WO2012111726A1

WO2012111726A1 - Method for producing condensate of resorcin and acetone, and rubber composition including condensate

Info

Publication number: WO2012111726A1
Application number: PCT/JP2012/053590
Authority: WO
Inventors: 板橋　太門; 竹内　謙一; 一祐松井
Original assignee: 住友化学株式会社
Priority date: 2011-02-18
Filing date: 2012-02-09
Publication date: 2012-08-23
Also published as: TW201238958A; JP2012184401A

Abstract

This method for producing a condensate of resorcin and acetone includes: a step for reacting resorcin and acetone in the presence of an acid; and a step for removing, in the presence of an acid, water produced as a byproduct of the reaction.

Description

Process for producing condensate of resorcin and acetone and rubber composition containing the condensate

The present invention relates to a method for producing a condensate of resorcin and acetone, a rubber composition containing the condensate, and the like.

A condensate of resorcin and acetone is useful as a reinforcing agent for various rubber compositions.
In Japanese Patent Application Laid-Open No. 2004-2431, after resorcin and acetone are reacted in the presence of an acid and an organic solvent, the acid is neutralized with an aqueous sodium hydroxide solution, and the neutralized mixture is dried under reduced pressure. To produce a condensate of resorcin and acetone.

The present invention
<1> a step of reacting resorcin and acetone in the presence of an acid;
Removing water by-produced by the reaction in the presence of an acid;
A method for producing a condensate of resorcin and acetone containing
<2> a step of reacting resorcin and acetone in the presence of an acid;
Removing water by-produced by the reaction in the presence of an acid;
Mixing the mixture after removing water and the base;
The production method according to <1>, comprising:
<3> a step of reacting resorcin and acetone in the presence of an acid;
Removing water by-produced by the reaction in the presence of an acid;
Mixing the mixture after removing water and acetone;
Mixing the mixture after mixing with acetone and a base;
The production method according to <1> or <2>, comprising:
<4> The step of removing water by-produced by the reaction in the presence of an acid is a step of removing water by-produced by the reaction in the presence of an acid and an organic solvent. The production method according to any one of the above;
<5> The step of removing water by-produced by the reaction in the presence of an acid and an organic solvent causes the water by-produced by the reaction to azeotrope with the organic solvent in the presence of an acid and an organic solvent. The production method according to <4>, which is a step of removing;
<6> The production method according to <4> or <5>, wherein the organic solvent is an aromatic hydrocarbon;
<7> The production method according to <6>, wherein the aromatic hydrocarbon is toluene or xylene;
<8> The production method according to any one of <1> to <7>, wherein the acid is at least one selected from the group consisting of p-toluenesulfonic acid, p-toluenesulfonic acid hydrate, hydrochloric acid, and sulfuric acid. ;
<9> A rubber composition comprising a condensate obtained by the production method according to any one of <1> to <8>, a rubber component, a filler, and a sulfur component;
<10> A tire belt including a steel cord coated with the rubber composition according to <9>.
<11> A tire carcass including a carcass fiber cord coated with the rubber composition according to <9>;
<12> A tire tread or a tire undertread comprising the rubber composition according to <9>;
<13> A pneumatic tire manufactured by processing the rubber composition according to <9>;
<14> A condensate of resorcin and acetone satisfying the following (1), (2) and (3);
(1) When the condensate was analyzed by gel permeation chromatography (differential refractive index detection), it was derived from 2,4,4-trimethyl-2 ′, 4 ′, 7-trihydroxyflavan relative to the total area of all peaks. The peak area ratio is in the range of 30 to 55%.
(2) When the condensate is analyzed by gel permeation chromatography (differential refractive index detection), the area ratio of the first eluting peak to the total area of all peaks is in the range of 20 to 50%.
(3) The weight average molecular weight of the first elution peak is in the range of 1500 to 1700;
<15> The condensate according to <14>, wherein the softening point is 160 ° C. or lower;
<16> The condensate according to <14> or <15>, wherein the increase rate of resorcin when stored at 120 ° C. for 24 hours is 2% or less.

