JP2018062611A - Method for manufacturing tire member - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a method for manufacturing a tire member capable of obtaining a vulcanized rubber having low heat generation property and a high tensile product (fracture resistance).SOLUTION: There is provided a method for manufacturing a tire member which comprises: (i) a step of mixing carbon black (hereinafter, CB), a dispersion solvent and a rubber latex solution to produce a CB-containing rubber latex solution; (ii) a step of coagulating the CB-containing rubber latex solution to produce a CB-containing rubber coagulated product; (iii) a step of dehydrating the CB-containing rubber coagulated product while adding a compound represented by the formula (I) to the CB-containing rubber coagulated product and dispersing the compound represented by the formula (I) in the CB-containing rubber coagulated product containing moisture to produce a rubber wet master batch (hereinafter, MB); and (iv) a step of adding calcium carbonate surface-treated with an organic material to MB, followed by dry-mixing.SELECTED DRAWING: None

Description

  The present invention relates to a method for manufacturing a tire member obtained using at least carbon black, a dispersion solvent, and a rubber latex solution as raw materials.

  Conventionally, in the rubber industry, it is known to use a rubber wet masterbatch in order to improve processability and carbon black dispersibility when producing a rubber composition containing carbon black. This is because carbon black and a dispersion solvent are mixed in a certain ratio in advance, and a carbon black-containing slurry solution in which carbon black is dispersed in a dispersion solvent by mechanical force and a rubber latex solution are mixed in a liquid phase. Thereafter, the solidified product obtained by adding a coagulant such as an acid is recovered and dried.

  When using a rubber wet masterbatch, compared to using a rubber dry masterbatch obtained by mixing carbon black and rubber in a solid phase, the dispersibility of carbon black is superior, and rubber properties such as processability and reinforcement A rubber composition having excellent resistance is obtained. By using such a rubber composition as a raw material, for example, a rubber product such as a pneumatic tire with reduced rolling resistance and excellent fatigue resistance can be manufactured.

  As a rubber composition using a rubber dry masterbatch, those containing a specific compound having a nitrogen functional group and a carbon-carbon double bond at the terminal are known (Patent Documents 1 and 2).

  In Patent Document 2, the above-mentioned specific compound can be bonded to carbon black by reacting a functional group at the terminal with a functional group such as a carboxyl group present on the surface of carbon black. It is described that the portion of the heavy bond can be bonded to the polymer by a reaction with a polymer radical or a reaction accompanying sulfur crosslinking. Therefore, it is described that the dispersibility of carbon black of the rubber composition can be improved, and the exothermic property of the rubber product (vulcanized rubber) obtained from the rubber composition can be suppressed.

  Patent Documents 1 and 2 describe the use of heavy calcium carbonate or calcium carbonate as a filler other than carbon black in a rubber composition.

JP 2013-209605 A JP 2014-95020 A

  On the other hand, in the market, rubber products (vulcanized rubber) made from a rubber composition have a lower heat buildup and a higher tensile product (destructive property), especially in the tread rubber of heavy duty tires. Although the thing is calculated | required, the vulcanized rubber obtained from the rubber composition like said patent document 1, 2 was not satisfying the said characteristic.

  The present invention has been made in view of the above circumstances, and provides a method for manufacturing a tire member from which a vulcanized rubber having low heat buildup and high tensile product (destructive property) can be obtained.

（式（Ｉ）中、Ｒ^１およびＲ^２は、水素原子、ならびに炭素数１〜２０のアルキル基、アルケニル基またはアルキニル基を示し、Ｒ^１およびＲ^２は同一であっても異なっていてもよい。Ｍ^＋はナトリウムイオン、カリウムイオンまたはリチウムイオンを示す。）で表される化合物を添加し、水分を含んだ前記カーボンブラック含有ゴム凝固物中で前記一般式（Ｉ）で表される化合物を分散させつつ、前記カーボンブラック含有ゴム凝固物を脱水して、ゴムウエットマスターバッチを製造する工程（ｉｉｉ）と、得られたゴムウエットマスターバッチに、有機材料によって表面処理された炭酸カルシウムを加えて、乾式混合する工程（ｉｖ）を含むことを特徴とするタイヤ部材の製造方法、に関する。 The present invention relates to a tire member manufacturing method obtained using at least carbon black, a dispersion solvent, and a rubber latex solution as raw materials, and the carbon black, the dispersion solvent, and the rubber latex solution are mixed to form a carbon. Step (i) for producing a black-containing rubber latex solution, step (ii) for producing a carbon black-containing rubber coagulum by coagulating the obtained carbon black-containing rubber latex solution, and the obtained carbon black-containing rubber General formula (I):

(In Formula (I), R ¹ and R ² represent a hydrogen atom and an alkyl group, alkenyl group or alkynyl group having 1 to 20 carbon atoms, and R ¹ and R ² may be the same or different. M ⁺ represents a sodium ion, a potassium ion or a lithium ion.) And a compound represented by the general formula (I) in the carbon black-containing rubber coagulated material containing water. Step (iii) of producing a rubber wet masterbatch by dehydrating the carbon black-containing rubber coagulated product while dispersing the carbon black, and adding calcium carbonate surface-treated with an organic material to the obtained rubber wet masterbatch In addition, the present invention relates to a method for manufacturing a tire member, comprising a dry mixing step (iv).

