TW201238958A - Method for producing condensate of resorcin and acetone, and rubber composition including condensate - Google Patents

Method for producing condensate of resorcin and acetone, and rubber composition including condensate Download PDF

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TW201238958A
TW201238958A TW101105126A TW101105126A TW201238958A TW 201238958 A TW201238958 A TW 201238958A TW 101105126 A TW101105126 A TW 101105126A TW 101105126 A TW101105126 A TW 101105126A TW 201238958 A TW201238958 A TW 201238958A
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acid
condensate
acetone
water
rubber
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TW101105126A
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Chinese (zh)
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Tamon Itahashi
Kenichi Takeuchi
Kazuhiro Matsui
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Sumitomo Chemical Co
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D311/00Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings
    • C07D311/02Heterocyclic compounds containing six-membered rings having one oxygen atom as the only hetero atom, condensed with other rings ortho- or peri-condensed with carbocyclic rings or ring systems
    • C07D311/04Benzo[b]pyrans, not hydrogenated in the carbocyclic ring
    • C07D311/58Benzo[b]pyrans, not hydrogenated in the carbocyclic ring other than with oxygen or sulphur atoms in position 2 or 4
    • C07D311/60Benzo[b]pyrans, not hydrogenated in the carbocyclic ring other than with oxygen or sulphur atoms in position 2 or 4 with aryl radicals attached in position 2
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60CVEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
    • B60C1/00Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/04Oxygen-containing compounds
    • C08K5/15Heterocyclic compounds having oxygen in the ring
    • C08K5/151Heterocyclic compounds having oxygen in the ring having one oxygen atom in the ring
    • C08K5/1545Six-membered rings
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/01Use of inorganic substances as compounding ingredients characterized by their specific function
    • C08K3/013Fillers, pigments or reinforcing additives

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Phenolic Resins Or Amino Resins (AREA)
  • Tires In General (AREA)

