JP2013203742A - p-tert-OCTYLPHENOL-SULFUR CHLORIDE CO-CONDENSED RESIN - Google Patents

p-tert-OCTYLPHENOL-SULFUR CHLORIDE CO-CONDENSED RESIN Download PDF

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JP2013203742A
JP2013203742A JP2012070498A JP2012070498A JP2013203742A JP 2013203742 A JP2013203742 A JP 2013203742A JP 2012070498 A JP2012070498 A JP 2012070498A JP 2012070498 A JP2012070498 A JP 2012070498A JP 2013203742 A JP2013203742 A JP 2013203742A
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resin
octylphenol
sulfur
tert
rubber
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Takafumi Yamamoto
貴文 山元
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Taoka Chemical Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a p-tert-octylphenol-sulfur chloride co-condensed resin useful as a resin-crosslinking agent having characteristics of improving viscoelastic characteristics compared to the case using sulfur without damaging breaking characteristics when added to a rubber.SOLUTION: There is provided a p-tert-octylphenol-sulfur chloride co-condensed resin obtained by reacting 1.2-1.8 mol of sulfur monochloride with 1 mol of p-tert-octylphenol, having 25-34 wt.% of a sulfur content in the resin, and usable as a resin curing agent.

Description

本発明は、ゴムの破断特性を低下させることなく粘弾性特性を向上させる樹脂架橋剤として使用可能なp−tert−オクチルフェノール塩化硫黄共縮合樹脂及びその応用に関する。 The present invention relates to a p-tert-octylphenol sulfur chloride cocondensation resin that can be used as a resin cross-linking agent that improves viscoelastic properties without lowering the breaking properties of rubber and its application.

従来から硫黄に変わる樹脂のゴム用架橋剤としてアルキルフェノール・塩化硫黄共縮合樹脂が使用されており、この中でも、p−オクチルフェノール塩化硫黄共縮合樹脂は、加工性能や接着性に優れていることが知られている。(特許文献1) Alkylphenol / sulfur chloride co-condensation resins have been used as rubber cross-linking agents for resins that change to sulfur, and among them, p-octylphenol sulfur chloride co-condensation resins are known to have excellent processing performance and adhesion. It has been. (Patent Document 1)

また、近年、環境保護の観点から、自動車の燃費向上(すなわち、低燃費化)が求められている。自動車の燃費向上には様々な手法が知られているが、この中の一つとしてタイヤの特性を変化させるといった手法があり、その為にはタイヤに使用するゴムの粘弾性特性を向上させることが求められ、その中でも損失正接(tanδ)と呼ばれる値が注目され、この値を低減させることが行われている。(例えば特許文献2、3)これら特許文献中には、tanδを低減させる為に、架橋剤として硫黄の代わりに、アルキルフェノール・塩化硫黄共縮合樹脂が使用されているが、本願発明者らがアルキルフェノール・塩化硫黄共縮合樹脂を使用したゴムの物性を確認した所、破断特性が悪化してしまうという問題があることを見出した。 In recent years, from the viewpoint of environmental protection, there has been a demand for improvement in fuel consumption (that is, reduction in fuel consumption) of automobiles. Various methods are known for improving the fuel efficiency of automobiles, and one of them is to change the characteristics of tires. To that end, it is necessary to improve the viscoelastic characteristics of rubber used in tires. Among them, a value called loss tangent (tan δ) has attracted attention, and this value is being reduced. (For example, Patent Documents 2 and 3) In these patent documents, an alkylphenol / sulfur chloride cocondensation resin is used in place of sulfur as a crosslinking agent in order to reduce tan δ. -When the physical properties of the rubber using the sulfur chloride co-condensation resin were confirmed, it was found that there was a problem that the breaking characteristics deteriorated.

特開昭58−13648号公報JP 58-13648 A 特開2009−138148号公報JP 2009-138148 A 特開2010−95670号公報JP 2010-95670 A

本発明の目的は、ゴムへ添加した場合、破断特性を損なわずに硫黄を使用した場合に比べて粘弾性特性が改善されるという特徴を有した樹脂架橋剤として有用なp−tert−オクチルフェノール塩化硫黄共縮合樹脂を提供することにある。 An object of the present invention is to add p-tert-octylphenol chloride useful as a resin cross-linking agent having a feature that when added to rubber, viscoelastic properties are improved as compared with the case where sulfur is used without impairing fracture properties. The object is to provide a sulfur co-condensation resin.