  In the production method, in the step (iii), the carbon black-containing rubber coagulated product is dehydrated while dispersing the compound represented by the general formula (I) in the water-containing carbon black-containing rubber coagulated product. Generally, rubber used for tires is hydrophobic in a dry state. On the other hand, since the compound represented by the general formula (I) exhibits hydrophilicity, even if the dry rubber and the compound represented by the general formula (I) are dry-mixed, the compound represented by the general formula (I) is represented. The dispersibility of the resulting compound is difficult to improve. However, in the production method, in the step (iii) corresponding to the dehydration step, the compound represented by the general formula (I) is dispersed in the carbon black-containing rubber coagulated material containing water. It is estimated that the dispersibility of the compound represented by the general formula (I) is remarkably increased. As a result, the compound represented by formula (I) can be dispersed at a high level in the carbon black-containing rubber coagulated product.

  Once the compound represented by the general formula (I) is dispersed in the carbon black-containing rubber coagulated product, the dispersibility of the compound represented by the general formula (I) even if the carbon black-containing rubber coagulated product is dehydrated. Therefore, the dispersibility of the compound represented by the general formula (I) is greatly improved even in a rubber wet masterbatch or a tire member finally obtained by drying. Therefore, the vulcanized rubber obtained from the tire member by the manufacturing method has improved the dispersibility of the carbon black contained in the vulcanized rubber, so than the vulcanized rubber obtained from the rubber dry masterbatch, It has low exothermic property and high tensile product (destructive property).

  In the manufacturing method, in step (iv), calcium carbonate surface-treated with an organic material is added to the rubber wet masterbatch obtained in step (iii) and dry-mixed. By using calcium carbonate surface-treated with an organic material, aggregates of calcium carbonate at the time of dry mixing can be reduced, so that it is difficult to deteriorate the exothermic property of the vulcanized rubber obtained from the tire member.

  Furthermore, the organic material treated on the surface of the above calcium carbonate comes to intervene around the nitrogen functional group (especially amino group) at the terminal of the compound represented by the general formula (I) during dry mixing. Thus, the calcium carbonate contained in the tire member can form a physical bond with the rubber component. As a result, the vulcanized rubber obtained from the tire member has a reinforcing property due to the physical bonding described above, and the tensile product (destructive property) of the vulcanized rubber can be further improved.

  The tire member manufacturing method according to the present invention uses at least carbon black, a dispersion solvent, and a rubber latex solution as raw materials.

  As the carbon black, for example, conductive carbon black such as acetylene black and ketjen black can be used in addition to carbon black used in normal rubber industry, such as SAF, ISAF, HAF, FEF, and GPF. . The carbon black may be a granulated carbon black or a non-granulated carbon black granulated in the normal rubber industry in consideration of its handleability. Carbon black may be used alone or in combination of two or more.

The carbon black preferably has a nitrogen adsorption specific surface area of 15 to 150 m ² / g from the viewpoint of excellent exothermic property and viscosity retention performance of the vulcanized rubber. In particular, carbon black having a nitrogen adsorption specific surface area of 80 to 150 m ² / g is preferable as a raw material for use in a tread rubber of a heavy load tire. Further, the content of the carbon black is preferably 30 to 80 parts by weight, and more preferably 40 to 70 parts by weight with respect to 100 parts by weight of the rubber component contained in the tire member.

  As the dispersion solvent, it is particularly preferable to use water, but for example, water containing an organic solvent may be used. Dispersing solvents may be used alone or in combination of two or more.

  As the rubber latex solution, a natural rubber latex solution and a synthetic rubber latex solution can be used.

  The natural rubber latex solution is a natural product produced by the metabolic action of plants, and is preferably a natural rubber / water system in which the dispersion solvent is water. The number average molecular weight of the natural rubber in the natural rubber latex is preferably 2 million or more, and more preferably 2.5 million or more. The natural rubber latex solution can be used without distinction such as concentrated latex and fresh latex called field latex. Examples of the synthetic rubber latex solution include those produced by emulsion polymerization of styrene-butadiene rubber, butadiene rubber, nitrile rubber, and chloroprene rubber. A rubber latex solution may be used independently and may use 2 or more types together.

（式（Ｉ）中、Ｒ^１およびＲ^２は、水素原子、ならびに炭素数１〜２０のアルキル基、アルケニル基またはアルキニル基を示し、Ｒ^１およびＲ^２は同一であっても異なっていてもよい。Ｍ^＋はナトリウムイオン、カリウムイオンまたはリチウムイオンを示す。）で表される化合物を添加する点が特徴である。 In the present invention, when dehydrating a carbon black-containing rubber coagulated material obtained using at least carbon black, a dispersion solvent, and a rubber latex solution as raw materials, the carbon black-containing rubber coagulated material is represented by the general formula (I):

(In Formula (I), R ¹ and R ² represent a hydrogen atom and an alkyl group, alkenyl group or alkynyl group having 1 to 20 carbon atoms, and R ¹ and R ² may be the same or different. M ⁺ is a sodium ion, a potassium ion or a lithium ion).