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

201238958 六、發明說明: 【發明所屬之技術領域】 本發明係關於一種間苯二紛與丙酮之縮合物之製造方法 及含有該縮合物之橡膠組合物等。 【先前技術】 間苯二酚與丙酮之縮合物係用作各種橡膠組合物之補強 劑。 於曰本專利特開2004-243 1號公報中記載有如下製造方 法·於使間苯二酚與丙酮於酸及有機溶劑之存在下進行反 應之後以虱氧化納水溶液中和上述酸,進而對中和後之 混合物進行減壓乾燥,藉此獲得間苯二酚與丙酮之縮合 物。 【發明内容】 本發明係提供如下者: &lt;1;&gt; 一種間苯二酚與丙酮之縮合物之製造方法,其包 括: 使間苯二酚與丙酮於酸之存在下進行反應之步驟,及 於I之存在下去除由上述反應所副生之水之步驟; &lt;2&gt;如上述&lt;丨&gt;之製造方法’其包括: 使間笨二酚與丙酮於酸之存在下進行反應之步驟, 於馱之存在下去除由上述反應所副生之水之步驟,及 使去除水後之混合物與鹼混合之步驟; &lt;3&gt;如上述《卜或ο之製造方法,其包括: 使間苯二酚與丙酮於酸之存在下進行反應之步驟, 162280.doc 201238958 副生之水之步驟 之步驟,及 合之步驟; 於酸之存在下去除由上述反應所 使去除水後之混合物與丙酮混合 使與丙酮混合後之混合物與鹼混 &lt;4&gt;如上述〇至&lt;3&gt;中任一項之製造方法,其中於酸之 存在下去除由上述反應所副生之水的步驟係於酸及有機溶 劑之存在下去除由上述反應所副生之水的步驟; &lt;5&gt;如上述&lt;4&gt;之製造方法’其中於酸及有機溶劑之存在 下去除由上述反應所副生之水的步驟係使由上述反應所副 生之水於酸及有機溶劑之存在下與有機溶劑共沸,藉此而 去除的步驟; &lt;6&gt;如上述&lt;4&gt;或&lt;5&gt;之製造方法’其中有機溶劑為芳香 族烴; &lt;7&gt;如上述&lt;6〉之製造方法,其中芳香族烴為甲苯或二曱 苯; &lt;8&gt;如上述 &lt;〗&gt; 至&lt;7&gt;中任一項之製造方法,其中酸係選 自由對甲苯磺酸、對曱苯磺酸水合物 '鹽酸及硫酸所組成 之群中之至少1種; &lt;9&gt;一種橡膠組合物’其包含利用如上述〇至&lt;8&gt;中任 一項之製造方法所獲得之縮合物、橡膠成分、填充劑、及 硫成分; &lt;1〇&gt;—種輪胎用帶束層,其包含由如上述&lt;9&gt;之橡膠組 合物所被覆之鋼簾線。 &lt;u&gt;—種輪胎用胎體,其包含由如上述&lt;9&gt;之橡膠組合 物所被覆之胎體纖維簾線; 162280.doc 201238958 12&gt;種輪胎用胎面膠或輪胎用基部膠,其包含如上述 &lt;9&gt;之橡膠組合物; ^^13 種充氣輪胎’其係藉由對如上述&lt;9&gt;之橡膠組合 物進行加工所製造; &lt;14&gt;一種間苯二酚與丙酮之縮合物,其滿足下述(1)、 (2)及(3): ^⑴於#!用凝膠滲透層析法(示差折射率檢測)對縮合物進 仃刀析時’由2,4,4_三甲基_2,,4,,7_三羥基黃酮所產生之波 峰之面積相對於所有波峰之合計面積的比為3 0〜5 5 之範 圍; ,(2)於利用凝膠渗透層析法(示差折射率檢測)對縮合物進 订刀析時,第-溶出波峰之面積相對於所有波峰之合計面 積之比為20〜50%之範圍; (3)上述第一溶出波峰之重量平均分子量為15〇〇〜17〇〇之 範圍; &lt;15&gt;如上述&lt;14&gt;之縮合物,其軟化點為16〇它以下; &lt;16〉如上述&lt;14&gt;或&lt;15&gt;之縮合物,其於l2〇t下保管μ 小時後之間苯二酚之增加率為2%以下。 【實施方式】 本發明之製造方法係間苯二酚與丙酮之縮合物之製造方 法,其包括: 使間苯二酚與丙酮於酸之存在下進行反應之步驟,及 於酸之存在下去除由上述反應所副生之水之步驟。 &lt;使間苯二酚與丙酮於酸之存在下進行反應之步騍(以下, J62280.doc 201238958 有時稱為「第1步驟」)&gt; 間苯二酚可使用市售品。丙酮亦可使用市售品◎丙鲷之 使用量為相對於間苯二酚i mo丨較佳為卜6 mol之範圍,更 佳為1.5〜4 mol之範圍。若丙酮之使用量為i m〇丨以上,則 有可減少未反應之間苯二酚之殘存率之傾向。 酸係於間苯二酚與丙酮之反應中作為觸媒而發揮作用 者,以下有時記載為「酸觸媒」。作為酸之具體例,可列 舉:苯磺酸、對甲苯磺酸、對甲笨磺酸水合物、草酸、磷 酸、聚磷酸、硼氟酸、鹽酸及硫酸。其中,較佳為選自由 對甲苯磺酸、對曱笨磺酸水合物、鹽酸及硫酸所組成之群 中之至少1種酸。該等酸可直接、或以適當濃度之水溶液 之形態使用。酸之使用量並無限制’相對於間苯二紛1 〇〇 mol較佳為〇·ι〜1〇 m〇i之範圍,更佳為〇 5〜5 m〇i之範圍。 間苯二盼與丙酮之反應較佳為於有機溶劑之存在下進 行。作為有機溶劑,可列舉:脂肪族烴、芳香族烴及經齒 基取代之芳香族烴。作為脂肪族烴之具體例,可列舉:己 烷、庚烷、辛烷及癸烷;作為芳香族烴之具體例,可列 舉:甲苯、二甲苯及乙基苯;作為經齒基取代之芳香族烴 之具體例,可列舉.氣本及一氣苯。較佳為芳香族烴,更 佳為甲苯或二甲苯。有機溶劑之使用量較佳為相對於間苯 二酚1重量份為0.5〜3重量份之範圍。 間苯二盼與丙嗣之反應之反應溫度較佳為3〇£&gt;c以上、 65°C以下之範圍。反應之進行可藉由氣相層析法(GC, chromatography)、高效液相層析法(ΗΡιχ ,Η· 162280.doc -6 · 201238958 performance liquid chromatography)、凝膠渗读 a ◊逐層析法 (GPC,gel-permeation chromatography)等通常之分析方 進行確認,可一面確認反應之進行一面決定反應終點 間苯二酚、丙酮、及酸之混合順序並無限定,例如可— 由使間苯二酌·與丙酮視需要而於有機溶劑之存在下見人 再使所獲得之混合物與酸於反應溫度條件下混合,— 反應。又’亦可隨著反應之進行’於混合物中連續 歇性地添加丙酮。隨著反應進行,有時間苯二__之 縮合物中所含之化合物之一的2,4,4_三f基_2,,4,,7_三經基 黃嗣會析出,為防止所析出之2,4,4·三甲基_2·,4,Ι三經基 黃酮固著於反應容器之壁上(所謂積垢),亦可使用2,4,4_^ 甲基·2’,4',7-三羥基黃酮作為種晶。再者,HA·三甲基_ 2·’4',7_三羥基黃酮係下述式所示之化合 。 HO、a η201238958 VI. Description of the Invention: [Technical Field of the Invention] The present invention relates to a method for producing a condensate of isophthalic acid and acetone, a rubber composition containing the condensate, and the like. [Prior Art] A condensate of resorcinol and acetone is used as a reinforcing agent for various rubber compositions. JP-A-2004-243 No. 1 discloses a method for producing a method in which resorcinol and acetone are reacted in the presence of an acid and an organic solvent, and then neutralized with an aqueous solution of cerium oxide, and further The neutralized mixture was dried under reduced pressure to obtain a condensate of resorcinol and acetone. SUMMARY OF THE INVENTION The present invention provides the following: &lt;1;&gt; A method for producing a condensate of resorcinol and acetone, comprising: a step of reacting resorcinol with acetone in the presence of an acid And the step of removing the water by-produced by the above reaction in the presence of I; &lt;2&gt; The manufacturing method of &lt;2&gt; as described above, which comprises: performing the treatment of m-diphenol and acetone in the presence of an acid a step of removing the water by-produced by the above reaction in the presence of hydrazine, and a step of mixing the mixture after removing the water with a base; &lt;3&gt; : a step of reacting resorcinol with acetone in the presence of an acid, 162280.doc 201238958 a step of a by-product water step, and a step of combining; removing the water after removal by the above reaction in the presence of an acid And a mixture of the mixture of the mixture of the acetone and the acetone, and the mixture of the mixture of the above-mentioned reaction, wherein the water produced by the above reaction is removed in the presence of an acid. The steps are based on acid and organic The step of removing the water by-produced by the above reaction in the presence of a solvent; &lt;5&gt; The method of producing the water by the above reaction in the presence of an acid and an organic solvent, as described in the above &lt;4&gt; And a step of removing the water by-produced by the above reaction with an organic solvent in the presence of an acid and an organic solvent, thereby removing; &lt;6&gt;&lt;4&gt; or &lt;5&gt; The organic solvent is an aromatic hydrocarbon. The method of the above <6>, wherein the aromatic hydrocarbon is toluene or diphenylbenzene; &lt;8&gt; is as described above in &lt;&gt;&gt; to &lt;7&gt; A method of producing, 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; &lt;9&gt; a rubber composition comprising The condensate, the rubber component, the filler, and the sulfur component obtained by the production method according to any one of the above-mentioned items <8>, wherein the belt layer for a tire is contained as described above. &lt;9&gt; The steel cord covered by the rubber composition. &lt;u&gt; - A tire carcass comprising a carcass fiber cord coated with the rubber composition as described in <9> above; 162280.doc 201238958 12&gt; Tyre rubber for tires or base rubber for tires And the rubber composition of the above &lt;9&gt;; ^13 kinds of pneumatic tires which are produced by processing the rubber composition as described above in &lt;9&gt;;&lt;14&gt; a resorcinol a condensate with acetone which satisfies the following (1), (2), and (3): ^(1) at #! by gel permeation chromatography (differential refractive index detection) when the condensate is subjected to cleavage analysis The ratio of the area of the peak generated by the 2,4,4-trimethyl-2,4,7-trihydroxyflavone relative to the total area of all the peaks is in the range of 3 0 to 5 5 ; (2) When the condensate is subjected to a solution by gel permeation chromatography (differential refractive index detection), the ratio of the area of the first elution peak to the total area of all the peaks is in the range of 20 to 50%; (3) The weight average molecular weight of a dissolved peak is in the range of 15 〇〇 to 17 ;; &lt;15&gt; The condensate of the above &lt;14&gt; has a softening point of 16 〇. The condensate of the above &lt;14&gt; or &lt;15&gt; is stored at 12 Torr for 1 hour, and the rate of increase of the benzenediol is 2% or less. [Embodiment] The production method of the present invention is a process for producing a condensate of resorcinol and acetone, which comprises the steps of: reacting resorcin with acetone in the presence of an acid, and removing it in the presence of an acid. The step of water by-produced by the above reaction. &lt;Step of reacting resorcin with acetone in the presence of an acid (hereinafter, J62280.doc 201238958 may be referred to as "first step")&gt; A commercial product may be used for resorcin. The acetone may also be used in the range of 1.5 mol, more preferably 1.5 to 4 mol, based on the amount of the resorcinol i mo丨. When the amount of acetone used is i m 〇丨 or more, there is a tendency to reduce the residual ratio of unreacted benzenediol. The acid acts as a catalyst in the reaction between resorcin and acetone, and may be described as "acid catalyst" hereinafter. 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 them, at least one acid selected from the group consisting of p-toluenesulfonic acid, p-toluenesulfonic acid hydrate, hydrochloric acid and sulfuric acid is preferred. These acids can be used either directly or in the form of an aqueous solution of a suitable concentration. The amount of acid used is not limited to the range of 〇·ι~1〇 m〇i, and more preferably 〇5 to 5 m〇i. The reaction of m-phenylene with acetone is preferably carried out in the presence of an organic solvent. The organic solvent may, for example, be an aliphatic hydrocarbon, an aromatic hydrocarbon or a dentate-substituted aromatic hydrocarbon. Specific examples of the aliphatic hydrocarbons include hexane, heptane, octane, and decane; and specific examples of the aromatic hydrocarbons include toluene, xylene, and ethylbenzene; Specific examples of the hydrocarbons include gas and benzene. It is preferably an aromatic hydrocarbon, more preferably toluene or xylene. The amount of the organic solvent to be used is preferably in the range of 0.5 to 3 parts by weight based on 1 part by weight of the resorcin. The reaction temperature of the reaction of m-phenylene and propylene is preferably in the range of 3 Å or more and 65 ° C or less. The reaction can be carried out by gas chromatography (GC, chromatography), high performance liquid chromatography (ΗΡιχ, Η·162280.doc -6 · 201238958 performance liquid chromatography), gel permeation a ◊ chromatography (GPC, gel-permeation chromatography), etc., confirming the normal analysis, and confirming the progress of the reaction, determining the reaction end point, the order of mixing the resorcinol, acetone, and acid is not limited, for example, The mixture is reacted with acetone in the presence of an organic solvent as needed, and the obtained mixture is mixed with an acid at a reaction temperature to react. Further, acetone may be continuously added to the mixture as the reaction progresses. As the reaction proceeds, 2,4,4_trif-based 2,4,7-7-trisole, which is one of the compounds contained in the condensate of the benzene __, precipitates in order to prevent precipitation. 2,4,4·trimethyl-2·,4, stilbene flavonoids are fixed on the wall of the reaction vessel (so-called scale), and 2,4,4_^methyl·2' can also be used. 4',7-trihydroxyflavone as seed crystal. Further, HA·trimethyl _ 2·'4', 7-trihydroxyflavone is a compound represented by the following formula. HO, a η

作為間苯二齡與丙嗣之縮合物中所含之化合物,1 外Μ-三曱基·2.,4,,7_三經基黃酮(下述式所示之化合物)As a compound contained in the condensate of meta-phenylene and acetophenone, 1 fluorene-trisyl group, 2., 4, 7-trisyl flavonoid (compound represented by the following formula)

ΟΗ 162280.doc 201238958 可列舉:7,7·-二羥基-4,4,4’,4'-四曱基-2,2·-螺二環己烷 (下述式所示之化合物), h3c chs h3c ch8 4,6-雙(7-羥基-2,4,4-三曱基色滿-2-基)-1,3_苯二酚(式(I) 所表示之化合物)及其異構物,162 162280.doc 201238958, exemplified by 7,7-dihydroxy-4,4,4',4'-tetradecyl-2,2·-spirobicyclohexane (compound represented by the following formula), H3c chs h3c ch8 4,6-bis(7-hydroxy-2,4,4-trimethylchroman-2-yl)-1,3-benzenediol (compound represented by formula (I)) and its Structure,

h3c ch3 2,4-雙(7-羥基-2,4,4-三甲基色滿-2-基)-1,3-苯二酚(式(II) 所表示之化合物)及其異構物,H3c ch3 2,4-bis(7-hydroxy-2,4,4-trimethylchroman-2-yl)-1,3-benzenediol (compound represented by formula (II)) and its isomer Object,