本発明者らは、前記課題を解決すべく鋭意検討した結果、p−tert−オクチルフェノール1モルに対して一塩化イオウ1.2〜1.8モルを反応させることで得られる樹脂であって、前記樹脂中の硫黄含量が25〜34重量%であるp−tert−オクチルフェノール塩化硫黄共縮合樹脂を樹脂架橋剤とすることで、前記課題が解決可能であることを見出した。 As a result of intensive studies to solve the above problems, the present inventors have obtained a resin obtained by reacting 1.2 to 1.8 mol of sulfur monochloride with 1 mol of p-tert-octylphenol, It has been found that the above problem can be solved by using a p-tert-octylphenol sulfur chloride cocondensation resin having a sulfur content of 25 to 34% by weight as the resin crosslinking agent.

本発明によれば、ゴムへ添加した場合、硫黄を使用した場合に比べ粘弾性特性が改善され、同時に、破断特性が悪化しないという特徴を有した樹脂架橋剤として使用可能なp−tert−オクチルフェノール塩化硫黄共縮合樹脂を提供することが可能となる。 According to the present invention, when added to rubber, p-tert-octylphenol which can be used as a resin crosslinking agent has the characteristics that viscoelastic properties are improved as compared with the case where sulfur is used, and at the same time, the breaking properties are not deteriorated. It becomes possible to provide a sulfur chloride co-condensation resin.

以下に、本発明を詳細に説明する。本発明で使用するオクチルフェノールは、様々な異性体が存在する中で、p−tert−オクチルフェノールを指す。o位やm位が置換されたオクチルフェノールの場合、一塩化硫黄と反応せず本願発明の目的とする共縮合樹脂が得られず、p−n−オクチルフェノールを使用した場合、共縮合樹脂は得られるものの、この共縮合樹脂を架橋剤として使用した場合、本願比較例に示す通り、本願発明の効果である粘弾性特性が向上せず好ましくない。 The present invention is described in detail below. Octylphenol used in the present invention refers to p-tert-octylphenol in the presence of various isomers. In the case of octylphenol substituted at the o-position and m-position, the co-condensation resin intended for the present invention is not obtained without reacting with sulfur monochloride, and when pn-octylphenol is used, the co-condensation resin is obtained. However, when this co-condensation resin is used as a cross-linking agent, as shown in the comparative example of the present application, the viscoelastic properties that are the effects of the present invention are not improved, which is not preferable.

本発明で使用する塩化硫黄は、一塩化硫黄(S2Cl2)を指す。二塩化硫黄(SCl2)を使用した場合、得られたp−tert−オクチルフェノール塩化硫黄共縮合樹脂中の硫黄含量を25〜34重量%とすることが出来ず、好ましくない。また、一塩化硫黄はp−tert-オクチルフェノール1モルに対し、1.2〜1.8モル使用する。1.2モルより少ない場合、得られた共縮合樹脂を架橋剤としても、粘弾性特性が向上せず、また、1.8モルより多い場合、破断強度及び耐摩耗性が悪化する傾向がある。 Sulfur chloride used in the present invention refers to sulfur monochloride (S2Cl2). When sulfur dichloride (SCl2) is used, the sulfur content in the obtained p-tert-octylphenol sulfur chloride cocondensation resin cannot be made 25 to 34% by weight, which is not preferable. Further, sulfur monochloride is used in an amount of 1.2 to 1.8 mol per 1 mol of p-tert-octylphenol. When the amount is less than 1.2 mol, the viscoelastic properties are not improved even when the obtained cocondensation resin is used as a cross-linking agent. .

p−tert-オクチルフェノールと一塩化硫黄との反応において、必要に応じ有機溶媒を用いて反応を行うことが出来る。この時使われる有機溶媒は、p−tert-オクチルフェノールや一塩化硫黄と副反応を起さず、反応を阻害しないものであればどのようなものでも良いが、例えばベンゼン、トルエン、キシレン、メシチレン、ヘプタン、シクロヘキサン等が使用可能である。 In the reaction of p-tert-octylphenol and sulfur monochloride, the reaction can be carried out using an organic solvent as necessary. Any organic solvent may be used as long as it does not cause side reactions with p-tert-octylphenol or sulfur monochloride and does not inhibit the reaction. For example, benzene, toluene, xylene, mesitylene, Heptane, cyclohexane, etc. can be used.