The production method of the present invention comprises a step of reacting resorcin and acetone in the presence of an acid;
Removing water by-produced by the reaction in the presence of an acid;
Is a method for producing a condensate of resorcin and acetone.
<Step of reacting resorcin and acetone in the presence of an acid (hereinafter sometimes referred to as “first step”)>
A commercially available resorcin can be used. Commercially available acetone can also be used. The amount of acetone used is preferably in the range of 1 to 6 mol and more preferably in the range of 1.5 to 4 mol with respect to 1 mol of resorcin. If the amount of acetone used is 1 mol or more, the residual rate of unreacted resorcin tends to be reduced.
The acid acts as a catalyst in the reaction between resorcin and acetone, and may be hereinafter referred to as “acid catalyst”. Specific examples of the acid include benzenesulfonic acid, p-toluenesulfonic acid, p-toluenesulfonic acid hydrate, oxalic acid, phosphoric acid, polyphosphoric acid, borofluoric acid, hydrochloric acid and sulfuric acid. Among these, at least one acid selected from the group consisting of p-toluenesulfonic acid, p-toluenesulfonic acid hydrate, hydrochloric acid and sulfuric acid is preferable. These acids can be used as they are or in the form of an aqueous solution having an appropriate concentration. The amount of acid used is not limited, but is preferably in the range of 0.1 to 10 mol, more preferably in the range of 0.5 to 5 mol, per 100 mol of resorcin.
The reaction between resorcin and acetone is preferably performed in the presence of an organic solvent. Examples of the organic solvent include aliphatic hydrocarbons, aromatic hydrocarbons, and halogen-substituted aromatic hydrocarbons. Specific examples of aliphatic hydrocarbons include hexane, heptane, octane, and decane. Specific examples of aromatic hydrocarbons include toluene, xylene, and ethylbenzene. Specific examples of halogen-substituted aromatic hydrocarbons. Includes chlorobenzene and dichlorobenzene. Aromatic hydrocarbons are preferred, and toluene or xylene is more preferred. The amount of the organic solvent used is preferably in the range of 0.5 to 3 parts by weight with respect to 1 part by weight of resorcin.
The reaction temperature of the reaction between resorcin and acetone is preferably in the range of 30 ° C. or higher and 65 ° C. or lower. The progress of the reaction can be confirmed by ordinary analytical means such as gas chromatography (GC), high performance liquid chromatography (HPLC), gel permeation chromatography (GPC), etc., while confirming the progress of the reaction, The end point can be determined.
The order of mixing resorcin, acetone and acid is not limited. For example, resorcin and acetone are mixed in the presence of an organic solvent as necessary, and the resulting mixture and acid are mixed under reaction temperature conditions. The reaction can be carried out. As the reaction proceeds, acetone may be added continuously or intermittently to the mixture. As the reaction proceeds, 2,4,4-trimethyl-2′4′7-trihydroxyflavan, which is one of the compounds contained in the condensate of resorcin and acetone, may precipitate, In order to prevent 4,4-trimethyl-2'4'7-trihydroxyflavan from sticking to the reaction vessel wall (so-called scaling), 2,4,4-trimethyl-2'4'7-trihydroxyflavan is used. It may be used as a seed crystal. In addition, 2,4,4-trimethyl-2′4′7-trihydroxyflavan is a compound represented by the following formula.

As a compound contained in the condensate of resorcin and acetone, in addition to 2,4,4-trimethyl-2′4′7-trihydroxyflavan (compound represented by the following formula),

7,7′-dihydroxy-4,4,4 ′, 4′-tetramethyl-2,2′-spirobichroman (compound represented by the following formula),

4,6-bis (7-hydroxy-2,4,4-trimethylchroman-2-yl) -1,3-benzenediol (compound represented by formula (I)) and isomers thereof,

2,4-bis (7-hydroxy-2,4,4-trimethylchroman-2-yl) -1,3-benzenediol (compound represented by formula (II)) and isomers thereof,