式(III)所表示之化合物及其異構物,及 h3c. xh3a compound represented by formula (III) and an isomer thereof, and h3c. xh3

162280.doc (IV) (IV) 201238958 式(ιν)所表示之化合物及其異構物,162280.doc (IV) (IV) 201238958 A compound represented by the formula (ιν) and an isomer thereof,

[式(IV)中’ n表示2以上之整數]。 &lt;於酸之存在下去除由上述反應所副生之水之步驟(以下 有時稱為「第2步驟」)&gt; ;自文之存在下去除由間苯二酚與丙酮之反應所副生之冰 的步驟亦可與使間苯二酚與丙酮於酸之存在下進行反應的 步驟同時進行’但為有效地進行水之去除,較佳為於使間 苯二盼與丙酮於酸之存在下進行反應之後,再於酸之存在 下去除由上述反應所副生之水。於該步驟令去除水所獲得 之混合物包含間苯二紛與丙酮之縮合物及酸。 進亦可利用可吸附水之物質或可分解水之物質而 之存在補由蒸㈣進行,更㈣11由於有機溶劑 之存在下使有機溶劑與水m 獲得之㈣中通常含有水,可藉二=或共相 除’但於錄分離為有機層與水層之情形^進仃水之去 水層分離去除,而有機層恢復至昆 夸,較佳為僅將 為進行至去除水所獲得之混合物水之去除較佳 %為止’更佳為進行至含水率成為G抓〜2重量 重4為止。[in the formula (IV), 'n represents an integer of 2 or more>. &lt;Step of removing water by-produced by the above reaction in the presence of an acid (hereinafter sometimes referred to as "second step")&gt;; removal of reaction by resorcinol and acetone in the presence of the text The step of raw ice can also be carried out simultaneously with the step of reacting resorcinol with acetone in the presence of an acid 'but effective for water removal, preferably for the purpose of making isophthalic acid and acetone in acid After the reaction is carried out in the presence of water, the water by the above reaction is removed in the presence of an acid. The mixture obtained by removing water in this step contains a condensate of isophthalic acid and acetone and an acid. It can also be carried out by using a substance capable of adsorbing water or a substance which can decompose water, and the addition of steam (4) is carried out, and (4) 11 is obtained by the organic solvent and water m in the presence of an organic solvent, and the water usually contains water. Or co-divisional 'but in the case of separation into an organic layer and an aqueous layer ^ separate into the dewatering layer of the hydrophobic water, and the organic layer is restored to Kunqu, preferably only to the mixture obtained by removing the water It is preferable that the removal of water is preferably carried out until the water content is G-grass to 2 weights and 4 weights.

162280,(j〇Q 201238958 作為有機溶劑,通常使用間苯二酚與丙酮之反應中所使 用之有機溶劑,但亦可制與此*同之有機溶劑。作為有 機吟齊丨,可列舉:戊烷、己烷、庚烷等脂肪族烴,環戊 烷、環己烷、甲基環己烷等脂環式烴,笨、甲苯、二曱苯 等芳香族烴,二氯甲烷'氣仿、四氣化碳、三氣乙烯、四 氣乙烯、二氣乙烯、氯化苯等氯化烴,乙酸甲酯、乙酸乙 雖、乙酸丙酯等醋’及乙腈等腈。其中,較佳為芳香族 煙’更佳為曱苯或二曱苯。 可將藉由第1步驟及第2步驟所獲得之混合物直接交付至 下述後處理步驟,或亦可視需要於進而交付至下述第3步 驟之後再交付至後處理步驟。 〈使去除水後之混合物與丙酮混合之步驟(以下,有時稱為 「第3步驟」 更佳為,使於酸之存在下去除由間苯二酚與丙酮之反應 所剎生之水後的混合物、與丙酮混合。第3步驟係使殘存 於包a間笨二酚與丙酮之縮合物及酸之混合物中的間苯二 盼、與丙酮進行反應之步驟。 關於第3步驟中所使用之丙酮之使用量,與第丨步驟中所 $用之丙酮之使用量之合計相對於第丨步驟中所使用之間 苯二酚1 〇1〇1為1〜6 m〇l之範圍的量即可。亦可視需要而於 第3步驟中使用酸或有機溶劑。第3步驟之反應溫度較佳為 3〇 C以上、65。〇以下之範圍。又,第3步驟亦可一面去除 水一面進行。關於水之去除,可與第2步驟相同地進行。 關於第3步驟,一面利用GC、hplc、GPC等通常之分析方 162280.doc •10- 201238958 法確ι2’4,4 一曱基_2’’4,,7·三羥基黃酮之 酚之含有率,一面適冬祐扒工 ,手及間本一 阁、i , 丙_直至該等成為所期望之範 圍’以此方式實施即可。 &lt;後處理步驟&gt; 將第2步驟或第3步驟中所獾、 ;t ^ ^ . 侍之混5物交付至包括過濾 戈/晨細·#之後處理步驟ψ,土卩人丄 — 去除有機溶劑,藉此可獲取間 本二酚與丙酮之縮合物。 &lt;使去除水後之混合物與驗混合之步驟&gt; 於將第2步驟或第3步驟 斤獲侍之此合物以鹼進行中和 後’藉由水洗或過濾進行固液分 附著於所獲得之固形物“見需要而於對 酉夂觸媒或由中和所生成之鹽進行 水洗之後,去除有機溶劑。 气““ 乍為驗’可列舉:氫氧化鈉、 =化鉀4驗金屬氫氧化物,碳酸氫納等驗金屬碳酸氣 瓜碳酸鈉等鹼金屬碳酸睡$ 审m 厌敗现等,較佳為鹼金屬氫氧化物,162280, (j〇Q 201238958 As an organic solvent, an organic solvent used in the reaction of resorcin and acetone is usually used, but an organic solvent similar to this can be used. As an organic solvent, pentane is mentioned. An aliphatic hydrocarbon such as an alkane, hexane or heptane; an alicyclic hydrocarbon such as cyclopentane, cyclohexane or methylcyclohexane; an aromatic hydrocarbon such as stupid, toluene or diphenylbenzene; a chlorinated hydrocarbon such as four gasified carbon, three gas ethylene, four gas ethylene, two gas ethylene, chlorinated benzene, a acetonitrile such as methyl acetate, ethyl acetate, propyl acetate or the like, and a nitrile such as acetonitrile. Among them, aroma is preferred. The family cigarette is more preferably benzene or diphenyl. The mixture obtained by the first step and the second step can be directly delivered to the following post-treatment step, or can be further delivered to the following step 3 as needed. Then, it is delivered to the post-treatment step. <The step of mixing the mixture after removing water with acetone (hereinafter, sometimes referred to as "the third step" is more preferable to remove the resorcinol and acetone in the presence of acid. The mixture after the reaction with the water is mixed with acetone. The third step is a step of reacting with the acetone in the mixture of the condensate of the diphenanthrene and the acetone and the acid, and reacting with the acetone. The amount of acetone used in the third step is the same as that used in the third step. The total amount of acetone used may be in the range of 1 to 6 m〇l relative to the amount of the resorcinol 1 〇1〇1 used in the second step. It may also be in the third step as needed. The acid or organic solvent is used. The reaction temperature in the third step is preferably in the range of 3 〇 C or more and 65 〇 。. Further, the third step can be carried out while removing water. With respect to water removal, the second step can be performed. The third step is to use the usual analysis method such as GC, hplc, GPC, etc. 162280.doc •10-201238958 to make ι2'4,4-mercapto-2''4,7-trihydroxyflavone The content of phenol is one of the best for the winter, the hand and the room, i, c _ until these are the desired range 'can be implemented in this way. &lt;post-processing steps> will be the second Step or step 3, t, ; ^ ^ ^. 侍之混5 delivery to include filtering Ge / Chen Xi·# The treatment step ψ, the soil cockroach 丄 - remove the organic solvent, thereby obtaining the condensate of the meta-diphenol and acetone. &lt;Step of mixing the mixture after removing water&gt; in the second step or the third After the step is neutralized with a base, the solid solution is attached to the obtained solid by washing with water or by filtration. "If necessary, the salt formed by the catalyst or neutralized is carried out. After washing with water, the organic solvent is removed. The gas "" 乍 test" can be enumerated: sodium hydroxide, = potassium, 4 metal hydroxide, sodium bicarbonate, etc., metal carbonate, carbonic acid, sodium carbonate, etc. Depressed, etc., preferably alkali metal hydroxide,