p−tert-オクチルフェノールと一塩化硫黄との反応は通常、(1)p−tert-オクチルフェノール及び(2)必要に応じ前記有機溶媒を反応容器に投入した後、(3)一塩化硫黄を一定時間かけながら反応容器へ添加し、(4)その後一定時間保温攪拌をすることにより実施される。以下、これらの反応条件及び手順について詳述する。 The reaction between p-tert-octylphenol and sulfur monochloride is usually carried out by adding (1) p-tert-octylphenol and (2) the organic solvent as necessary to the reaction vessel, and (3) sulfur monochloride for a certain period of time. (4) After that, it is carried out by stirring for a certain period of time. Hereinafter, these reaction conditions and procedures will be described in detail.

一塩化硫黄を添加する際の温度は通常40〜180℃、好ましくは70〜120℃である。40℃より低ければ反応の進行が遅く経済的に不利であり、180℃以上であると分解が生じる傾向がある。また、ここで言う添加とは、滴下のように間欠的に反応系へ投入する操作、流量を制御しながら連続的に反応系へ投入する操作の両方を包含する。添加時間は反応スケールにより異なるが、通常1〜12時間要する。なお、添加時間は添加時の温度変化を逐次確認することにより、当業者であれば容易に設定可能である。 The temperature at which sulfur monochloride is added is usually 40 to 180 ° C, preferably 70 to 120 ° C. If the temperature is lower than 40 ° C, the reaction proceeds slowly, which is economically disadvantageous. If the temperature is higher than 180 ° C, decomposition tends to occur. Moreover, the addition mentioned here includes both an operation of intermittently charging into the reaction system such as dropping, and an operation of continuously charging into the reaction system while controlling the flow rate. Although the addition time varies depending on the reaction scale, it usually takes 1 to 12 hours. The addition time can be easily set by those skilled in the art by sequentially confirming the temperature change during the addition.

塩化硫黄添加後の反応は、通常40〜180℃、好ましくは70〜120℃で実施する。40℃より低ければ反応の進行が遅く経済的に不利であり、180℃以上であると分解が生じる傾向がある。反応時間は温度によって異なるが、通常1〜10時間である。なお、反応時間は未反応p-tert-オクチルフェノールの残量を測定するか、反応系の粘度変化を測定する等により、当業者であれば容易に設定可能である。 The reaction after the addition of sulfur chloride is usually carried out at 40 to 180 ° C, preferably 70 to 120 ° C. If the temperature is lower than 40 ° C, the reaction proceeds slowly, which is economically disadvantageous. If the temperature is higher than 180 ° C, decomposition tends to occur. Although reaction time changes with temperature, it is 1 to 10 hours normally. The reaction time can be easily set by those skilled in the art by measuring the remaining amount of unreacted p-tert-octylphenol or measuring the viscosity change of the reaction system.

こうして得られたp−tert−オクチルフェノール塩化硫黄共縮合樹脂は樹脂中の硫黄含量が25〜34重量%である必要がある。25重量%より低い場合、粘弾性特性が改善されず、34重量%より高い場合破断強度及び耐摩耗性が悪化する。 The p-tert-octylphenol sulfur chloride cocondensation resin thus obtained needs to have a sulfur content of 25 to 34% by weight in the resin. When it is lower than 25% by weight, the viscoelastic properties are not improved, and when it is higher than 34% by weight, the breaking strength and the wear resistance are deteriorated.

