JP2017128071A - Method of and device for kneading rubber material - Google Patents

Method of and device for kneading rubber material Download PDF

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JP2017128071A
JP2017128071A JP2016010211A JP2016010211A JP2017128071A JP 2017128071 A JP2017128071 A JP 2017128071A JP 2016010211 A JP2016010211 A JP 2016010211A JP 2016010211 A JP2016010211 A JP 2016010211A JP 2017128071 A JP2017128071 A JP 2017128071A
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rubber material
kneading
silica
water
rubber
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JP6724383B2 (en
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慶知 佐藤
Yoshitomo Sato
慶知 佐藤
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Yokohama Rubber Co Ltd
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Yokohama Rubber Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7476Systems, i.e. flow charts or diagrams; Plants
    • B29B7/7495Systems, i.e. flow charts or diagrams; Plants for mixing rubber
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/06Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
    • B29B7/10Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
    • B29B7/18Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/183Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft having a casing closely surrounding the rotors, e.g. of Banbury type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/06Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices
    • B29B7/10Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary
    • B29B7/18Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft
    • B29B7/183Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type with movable mixing or kneading devices rotary with more than one shaft having a casing closely surrounding the rotors, e.g. of Banbury type
    • B29B7/186Rotors therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/02Mixing; Kneading non-continuous, with mechanical mixing or kneading devices, i.e. batch type
    • B29B7/22Component parts, details or accessories; Auxiliary operations
    • B29B7/28Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control
    • B29B7/286Component parts, details or accessories; Auxiliary operations for measuring, controlling or regulating, e.g. viscosity control measuring properties of the mixture, e.g. temperature, density
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/82Heating or cooling
    • B29B7/823Temperature control
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/88Adding charges, i.e. additives
    • B29B7/94Liquid charges

Abstract

PROBLEM TO BE SOLVED: To provide a method of and device for kneading a rubber material capable of accelerating a chemical reaction when kneading a silica-blended rubber material, and capable of improving the specified physical properties of a rubber composition obtained by vulcanization after kneading.SOLUTION: A method of kneading a rubber material includes: detecting by a temperature sensor 11, the temperature of a silica-blended rubber material R comprising a raw material rubber G, silica, and a nonvulcanizing ingredient N including a silane coupling agent during kneading by a closed type kneader 2; controlling the rotation of a rotor 3 by a control part 12 based on the above detection data; and maintaining the silica-blended rubber material R in which a prescribed amount of the water W is added by a water supply mechanism 13 in a previously set prescribed temperature range to knead.SELECTED DRAWING: Figure 1

Description

本発明は、ゴム材料の混練方法および装置に関し、さらに詳しくは、シリカ配合ゴム材料を混練する際の化学反応を促進させることができ、混練後に加硫して得たゴム組成物の特定のゴム物性を向上させることができるゴム材料の混練方法および装置に関するものである。   The present invention relates to a rubber material kneading method and apparatus, and more particularly, a specific rubber of a rubber composition that can promote a chemical reaction when kneading a silica-blended rubber material and is vulcanized after kneading. The present invention relates to a rubber material kneading method and apparatus capable of improving physical properties.

タイヤのトレッドゴム等に対してはシリカ配合ゴムを用いることによって、タイヤの転がり抵抗やウエットグリップ性能を向上させることができる。シリカは粒子どうしが凝集しやすいため、ゴム材料に対する分散性が悪く、シランカップリング剤を配合してシリカとカップリング反応させることによって分散性を向上させている。シリカ配合ゴム材料は、通常のゴム材料とは異なるこのような性質を有しているので、シリカ配合ゴム材料に適した混練方法、装置が種々提案されている(例えば特許文献1参照)。   By using silica-containing rubber for tire tread rubber and the like, tire rolling resistance and wet grip performance can be improved. Since silica is easy to aggregate particles, the dispersibility with respect to a rubber material is bad, and the dispersibility is improved by mix | blending a silane coupling agent and carrying out a coupling reaction with a silica. Since silica compounded rubber materials have such properties different from ordinary rubber materials, various kneading methods and apparatuses suitable for silica compounded rubber materials have been proposed (see, for example, Patent Document 1).

特許文献1では、密閉型混練機とオープン構造のロール混練機とを組み合わせて、シリカ配合ゴム材料を混練する混練システムが提案されている。この混練システムでは、オープン構造のロール混練機を用いることで、シリカ配合ゴム材料を混練する際に生成されるアルコール等を外部に発散させてカップリング反応を促進させるようにしている。   Patent Document 1 proposes a kneading system for kneading a silica-blended rubber material by combining a closed kneader and an open structure roll kneader. In this kneading system, by using an open structure roll kneader, alcohol generated when kneading the silica-blended rubber material is diffused to the outside to promote the coupling reaction.

一方、本願発明者は密閉型混練機で混練する工程に注目して、シリカ配合ゴム材料を混練する際の化学反応を促進させることができ、しかも、混練後に加硫して得たゴム組成物の特定のゴム物性が向上することを知得した。そして、この知得に基づいて本願発明を創作するに至った。   On the other hand, the inventor of the present application pays attention to the process of kneading with a closed kneader, can promote the chemical reaction when kneading the silica-blended rubber material, and vulcanized after kneading. It was found that the specific rubber physical properties were improved. And based on this knowledge, it came to create this invention.

特開2007−216471号公報JP 2007-216471 A

本発明の目的は、シリカ配合ゴム材料を混練する際の化学反応を促進させることができ、混練後に加硫して得たゴム組成物の特定のゴム物性を向上させることができるゴム材料の混練方法および装置を提供することにある。   An object of the present invention is to knead a rubber material capable of promoting a chemical reaction when kneading a silica-blended rubber material and improving specific rubber physical properties of a rubber composition obtained by vulcanization after kneading. It is to provide a method and apparatus.

上記目的を達成するための本発明のゴム材料の混練方法は、原料ゴムとシリカおよびシランカップリング剤を含む非加硫系配合剤とからなるシリカ配合ゴム材料を密閉型混練機により混練するゴム材料の混練方法において、所定量の水を添加した状態の前記シリカ配合ゴム材料を、予め設定された所定の温度範囲に維持して前記密閉型混練機により混練することを特徴とする。   The rubber material kneading method of the present invention for achieving the above object is a rubber in which a silica-containing rubber material comprising a raw rubber and a non-vulcanizing compound containing silica and a silane coupling agent is kneaded by a closed kneader. The material kneading method is characterized in that the silica-blended rubber material with a predetermined amount of water added is kneaded by the closed kneader while maintaining a predetermined temperature range set in advance.