更佳為虱氧化鈉。鹼較佳A 使用。 ㈣佳為以適當濃度之水溶液之形態而 間苯二酚之殘留率較 量%以下。 較佳為5.〇重量%以下,更佳為!』重 &lt;所獲得之縮合物&gt; 於本發明中,所謂「 膠滲透層析法m 」’意指:於利用凝 得之心 射率檢測)對縮合物進行分析時所獲 仔之層析圖中之所右油1 t 1頌· 「 /峰中,保持時間最短之波峰;所謂 ^ ;皮峰」,意指:於利用凝膠渗透層析法 射率檢測)對縮合物進行分析時所獲得之層析圖中之所^ 162280.doc 201238958 :峰::保持時間第二短之波峰;所胃「第三 膠滲透層析法(示 第三短之波峰。 之所有波峰中,保持時間 於凝膠滲透層析法(示差折射率檢測)中包含式卿斤 :不之化合物及其異構物之化合物群係設為第 峰,包含式(III)所表示之化合物及 波 異構物之化合物群係 2第-溶出“’包含式⑴所表示之化合物及其異構 以及式(II)所表示之化合物及其 異構物之化合物群係 »又為第一,合出波峰,分別進行檢測。 所獲得之縮合物較佳為滿足下述⑴、⑺及(3)之縮合 物。 於利用凝膠渗透層析法(示差折射率檢測)對縮合物進 斤時,因2,4,4-三甲基_2,,41,7_三羥基黃酮所產生之波 面積相對於所有波峰之合計面積的比為3㈣$ 圍; ⑺於利用凝膠滲透層析法(示差折射率檢測)對縮合物進 仃分析時,第一溶出波峰之面積相對於所有波峰之合計面 積之比為20〜50%之範圍; (3)上述第一溶出波峰之重量平均分子量為⑼㈡_之 範圍。 所獲仔之縮合物較佳為軟化點為i6〇t以下。 所獲得之縮合物較佳為於J 2 〇。。下保管2 4小時後之間苯 二齡之增加率為2%以下。 162280.doc 201238958 甲基-2’,4’,7-三羥基黃 圍’更佳為35〜50重量 所獲得之縮合物中所含之2,4,4-三 酮之含有率較佳為30〜55重量%之範 °/〇之範圍。 所獲得之縮合物t所含之4,6·雙(7,基_2,4,4•三甲基色 滿-2-基H,3-苯二酹(式⑴所表示之化合物)及其異構‘、 以及2斗雙(7-經基_2,4’4_三甲基色滿基h,3•苯二紛(式 (II)所表示之化合物)及其異構物之合計之含有率較佳為 5〜10重量%之範圍。 所獲得之縮合物中所含之式_所表示之化合物及其異 構物之合計的含有率較佳為5〜15重量%之範圍。 所獲得之縮合物中所含之式(IV)所表示之化合物及其異 構物之合計的含有率較佳為2〇〜5〇重量%之範圍,更佳為 25〜35重量%之範圍。 所獲得之間苯二酚與丙酮之縮合物可用作橡膠之補強 劑。尤其是用作輪胎用橡膠之補強劑。 接著’針對包含間苯二酚與丙酮之縮合物、橡膠成分、 填充劑、及硫成分之橡膠組合物進行說明。 作為橡膠成分,可列舉:天然橡膠、苯乙烯丁二烯共聚 橡膠、丁二烯橡膠、異戊二烯橡膠、及以該等為主成分之 橡膠成分。間苯二酚與丙酮之縮合物之使用量相對於該等 橡膠成分100重量份較佳為〇.5〜3重量份之範圍,更佳為 1〜2重量份之範圍。 作為填充劑,可列舉橡膠領域中通常所使用之碳黑、二 氧化矽、滑石及黏土,更佳地使用碳黑。作為碳黑,較佳 I62280.doc .13· 201238958 為 HAF(High Abrasion Furnace,高对磨碳黑)、More preferably, it is sodium oxide. The base is preferably used in A. (4) Preferably, the residual ratio of resorcinol is less than or equal to % of the aqueous solution in an appropriate concentration. It is preferably 5.% by weight or less, more preferably! "Heavy &lt; Obtained Condensate&gt; In the present invention, the term "gel permeation chromatography m" means: the layer obtained when the condensate is analyzed by the centrifugation rate detection of coagulation) In the figure, the right oil 1 t 1颂· "/ peak, the peak with the shortest retention time; so-called ^; skin peak" means: using gel permeation chromatography to detect the condensate) In the chromatogram obtained at the time 162280.doc 201238958: Peak:: the second shortest peak of the retention time; the stomach "third gel permeation chromatography (showing the third short peak. Among all the peaks, The retention time is included in the gel permeation chromatography (differential refractive index detection): the compound group of the compound and its isomer is set as the peak, and the compound represented by the formula (III) and the wave are included. The compound group 2 of the structure-dissolution "' contains the compound represented by the formula (1) and its isomer and the compound represented by the formula (II) and the compound group thereof of the isomer thereof are again the first, and the peak is combined The detection is performed separately. The condensate obtained preferably satisfies the following (1), (7) (3) Condensate. When using gel permeation chromatography (differential refractive index detection) for condensate, due to 2,4,4-trimethyl-2,41,7-trihydroxyflavone The ratio of the generated wave area to the total area of all the peaks is 3 (four) $; (7) When the condensate is analyzed by gel permeation chromatography (differential refractive index detection), the area of the first eluted peak is relative to all The ratio of the total area of the 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 (9) (b) _. The condensate of the obtained condensate preferably has a softening point of i6 〇t or less. The obtained condensate is preferably J 2 〇. The increase rate of the benzene age is 2% or less after storage for 24 hours. 162280.doc 201238958 Methyl-2',4',7-trihydroxy yellow The content of 2,4,4-trione contained in the condensate obtained by more preferably 35 to 50 parts by weight is preferably in the range of 30 to 55 % by weight. 4,6·bis(7,yl-2,4,4•trimethylchroman-2-yl H,3-benzenediindole (a compound represented by the formula (1)) and its isomerization,And the content ratio of 2 buckets (7-carbyl-2,4'4_trimethylchromanyl h,3•benzoic acid (the compound represented by formula (II)) and its isomers It is preferably in the range of 5 to 10% by weight. The total content of the compound represented by the formula _ and the isomer thereof contained in the obtained condensate is preferably in the range of 5 to 15% by weight. The content of the compound represented by the formula (IV) and the total amount of the isomer thereof contained in the product is preferably in the range of 2 Å to 5 Å by weight, more preferably in the range of 25 to 35% by weight. A condensate of resorcinol and acetone can be used as a reinforcing agent for rubber. In particular, it is used 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 a rubber component containing these as a main component. The amount of the condensate of resorcin and acetone is preferably in the range of from 0.5 to 3 parts by weight, more preferably from 1 to 2 parts by weight, per 100 parts by weight of the rubber component. Examples of the filler include carbon black, cerium oxide, talc, and clay which are generally used in the rubber field, and carbon black is more preferably used. As carbon black, it is preferable that I62280.doc .13· 201238958 is HAF (High Abrasion Furnace),