本発明のp−tert−オクチルフェノール塩化硫黄共縮合樹脂は硫黄架橋可能な全てのゴムに適用可能であり、天然ゴム(NR)、スチレンブタジエンゴム(SBR)、ポリブタジエンゴム(BR)、ポリイソプレンゴム(IR)、クロロプレンゴム(CR)、アクリロニトリル−ブタジエン共重合ゴム(NBR)、イソプレン−イソブチレン共重合ゴム(IIR)、エチレン−プロピレンターポリマー(EPDM)、等が例示される。この中でも天然ゴム(NR)、スチレンブタジエンゴム(SBR)、アクリロニトリル−ブタジエン共重合ゴム(NBR)、ポリブタジエンゴム(BR)、に好適に使用される。また、p−tert−オクチルフェノール塩化硫黄共縮合樹脂をゴムに使用する際の使用量は、ゴム100重量部に対して、本発明のp−tert−オクチルフェノール塩化硫黄共縮合樹脂を0.5〜50重量部、好ましくは1〜30重量部、さらに好ましくは1〜20重量部使用する。0.5重量部より少ない場合、架橋密度が低くなり粘弾性特性が悪化する傾向があり、50重量部より多い場合、破断特性や耐磨耗性が悪化する傾向がある。 The p-tert-octylphenol sulfur chloride co-condensation resin of the present invention can be applied to all rubbers capable of sulfur crosslinking. Natural rubber (NR), styrene butadiene rubber (SBR), polybutadiene rubber (BR), polyisoprene rubber ( IR), chloroprene rubber (CR), acrylonitrile-butadiene copolymer rubber (NBR), isoprene-isobutylene copolymer rubber (IIR), ethylene-propylene terpolymer (EPDM), and the like. Among these, it is suitably used for natural rubber (NR), styrene butadiene rubber (SBR), acrylonitrile-butadiene copolymer rubber (NBR), and polybutadiene rubber (BR). The amount of p-tert-octylphenol sulfur chloride cocondensation resin used in rubber is 0.5 to 50% of the p-tert-octylphenol sulfur chloride cocondensation resin of the present invention relative to 100 parts by weight of rubber. Part by weight, preferably 1 to 30 parts by weight, more preferably 1 to 20 parts by weight is used. When the amount is less than 0.5 parts by weight, the crosslink density tends to be low and the viscoelastic properties tend to be deteriorated.

本発明のp−tert−オクチルフェノール塩化硫黄共縮合樹脂をゴムに配合し使用する際は、ゴム工業界で通常使用される配合剤、例えば、カーボンブラック等の充填剤、酸化亜鉛、ステアリン酸、オイル類等を、本発明の目的を阻害しない範囲内で適宜選択して配合することができ、これら配合剤としては、市販品を好適に使用することができる。 When the p-tert-octylphenol sulfur chloride cocondensation resin of the present invention is blended and used in rubber, a compounding agent usually used in the rubber industry, for example, a filler such as carbon black, zinc oxide, stearic acid, oil In the range which does not impair the object of the present invention, etc. can be appropriately selected and blended, and as these blending agents, commercially available products can be suitably used.

本発明におけるp−tert−オクチルフェノール塩化硫黄共縮合樹脂を0.5〜50重量部含むゴム組成物は、タイヤ、ホース、チューブ、ガスケット、家電部品等に使用されるゴム製品に好適に使用される。 The rubber composition containing 0.5 to 50 parts by weight of the p-tert-octylphenol sulfur chloride cocondensation resin in the present invention is suitably used for rubber products used for tires, hoses, tubes, gaskets, home appliance parts and the like. .

以下に、実施例を挙げて本発明を更に詳しく説明するが、本発明は下記の実施例に何ら
限定されるものではない。
Hereinafter, the present invention will be described in more detail with reference to examples. However, the present invention is not limited to the following examples.

(各樹脂の製造)
各樹脂の製造においては以下の分析条件に基づき分析を行った。
(Manufacture of each resin)
In the production of each resin, analysis was performed based on the following analysis conditions.

<硫黄含量>
活栓付フラスコを用いて約0.01gの試料(p−tert−オクチルフェノール塩化硫黄共縮合樹脂)を30%過酸化水素水0.5mlと水5ml中に圧縮酸素と共に入れ、着火した後、素早く活栓を付けて密栓する。燃焼完了後、2−プロパノール20mLにて、フラスコ内を洗い込み、トリン混合指示薬を3滴加え、0.01mol/L過塩素酸バリウム溶液で滴定し、その滴定量をAmlとする。液色が緑黄色から、微赤褐色に変化した時を終点とする。また補正の為に別に空試験を行い、空試験時の滴定量をBmlとし、硫黄含量を次の式によって求めた。
硫黄含量(重量%)=[32.06×(A−B)×0.01mol/L過塩素酸バリウ
ム溶液のファクター]/(試料秤取量(g)×100)
<Sulfur content>
About 0.01 g of sample (p-tert-octylphenol sulfur chloride co-condensation resin) was placed in 0.5 ml of 30% hydrogen peroxide solution and 5 ml of water with compressed oxygen using a flask with a stopcock, ignited, and then quickly turned on Put on and seal tightly. After the completion of combustion, the flask is washed with 20 mL of 2-propanol, 3 drops of tritium mixed indicator is added, and titrated with a 0.01 mol / L barium perchlorate solution, and the titer is set to A ml. The end point is when the liquid color changes from greenish yellow to slightly reddish brown. In addition, a blank test was separately performed for correction, and the titer at the blank test was set to B ml, and the sulfur content was determined by the following formula.
Sulfur content (% by weight) = [32.06 × (AB) × 0.01 mol / L factor of barium perchlorate solution] / (sample weighed amount (g) × 100)