本発明のゴム材料の混練装置は、原料ゴムとシリカおよびシランカップリング剤を含む非加硫系配合剤とからなるシリカ配合ゴム材料を混練する密閉型混練機を備えたゴム材料の混練装置において、前記密閉型混練機により混練中の前記シリカ配合ゴム材料の温度を検知する温度センサと、前記密閉型混練機のロータの回転を制御する制御部と、前記密閉型混練機の混練室に水を供給する水供給機構とを備え、前記温度センサの検知データに基づいて前記ロータの回転数を制御することにより、前記水供給機構により所定量の水を添加した状態の前記シリカ配合ゴム材料を、予め設定された所定の温度範囲に維持して混練する構成にしたことを特徴とする。   The rubber material kneading apparatus of the present invention is a rubber material kneading apparatus provided with a closed kneader for kneading a silica-blended rubber material comprising a raw rubber and a non-vulcanizing compound containing silica and a silane coupling agent. A temperature sensor that detects the temperature of the silica-containing rubber material being kneaded by the closed kneader, a control unit that controls the rotation of the rotor of the closed kneader, and water in the kneading chamber of the closed kneader. The silica-containing rubber material in a state where a predetermined amount of water is added by the water supply mechanism by controlling the number of rotations of the rotor based on detection data of the temperature sensor. The kneading is performed while maintaining the temperature in a predetermined temperature range set in advance.

本発明によれば、所定量の水を添加した状態のシリカ配合ゴム材料を、所定の温度範囲に維持して混練することで、シリカ配合ゴム材料における化学反応(加水分解反応)を促進させることができる。さらに、混練後に加硫して得たゴム組成物の特定のゴム物性を向上させることができる。具体的には、加硫して得たゴム組成物をタイヤのトレッドゴムに使用すると、タイヤの転がり抵抗やウエットグリップ性能を向上させることが可能になる。   According to the present invention, the chemical reaction (hydrolysis reaction) in the silica-blended rubber material is promoted by kneading the silica-blended rubber material to which a predetermined amount of water has been added while maintaining the predetermined temperature range. Can do. Furthermore, specific rubber properties of the rubber composition obtained by vulcanization after kneading can be improved. Specifically, when a rubber composition obtained by vulcanization is used for a tread rubber of a tire, the rolling resistance and wet grip performance of the tire can be improved.

前記所定の温度範囲は例えば130℃以上160℃以下にする。この温度範囲にすることで、混練中のシリカ配合ゴム材料における化学反応をより促進させ易くなる。また、加硫して得たゴム組成物をタイヤのトレッドゴムに使用すると、タイヤの転がり抵抗やウエットグリップ性能を一段と向上させ易くなる。   The predetermined temperature range is, for example, 130 ° C. or higher and 160 ° C. or lower. By setting this temperature range, it becomes easier to promote the chemical reaction in the silica-blended rubber material being kneaded. Moreover, when the rubber composition obtained by vulcanization is used for a tread rubber of a tire, it becomes easier to further improve the rolling resistance and wet grip performance of the tire.

前記水を例えば前記密閉型混練機の混練室に噴霧または滴下することにより、前記シリカ配合ゴム材料に添加する。或いは、前記密閉型混練機を構成するラムを、前記密閉型混練機のラム室の下端から上昇させた状態で、前記水を前記シリカ配合ゴム材料に添加することもできる。これにより、水をシリカ配合ゴム材料に均一に混合し易くなって、加硫して得たゴム組成物の品質のばらつきを抑えるには有利になる。   The water is added to the silica-blended rubber material, for example, by spraying or dropping into the kneading chamber of the closed kneader. Alternatively, the water can be added to the silica-containing rubber material in a state where the ram constituting the closed kneader is raised from the lower end of the ram chamber of the closed kneader. This facilitates uniform mixing of water with the silica-containing rubber material, which is advantageous for suppressing variations in the quality of the rubber composition obtained by vulcanization.

前記水の温度を例えば混練中の前記シリカ配合ゴム材料よりも低温である10℃以上50℃以下にする。10℃以上50℃以下の相対的に低温の水を使用することで、シリカ配合ゴム材料を前記所定の温度範囲に維持するために密閉型混練機のロータ回転速度が早くなる。それ故、加硫して得たゴム組成物の一定のゴム品質を確保しつつ混練時間の短縮を図ることが可能になる。   The temperature of the water is, for example, 10 ° C. or higher and 50 ° C. or lower, which is lower than the silica-containing rubber material being kneaded. By using relatively low temperature water of 10 ° C. or more and 50 ° C. or less, the rotational speed of the rotor of the closed kneader is increased in order to maintain the silica-containing rubber material in the predetermined temperature range. Therefore, the kneading time can be shortened while ensuring a certain rubber quality of the rubber composition obtained by vulcanization.

本発明のゴム材料の混練装置を例示する説明図である。It is explanatory drawing which illustrates the kneading apparatus of the rubber material of this invention. 図1のA−A断面図である。It is AA sectional drawing of FIG. 図1の混練装置によってシリカ配合ゴム材料を混練している状態を例示する説明図である。It is explanatory drawing which illustrates the state which knead | mixes the silica compound rubber material with the kneading apparatus of FIG. 図1の混練室で混練されているシリカ配合ゴム材料に水を添加している状態を例示する説明図である。It is explanatory drawing which illustrates the state which has added water to the silica compounding rubber material kneaded in the kneading chamber of FIG. シリカ配合ゴム材料の混練過程におけるロータの回転駆動に要する瞬時電力およびシリカ配合ゴム材料の温度の経時変化を例示するグラフ図である。It is a graph which illustrates the time-dependent change of the instantaneous electric power required for the rotational drive of the rotor in the kneading process of a silica compounding rubber material, and the temperature of a silica compounding rubber material.