Abrasion Furnace,超耐磨碳黑)、 SAF,中超耐磨碳黑)等碳黑。又,併用碳黑與三氧化石夕等 將數種填充劑進行組合之方式亦較佳。填充劑之使用量相 對於橡膠成分每1〇〇重量份較佳為1〇〜1〇〇重量份之範圍, 更佳為30〜70重量份之範圍。 作為硫成分,可列舉:硫粉末、沈澱硫、膠態硫、不溶 性硫及高分散性硫,較佳為硫粉末及不溶性硫。硫成分之 使用量相對於橡膠成分每100重量份較佳為卜⑺重量份之 Ιϋ圍’更佳為2〜6重量份之範圍。 進而,可使用硫化促進劑、甲氧基化羥甲基三聚氰胺樹 脂、有機鈷化合物及氧化鋅製造橡膠組合物。 作為硫化促進劑之例,可列舉橡膠工業便覽 &lt; 第四版&gt; (平成6年1月20日社團法人日本橡膠協會發行)之412〜413 頁所5己載之噻唑系硫化促進劑、亞磺醯胺系硫化促進劑及 胍系硫化促進劑。硫化促進劑之使用量相對於橡膠成分每 100重量份較佳為〇.5〜1重量份之範圍,更佳為0.6〜0.8重量 份之範圍。 作為甲氧基化羥甲基三聚氰胺樹脂,可列舉:六(甲氧 基甲基)三聚氰胺、五(甲氧基甲基)羥甲基三聚氰胺、四 (曱氧基甲基)二羥甲基三聚氰胺等橡膠工業中通常使用 者’較佳為單獨之六(甲氧基甲基)三聚氰胺或以其為主成 分之混合物。該等甲氧基化羥甲基三聚氰胺樹脂可分別單 獨使用’或將兩種以上組合而使用,其調配量相對於橡膠 162280.doc 201238958 成分100重量份較佳為0.5〜6.0重量份之範圍,更佳為 1·〇〜3·〇重量份之範圍。 作為有機鈷化合物,可列舉:環烷酸鈷、硬脂酸鈷等酸 鈷鹽,或脂肪酸鈷.硼錯合物(例如,商品名「Man〇b〇nd C(5主冊商標)」:Manchem公司製造卜關於有機鈷化合物之 使用量,相對於橡膠成分100重量份,換算為鈷含量,較 佳為0.1〜0.4重量份之範圍,更佳為〇1〜〇 3重量份之範 圍。 亦可視需要而使用橡膠工業中通常使用之各種橡膠化學 扣,例如:抗氧化劑或抗臭氧化劑之類之抗老化劑、膠溶 劑、加工助劑、蠟、油、硬脂酸、賦黏劑等之丨種或2種以 上。該等化學品之調配量係根據橡膠組合物之用途而有所 不同,但分別可使用橡膠工業中通常使用之範圍之量。 橡膠組合物例如係藉由依據橡膠業界中通常所實施之方 法經由成形、硫化等步驟,而可衍生為橡膠製品β尤其是 可用於輪胎之各種構件,例如:胎面膠、基部膠、帶束 層、胎體、胎緣、胎壁、橡膠包布等。又,亦可用於引擎 腳、避震器上座、襯套、排氣管吊耳等汽車用抗振橡膠, 軟管類,橡膠皮帶等。 例如’可藉由以橡膠組合物被覆鋼簾線而製造輪胎用帶 束層。鋼簾線通常以拉齊之狀態而使用。 就與橡膠之接著性之觀點而言,鋼簾線較佳為以黃鋼 鋅、或於其中含有鎳或鈷之合金進行鍍敷處理,特佳為實 施有黃銅鍍敷處理者。尤其是,實施有黃銅鍍敷中之匚口之 162280.doc 15 201238958 含有率為75重量%以下、較佳為55〜70重量%之黃銅鍍敷處 理的鋼簾線較為合適。鋼簾線之扭絞結構並無限制》 帶束層亦可積層複數片而使用。帶束層主要用作胎體之 補強材料。 又,例如’亦可將橡膠組合物依照輪胎之胎體形狀進行 擠壓加工’並貼附於胎體纖維簾線之上下,藉此而製造胎 體月。體纖維簾線通常以平行地拉齊之狀態而使用。作為 胎體纖維簾線,較佳為彈性模數及耐疲勞性良好、耐蠕變 性亦優異、且廉價之聚酯。該等係藉由i片或積層複數片 而用作輪胎補強材料。 可使用橡膠組合物利用通常之製造方法而製造充氣輪 胎。例如’對橡膠組合物進行擠壓加工而獲得輪胎用構 件’再於輪胎成形機上利用通常之方法使其貼附於其他輪 胎構件上而絲,形成生胎。於硫化機中對該生胎進行加 熱加壓而獲得輪胎。 實施例 以下,藉由實施例及試驗例具體說明本發 以下之實施例中,2,4,4-三甲美2,4|7 、 -^ 土 2,4,7-二羥基黃酮及間苯 一酚之含有率係利用Gpc面 制-—⑼ ㈣百刀率法而求出。軟化點之 測疋係依據JIS Κ6220-1實施。 示「重量份」。 又於貫施例中,「份」表 於GPC分析中,包含式(Ιν _ 之化合物群係、設為第-溶出波峰,^合物及其異構物 合物及其異構物之化合物群表示之化 ^乐一W合出波峰,包含式 162280.doc 201238958 (I)所表示之化合物及其異構物、以及式(II)所表示之化合 物及其異輪物之化合物群係設為第三溶出波峰,進行檢 測。 &lt;GPC分析條件&gt; 管柱:使 TOSOH TSGel Super HZ2000(4.6 mm 卢xl5〇 cm) 與 TOSOH TSGel Super HZ1000(4.6 mm 多 xl50 cm)2 根連接Carbon black such as Abrasion Furnace, super wear-resistant carbon black, SAF, medium wear-resistant carbon black. Further, it is also preferable to use a combination of a plurality of fillers such as carbon black and sulphur trioxide. The amount of the filler to be used is preferably in the range of 1 Torr to 1 Torr, more preferably in the range of 30 to 70 parts by weight per 1 part by weight of the rubber component. Examples of the sulfur component include sulfur powder, precipitated sulfur, colloidal sulfur, insoluble sulfur, and highly dispersible sulfur, and sulfur powder and insoluble sulfur are preferred. The amount of the sulfur component to be used is preferably in the range of 2 to 6 parts by weight based on 100 parts by weight of the rubber component. Further, a rubber composition can be produced using a vulcanization accelerator, a methoxylated methylol melamine resin, an organic cobalt compound, and zinc oxide. As an example of the vulcanization accelerator, there are thiazole-based vulcanization accelerators, which are contained in 412 to 413 pages of 412 to 413 pages of the Rubber Industry Fact Sheets, "The Fourth Edition" (issued by the Japan Rubber Association, January 20, 2008). A sulfoximine vulcanization accelerator and an oxime vulcanization accelerator. The amount of the vulcanization accelerator to be 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 hexakis(methoxymethyl)melamine, penta(methoxymethyl)hydroxymethylmelamine, and tetrakis(methoxymethyl)dimethylol melamine. The usual user in the rubber industry is preferably 'single hexa(methoxymethyl)melamine alone or a mixture thereof as a main component. These methoxylated methylol melamine resins may be used singly or in combination of two or more kinds, and the amount thereof is preferably in the range of 0.5 to 6.0 parts by weight based on 100 parts by weight of the rubber 162280.doc 201238958 component. More preferably, it is a range of 1·〇~3·〇 by weight. Examples of the organic cobalt compound include acid cobalt salts such as cobalt naphthenate and cobalt stearate, or fatty acid cobalt and boron complex compounds (for example, trade name "Man〇b〇nd C (5 main volume trademark)": The amount of the organic cobalt compound to be used by Manchem is preferably in the range of 0.1 to 0.4 parts by weight, more preferably in the range of 〇1 to 〇3 parts by weight, based on 100 parts by weight of the rubber component. Various rubber chemical buckles commonly used in the rubber industry, such as anti-aging agents such as antioxidants or anti-odor oxidizing agents, peptizers, processing aids, waxes, oils, stearic acid, adhesives, etc., may be used as needed. The amount of the chemicals may vary depending on the use of the rubber composition, but the amount generally used in the rubber industry may be used. The rubber composition is, for example, based on the rubber industry. The method generally carried out can be derivatized into a rubber product β, in particular, various components that can be used for a tire, such as a tread rubber, a base rubber, a belt layer, a carcass, a bead, and a sidewall, through steps of forming, vulcanization, and the like. , rubber blankets, etc. Also, it can be used for anti-vibration rubber, hoses, rubber belts, etc. for engines such as engine feet, shock absorber seats, bushings, exhaust pipe hangers, etc. For example, 'by rubber combination The steel cord is coated with a steel belt to produce a belt layer for a tire. The steel cord is usually used in a state of lacy. In terms of adhesion to rubber, the steel cord is preferably made of yellow steel or zinc. An alloy containing nickel or cobalt is subjected to a plating treatment, and particularly preferably a brass plating treatment is carried out. In particular, a 162280.doc 15 201238958 having a mouthwash in brass plating is used, and the content is 75 wt% or less. Preferably, the brass-plated steel cord is preferably 55 to 70% by weight. The twisted structure of the steel cord is not limited. The belt layer may also be used in a plurality of layers. The belt layer is mainly used as a tire. Further, for example, 'the rubber composition may be extrusion-processed according to the carcass shape of the tire' and attached to the carcass fiber cord above and below, thereby producing a carcass month. Usually used in a state of parallel lagging. As a carcass fiber The cord is preferably a polyester which is excellent in modulus of elasticity and fatigue resistance, excellent in creep resistance, and inexpensive, and is used as a tire reinforcing material by using an i-piece or a plurality of laminated sheets. The pneumatic tire is manufactured by a usual manufacturing method, for example, 'the rubber composition is subjected to extrusion processing to obtain a member for a tire', and then attached to other tire members by a usual method on a tire molding machine to form a yarn. The tire is obtained by heating and pressurizing the green tire in a vulcanizer. EXAMPLES Hereinafter, in the examples and the following examples, 2,4,4-trisole 2 will be specifically described by way of examples and test examples. 4|7, -^ The content of 2,4,7-dihydroxyflavone and m-phenylene phenol is determined by the Gpc method--(9) (four) hundred-knife rate method. The softening point is measured according to JIS Κ6220 -1 implementation. Show "parts by weight". Further, in the examples, the "parts" table contains a compound of the formula (Ιν _, a set-dissolved peak, a compound, an isomer thereof, and an isomer thereof) in a GPC analysis. The group represents the compound, and the compound represented by the formula 162280.doc 201238958 (I), and the isomer thereof, and the compound represented by the formula (II) and the compound group thereof The third elution peak was detected. &lt;GPC analysis conditions&gt; Column: TOSOH TSGel Super HZ2000 (4.6 mm Lu xl5〇cm) was connected to TOSOH TSGel Super HZ1000 (4.6 mm x l50 cm)