以下製造例において記載する当量及び重量倍は特に断りのない限り、p−tert−オクチルフェノールに対する当量、重量倍である。 The equivalent weights and weight times described in the production examples below are equivalent weights and weight times with respect to p-tert-octylphenol unless otherwise specified.

<製造例1 樹脂Aの合成>
還流冷却機および温度計を備えた4つ口フラスコにp−tert−オクチルフェノール900g(4.36モル)とトルエン290gを仕込み、一塩化イオウ709g(5.25モル、1.2当量)をフラスコ内の内温を70〜80℃に保持しつつ5時間で滴下し、滴下終了後内温を120℃に上昇させ3時間保温する。得られた反応液を減圧下において濃縮し、p−tert−オクチルフェノール塩化硫黄共縮合樹脂(樹脂Aと称する)1220gを得た。樹脂A中の硫黄含量について表1に示す。
<Production Example 1 Synthesis of Resin A>
A 4-necked flask equipped with a reflux condenser and a thermometer was charged with 900 g (4.36 mol) of p-tert-octylphenol and 290 g of toluene, and 709 g of sulfur monochloride (5.25 mol, 1.2 equivalents) was placed in the flask. Is dropped in 5 hours while maintaining the internal temperature of 70-80 ° C., and the internal temperature is raised to 120 ° C. after the completion of the dropwise addition, and kept for 3 hours. The resulting reaction solution was concentrated under reduced pressure to obtain 1220 g of p-tert-octylphenol sulfur chloride cocondensation resin (referred to as resin A). The sulfur content in the resin A is shown in Table 1.

<製造例2 樹脂Bの合成>
還流冷却機および温度計を備えた4つ口フラスコにp−tert−オクチルフェノール900g(4.36モル)とトルエン300gを仕込み、一塩化イオウ736g(5.76モル、1.3当量)をフラスコ内の内温を70〜80℃に保持しつつ5時間で滴下し、滴下終了後内温を120℃に上昇させ3時間保温する。得られた反応液を減圧下において濃縮し、p−tert−オクチルフェノール塩化硫黄共縮合樹脂(樹脂Bと称する)1240gを得た。樹脂B中の硫黄含量について表1に示す。
<Production Example 2 Synthesis of Resin B>
A 4-necked flask equipped with a reflux condenser and a thermometer was charged with 900 g (4.36 mol) of p-tert-octylphenol and 300 g of toluene, and 736 g (5.76 mol, 1.3 equivalents) of sulfur monochloride was placed in the flask. Is dropped in 5 hours while maintaining the internal temperature of 70-80 ° C., and the internal temperature is raised to 120 ° C. after the completion of the dropwise addition, and kept for 3 hours. The obtained reaction solution was concentrated under reduced pressure to obtain 1240 g of p-tert-octylphenol sulfur chloride cocondensation resin (referred to as resin B). The sulfur content in resin B is shown in Table 1.