Compounds represented by formula (III) and isomers thereof,

And a compound represented by formula (IV) and an isomer thereof,

[In the formula (IV), n represents an integer of 2 or more. ]
Is mentioned.
<Step of removing water by-produced by the reaction in the presence of an acid (hereinafter sometimes referred to as “second step”)>
The step of removing water by-produced by the reaction of resorcin and acetone in the presence of an acid may be performed simultaneously with the step of reacting resorcin and acetone in the presence of an acid. For the purpose of the above, it is preferable to react resorcin and acetone in the presence of an acid, and then remove water by-produced by the reaction in the presence of an acid. The mixture obtained by removing water in this step contains a condensate of resorcin and acetone and an acid.
The removal of water may be carried out using a substance capable of adsorbing water or a substance capable of decomposing water, but is preferably carried out by distillation, by azeotropy of the organic solvent and water in the presence of the organic solvent. More preferably. The fraction obtained by distillation or azeotrope usually contains water, and water can be removed by removing the fraction, but the fraction is separated into an organic layer and an aqueous layer. When it is, it is preferable that only the aqueous layer is separated and removed, and the organic layer is returned to the mixture. The removal of water is preferably carried out until the water content of the mixture obtained by removing water becomes 0.01 to 2% by weight, more preferably until the water content becomes 0.01 to 1% by weight. preferable.
As the organic solvent, the organic solvent used for the reaction of resorcin and acetone is usually used, but an organic solvent different from this can also be used. Examples of the organic solvent include aliphatic hydrocarbons such as pentane, hexane, and heptane, alicyclic hydrocarbons such as cyclopentane, cyclohexane, and methylcyclohexane, aromatic hydrocarbons such as benzene, toluene, and xylene, methylene chloride, chloroform, Examples thereof include chlorinated hydrocarbons such as carbon chloride, trichrene, barkrene, ethylene dichloride, and benzene chloride, esters such as methyl acetate, ethyl acetate, and propyl acetate, and nitriles such as acetonitrile. Of these, aromatic hydrocarbons are preferable, and toluene or xylene is more preferable.
The mixture obtained in the first step and the second step may be subjected to a post-treatment step which will be described later, or, if necessary, further subjected to a third step, which will be described later, followed by a post-treatment step. Also good.
<A step of mixing the mixture after removing water and acetone (hereinafter sometimes referred to as “third step”)>
More preferably, acetone is mixed with the mixture after removing water by-produced by the reaction between resorcin and acetone in the presence of an acid. The third step is a step of reacting acetone with resorcin remaining in a mixture containing a condensate of resorcin and acetone and an acid.
The amount of acetone used in the third step is such that the sum of the amount of acetone used in the first step is in the range of 1 to 6 moles per mole of resorcin used in the first step. Good. An acid or an organic solvent may be used in the third step as necessary. The reaction temperature in the third step is preferably in the range of 30 ° C. or higher and 65 ° C. or lower. Moreover, you may perform a 3rd process, removing water. About removal of water, it can carry out similarly to a 2nd process. In the third step, while confirming the content ratio of 2,4,4-trimethyl-2 ′, 4 ′, 7-trihydroxyflavan and the content ratio of resorcin, by ordinary analysis means such as GC, HPLC, GPC and the like. Then, it may be carried out while adding acetone as appropriate until they reach the desired range.
<Post-processing process>
A condensate of resorcin and acetone can be taken out by subjecting the mixture obtained in the second step or the third step to a post-treatment step including filtration and concentration and removing the organic solvent.
<The process of mixing the mixture after removing water and a base>
After neutralizing the mixture obtained in the second step or the third step with a base, it is separated by solid-liquid separation by washing with water or filtering, and generated by acid catalyst or neutralization attached to the obtained solid as necessary. After the washed salt is washed with water, the organic solvent may be removed. Examples of the base include alkali metal hydroxides such as sodium hydroxide and potassium hydroxide, alkali metal hydrogen carbonates such as sodium hydrogen carbonate, alkali metal carbonates such as sodium carbonate, etc., and alkali metal hydroxides are preferred. Sodium hydroxide is more preferable. The base is preferably used in the form of an aqueous solution having an appropriate concentration.
