the dry weight of the phenolized lignin. Subsequently, the mixture was filtered and separated into solid and liquid, and the resulting solid phase was naturally dried to obtain flaky phenolized lignin.

(Comparative Example 1)
Phenolized lignin was obtained in the same manner as in Example 1 except that it was neutralized with sodium hydroxide.

(Comparative Example 2)
It neutralized similarly to the comparative example 1, and the filtration process was not performed.

  The filterability of the obtained Example 1 and each comparative example, the water content in the phenolized lignin cake, the ash content, and the electrical conductivity were measured and compared. The results are shown in Table 1. Various data measurement methods are as follows.

<Filterability>
It was calculated by the following calculation method.
Filterability (%) = (weight of filtrate after 10 minutes / amount of input slurry) × 100
In addition, the one where the numerical value calculated by the said calculation method is higher means that the flow rate through the filter paper, that is, the filtration speed is faster, and the higher this numerical value means that the filterability is better.

<Moisture content>
It was calculated by the following calculation method.
Water content (%) = (weight immediately after filtration−weight after drying / weight immediately after filtration) × 100
In addition, the one where this figure is low has little water in a phenolization lignin cake, and will be suitable for drying.

<Ash content>
The powder sample was heat-dried at 135 ° C. for 1 hour in a crucible, and then ashed at 800 ° C. for 6 hours. And it computed with the following calculation method.
Ash content (%) = (weight after ashing / weight after drying) × 100
By the above treatment, the phenolized lignin is ashed, and impurities such as metals and sulfates remain as they are. Therefore, the lower the ash value, the fewer impurities.

<Electrical conductivity>
In a Teflon (registered trademark) container, 6 g of a powder sample was mixed with 40 g of ultrapure water, the container was sealed and heated at 125 ° C. for 20 hours, and the electrical conductivity of the resulting solution was measured.
Note that the lower the electrical conductivity, the smaller the amount of water-soluble ions remaining as impurities.

  From the results shown in Table 1, Comparative Example 2 in which the filtration was not performed has an extremely high water content and ash content compared to Example 1 and Comparative Example 1 in which the filtration was performed, which is not preferable for the drying treatment and contains a large amount of impurities. I understand that. Further, when Example 1 was compared with Comparative Example 1, Example 1 was better than Comparative Example 1 in all aspects of filterability, moisture content, ash content, and electrical conductivity. Thus, it can be seen that neutralization with ammonia dramatically improves the filterability, reduces impurities, and enables rapid drying.

It is a conceptual flow diagram of the present invention.

Claims (5)

An acid reaction step in which the vegetative material is soaked in an acid solution together with a phenol derivative;
A neutralization step of neutralizing the solid phase extracted by the acid reaction step with a volatile base substance;
A method for producing a phenolized lignin having a filtration step of filtering the solid phase after the neutralization step.   The method for producing a phenolized lignin according to claim 1, wherein the boiling point of the volatile basic substance is 150 ° C or lower.   The method for producing a phenolized lignin according to claim 1 or 2, wherein the volatile basic substance is an amine.   The method for producing a phenolized lignin according to claim 3, wherein the amine is one or more of a substituted alkylamine, an alkanolamine, and a cyclic amine. The method for producing a phenolized lignin according to claim 3, wherein the amine is ammonia.

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