<製造例3 樹脂Cの合成>
還流冷却機および温度計を備えた4つ口フラスコにp−tert−オクチルフェノール900g(4.36モル)とトルエン370gを仕込み、一塩化イオウ901g(6.67モル、1.53当量)をフラスコ内の内温を70〜80℃に保持しつつ5時間で滴下し、滴下終了後内温を120℃に上昇させ3時間保温する。得られた反応液を減圧下において濃縮し、p−tert−オクチルフェノール塩化硫黄共縮合樹脂(樹脂Cと称する)1300gを得た。樹脂C中の硫黄含量について表1に示す。
<Production Example 3 Synthesis of Resin C>
A four-necked flask equipped with a reflux condenser and a thermometer was charged with 900 g (4.36 mol) of p-tert-octylphenol and 370 g of toluene, and 901 g (6.67 mol, 1.53 equivalents) of sulfur monochloride was placed in the flask. Is dropped in 5 hours while maintaining the internal temperature of 70-80 ° C., and the internal temperature is raised to 120 ° C. after the completion of the dropwise addition, and kept for 3 hours. The obtained reaction liquid was concentrated under reduced pressure to obtain 1300 g of p-tert-octylphenol sulfur chloride cocondensation resin (referred to as resin C). The sulfur content in the resin C is shown in Table 1.

<製造例4 樹脂Dの合成>
還流冷却機および温度計を備えた4つ口フラスコにp−tert−オクチルフェノール900g(4.36モル)とトルエン460gを仕込み、一塩化イオウ1119g(8.29モル、1.9当量)をフラスコ内の内温を70〜80℃に保持しつつ7時間で滴下し、滴下終了後内温を120℃に上昇させ3時間保温する。得られた反応液を減圧下において濃縮し、p−tert−オクチルフェノール塩化硫黄共縮合樹脂(樹脂Dと称する)1400gを得た。樹脂D中の硫黄含量について表2に示す。
<Production Example 4 Synthesis of Resin D>
A four-necked flask equipped with a reflux condenser and a thermometer was charged with 900 g (4.36 mol) of p-tert-octylphenol and 460 g of toluene, and 1119 g of sulfur monochloride (8.29 mol, 1.9 equivalents) was placed in the flask. While maintaining the internal temperature of 70-80 ° C., the solution is dropped in 7 hours, and after completion of the dropwise addition, the internal temperature is raised to 120 ° C. and kept for 3 hours. The obtained reaction solution was concentrated under reduced pressure to obtain 1400 g of p-tert-octylphenol sulfur chloride cocondensation resin (referred to as resin D). The sulfur content in Resin D is shown in Table 2.

<製造例5 樹脂Eの合成>
還流冷却機および温度計を備えた4つ口フラスコにp−n−オクチルフェノール900g(4.36モル)とトルエン290gを仕込み、一塩化イオウ709g(5.45モル、1.2当量)をフラスコ内の内温を70〜80℃に保持しつつ5時間で滴下し、滴下終了後内温を120℃に上昇させ3時間保温する。得られた反応液を減圧下において濃縮し、p−tert−オクチルフェノール塩化硫黄共縮合樹脂(樹脂Eと称する)1230gを得た。樹脂E中の硫黄含量について表2に示す。
<Production Example 5 Synthesis of Resin E>
A 4-necked flask equipped with a reflux condenser and a thermometer was charged with 900 g (4.36 mol) of pn-octylphenol and 290 g of toluene, and 709 g of sulfur monochloride (5.45 mol, 1.2 equivalents) was placed in the flask. Is dropped in 5 hours while maintaining the internal temperature of 70-80 ° C., and the internal temperature is raised to 120 ° C. after the completion of the dropwise addition, and kept for 3 hours. The obtained reaction liquid was concentrated under reduced pressure to obtain 1230 g of p-tert-octylphenol sulfur chloride co-condensation resin (referred to as resin E). The sulfur content in Resin E is shown in Table 2.

<樹脂F>
田岡化学工業社製p−tert−オクチルフェノール塩化硫黄共縮合樹脂、V−200を樹脂Fとしてそのまま使用した。樹脂F中の硫黄含量について表1に示す。
<Resin F>
A p-tert-octylphenol sulfur chloride cocondensation resin, V-200, manufactured by Taoka Chemical Industries, Ltd. was used as resin F as it was. The sulfur content in resin F is shown in Table 1.