The residual ratio of resorcin is preferably 5.0% by weight or less, and more preferably 1.0% by weight or less.
<Condensate obtained>
In the present invention, the “first elution peak” is a peak having the shortest retention time among all peaks in a chromatogram obtained when a condensate is analyzed by gel permeation chromatography (differential refractive index detection). The “second eluting peak” means that the retention time is the second of all peaks in the chromatogram obtained when the condensate is analyzed by gel permeation chromatography (differential refractive index detection). A short peak means “third elution peak”, and among all peaks in the chromatogram obtained when the condensate is analyzed by gel permeation chromatography (differential refractive index detection), the retention time is three. Means the second shortest peak.
In gel permeation chromatography (differential refractive index detection), the compound group consisting of the compound represented by formula (IV) and its isomer is taken as the first elution peak from the compound represented by formula (III) and its isomer. The compound group consisting of the compound represented by formula (I) and its isomer, and the compound group consisting of the compound represented by formula (II) and its isomer as the third elution peak, Each is detected.
The obtained condensate is preferably a condensate satisfying the following (1), (2) and (3).
(1) When the condensate was analyzed by gel permeation chromatography (differential refractive index detection), it was derived from 2,4,4-trimethyl-2 ′, 4 ′, 7-trihydroxyflavan relative to the total area of all peaks. The peak area ratio is in the range of 30 to 55%.
(2) When the condensate is analyzed by gel permeation chromatography (differential refractive index detection), the area ratio of the first eluting peak to the total area of all peaks is in the range of 20 to 50%.
(3) The weight average molecular weight of the first elution peak is in the range of 1500 to 1700.
The obtained condensate preferably has a softening point of 160 ° C. or lower.
The obtained condensate preferably has a resorcin increase rate of 2% or less when stored at 120 ° C. for 24 hours.
The content of 2,4,4-trimethyl-2′4′7-trihydroxyflavan contained in the obtained condensate is preferably in the range of 30 to 55% by weight, and 35 to 50% by weight. A range is more preferable.
4,6-bis (7-hydroxy-2,4,4-trimethylchroman-2-yl) -1,3-benzenediol (compound represented by formula (I)) contained in the obtained condensate And its isomers, and 2,4-bis (7-hydroxy-2,4,4-trimethylchroman-2-yl) -1,3-benzenediol (compound represented by formula (II)) and its The total content of isomers is preferably in the range of 5 to 10% by weight.
The total content of the compound represented by the formula (III) and its isomer contained in the obtained condensate is preferably in the range of 5 to 15% by weight.
The total content of the compound represented by formula (IV) and the isomers contained in the obtained condensate is preferably in the range of 20 to 50% by weight, and in the range of 25 to 35% by weight. More preferably.
The resulting condensate of resorcin and acetone can be used as a rubber reinforcing agent. It is particularly useful as a reinforcing agent for rubber for tires.
Next, a rubber composition containing a condensate of resorcin and acetone, a rubber component, a filler, and a sulfur component will be described.
Examples of the rubber component include natural rubber, styrene butadiene copolymer rubber, butadiene rubber, isoprene rubber, and rubber components containing them as a main component. The amount of the condensate of resorcin and acetone used is preferably in the range of 0.5 to 3 parts by weight, more preferably in the range of 1 to 2 parts by weight with respect to 100 parts by weight of these rubber components.
Examples of the filler include carbon black, silica, talc and clay which are usually used in the rubber field, and carbon black is more preferably used. As the carbon black, carbon black such as HAF (High Ablation Furnace), SAF (Super Ablation Furnace), ISAF (Intermediate SAF) is preferable. It is also preferable to combine several kinds of fillers such as a combination of carbon black and silica. The amount of the filler used is preferably in the range of 10 to 100 parts by weight, more preferably in the range of 30 to 70 parts by weight per 100 parts by weight of the rubber component.