溫度:40°C 流動相:四氫呋喃 檢測器:RI 實施例1 於具備溫度计、授拌機及冷凝器之1000 ml之四口燒瓶 中’加入間苯二酚198.2 g(l .8 mol) ’於對燒瓶内部進行氮 氣置換後,加入丙酮167.3 g(2.88 mol)及曱苯501 g。於使 所獲得之混合物升溫至40°C後’加入98%之硫酸1.98 g。 使所獲得之混合物升溫至内溫為60〇c,保溫4小時。 此後,於内溫為60 C之狀態下對燒瓶内部進行減壓而自 反應系統内將水去除〇於該溫度下加入丙酮52.3 g(〇 9 mol),一面對燒瓶内部進行減壓而自反應系統内將水去 除,一面將所獲得之混合物於6(rc下保溫2小時。此後, 利用10%之氫氧化鈉水溶液進行中和,進而KPa以下之 減屢下、於8G°C下進行乾燥12小時,獲得間苯二紛與丙_ 之縮合物313 g。所獲得之縮合物中之2,4,4_三甲基_2·,4,,7· 二經基黃酮及間本二酚之含有率分別如下。 2,4,4-三甲基-2i,4,,7-三羥基黃酮:44 4% I62280.doc -17- 201238958 間苯二紛:0,7〇/。 第一溶出波峰:34.1% 第一溶出波峰之重量平均分子量:1441 軟化點:144°C 實施例2 於具備溫度計、攪拌機及冷凝器之500 ml四口燒瓶中, 加入間笨二酚88.1 g(〇.8 mol),於對燒瓶内部進行氮氣置 換後’加入丙酮65.0 g(l. 12 mol)及甲苯132 g。於使所獲 得之混合物升溫至4〇°c後,加入98%之硫酸〇.88 g ^使所 獲得之混合物升溫至内溫為50°c,保溫4小時。此後,進 &quot;f亍升/皿直至内溫為6 〇 c為止’並對燒瓶内部進行減壓而自 反應系内將水去除。恢復至常壓’於冷卻至45。〇之後,加 入丙酮69.7 g(l .2 mol),將所獲得之混合物於該溫度下保 溫3.5小時。此後,利用1〇%之氫氧化鈉水溶液進行中和, 進而於1 KPa以下之減壓下、於8(rc下進行乾燥12小時, 獲知間苯二酚與丙酮之縮合物丨36 g。所獲得之縮合物中 之2,4’4-三曱基_2,,4,,7-三羥基黃酮及間苯二酚之含有率分 別如下。 2,4,4-三甲基_2’,4’,7-三羥基黃酮:50.4重量% 間苯二酚:0.9重量% 實施例3 於具備溫度計、攪拌器及冷凝器之5〇〇凼之四口 :〇入間苯二酚88.1g(〇.8mol),於對燒瓶内部進行氮 氣置換後,加入丙酮65 〇 gG 12 m〇1)及曱笨223 。 §。於蚀 I62280.doc -18. 201238958 所獲得之混合物升溫至40〇c後,加入98%之硫酸〇 40 g。 使所獲得之混合物升溫至内溫為5(rc,保溫3 5小時。於 内溫為60 C之狀態下對燒瓶内部進行減壓而自反應系内將 水去除。恢復至常壓,加入丙酮69 7 g(i 2 m〇丨),並將所 獲得之混合物於該溫度下保溫5小時,此後,以1〇%之氫 氧化鈉水溶液進行中和,進而於1 KPa以下之減壓下、於 80 C下進行乾燥12小時,獲得間苯二酚與丙酮之縮合物 136 g。所獲得之縮合物中之2,4,4_三甲基_2,,4,,7_三羥基黃 酮及間苯二酚之含有率分別如下。 2,4,4-三甲基-2’,4’,7-三羥基黃酮:45.8重量% 間苯二酚:〇·97重量% 第一溶出波峰:28.1%Temperature: 40 ° C Mobile phase: Tetrahydrofuran detector: RI Example 1 Adding resorcinol 198.2 g (1.8 mol) to a 1000 ml four-necked flask equipped with a thermometer, a mixer and a condenser After replacing the inside of the flask with nitrogen, 167.3 g (2.88 mol) of acetone and 501 g of toluene were added. After the obtained mixture was heated to 40 ° C, 1.98 g of 98% sulfuric acid was added. The obtained mixture was allowed to warm to an internal temperature of 60 ° C and kept for 4 hours. Thereafter, the inside of the flask was depressurized while the internal temperature was 60 C, and water was removed from the reaction system. At this temperature, 52.3 g of acetone (〇9 mol) was added, and the inside of the flask was depressurized. The water was removed in the reaction system, and the obtained mixture was kept at 6 (rc) for 2 hours. Thereafter, it was neutralized with a 10% aqueous sodium hydroxide solution, and further reduced by KPa or less at 8 G ° C. After drying for 12 hours, 313 g of a condensate of isophthalic acid and propylene was obtained. 2,4,4-trimethyl-2·,4,,7·di-based flavonoids and a mixture were obtained in the obtained condensate. The content of diphenol is as follows: 2,4,4-trimethyl-2i,4,,7-trihydroxyflavone: 44 4% I62280.doc -17- 201238958 Benzene: 0,7〇/. First elution peak: 34.1% Weight average molecular weight of the first elution peak: 1441 Softening point: 144 ° C Example 2 In a 500 ml four-necked flask equipped with a thermometer, a stirrer, and a condenser, 88.1 g of streptophenol was added ( 〇.8 mol), after replacing the inside of the flask with nitrogen, 'add 65.0 g of acetone (1.1 mol) and 132 g of toluene. After warming to 4 ° C, add 98% barium sulfate .88 g ^ and warm the mixture to an internal temperature of 50 ° C for 4 hours. After that, enter &quot;f亍 / dish until the internal temperature is 6 〇c' and the inside of the flask was decompressed and the water was removed from the reaction system. After returning to normal pressure, it was cooled to 45. After 〇, 69.7 g (1.2 mol) of acetone was added, and the obtained mixture was obtained. The mixture was kept at this temperature for 3.5 hours. Thereafter, it was neutralized with a 1% by weight aqueous sodium hydroxide solution, and further dried under a reduced pressure of 1 KPa at 8 (rc) for 12 hours to obtain resorcinol and acetone. The condensate 丨 36 g. The contents of 2,4'4-trimethylidene-2,4,7-trihydroxyflavone and resorcinol in the obtained condensate are as follows. 2, 4, 4-trimethyl-2',4',7-trihydroxyflavone: 50.4% by weight Resorcinol: 0.9% by weight Example 3 Four mils with a thermometer, stirrer and condenser: 88.1 g (〇. 8 mol) of resorcinol was added, and after the inside of the flask was replaced with nitrogen, acetone 65 〇gG 12 m〇1) and 曱 223 were added. §. Eclipse I62280.doc -18. 2 01238958 The mixture obtained was heated to 40 ° C, and then added with 98% barium sulfate 40 g. The obtained mixture was heated to an internal temperature of 5 (rc, heat for 35 hours. At an internal temperature of 60 C) The inside of the flask was decompressed and the water was removed from the reaction system. The pressure was returned to normal pressure, 69 7 g of acetone (i 2 m〇丨) was added, and the obtained mixture was kept at this temperature for 5 hours, after which, 1 was The sodium hydroxide aqueous solution of 〇% was neutralized, and further dried at 80 C under a reduced pressure of 1 KPa or less for 12 hours to obtain 136 g of a condensate of resorcinol and acetone. The contents of 2,4,4-trimethyl-2,4,7-trihydroxyxanone and resorcin in the obtained condensate are as follows. 2,4,4-trimethyl-2',4',7-trihydroxyflavone: 45.8 wt% resorcinol: 〇·97 wt% First dissolution peak: 28.1%