以下、本発明のシリカ配合ゴム材料の混練方法および装置を図に示した実施形態に基づいて説明する。   Hereinafter, the kneading method and apparatus for silica-containing rubber material of the present invention will be described based on the embodiments shown in the drawings.

図1〜図2に例示する本発明のゴム材料の混練装置1(以下、混練装置1という)は、シリカ配合ゴム材料Rを混練する。シリカ配合ゴム材料Rは、原料ゴムGとシリカおよびシランカップリング剤を含む非加硫系配合剤Nとからなり、混練することで原料ゴムGに非加硫系配合剤Nを均等に分散させるようにして適切な粘度にする。   A rubber material kneading apparatus 1 (hereinafter referred to as a kneading apparatus 1) of the present invention illustrated in FIGS. 1 to 2 kneads a silica-blended rubber material R. The silica-containing rubber material R is composed of a raw rubber G and a non-vulcanizing compound N containing silica and a silane coupling agent, and the non-vulcanizing compound N is uniformly dispersed in the raw rubber G by kneading. In this way, an appropriate viscosity is obtained.

原料ゴムGとしては、天然ゴム(NR)、イソプレンゴム(IR)、ブタジエンゴム(BR)、1,2−ポリブタジエン、クロロプレンゴム、ブチルゴム、スチレン−ブタジエンゴム(SBR)、ニトリルゴム(アクリルニトリルゴム、水素化ニトリルゴム)、エチレンプロピレンジエンゴム等を例示できる。これらを1種単独でまたは2種以上を組合せて使用する。   As the raw rubber G, natural rubber (NR), isoprene rubber (IR), butadiene rubber (BR), 1,2-polybutadiene, chloroprene rubber, butyl rubber, styrene-butadiene rubber (SBR), nitrile rubber (acrylonitrile rubber, Examples thereof include hydrogenated nitrile rubber) and ethylene propylene diene rubber. These are used individually by 1 type or in combination of 2 or more types.

非加硫系配合剤Nとしては、シリカおよびシランカップリング剤の他に、必要に応じて、シリカ以外の充填剤(例えば、カーボンブラック)、酸化亜鉛、ステアリン酸等を用いる。   As the non-vulcanizing compounding agent N, in addition to silica and a silane coupling agent, a filler other than silica (for example, carbon black), zinc oxide, stearic acid and the like are used as necessary.

シリカとしては、タイヤ等の用途でゴム組成物に配合されている公知のシリカを使用でき、具体的には、例えば、湿式シリカ、乾式シリカ、ヒュームドシリカ、珪藻土などを例示できる。これらを1種単独でまたは2種以上を組合せて使用する。   As silica, the well-known silica mix | blended with the rubber composition for uses, such as a tire, can be used, Specifically, wet silica, dry silica, fumed silica, diatomaceous earth etc. can be illustrated, for example. These are used individually by 1 type or in combination of 2 or more types.

シランカップリング剤としては、公知のものを使用でき、具体的には、例えば、ビス(3−トリエトキシシリルプロピル)テトラスルフィド、ビス(3−トリメトキシシリルプロピル)テトラスルフィド、ビス(3−トリエトキシシリルプロピル)ジスルフィド、メルカプトプロピルトリメトキシシラン、メルカプトプロピルトリエトキシシラン、3−トリメトキシシリルプロピル−N,N−ジメチルチオカルバモイル−テトラスルフィド、トリメトキシシリルプロピル−メルカプトベンゾチアゾールテトラスルフィド、トリエトキシシリルプロピル−メタクリレート−モノスルフィド、ジメトキシメチルシリルプロピル−N,N−ジメチルチオカルバモイル−テトラスルフィド等を例示できる。これらを1種単独でまたは2種以上を組合せて使用する。   As the silane coupling agent, known ones can be used. Specifically, for example, bis (3-triethoxysilylpropyl) tetrasulfide, bis (3-trimethoxysilylpropyl) tetrasulfide, bis (3-tri Ethoxysilylpropyl) disulfide, mercaptopropyltrimethoxysilane, mercaptopropyltriethoxysilane, 3-trimethoxysilylpropyl-N, N-dimethylthiocarbamoyl-tetrasulfide, trimethoxysilylpropyl-mercaptobenzothiazole tetrasulfide, triethoxysilyl Examples thereof include propyl-methacrylate-monosulfide and dimethoxymethylsilylpropyl-N, N-dimethylthiocarbamoyl-tetrasulfide. These are used individually by 1 type or in combination of 2 or more types.

この混練装置1は、ロータ3を備えたバンバリーミキサー等の密閉型混練機2と、温度センサ11と、ロータの回転を制御する制御部12と、水供給機構13とを備えている。   The kneading apparatus 1 includes a closed kneader 2 such as a Banbury mixer including a rotor 3, a temperature sensor 11, a control unit 12 that controls rotation of the rotor, and a water supply mechanism 13.

密閉型混練機2は、混練室4aと、混練室4aの上方に連接されたラム室4bとを備えていて、混練室4aには対向配置された一対のロータ3と油投入部5とが設けられている。それぞれのロータ3の回転軸3aには翼3bが突設されていて、平行して配置された回転軸3aは駆動用モータによって回転駆動される。混練室4aの底面には開閉する排出扉10が設けられている。   The closed kneading machine 2 includes a kneading chamber 4a and a ram chamber 4b connected to the upper side of the kneading chamber 4a. The kneading chamber 4a includes a pair of rotors 3 and an oil charging unit 5 that are opposed to each other. Is provided. A blade 3b is projected from the rotating shaft 3a of each rotor 3, and the rotating shaft 3a arranged in parallel is driven to rotate by a driving motor. A discharge door 10 that opens and closes is provided on the bottom surface of the kneading chamber 4a.

ラム室4bには、上下移動して混練室4a内の圧力(ラム圧力)を調整するラム8が配置されている。ラム室4bにはさらに、原料ゴムGを投入するゴム投入部6と、非加硫系配合剤Nをホッパ7から投入する配合剤投入部9とが設けられている。   In the ram chamber 4b, a ram 8 that moves up and down to adjust the pressure (ram pressure) in the kneading chamber 4a is disposed. The ram chamber 4 b is further provided with a rubber charging unit 6 for charging the raw rubber G and a compounding agent charging unit 9 for charging the non-vulcanized compounding agent N from the hopper 7.