<製造例6 樹脂Gの合成>
還流冷却機および温度計を備えた4つ口フラスコにp−t−オクチルフェノール900g(4.36モル)とトルエン240gを仕込み、一塩化イオウ590g(4.46モル、1.0当量)をフラスコ内の内温を70〜80℃に保持しつつ5時間で滴下し、滴下終了後内温を120℃に上昇させ3時間保温する。得られた反応液に粉末硫黄85gを添加後、減圧下において濃縮し、p−tert−オクチルフェノール塩化硫黄共縮合樹脂(樹脂Gと称する)1240gを得た。樹脂G中の硫黄含量について表2に示す。
<Production Example 6 Synthesis of Resin G>
A four-necked flask equipped with a reflux condenser and a thermometer was charged with 900 g (4.36 mol) of pt-octylphenol and 240 g of toluene, and 590 g (4.46 mol, 1.0 equivalent) of sulfur monochloride was placed in the flask. Is dropped in 5 hours while maintaining the internal temperature of 70-80 ° C., and the internal temperature is raised to 120 ° C. after the completion of the dropwise addition, and kept for 3 hours. After adding powder sulfur 85g to the obtained reaction liquid, it concentrated under pressure reduction and obtained 1240g of p-tert-octyl phenol sulfur chloride cocondensation resin (referred to as resin G). The sulfur content in resin G is shown in Table 2.

<評価用ゴムシートの作成>
下記配合のゴムコンパウンド200gを 関西ロール社製の6インチオープンロールを用いて設定温度40℃、10分混練で作成した。
<配合>
スチレン・ブタジエンゴム(SBR)(JSR社製 JSR1502)70重量部
ブタジエンゴム(BR)(宇部興産社製 BR150B) 30重量部
シリカ(東ソー・シリカ社製 VN3) 50重量部
カーボンブラック(昭和キャボット社製 N330) 5重量部
シランカップリング剤(デグザ社製 Si69) 5重量部
老化防止剤(大内新興化学工業社製 ノクラック6C) 2重量部
酸化亜鉛(堺化学社製) 3重量部
ステアリン酸(日本油脂製) 2重量部
加硫促進剤(大内新興化学工業社製 CZ-G) 3重量部
不溶性硫黄(フレキシス社製 クリステックスHS OT-20) 2重量部
p−tert−オクチルフェノール塩化硫黄共縮合樹脂 2重量部
<Creation of rubber sheet for evaluation>
200 g of a rubber compound having the following composition was prepared by kneading at a set temperature of 40 ° C. for 10 minutes using a 6-inch open roll manufactured by Kansai Roll.
<Combination>
Styrene butadiene rubber (SBR) (JSR 1502 made by JSR) 70 parts butadiene rubber (BR) (Ube Industries BR150B) 30 parts silica (Tosoh Silica VN3) 50 parts carbon black (Showa Cabot) N330) 5 parts by weight silane coupling agent (Degussa Si69) 5 parts by weight anti-aging agent (Ouchi Shinsei Chemical Co., Ltd. Nocrack 6C) 2 parts by weight zinc oxide (manufactured by Sakai Chemical) 3 parts by weight stearic acid (Japan) 2 parts by weight vulcanization accelerator (CZ-G made by Ouchi Shinsei Chemical Co., Ltd.) 3 parts by weight insoluble sulfur (Crytex HS OT-20 made by Flexis) 2 parts by weight p-tert-octylphenol sulfur chloride cocondensation 2 parts by weight of resin

<ゴム物性評価方法>
(引張試験)
JIS K6251に準拠し、ダンベル状3号形試験片を用い、破断点強度(MPa)を測定した。
(転がり抵抗;tanδ(70℃))
動的粘弾性を、セイコーインスツルメンツ(株)製動的粘弾性測定装置にて、初期歪み1%、振幅±0.2%、周波数10Hzで測定し、温度70℃におけるtanδを求めた。試験片の作成は160℃×15分で架橋を行った。
<Rubber physical property evaluation method>
(Tensile test)
Based on JIS K6251, the strength at break (MPa) was measured using a dumbbell-shaped No. 3 test piece.
(Rolling resistance; tan δ (70 ° C))
Dynamic viscoelasticity was measured with a dynamic viscoelasticity measuring device manufactured by Seiko Instruments Inc. at an initial strain of 1%, an amplitude of ± 0.2%, and a frequency of 10 Hz, and tan δ at a temperature of 70 ° C. was determined. The test piece was cross-linked at 160 ° C. for 15 minutes.