Examples of the sulfur component include powdered sulfur, precipitated sulfur, colloidal sulfur, insoluble sulfur and highly dispersible sulfur, with powdered sulfur and insoluble sulfur being preferred. The amount of the sulfur component used is preferably in the range of 1 to 10 parts by weight, more preferably in the range of 2 to 6 parts by weight per 100 parts by weight of the rubber component.
Furthermore, a rubber composition can be produced using a vulcanization accelerator, a methoxylated methylol melamine resin, an organic cobalt compound and zinc oxide.
Examples of vulcanization accelerators include thiazole-based vulcanization accelerators described in pages 412 to 413 of Rubber Industry Handbook <Fourth Edition> (issued by the Japan Rubber Association on January 20, 1994), Examples thereof include phenamide vulcanization accelerators and guanidine vulcanization accelerators. The amount of vulcanization accelerator used is preferably in the range of 0.5 to 1 part by weight, more preferably in the range of 0.6 to 0.8 part by weight per 100 parts by weight of the rubber component.
Examples of the methoxylated methylol melamine resin include those commonly used in the rubber industry such as hexakis (methoxymethyl) melamine, pentakis (methoxymethyl) methylol melamine, tetrakis (methoxymethyl) dimethylol melamine, and hexakis (methoxymethyl). ) Melamine alone or a mixture based on it is preferred. These methoxylated methylol melamine resins can be used alone or in combination of two or more, and the blending amount thereof is 0.5 to 6.0 parts by weight with respect to 100 parts by weight of the rubber component. The range is preferable, and the range of 1.0 to 3.0 parts by weight is more preferable.
Examples of the organic cobalt compound include acid cobalt salts such as cobalt naphthenate and cobalt stearate, and fatty acid cobalt / boron complex compounds (for example, trade name “Manobond C (registered trademark)” manufactured by Manchem). The amount of the organic cobalt compound used is preferably in the range of 0.1 to 0.4 parts by weight and in the range of 0.1 to 0.3 parts by weight in terms of cobalt content with respect to 100 parts by weight of the rubber component. More preferred.
Various rubber chemicals commonly used in the rubber industry, such as anti-aging agents such as antioxidants and ozone degradation inhibitors, peptizers, processing aids, waxes, oils, stearic acid, tackifiers, etc. You may use 1 type (s) or 2 or more types as needed. The compounding amount of these chemicals varies depending on the use of the rubber composition, but an amount in a range usually used in the rubber industry can be used.
The rubber composition can be derived into a rubber product through a process such as molding and vulcanization, for example, in accordance with a method commonly practiced in the rubber industry. In particular, it can be used for various members of tires such as cap treads, under treads, belts, carcass, beads, sidewalls, rubber chafers and the like. Further, it can also be used for anti-vibration rubbers for automobiles such as engine mounts, strut mounts, bushes and exhaust hangers, hoses, rubber belts and the like.
For example, a tire belt can be manufactured by coating a steel cord with a rubber composition. Steel cords are usually used in an aligned state.
From the viewpoint of adhesion to rubber, the steel cord is preferably plated with brass, zinc, or an alloy containing nickel or cobalt, and is preferably subjected to brass plating. is there. In particular, a steel cord subjected to a brass plating process in which the Cu content in the brass plating is 75% by weight or less, preferably 55 to 70% by weight is suitable. The twist structure of the steel cord is not limited.
A plurality of belts may be laminated and used. The belt is mainly used as a carcass reinforcing material.
In addition, for example, a carcass can be manufactured by extruding a rubber composition in accordance with a carcass shape of a tire and attaching the rubber composition on the upper and lower sides of a carcass fiber cord. The carcass fiber cord is usually used in a state of being aligned in parallel. As the carcass fiber cord, preferred is an inexpensive polyester that has good elastic modulus and fatigue resistance and excellent creep resistance. These are used as a tire reinforcing material by laminating one sheet or a plurality of sheets.
A pneumatic tire can be manufactured by a normal manufacturing method using a rubber composition. For example, a rubber composition is extruded to obtain a tire member, which is pasted and molded on another tire member by a normal method on a tire molding machine to form a raw tire. The green tire is heated and pressed in a vulcanizer to obtain a tire.