温度センサ11は、混練室4aに先端部を露出して設けられている。温度センサ11は混練室4aで混練されているシリカ配合ゴム材料Rの温度を逐次検知する。温度センサ11による検知データは制御部12に入力される。   The temperature sensor 11 is provided in the kneading chamber 4a with its tip portion exposed. The temperature sensor 11 sequentially detects the temperature of the silica-containing rubber material R kneaded in the kneading chamber 4a. Data detected by the temperature sensor 11 is input to the control unit 12.

水供給機構13は混練室4aに所定量の水Wを供給する。この実施形態では、水供給機構13はラム8に付設されている。この水供給機構13は、ラム8の内部に配置された貯水部13aと、貯水部13aから下方に延びる流路13cの下端部に設置されたノズル13bとを有している。例えば、流路13cに設置された開閉弁を開弁することにより、ノズル13bから水Wが供給される。ノズル13bの仕様に応じて水Wを混練室4aに噴霧することも、滴下することも、単純に垂れ流すこともできる。   The water supply mechanism 13 supplies a predetermined amount of water W to the kneading chamber 4a. In this embodiment, the water supply mechanism 13 is attached to the ram 8. The water supply mechanism 13 includes a water storage portion 13a disposed inside the ram 8, and a nozzle 13b installed at a lower end portion of a flow path 13c extending downward from the water storage portion 13a. For example, water W is supplied from the nozzle 13b by opening an on-off valve installed in the flow path 13c. Depending on the specifications of the nozzle 13b, the water W can be sprayed into the kneading chamber 4a, dropped, or simply dripped down.

水供給機構13は例示した形態に限らず、その他、様々な形態を採用することができる。例えば、ゴム投入部6や配合剤投入部9を通じて、水Wを混練室4aに供給することもできる。混練室4aに供給する水Wの温度は、例えば10℃以上50℃以下である。   The water supply mechanism 13 is not limited to the exemplified form, and various other forms can be adopted. For example, the water W can be supplied to the kneading chamber 4a through the rubber charging unit 6 and the compounding agent charging unit 9. The temperature of the water W supplied to the kneading chamber 4a is, for example, 10 ° C. or more and 50 ° C. or less.

制御部12には電力計12aが付設されている。ロータ3の回転駆動に要した瞬時電力が電力計12aにより逐次検知される。電力計12aによる検知データは、制御部12に入力される。制御部12では瞬時電力を積算した積算電力量が算出され、任意の混練期間おけるロータ3の回転駆動に要した電力量(ロータ3に作用する負荷)を把握することができる。制御部12にはその他に、ロータ3の回転数やラム圧力等が入力される。   A wattmeter 12 a is attached to the control unit 12. Instantaneous power required for rotationally driving the rotor 3 is sequentially detected by the wattmeter 12a. Data detected by the wattmeter 12 a is input to the control unit 12. The control unit 12 calculates an integrated electric energy obtained by integrating the instantaneous electric power, and can grasp the electric energy (load acting on the rotor 3) required for the rotational driving of the rotor 3 in an arbitrary kneading period. In addition, the rotational speed of the rotor 3, the ram pressure, and the like are input to the control unit 12.

制御部12は、ロータ3の回転数、ラム圧力(ラムの上下移動)、水供給機構13の作動等を制御する。制御部12には、混練するシリカ配合ゴム材料Rの仕様に応じて、混練する際に維持するシリカ配合ゴム材料Rの最適な所定の温度範囲、水供給機構13から水Wを供給するタイミングやその供給量などが入力されている。そして、ロータ3の回転数は、温度センサ11による検知データに基づいて制御される。基本的には、ロータ3の回転数を大きくする(回転速度を速くする)程、混練しているシリカ配合ゴム材料Rの温度は高くなる。   The control unit 12 controls the number of rotations of the rotor 3, the ram pressure (the vertical movement of the ram), the operation of the water supply mechanism 13, and the like. Depending on the specifications of the silica-blended rubber material R to be kneaded, the control unit 12 has an optimum predetermined temperature range of the silica-blended rubber material R to be maintained when kneading, the timing of supplying water W from the water supply mechanism 13, The supply amount is input. The rotational speed of the rotor 3 is controlled based on the detection data from the temperature sensor 11. Basically, the temperature of the silica-blended rubber material R being kneaded increases as the rotational speed of the rotor 3 is increased (the rotational speed is increased).

以下、本発明のゴム材料の混練方法の手順を説明する。   The procedure of the rubber material kneading method of the present invention will be described below.

ゴム材料の混練過程は、図5に例示するようにゴム素練り工程(S1)、配合剤取り込み工程(S2)、均一分散工程(S3)で構成される。図5には本願発明を適用した混練過程でのロータ3の回転駆動に要する瞬時電力Pおよびシリカ配合ゴム材料R(原料ゴムG)の温度Tの経時データを例示している。   The rubber material kneading process includes a rubber kneading step (S1), a compounding agent intake step (S2), and a uniform dispersion step (S3) as illustrated in FIG. FIG. 5 exemplifies time-lapse data of the instantaneous power P required for rotational driving of the rotor 3 and the temperature T of the silica-containing rubber material R (raw rubber G) in the kneading process to which the present invention is applied.

ゴム素練り工程においては、図1に例示するようにラム8をラム室4bの上端部の待機位置に保持した状態で、ゴム投入部6を通じて、予め設定された所定量の原料ゴムGを混練室4aに投入する。その後、ラム8をラム室4bの下端まで下方移動させて、ラム8によって混練室4aの上面を形成する。この状態で、油投入部5を通じてオイルを混練室4aに投入しながらロータ3を回転駆動して原料ゴムGとオイルとを混練する。この工程では、ロータ3の負荷を示す瞬時電力Pは比較的小さい。原料ゴムGの温度Tは徐々に低下する。   In the rubber mastication step, as shown in FIG. 1, a predetermined amount of raw rubber G set in advance is kneaded through the rubber charging unit 6 with the ram 8 held at the standby position at the upper end of the ram chamber 4b. It puts into the chamber 4a. Thereafter, the ram 8 is moved downward to the lower end of the ram chamber 4b, and the upper surface of the kneading chamber 4a is formed by the ram 8. In this state, the raw rubber G and the oil are kneaded by rotating the rotor 3 while supplying the oil into the kneading chamber 4a through the oil charging unit 5. In this step, the instantaneous power P indicating the load of the rotor 3 is relatively small. The temperature T of the raw rubber G gradually decreases.