第一溶出波峰之重量平均分子量:1211 軟化點:112°C 比較參考例1 於具備溫度計、攪拌機及冷凝器之500 ml四口燒瓶令, 加入間苯二酚44.0 g(〇.4 mol),於對燒瓶内部進行氮氣置 換後’加入丙酮25.6 g(0.44 mol)及甲苯111 g。於使所獲得 之混合物升溫至40t後,加入98%之硫酸0.44 g。使所獲 得之混合物升溫至内溫為80t,保溫3小時。繼而,加入 丙胴23.2 g(0.40 mol),並對所獲得之混合物保溫4小時。 繼而,加入丙酮23.2 g(0.40 mol),並對所獲得之混人物保 溫3小時。此後’以1 〇%之氫氧化鈉水溶液進行令和進 而於1 KPa以下之減壓下、於8(TC下進行乾燥丨2小時,獲 I62280.doc 19 201238958 得間苯二酚與丙酮之縮合物12〇 g。所獲得之縮合物中之 2,4,4-三甲基_2,,4,,7-三羥基黃酮及間苯二酚之含有率分別 如下。 2,4,4-三曱基-2’,4,,7-三羥基黃酮:42.9重量% 間苯二酚:15.8重量% 實施例4[橡膠組合物之製造] 使用0.6 L之密閉型混練機,將初始之系統内溫度設為 150°C ’基於下述組成配方,首先投入天然橡膠(RSS#1)進 行素練(rnastication)3分鐘,繼而投入碳黑(N330)、水合二 氧化矽、硬脂酸、鋅白、防老化劑(2,2,4-三曱基-1,2-二氫 喹啉縮合物)及實施例1中所獲得之縮合物,混練5分鐘並 排出。繼而,將該排出之橡膠移至開口滾筒中,將初始容 器内溫度設為6(TC,添加下述組成配方中所示之硫、硫化 促進劑(N,N-二環己基-2-苯并噻唑次磺醯胺)、甲氧基化羥 曱基三聚氰胺樹脂(Sumikanol 507AP(住友化學公司製造)) 及環烷酸鈷,一面控制溫度以使橡膠之溫度成為80°C以下 一面進行混練,藉此獲得橡膠組合物。 &lt;組成配方〉 •天然橡膠(RSS#1) 100份 •N330碳黑 45份 •水合二氧化矽(Tosoh Silica(股)製造Nipsil AQ) 10份 •硬脂酸 3份 •鋅白 5重量份 162280.doc -20- 201238958 •防老化劑(2,2,4-三曱基-1,2-二氫喹淋縮合物) 2份 •成分A(實施例1中所獲得之間苯二酚與丙酮之縮合物) 2份 •硫 4份 .硫化促進劑(N,N-二環己基·2-苯并噻唑次磺醯胺) 0.7份 •甲氧基化羥甲基三聚氰胺樹脂(Sumikanol 507AP(住友 化學公司製造)) 3份(有效成分2份) •環烧酸結 2份(鈷含量0.2份) 實施例5 [橡膠組合物之製造] 於實施例4中,使用實施例2中所獲得之縮合物代替實施 例1中所獲得之縮合物,除此以外以與實施例4相同之方式 實施而獲得橡膠組合物。 實施例6 [輪胎用帶束層及使用其之輪胎之製造] 藉由以實施例4中所獲得之橡膠組合物被覆實施有黃銅 鍍敷處理之鋼簾線而獲得帶束層。使用所獲得之帶束層並 依據通常之製造方法而成形生胎,並於硫化機中對所獲得 之生胎加熱加壓,藉此而獲得輪胎。 實施例7[輪胎用胎體及使用其之輪胎之製造] 對實施例4中所獲得之橡膠組合物進行擠壓加工而製備 對應貼體形狀之形狀之橡膠組合物,並貼附於聚酯製之胎 體纖維簾線之上下,藉此而獲得胎體^使用所獲得之胎體 依據通*之製造方法成形生胎,並於硫化機中對所獲得之 162280.doc -21 - 201238958 生胎進行加熱加壓,藉此而獲得輪胎。 實施例8[輪胎用胎面膠及使用其之輪胎之製造] 對實施例4中所獲得之橡膠組合物進行擠壓如工而獲得 胎面膠。使用所獲得之基部膠依據通常之製造方法成形生 胎,並於硫化機中對所獲得之生胎進行加熱加壓,藉此而 獲得輪胎。 實施例9[輪胎用基部膠及使用其之輪胎之製造] 對實施例4中所獲得之橡膠組合物進行擠壓加工而獲得 基部膠。使用所獲得之基部膠依據通常之製造方法成形生 胎,並於硫化機中對所獲得之生胎進行加熱加壓,藉此而 獲得輪胎。 產業上之可利用性 依據本發明之製造方法,可使未反應之間笨二酚之殘留 量較少。依據本發明之製造方法所獲得之間苯二酚與丙_ 之縮合物由於作為各種橡膠組合物之補強劑之性能優異, 且亦可防止由橡膠組合物加工時之殘留間苯二酚之蒸散所 導致之作業環境之惡化,故而於工業上有利。 162280.doc •22·Weight average molecular weight of the first elution peak: 1211 Softening point: 112 ° C Comparative Reference Example 1 In a 500 ml four-necked flask with a thermometer, a stirrer, and a condenser, 44.0 g (〇. 4 mol) of resorcin was added. After the inside of the flask was purged with nitrogen, '25.6 g (0.44 mol) of acetone and 111 g of toluene were added. After the obtained mixture was heated to 40 t, 98% of sulfuric acid was added in an amount of 0.44 g. The obtained mixture was allowed to warm to an internal temperature of 80 t and kept for 3 hours. Then, 23.2 g (0.40 mol) of propylene oxide was added, and the obtained mixture was kept for 4 hours. Then, 23.2 g (0.40 mol) of acetone was added, and the obtained mixed person was kept warm for 3 hours. Thereafter, the mixture was subjected to a sodium hydroxide aqueous solution of 1% by weight and further dried under a reduced pressure of 1 KPa for 8 hours at TC for 2 hours to obtain a condensation of resorcinol with acetone at I62280.doc 19 201238958. 12〇g. The contents of 2,4,4-trimethyl-2,4,7-trihydroxyflavone and resorcinol in the obtained condensate are as follows. 2,4,4- Tridecyl-2',4,,7-trihydroxyflavone: 42.9 wt% resorcinol: 15.8% by weight Example 4 [Manufacturing of rubber composition] The initial system was used using a 0.6 L closed type kneader The internal temperature is set to 150 ° C. Based on the following composition formula, natural rubber (RSS #1) is first introduced for rnastication for 3 minutes, followed by carbon black (N330), hydrated cerium oxide, stearic acid, zinc. White, an anti-aging agent (2,2,4-tridecyl-1,2-dihydroquinoline condensate) and the condensate obtained in Example 1 were kneaded for 5 minutes and discharged. Then, the discharged product was discharged. The rubber was moved to the open drum, and the temperature in the initial vessel was set to 6 (TC, sulfur and vulcanization accelerator (N, N-dicyclohexyl-2-) shown in the following composition was added. And thiazole sulfoximine), methoxylated hydroxy decyl melamine resin (Sumikanol 507AP (manufactured by Sumitomo Chemical Co., Ltd.), and cobalt naphthenate, and the temperature is controlled so that the temperature of the rubber becomes 80 ° C or less, and kneading is performed. Thereby, a rubber composition is obtained. &lt;Composition formula> • Natural rubber (RSS #1) 100 parts • N330 carbon black 45 parts • Hydrated cerium oxide (Tosoh Silica (manufactured by Nipsil AQ) 10 parts • Stearic acid 3 Parts • Zinc White 5 parts by weight 162280.doc -20- 201238958 • Anti-aging agent (2,2,4-tridecyl-1,2-dihydroquinoline condensate) 2 parts • Ingredient A (In Example 1 The obtained condensate of resorcinol and acetone) 2 parts • sulfur 4 parts. vulcanization accelerator (N, N-dicyclohexyl-2-benzothiazole sulfoximine) 0.7 parts • methoxylated hydroxyl Methyl melamine resin (Sumikanol 507AP (manufactured by Sumitomo Chemical Co., Ltd.)) 3 parts (2 parts of active ingredient) • 2 parts of ring-burning acid salt (cobalt content: 0.2 parts) Example 5 [Production of rubber composition] In Example 4 Using the condensate obtained in Example 2 in place of the condensate obtained in Example 1, except The rubber composition was obtained in the same manner as in Example 4. Example 6 [Manufacture of belt for tire and manufacture of tire using the same] Brass plating was carried out by coating the rubber composition obtained in Example 4 The steel cord is treated to obtain a belt layer, and the obtained green belt is formed by using the obtained belt layer according to a usual manufacturing method, and the obtained green tire is heated and pressurized in a vulcanizer, thereby obtaining a tire. Example 7 [Production of Tire for Tire and Tire Using the Same] The rubber composition obtained in Example 4 was subjected to extrusion processing to prepare a rubber composition having a shape corresponding to a shape of a sticker, and was attached to a polyester. The carcass fiber cord is made up and down, thereby obtaining the carcass, and the carcass obtained by using the carcass is formed according to the manufacturing method of the method, and is obtained in the vulcanizer by the 162280.doc -21 - 201238958 The tire is heated and pressurized to obtain a tire. Example 8 [Production of tread rubber for tire and tire using the same] The rubber composition obtained in Example 4 was subjected to extrusion to obtain a tread rubber. The obtained base rubber was molded into a green tire by a usual manufacturing method, and the obtained green tire was heated and pressurized in a vulcanizer to obtain a tire. Example 9 [Production of base rubber for tire and tire using the same] The rubber composition obtained in Example 4 was subjected to extrusion processing to obtain a base rubber. The obtained base rubber was molded into a green tire by a usual manufacturing method, and the obtained green tire was heated and pressurized in a vulcanizer to obtain a tire. Industrial Applicability According to the production method of the present invention, the residual amount of the streptophenol in the unreacted portion can be made small. The condensate of the resorcinol and the propylene obtained by the production method of the present invention is excellent in the performance as a reinforcing agent for various rubber compositions, and also prevents the evapotranspiration of residual resorcinol when processed from the rubber composition. The resulting deterioration of the working environment is industrially advantageous. 162280.doc •22·