Hereinafter, the present invention will be specifically described with reference to Examples and Test Examples. In the following examples, the contents of 2,4,4-trimethyl-2′4′7-trihydroxyflavan and resorcin were determined by the GPC area percentage method. The softening point was measured according to JIS K6220-1. In the examples, “part” represents “part by weight”.
In GPC analysis, the compound group consisting of the compound represented by formula (IV) and its isomer is the first eluting peak, and the compound group consisting of the compound represented by formula (III) and its isomer is the second eluting peak. As a third elution peak, the compound represented by the formula (I) and its isomer, and the compound group consisting of the compound represented by the formula (II) and its isomer were detected.
<GPC analysis conditions>
Column: TOSOH TSGel Super HZ2000 (4.6 mmφ × 150 cm) and two TOSOH TSGel Super HZ1000 (4.6 mmφx150 cm) connection temperature: 40 ° C.
Mobile phase: Tetrahydrofuran Detector: RI
Example 1
A 1000 ml four-necked flask equipped with a thermometer, a stirrer and a condenser was charged with 198.2 g (1.8 mol) of resorcin, and the inside of the flask was purged with nitrogen, and then 167.3 g (2.88 mol) of acetone and 501 g of toluene. Was charged. The temperature of the resulting mixture was raised to 40 ° C., and then 1.98 g of 98% sulfuric acid was charged. The obtained mixture was heated to an internal temperature of 60 ° C. and kept warm for 4 hours.
Thereafter, water was removed from the reaction system by reducing the pressure inside the flask while maintaining the internal temperature at 60 ° C. At the same temperature, 52.3 g (0.9 mol) of acetone was charged, and the resulting mixture was kept at 60 ° C. for 2 hours while removing the water from the reaction system by reducing the pressure inside the flask. Thereafter, the mixture was neutralized with a 10% aqueous sodium hydroxide solution and further dried at 80 ° C. for 12 hours under a reduced pressure of 1 KPa or less to obtain 313 g of a condensate of resorcin and acetone. The contents of 2,4,4-trimethyl-2′4′7-trihydroxyflavan and resorcin in the obtained condensate were as follows.
2,4,4-trimethyl-2'4'7-trihydroxyflavan: 44.4%
Resorcin: 0.7%
First eluting peak: 34.1%
Weight average molecular weight of first elution peak: 1441
Softening point 144 ° C
Example 2
A 500 ml four-necked flask equipped with a thermometer, a stirrer and a condenser was charged with 88.1 g (0.8 mol) of resorcin, and the inside of the flask was purged with nitrogen, and then 65.0 g (1.12 mol) of acetone and 132 g of toluene. Was charged. The obtained mixture was heated to 40 ° C., and then charged with 0.88 g of 98% sulfuric acid. The obtained mixture was heated to an internal temperature of 50 ° C. and kept warm for 4 hours. Thereafter, the temperature was raised to an internal temperature of 60 ° C., and the inside of the flask was decompressed to remove water from the reaction system. After returning to normal pressure and cooling to 45 ° C., 69.7 g (1.2 mol) of acetone was charged, and the resulting mixture was kept at the same temperature for 3.5 hours. Thereafter, neutralization was performed with a 10% aqueous sodium hydroxide solution, followed by drying at 80 ° C. for 12 hours under reduced pressure of 1 KPa or less to obtain 136 g of a condensate of resorcin and acetone. The contents of 2,4,4-trimethyl-2′4′7-trihydroxyflavan and resorcin in the obtained condensate were as follows.
2,4,4-trimethyl-2′4′7-trihydroxyflavan: 50.4% by weight
Resorcin: 0.9% by weight
Example 3
A 500 ml four-necked flask equipped with a thermometer, a stirrer and a condenser was charged with 88.1 g (0.8 mol) of resorcin, and the inside of the flask was purged with nitrogen, and then 65.0 g (1.12 mol) of acetone and 223 g of toluene. Was charged. The temperature of the obtained mixture was raised to 40 ° C., and then 0.40 g of 98% sulfuric acid was charged. The obtained mixture was heated to an internal temperature of 50 ° C. and kept warm for 3.5 hours. With the internal temperature kept at 60 ° C., the inside of the flask was decompressed to remove water from the reaction system. The pressure was returned to normal pressure, 69.7 g (1.2 mol) of acetone was charged, and the resulting mixture was kept at the same temperature for 5 hours. Thereafter, the solution was neutralized with a 10% aqueous sodium hydroxide solution and dried at 80 ° C. under a reduced pressure of 1 KPa or less for 12 hours to obtain 136 g of a resorcin-acetone condensate. The contents of 2,4,4-trimethyl-2′4′7-trihydroxyflavan and resorcin in the obtained condensate were as follows.