ゴム素練り工程の終了後は、配合剤取り込み工程に移行する。配合剤取り込み工程では、ラム8をラム室4bの上端部の待機位置に移動させて、予め設定された種類の所定量の非加硫系配合剤N(シリカやシランカップリング剤など)をホッパ7から配合剤投入部9を通じて混練室4aに投入する。その後、ラム8をラム室4bの下端まで下方移動させて、ラム8によって混練室4aの上面を形成する。この状態で図3に例示するようにロータ3を回転駆動して、原料ゴムGと非加硫系配合剤Nとをからなるシリカ配合ゴム材料Rを混練する。原料ゴムGや非加硫系配合剤Nによってノズル13bが目詰まりしなように、ノズル13bには目詰まり防止カバー等を設置することもできる。   After the rubber mastication process is completed, the process proceeds to the compounding agent incorporation process. In the compounding agent intake step, the ram 8 is moved to the standby position at the upper end of the ram chamber 4b, and a predetermined amount of a non-vulcanized compounding agent N (silica, silane coupling agent, etc.) of a preset type is placed in the hopper. 7 is charged into the kneading chamber 4a through the compounding agent charging unit 9. Thereafter, the ram 8 is moved downward to the lower end of the ram chamber 4b, and the upper surface of the kneading chamber 4a is formed by the ram 8. In this state, the rotor 3 is rotationally driven as illustrated in FIG. 3 to knead the silica-containing rubber material R composed of the raw rubber G and the non-vulcanized compounding agent N. In order to prevent the nozzle 13b from being clogged by the raw rubber G or the non-vulcanizing compounding agent N, a clogging prevention cover or the like can be installed on the nozzle 13b.

配合剤取り込み工程では、ゴム素練りした原料ゴムGの上に載った非加硫系配合剤Nを大きくかき混ぜて、徐々に小さなゴムの固まりが形成される。次いで、小さなゴムの固まりが徐々に大きくなり、最後には一塊りになる。配合剤取り込み工程では、ラム8を数回、ラム室4bの上端部に上昇させた状態にしてロータ3を回転させることによりシリカ配合ゴム材料Rの上下を反転させるラム反転を行う。この工程では、シリカ配合ゴム材料Rの温度Tは徐々に上昇する。   In the compounding agent incorporation step, the non-vulcanized compounding agent N placed on the rubber kneaded raw material rubber G is agitated greatly, and a small rubber lump is gradually formed. Then a small mass of rubber gradually grows and eventually lumps. In the compounding agent taking-in step, ram inversion is performed to invert the silica compounded rubber material R up and down by rotating the rotor 3 with the ram 8 raised to the upper end of the ram chamber 4b several times. In this step, the temperature T of the silica-containing rubber material R gradually increases.

カーボン取り込み工程が終了すると、均一分散工程に移行する。この工程では、非加硫系配合剤Nを原料ゴムGの全体に渡り均一に分散させる。この工程では、瞬時電力Pは当初は大きいが徐々に低下して一定になる。混練しているシリカ配合ゴム材料Rの温度Tは所定の温度範囲でほぼ一定に維持する。即ち、この工程では、温度センサ11により逐次検知したシリカ配合ゴム材料Rの温度Tの検知データに基づいて、制御部12によりロータ3の回転数を制御して、シリカ配合ゴム材料Rの温度Tを所定の温度範囲に維持して混練する。この所定の温度範囲は、例えば130℃以上160℃以下にする。   When the carbon uptake process ends, the process moves to a uniform dispersion process. In this step, the non-vulcanizing compounding agent N is uniformly dispersed throughout the raw rubber G. In this step, the instantaneous power P is initially large but gradually decreases and becomes constant. The temperature T of the silica compounded rubber material R being kneaded is maintained substantially constant within a predetermined temperature range. That is, in this process, the controller 12 controls the number of rotations of the rotor 3 based on the detection data of the temperature T of the silica-blended rubber material R sequentially detected by the temperature sensor 11, and the temperature T of the silica-blended rubber material R is controlled. Is maintained in a predetermined temperature range and kneaded. This predetermined temperature range is, for example, 130 ° C. or more and 160 ° C. or less.

シリカ配合ゴム材料Rの温度Tが所定の温度範囲よりも低くなりそうであればロータ3の回転数を大きく、所定の温度範囲よりも高くなりそうであればロータ3の回転数を小さくする制御を行う。或いは、ラム8を上昇させてラム圧力を下げることによりシリカ配合ゴム材料Rの温度Tを低下させ、ラム8を降下させてラム圧力を上げることにより温度Tを上昇させることもできる。   Control for increasing the rotational speed of the rotor 3 if the temperature T of the silica-containing rubber material R is likely to be lower than the predetermined temperature range, and decreasing the rotational speed of the rotor 3 if it is likely to be higher than the predetermined temperature range. I do. Alternatively, the temperature T of the silica-containing rubber material R can be lowered by raising the ram 8 and lowering the ram pressure, and the temperature T can be raised by lowering the ram 8 and raising the ram pressure.

本願発明では、上述の配合剤取り込み工程または均一分散工程のいずれかにおいて、図4に例示するように混練室4aに所定量の水Wを供給してシリカ配合ゴム材料Rに添加した状態にする。この実施形態では、ラム8を、ラム室4bの下端から待機位置まで上昇させた状態にして、ノズル13bから水Wを噴霧してシリカ配合ゴム材料Rに添加している。   In the present invention, a predetermined amount of water W is supplied to the kneading chamber 4a and added to the silica compounded rubber material R as illustrated in FIG. . In this embodiment, the ram 8 is raised from the lower end of the ram chamber 4b to the standby position, and water W is sprayed from the nozzle 13b and added to the silica compounded rubber material R.