Claims (1)

201238958 七、申請專利範圍·· 1. 一種間苯二酚與丙酮之縮合物之製造方法,其包括: 使間笨二酚與丙酮於酸之存在下進行反應之步驟,及 於酸之存在下去除由上述反應所副生之水之步驟。 2. 如請求項1之製造方法,其包括: 使間笨二酚與丙酮於酸之存在下進行反應之步驟, 於酸之存在下去除由上述反應所副生之水之步驟,及 使去除水後之混合物與鹼混合之步驟。 3. 如請求項丨或2之製造方法,其包括: 使間笨二酚與丙酮於酸之存在下進行反應之步驟, 於酸之存在下去除由上述反應所副生之水之步驟, 使去除水後之混合物與丙酮混合之步驟,及 使與两嗣混合後之混合物與驗混合之步驟。 4. 如請求項⑴中任—項之製造方法’其中於酸之存在下 去除由上述反應所副生之水的步驟⑽酸及有機溶劑之 存在下去除由上述反應所副生之水的步驟。 5. 如請求項4之製造方法’其令於酸及有機溶劑之存在下 去除由上述反應利生之水的步驟錢由上述反應所副 生之水於I及有機溶劑之存在下與有機溶劑共沸,藉此 去除的步驟。 6. 如請求項4或5之製造方法,其中古 、 ^共f有機溶劑為芳香族烴。 7·如請求項6之製造方法,其中婪 ^ 丹T方香族烴為甲苯或二甲 苯。 其中酸係選自由對 8·如請求項1至7中任一項之製造方法 I62280.doc 201238958 甲笨磺酸、對甲苯磺酸水合物、鹽酸及硫酸所組成之群 中之至少1種。 9. 一種橡膠組合物,其包含利用如請求項丨至8中任一項之 製造方法所獲得之縮合物、橡膠成分、填充劑、及硫成 分。 其包含由如請求項9之橡膠組合物 10· —種輪胎用帶束層 所被覆之鋼簾線。 11 · 一種輪胎用胎體,其包含由古軎、七 3由凊求項9之橡膠組合物所被 覆之胎體纖維簾線。 其包含如請求項9 12. —種輪胎用胎面膠或輪胎用基部膠 之橡膠組合物。 13.—種充氣輪胎, 行加工所製造。 14· 一種間苯二酚與 (3): 其係藉由對如請电拒〇 &gt; a _ f衣項9之橡膠組合物進 丙_之縮合物,其 再滿足下述(1)、(2)及 進行分析時,因2’4,4:三甲基:,二射率檢測)對縮 之波峰之面積相對於所有波峰之合:·:㈣黃嗣所 之範圍; σ叶面積的比為30 ⑺於利用凝膠滲透層析法 進行分析時,第一溶出波 折射率檢測)對縮合物 計面積之比為20〜50%之範目;積才目對於所有波蜂之合 (3)上述第一溶出波峰之 之範圍。 千均刀子量為15〇〇〜17⑼ 162280.doc 201238958 1 5 ·如請求項14之縮合物,其軟化點為1 60°C以下。 16.如請求項14或15之縮合物,其於120°C下保管24小時後 之間苯二酚之增加率為2%以下。 162280.doc 201238958 四、指定代表圖: (一) 本案指定代表圖為:(無) (二) 本代表圖之元件符號簡單說明: 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式: (無) 162280.doc201238958 VII. Patent Application Range 1. A method for producing a condensate of resorcinol and acetone, comprising: a step of reacting m-diphenol with acetone in the presence of an acid, and in the presence of an acid The step of removing water by-produced by the above reaction. 2. The method of claim 1, comprising the steps of: reacting m-diphenol with acetone in the presence of an acid, removing the water by the reaction in the presence of an acid, and removing the water The step of mixing the mixture after water with the base. 3. The method of claim 2 or 2, comprising: the step of reacting m-diphenol with acetone in the presence of an acid, and removing the water by-produced by the reaction in the presence of an acid, The step of mixing the mixture after removing water with acetone, and the step of mixing the mixture with the two mashes. 4. The method according to any one of the items (1) of the present invention, wherein the step (10) of removing the water by the reaction is carried out in the presence of an acid, and removing the water by the reaction . 5. The method of claim 4, wherein the step of removing the water derived from the reaction in the presence of an acid and an organic solvent is carried out by the water of the above reaction in the presence of I and an organic solvent together with the organic solvent. Boiling, the step of removing this. 6. The method of claim 4, wherein the organic solvent is an aromatic hydrocarbon. 7. The method of claim 6, wherein the T^丹T-fragrant hydrocarbon is toluene or xylene. The acid is at least one selected from the group consisting of the production method I62280.doc 201238958 of any one of claims 1 to 7 and the group consisting of methyl sulfonic acid, p-toluenesulfonic acid hydrate, hydrochloric acid and sulfuric acid. A rubber composition comprising the condensate, the rubber component, the filler, and the sulfur component obtained by the production method according to any one of claims 1 to 8. It comprises a steel cord covered with a rubber composition as claimed in claim 9 for a tire belt. A carcass for a tire comprising a carcass fiber cord covered with a rubber composition of the ruthenium, VII, and the ninth article. It comprises a rubber composition as claimed in claim 9 12. A tire tread rubber or a base rubber for a tire. 13. - A pneumatic tire, manufactured by a line of processing. 14· a resorcinol and (3): a condensate of the rubber composition of the item 9 by electro-rejection &gt; a _ f, which further satisfies the following (1), (2) and when performing the analysis, because 2'4,4: trimethyl:, the rate of detection of the two-shot ratio) is the sum of the area of the peak of the contraction with respect to all the peaks: ·: (4) the range of the jaundice; the area of the σ leaf The ratio of 30 (7) in the analysis by gel permeation chromatography, the ratio of the first eluted wave refractive index detection) to the area of the condensate is 20 to 50%; the product is for all the bees. (3) The range of the first elution peak described above. The amount of the knife per thousand is 15 〇〇 17 (9) 162 280. doc 201238958 1 5 The condensate of claim 14 has a softening point of 1 60 ° C or less. 16. The condensate of claim 14 or 15, which is stored at 120 ° C for 24 hours, and the rate of increase of the resorcinol is 2% or less. 162280.doc 201238958 IV. Designated representative map: (1) The representative representative of the case is: (none) (2) The symbolic symbol of the representative figure is simple: 5. If there is a chemical formula in this case, please reveal the best indication of the characteristics of the invention. Chemical formula: (none) 162280.doc
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