<ゴム物性評価基準>
樹脂架橋剤として硫黄を使用した参考例の各評価結果を100とした時の、それぞれの樹脂架橋剤を使用した際の評価結果を相対的に記載した。併せて、次の評価基準に基づき、評価結果を可視化した。
Tb(破断点強度:破断特性に係る値。値が高いほうが破断特性が良い。)
参考例に比べ5%以内の低下:○
5%より低く、10%以内の低下:△
10%以上低下:×
tanδ(粘弾性特性に関する値。値が低いほうが粘弾性特性が良好となる。)
参考例に比べ上昇:×
5%未満の低下:△
5%以下、10%以内の低下:○
10%以上低下:◎
<Rubber properties evaluation criteria>
The evaluation results when using the respective resin cross-linking agents when the evaluation results of the reference examples using sulfur as the resin cross-linking agent were set to 100 were relatively described. In addition, the evaluation results were visualized based on the following evaluation criteria.
Tb (strength at break: value related to break characteristics. The higher the value, the better the break characteristics)
Reduction within 5% compared to the reference example: ○
Lower than 5% and within 10%: △
Decrease by 10% or more: ×
tan δ (value relating to viscoelastic properties. The lower the value, the better the viscoelastic properties)
Increased compared to the reference example: ×
Less than 5% drop:
Less than 5%, less than 10%: ○
Decrease by 10% or more: ◎

<表1>

Figure 2013203742
<Table 1>
Figure 2013203742

<表2>

Figure 2013203742
<Table 2>
Figure 2013203742

Claims (2)

p−tert−オクチルフェノール1モルに対して一塩化イオウ1.2〜1.8モルを反応させることで得られる樹脂であって、前記樹脂中の硫黄含量が25〜34重量%であることを特徴とするp−tert−オクチルフェノール塩化硫黄共縮合樹脂。 A resin obtained by reacting 1.2 to 1.8 mol of sulfur monochloride with 1 mol of p-tert-octylphenol, wherein the sulfur content in the resin is 25 to 34% by weight. P-tert-octylphenol sulfur chloride co-condensation resin. 請求項1記載のp−tert−オクチルフェノール塩化硫黄共縮合樹脂を0.5〜50重量部含むことを特徴とするゴム組成物。 A rubber composition comprising 0.5 to 50 parts by weight of the p-tert-octylphenol sulfur chloride cocondensation resin according to claim 1.
JP2012070498A 2012-03-27 2012-03-27 p-tert-OCTYLPHENOL-SULFUR CHLORIDE CO-CONDENSED RESIN Pending JP2013203742A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014201662A (en) * 2013-04-05 2014-10-27 田岡化学工業株式会社 p-tert-OCTYLPHENOL SULFUR CHLORIDE CO-CONDENSATION RESIN COMPOSITION AND MANUFACTURING METHOD THEREOF
JP2016074837A (en) * 2014-10-08 2016-05-12 田岡化学工業株式会社 p-tert-OCTYLPHENOL SULFUR CHLORIDE CO-CONDENSATION RESIN COMPOSITION AND METHOD FOR PRODUCING THE SAME

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5540603A (en) * 1978-09-14 1980-03-22 Mitsui Toatsu Chem Inc Preparation of 2,2'-bis(4-(1,1,3,3-tetramethylbutyl)phenol)sulfide
JPS55125137A (en) * 1979-03-22 1980-09-26 Sumitomo Chem Co Ltd Rubber composition
JPS5813648A (en) * 1981-07-17 1983-01-26 Sumitomo Chem Co Ltd Rubber composition

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5540603A (en) * 1978-09-14 1980-03-22 Mitsui Toatsu Chem Inc Preparation of 2,2'-bis(4-(1,1,3,3-tetramethylbutyl)phenol)sulfide
JPS55125137A (en) * 1979-03-22 1980-09-26 Sumitomo Chem Co Ltd Rubber composition
JPS5813648A (en) * 1981-07-17 1983-01-26 Sumitomo Chem Co Ltd Rubber composition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014201662A (en) * 2013-04-05 2014-10-27 田岡化学工業株式会社 p-tert-OCTYLPHENOL SULFUR CHLORIDE CO-CONDENSATION RESIN COMPOSITION AND MANUFACTURING METHOD THEREOF
JP2016074837A (en) * 2014-10-08 2016-05-12 田岡化学工業株式会社 p-tert-OCTYLPHENOL SULFUR CHLORIDE CO-CONDENSATION RESIN COMPOSITION AND METHOD FOR PRODUCING THE SAME

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