シリカ配合ゴム材料Rに添加する水Wの所定量は、例えば、原料ゴムG(100質量部)に対して0.5重量部以上5.0重量部以下にする。所定量の水Wをシリカ配合ゴム材料Rに添加した後は、ラム8をラム室4bの下端に移動させた状態にして、図3に例示するようにシリカ配合ゴム材料Rを混練する。   The predetermined amount of water W added to the silica-containing rubber material R is, for example, 0.5 parts by weight or more and 5.0 parts by weight or less with respect to the raw rubber G (100 parts by weight). After the predetermined amount of water W is added to the silica-blended rubber material R, the silica-blended rubber material R is kneaded as illustrated in FIG. 3 with the ram 8 being moved to the lower end of the ram chamber 4b.

均一分散工程の終了後、シリカ配合ゴム材料Rを混練して製造された未加硫のゴム組成物を、開口した放出扉10から密閉型混練機2の外部に放出する。放出されたゴム組成物は、次工程において、硫黄や加硫促進剤等の加硫系配合剤が所定割合で配合されて混練される。この工程を経て製造された未加硫のゴム組成物は、様々な形状に成形されて金型の内部で加硫される。   After completion of the uniform dispersion step, the unvulcanized rubber composition produced by kneading the silica-blended rubber material R is discharged from the open discharge door 10 to the outside of the closed kneader 2. In the next step, the released rubber composition is kneaded with a vulcanizing compound such as sulfur or a vulcanization accelerator in a predetermined ratio. The unvulcanized rubber composition produced through this process is molded into various shapes and vulcanized inside the mold.

加硫工程を経て加硫されたゴム組成物は、様々なゴム製品或いはゴム製品の一部になる。例えば、加硫されたゴム組成物は、タイヤの製造工程において、トレッドゴムやショルダ部のゴム、サイド部のゴムとして使用される。   The rubber composition vulcanized through the vulcanization process becomes a part of various rubber products or rubber products. For example, a vulcanized rubber composition is used as a tread rubber, a shoulder rubber, or a side rubber in a tire manufacturing process.

上述したように、所定量の水Wを添加した状態のシリカ配合ゴム材料Rを、所定の温度範囲に維持して混練することで、シリカ配合ゴム材料Rにおける化学反応(加水分解反応)を促進させることができる。これに伴い、混練時間の短縮が期待できる。さらには、混練後に加硫して得たゴム組成物の特定のゴム物性を向上させることができる。具体的には、加硫して得たゴム組成物をタイヤのトレッドゴムに使用すると、タイヤの転がり抵抗やウエットグリップ性能を向上させることが可能になる。このゴム物性の向上については後述する。   As described above, the silica-containing rubber material R with a predetermined amount of water W added thereto is kneaded while maintaining a predetermined temperature range, thereby promoting the chemical reaction (hydrolysis reaction) in the silica-containing rubber material R. Can be made. Along with this, shortening of the kneading time can be expected. Furthermore, specific rubber properties of the rubber composition obtained by vulcanization after kneading can be improved. Specifically, when a rubber composition obtained by vulcanization is used for a tread rubber of a tire, the rolling resistance and wet grip performance of the tire can be improved. The improvement of the rubber physical properties will be described later.

シリカ配合ゴム材料Rに添加する水Wの所定量は、原料ゴムG(100質量部)に対して0.5重量部未満では、シリカ配合ゴム材料Rの加水分解反応を十分に促進することができない。一方、5.0重量部超であると、シリカ配合ゴム材料Rを混練した後の工程(ゴム押出工程等)において、ゴム組成物にポーラスが発生(発泡して多孔状になる)して品質が低下するリスクが高くなる。   If the predetermined amount of water W added to the silica-blended rubber material R is less than 0.5 parts by weight relative to the raw rubber G (100 parts by mass), the hydrolysis reaction of the silica-blended rubber material R can be sufficiently accelerated. Can not. On the other hand, if the amount exceeds 5.0 parts by weight, the rubber composition is porous (foamed and made porous) in the process after kneading the silica-containing rubber material R (rubber extrusion process, etc.), and the quality is increased. Increases the risk of decline.

尚、水を添加した未加硫のゴム組成物を押出等するとゴム組成物にポーラスが発生し易くなることが知られている。そのため、従来、ゴム材料の混練時に意図的に水を添加することは避けられていた。しかし、シリカ配合ゴム材料Rの混練においては、適切な量の水Wの添加であれば、シリカ配合ゴム材料Rにおける加水分解反応が促進されることが判明した。さらには、加硫して得たゴム組成物の特定のゴム物性が向上することが判明したので、むしろ有益であるとの知見に基づいて本願発明が創作されている。   It is known that when an unvulcanized rubber composition to which water has been added is extruded, the rubber composition is likely to be porous. Therefore, conventionally, intentional addition of water during kneading of the rubber material has been avoided. However, in the kneading of the silica-blended rubber material R, it has been found that the hydrolysis reaction in the silica-blended rubber material R is promoted if an appropriate amount of water W is added. Furthermore, since it has been found that the specific rubber properties of the rubber composition obtained by vulcanization are improved, the present invention has been created based on the knowledge that it is rather beneficial.

混練しているシリカ配合ゴム材料Rの温度Tを130℃以上160℃以下に維持することで、混練中のシリカ配合ゴム材料Rにおける化学反応をより促進させ易くなる。加えて、本願発明を適用して製造されたゴム組成物をタイヤのトレッドゴムとして使用すると、タイヤの転がり抵抗やウエットグリップ性能を一段と向上させ易くなる。   By maintaining the temperature T of the silica-blended rubber material R being kneaded at 130 ° C. or higher and 160 ° C. or lower, the chemical reaction in the silica-blended rubber material R being kneaded can be more easily promoted. In addition, when a rubber composition produced by applying the present invention is used as a tread rubber of a tire, the rolling resistance and wet grip performance of the tire can be further improved.