2,4,4-trimethyl-2′4′7-trihydroxyflavan: 45.8% by weight
Resorcin: 0.97% by weight
First eluting peak: 28.1%
Weight average molecular weight of the first eluting peak: 1211
Softening point 112 ° C
Comparative Reference Example 1
A 500 ml four-necked flask equipped with a thermometer, a stirrer and a condenser was charged with 44.0 g (0.4 mol) of resorcin, and the inside of the flask was purged with nitrogen. Then, 25.6 g (0.44 mol) of acetone and 111 g of toluene were added. Was charged. The temperature of the obtained mixture was raised to 40 ° C., and then 0.44 g of 98% sulfuric acid was charged. The obtained mixture was heated to an internal temperature of 80 ° C. and kept warm for 3 hours. Next, 23.2 g (0.40 mol) of acetone was charged, and the resulting mixture was kept warm for 4 hours. Next, 23.2 g (0.40 mol) of acetone was charged, and the resulting mixture was kept warm for 3 hours. Thereafter, the mixture was neutralized with a 10% aqueous sodium hydroxide solution and further dried at 80 ° C. for 12 hours under reduced pressure of 1 KPa or less to obtain 120 g of a condensate of resorcin and acetone. The contents of 2,4,4-trimethyl-2′4′7-trihydroxyflavan and resorcin in the obtained condensate were as follows.
2,4,4-trimethyl-2′4′7-trihydroxyflavan: 42.9% by weight
Resorcin: 15.8% by weight
Example 4 [Production of rubber composition]
Using a 0.6 liter lab plast mill, the initial system temperature is set to 150 ° C., and based on the following formulation, first, natural rubber (RSS # 1) is added and mastication is performed for 3 minutes. Subsequently, carbon black (N330), hydrous silica, stearic acid, zinc white, anti-aging agent (2,2,4-trimethyl-1,2-dihydroquinoline condensate) and the condensate obtained in Example 1 were added. Kneaded for 5 minutes and discharged. Next, the discharged rubber was transferred to an open roll, the initial product temperature was set to 60 ° C., sulfur, vulcanization accelerator (N, N-dicyclohexyl-2-benzothiazylsulfenamide), methoxylation shown in the following formulation A rubber composition was obtained by adding a methylol melamine resin (Sumikanol 507AP (manufactured by Sumitomo Chemical Co., Ltd.)) and cobalt naphthenate while kneading while controlling the temperature of the rubber to 80 ° C. or less.
<Combination prescription>
・ Natural rubber (RSS # 1) 100 parts ・ N330 carbon black 45 parts ・ Hydrosilicate silica (Nipsil AQ manufactured by Tosoh Silica Co., Ltd.) 10 parts ・ Stearic acid 3 parts ・ Zinc flower 5 parts by weight ・ Anti-aging agent (2, 2,4-trimethyl-1,2-dihydroquinoline condensate) 2 parts, component A (condensate of resorcin and acetone obtained in Example 1) 2 parts, sulfur 4 parts, vulcanization accelerator (N, N- Dicyclohexyl-2-benzothiazylsulfenamide) 0.7 parts ・ Methoxylated methylol melamine resin (Sumikanol 507AP (manufactured by Sumitomo Chemical Co.)) 3 parts (2 parts active ingredient)
・ Cobalt naphthenate 2 parts (cobalt content 0.2 parts)
Example 5 [Production of rubber composition]
In Example 4, it replaced with the condensate obtained in Example 1, and carried out similarly to Example 4 except having used the condensate obtained in Example 2, and obtained the rubber composition.
Example 6 [Production of tire belt and tire using the same]
A belt is obtained by covering the steel cord subjected to the brass plating treatment with the rubber composition obtained in Example 4. A tire is obtained by forming a green tire using the obtained belt according to a normal production method and heating and pressing the obtained green tire in a vulcanizer.
Example 7 [Production of tire carcass and tire using the same]
By extruding the rubber composition obtained in Example 4, a rubber composition having a shape corresponding to the carcass shape is prepared, and carcass is obtained by applying the rubber composition on top and bottom of a polyester carcass fiber cord. Using the obtained carcass, a tire is obtained by molding a green tire according to a normal manufacturing method and heating and pressing the obtained green tire in a vulcanizer.
Example 8 [Production of tire tread and tire using the same]
The rubber composition obtained in Example 4 is extruded to obtain a cap tread. Using the obtained cap tread, a tire is obtained by molding a green tire according to a normal production method and heating and pressing the obtained green tire in a vulcanizer.
Example 9 [Production of tire undertread and tire using the same]
The rubber composition obtained in Example 4 is extruded to obtain an undertread. Using the obtained undertread, a tire is obtained by molding a green tire according to a normal manufacturing method and heating and pressing the obtained green tire in a vulcanizer.