シリカ配合ゴム材料Rに水Wを添加する方法は特に限定されないが、混練室4aに噴霧または滴下すると、シリカ配合ゴム材料Rに均一に混合し易くなる。これに伴い、加硫して得たゴム組成物の品質のばらつきを抑えるには有利になる。或いは、図4に例示するように、ラム8をラム室4bの下端から上昇させた状態にして、水Wをシリカ配合ゴム材料Rの上方位置から供給して添加すると、シリカ配合ゴム材料Rに均一に混合し易くなる。   The method of adding water W to the silica-blended rubber material R is not particularly limited, but when sprayed or dropped into the kneading chamber 4a, it becomes easy to uniformly mix with the silica-blended rubber material R. In connection with this, it becomes advantageous to suppress the dispersion | variation in the quality of the rubber composition obtained by vulcanization | cure. Alternatively, as illustrated in FIG. 4, when the ram 8 is raised from the lower end of the ram chamber 4 b and water W is supplied from the upper position of the silica compound rubber material R and added, the silica compound rubber material R is added. It becomes easy to mix uniformly.

添加する水Wの温度は、混練しているシリカ配合材料Rと同等またはそれ以上の温度にすることもできるが、相対的に低温(例えば10℃以上50℃以下)にすることもできる。10℃以上50℃以下の相対的に低温の水Wを添加すると、シリカ配合ゴム材料Rの温度Tが若干低下するので、所定の温度範囲に維持するためにロータ3の回転数が大きくなる(回転速度が早くなる)。これに起因して混練時間の短縮を図ることが可能になる。また、シリカ配合材料Rは所定の温度範囲に維持されて混練されるので、加硫して得たゴム組成物については一定のゴム品質を確保できる。   The temperature of the water W to be added can be equal to or higher than that of the silica compounding material R being kneaded, but can also be relatively low (for example, 10 ° C. or more and 50 ° C. or less). When relatively low-temperature water W of 10 ° C. or more and 50 ° C. or less is added, the temperature T of the silica-blended rubber material R is slightly lowered, so that the number of rotations of the rotor 3 is increased in order to maintain it within a predetermined temperature range ( Rotational speed is faster). This makes it possible to shorten the kneading time. Moreover, since the silica compounding material R is kneaded while being maintained in a predetermined temperature range, a certain rubber quality can be ensured for the rubber composition obtained by vulcanization.

この実施形態のように、水供給機構13の貯水部13aをラム8に設けると、貯水部13aに貯める水Wを、ラム8のウエイト調整部材として利用することができる。これに伴って、ラム8を構成している金属部材の総重量を低減することも可能になる。   If the water storage part 13a of the water supply mechanism 13 is provided in the ram 8 as in this embodiment, the water W stored in the water storage part 13a can be used as a weight adjusting member of the ram 8. Accordingly, the total weight of the metal members constituting the ram 8 can be reduced.

乗用車用タイヤのトレッドゴムを混練する際に、シリカ配合ゴム材料に対して水の添加の有無だけを異ならせて2種類の未加硫のゴム組成物を製造した。そして、水を添加したゴム組成物(実施例)と、水を添加しなかったゴム組成物(従来例)とのそれぞれを、金型(15cm×15cm×0.2cm)の中に配置して160℃で20分間プレス加硫して、加硫ゴムシートを作製した。尚、実施例における水の添加量は、原料ゴム100質量部に対して2重量部であった。また、実施例および従来例では、シリカ配合ゴム材料を130℃以上160℃以下の温度範囲で混練した。   When kneading the tread rubber of a passenger car tire, two types of unvulcanized rubber compositions were produced by changing only whether or not water was added to the silica-containing rubber material. Then, each of the rubber composition to which water was added (Example) and the rubber composition to which water was not added (conventional example) was placed in a mold (15 cm × 15 cm × 0.2 cm). Press vulcanized at 160 ° C. for 20 minutes to produce a vulcanized rubber sheet. In addition, the addition amount of water in the Examples was 2 parts by weight with respect to 100 parts by mass of the raw rubber. In the examples and conventional examples, the silica-containing rubber material was kneaded in a temperature range of 130 ° C. or higher and 160 ° C. or lower.

[タイヤの転がり抵抗]
それぞれの加硫ゴムシートについて、粘弾性スペクトロメーター(東洋精機製作所社製)を用いて、初期歪み10%、振幅±2%、周波数20Hzの条件下で、温度60℃の損失正接tanδを測定した。tanδ(60℃)はタイヤの転がり抵抗の評価指標として用いられている。従来例の加硫ゴムシートと実施例の加硫ゴムシートとの測定結果を比較した結果、実施例は従来例に比して転がり抵抗が約3%低下することが確認できた。
[Tire rolling resistance]
For each vulcanized rubber sheet, a loss tangent tan δ at a temperature of 60 ° C. was measured using a viscoelastic spectrometer (manufactured by Toyo Seiki Seisakusho) under the conditions of an initial strain of 10%, an amplitude of ± 2%, and a frequency of 20 Hz. . Tan δ (60 ° C.) is used as an evaluation index of tire rolling resistance. As a result of comparing the measurement results of the vulcanized rubber sheet of the conventional example and the vulcanized rubber sheet of the example, it was confirmed that the rolling resistance was reduced by about 3% as compared with the conventional example.

[ウエットグリップ性能]
それぞれの加硫ゴムシートについて、粘弾性スペクトロメーター(東洋精機製作所社製)を用いて、初期歪み10%、振幅±2%、周波数20Hzの条件下で、温度0℃の損失正接tanδを測定した。tanδ(0℃)はタイヤのウエットグリップ性能の評価指標として用いられている。従来例の加硫ゴムシートと実施例の加硫ゴムシートとの測定結果を比較した結果、実施例は従来例に比してウエットグリップ性能が約3.5%向上することが確認できた。
[Wet grip performance]
For each vulcanized rubber sheet, a loss tangent tan δ at a temperature of 0 ° C. was measured using a viscoelastic spectrometer (manufactured by Toyo Seiki Seisakusho Co., Ltd.) under conditions of an initial strain of 10%, an amplitude of ± 2%, and a frequency of 20 Hz. . Tan δ (0 ° C.) is used as an evaluation index of the wet grip performance of the tire. As a result of comparing the measurement results of the vulcanized rubber sheet of the conventional example and the vulcanized rubber sheet of the example, it was confirmed that the wet grip performance of the example was improved by about 3.5% compared to the conventional example.

1 混練装置
2 密閉型混練機
3 ロータ
3a 回転軸
3b 翼
4a 混練室
4b ラム室
5 油投入部
6 ゴム投入部
7 ホッパ
8 ラム
9 配合剤投入部
10 排出扉
11 温度センサ
12 制御部
12a 電力計
13 水供給機構
13a 貯水部
13b ノズル
13c 流路
G 原料ゴム
N 非加硫系配合剤
R シリカ配合ゴム材料
W 水
DESCRIPTION OF SYMBOLS 1 Kneading apparatus 2 Sealed kneading machine 3 Rotor 3a Rotating shaft 3b Blade 4a Kneading chamber 4b Ram chamber 5 Oil charging unit 6 Rubber charging unit 7 Hopper 8 Ram 9 Compounding agent charging unit 10 Discharge door 11 Temperature sensor 12 Control unit 12a Power meter 13 Water supply mechanism 13a Water reservoir 13b Nozzle 13c Channel G Raw material rubber N Non-vulcanized compounding agent R Silica compounding rubber material W Water

Claims (10)

原料ゴムとシリカおよびシランカップリング剤を含む非加硫系配合剤とからなるシリカ配合ゴム材料を密閉型混練機により混練するゴム材料の混練方法において、
所定量の水を添加した状態の前記シリカ配合ゴム材料を、予め設定された所定の温度範囲に維持して前記密閉型混練機により混練することを特徴とするゴム材料の混練方法。
In the kneading method of the rubber material in which the silica compounded rubber material composed of the raw rubber and the non-vulcanized compounding agent containing silica and the silane coupling agent is kneaded by the closed kneader,
A method for kneading a rubber material, characterized in that the silica-containing rubber material in a state where a predetermined amount of water is added is kneaded by the closed kneader while maintaining a predetermined temperature range set in advance.
前記所定の温度範囲が130℃以上160℃以下である請求項1に記載のゴム材料の混練方法。   The method for kneading a rubber material according to claim 1, wherein the predetermined temperature range is 130 ° C or higher and 160 ° C or lower. 前記水を前記密閉型混練機の混練室に噴霧または滴下することにより、前記シリカ配合ゴム材料に添加する請求項1または2に記載のゴム材料の混練方法。   The method for kneading a rubber material according to claim 1 or 2, wherein the water is added to the silica-blended rubber material by spraying or dripping the water into a kneading chamber of the closed kneader. 前記密閉型混練機を構成するラムを、前記密閉型混練機のラム室の下端から上昇させた状態で、前記水を前記シリカ配合ゴム材料に添加する請求項1〜3のいずれかに記載のゴム材料の混練方法。   4. The water according to claim 1, wherein the water is added to the silica-containing rubber material in a state where the ram constituting the closed kneader is raised from the lower end of the ram chamber of the closed kneader. Rubber material kneading method. 前記水の温度を、混練中の前記シリカ配合ゴム材料よりも低温である10℃以上50℃以下にする請求項1〜4のいずれかに記載のゴム材料の混練方法。   The method for kneading a rubber material according to any one of claims 1 to 4, wherein the temperature of the water is 10 ° C to 50 ° C, which is lower than that of the silica-containing rubber material being kneaded. 原料ゴムとシリカおよびシランカップリング剤を含む非加硫系配合剤とからなるシリカ配合ゴム材料を混練する密閉型混練機を備えたゴム材料の混練装置において、
前記密閉型混練機により混練中の前記シリカ配合ゴム材料の温度を検知する温度センサと、前記密閉型混練機のロータの回転を制御する制御部と、前記密閉型混練機の混練室に水を供給する水供給機構とを備え、
前記温度センサの検知データに基づいて前記ロータの回転数を制御することにより、前記水供給機構により所定量の水を添加した状態の前記シリカ配合ゴム材料を、予め設定された所定の温度範囲に維持して混練する構成にしたことを特徴とするシリカ配合ゴム材料の混練装置。
In a rubber material kneading apparatus equipped with a closed kneader for kneading a silica-blended rubber material comprising a raw rubber and a non-vulcanized compounding agent containing silica and a silane coupling agent,
A temperature sensor that detects the temperature of the silica-containing rubber material being kneaded by the closed kneader, a control unit that controls the rotation of the rotor of the closed kneader, and water in the kneading chamber of the closed kneader. A water supply mechanism for supplying,
By controlling the number of rotations of the rotor based on the detection data of the temperature sensor, the silica-containing rubber material in a state where a predetermined amount of water is added by the water supply mechanism is kept within a predetermined temperature range set in advance. A kneading apparatus for a silica-containing rubber material, characterized in that the kneading is performed while maintaining.
前記所定の温度範囲が130℃以上160℃以下に設定される請求項6に記載のゴム材料の混練装置。   The rubber material kneading apparatus according to claim 6, wherein the predetermined temperature range is set to 130 ° C. or higher and 160 ° C. or lower. 前記水供給機構が、前記水を貯留する貯水部と、前記水を噴霧または滴下するノズルとを有する請求項6または7に記載のゴム材料の混練装置。   The rubber material kneading apparatus according to claim 6 or 7, wherein the water supply mechanism includes a water storage section that stores the water and a nozzle that sprays or drops the water. 前記密閉型混練機を構成するラムを、前記密閉型混練機の混練室の上方に連接されているラム室の下端よりも上方に配置した状態で、前記水供給機構による前記水の供給を行う構成にした請求項6〜8のいずれかに記載のゴム材料の混練装置。   The water is supplied by the water supply mechanism in a state where the ram constituting the closed kneader is arranged above the lower end of the ram chamber connected to the upper side of the kneading chamber of the closed kneader. The rubber material kneading apparatus according to any one of claims 6 to 8, which is configured. 前記水の温度が、混練中の前記シリカ配合ゴム材料よりも低温である10℃以上50℃以下に設定される請求項6〜9のいずれかに記載のゴム材料の混練装置。   The rubber material kneading apparatus according to claim 6, wherein the temperature of the water is set to 10 ° C. or more and 50 ° C. or less, which is lower than the silica-containing rubber material being kneaded.
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JP2019093586A (en) * 2017-11-20 2019-06-20 横浜ゴム株式会社 Method and apparatus for kneading rubber material
JP2019093585A (en) * 2017-11-20 2019-06-20 横浜ゴム株式会社 Method and apparatus for kneading rubber material
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