According to the production method of the present invention, the residual amount of unreacted resorcin can be reduced. The condensate of resorcin and acetone obtained by the production method of the present invention is excellent in performance as a reinforcing agent for various rubber compositions, and can also prevent deterioration of the working environment due to transpiration of residual resorcin during processing of the rubber composition. Therefore, it is industrially advantageous.

Claims

Reacting resorcin and acetone in the presence of an acid;
Removing water by-produced by the reaction in the presence of an acid;
A method for producing a condensate of resorcin and acetone containing
Reacting resorcin and acetone in the presence of an acid;
Removing water by-produced by the reaction in the presence of an acid;
Mixing the mixture after removing water and the base;
The manufacturing method of Claim 1 containing this.
Reacting resorcin and acetone in the presence of an acid;
Removing water by-produced by the reaction in the presence of an acid;
Mixing the mixture after removing water and acetone;
Mixing the mixture after mixing with acetone and a base;
The manufacturing method of Claim 1 or 2 containing.
4. The step of removing water by-produced by the reaction in the presence of an acid is a step of removing water by-produced by the reaction in the presence of an acid and an organic solvent. Production method.
The step of removing water by-produced by the reaction in the presence of an acid and an organic solvent is a step of removing water by-produced by the reaction by azeotroping with the organic solvent in the presence of an acid and an organic solvent. The manufacturing method according to claim 4.
The production method according to claim 4 or 5, wherein the organic solvent is an aromatic hydrocarbon.
The production method according to claim 6, wherein the aromatic hydrocarbon is toluene or xylene.
The production method according to any one of claims 1 to 7, wherein the acid is at least one selected from the group consisting of p-toluenesulfonic acid, p-toluenesulfonic acid hydrate, hydrochloric acid, and sulfuric acid.
A rubber composition comprising a condensate obtained by the production method according to any one of claims 1 to 8, a rubber component, a filler, and a sulfur component.
A tire belt comprising a steel cord coated with the rubber composition according to claim 9.
A tire carcass comprising a carcass fiber cord coated with the rubber composition according to claim 9.
A tire tread or a tire undertread comprising the rubber composition according to claim 9.
A pneumatic tire manufactured by processing the rubber composition according to claim 9.
A condensate of resorcin and acetone satisfying the following (1), (2) and (3).
(1) When the condensate was analyzed by gel permeation chromatography (differential refractive index detection), it was derived from 2,4,4-trimethyl-2 ', 4', 7-trihydroxyflavan relative to the total area of all peaks. The peak area ratio is in the range of 30 to 55%.
(2) When the condensate is analyzed by gel permeation chromatography (differential refractive index detection), the area ratio of the first elution peak to the total area of all peaks is in the range of 20 to 50%.
(3) The weight average molecular weight of the first elution peak is in the range of 1500 to 1700.
The condensate according to claim 14, which has a softening point of 160 ° C or lower.
The condensate according to claim 14 or 15, wherein the increase rate of resorcin when stored at 120 ° C for 24 hours is 2% or less.