を使用することが好ましい。 In particular, from the viewpoint of increasing the affinity for carbon black, the compound according to the general formula (I ′) in which R ¹ and R ² in the general formula (I) are hydrogen atoms and M ⁺ is a sodium ion:

Is preferably used.

  Below, the manufacturing method of the tire member concerning the present invention is explained concretely. Such a manufacturing method is a method for manufacturing a tire member obtained using at least carbon black, a dispersion solvent, and a rubber latex solution as a raw material, and the carbon black, the dispersion solvent, and the rubber latex solution are mixed, Step (i) for producing a carbon black-containing rubber latex solution, step (ii) for producing a carbon black-containing rubber coagulated product by coagulating the obtained carbon black-containing rubber latex solution, and the obtained carbon black-containing solution The compound represented by the general formula (I) is added to the rubber coagulated product, and the compound represented by the general formula (I) is dispersed in the carbon black-containing rubber coagulated product containing moisture. Dehydrating the carbon black-containing rubber coagulum to produce a rubber wet masterbatch (iii); The obtained rubber wet master batch, in addition to surface-treated calcium carbonate with an organic material, characterized in that it comprises a step of dry mixing (iv).

<Process (i)>
In step (i) of the present invention, carbon black, a dispersion solvent, and a rubber latex solution are mixed to produce a carbon black-containing rubber latex solution. In particular, in the present invention, when the step (i) disperses the carbon black in the dispersion solvent, by adding at least a part of the rubber latex solution, the carbon latex particles adhered thereto are added. A step of producing a slurry solution containing black (i- (a)), a slurry solution containing the carbon black to which rubber latex particles are adhered, and the remaining rubber latex solution are mixed together to produce rubber latex particles. It is preferable to include the step (i- (b)) of producing the carbon black-containing rubber latex solution to which is adhered. The step (i- (a)) and the step (i- (b)) will be described below.

<Process (i- (a))>
In the step (i- (a)) of the present invention, when carbon black is dispersed in a dispersion solvent, a slurry containing carbon black to which rubber latex particles are adhered by adding at least a part of a rubber latex solution. A solution is produced. The rubber latex solution may be mixed with a dispersion solvent in advance, and then carbon black may be added and dispersed. Alternatively, carbon black may be added to the dispersion solvent, and then carbon black may be dispersed in the dispersion solvent while adding the rubber latex solution at a predetermined addition rate, or carbon black may be added to the dispersion solvent. Then, carbon black may be dispersed in a dispersion solvent while adding a certain amount of rubber latex solution in several times. By dispersing carbon black in a dispersion solvent in the state where the rubber latex solution is present, a slurry solution containing carbon black with rubber latex particles attached thereto can be produced. The amount of rubber latex solution added in step (i- (a)) is the total amount of rubber latex solution used (total amount added in step (i- (a)) and step (i- (b))). 0.075 to 12% by weight is exemplified.

  In the step (i- (a)), the amount of rubber solid content of the rubber latex solution to be added is preferably 0.25 to 15% by weight ratio to carbon black, and 0.5 to 6%. Preferably there is. Moreover, it is preferable that the density | concentration of the rubber solid content in the rubber latex solution to add is 0.2 to 5 weight%, and it is more preferable that it is 0.25 to 1.5 weight%. In these cases, it is possible to produce a rubber wet masterbatch in which the degree of dispersion of carbon black is increased while reliably attaching rubber latex particles to carbon black.

  In the step (i- (a)), as a method of mixing carbon black and a dispersion solvent in the presence of a rubber latex solution, for example, a high shear mixer, a high shear mixer, a homomixer, a ball mill, a bead mill, a high pressure homogenizer, The method of disperse | distributing carbon black using common dispersers, such as a sonic homogenizer and a colloid mill, is mentioned.

  The “high shear mixer” is a mixer including a rotor and a stator, and the rotor rotates with a precise clearance between a rotor capable of high-speed rotation and a fixed stator. Means a mixer with a high shearing action. In order to produce such a high shearing action, it is preferable that the clearance between the rotor and the stator is 0.8 mm or less and the circumferential speed of the rotor is 5 m / s or more. A commercial item can be used for such a high shear mixer, for example, “High Shear Mixer” manufactured by SILVERSON.

  In the present invention, when a slurry solution containing carbon black to which rubber latex particles are adhered is produced by mixing carbon black and a dispersion solvent in the presence of a rubber latex solution, a surfactant is used to improve the dispersibility of the carbon black. May be added. As the surfactant, a surfactant known in the rubber industry can be used. For example, a nonionic surfactant, an anionic surfactant, a cationic surfactant, a zwitterionic surfactant, etc. Can be mentioned. Further, alcohol such as ethanol may be used instead of or in addition to the surfactant. However, when a surfactant is used, there is a concern that the rubber physical properties of the final vulcanized rubber will deteriorate. Therefore, the amount of the surfactant to be added is 100 parts by weight of the rubber solid content of the rubber latex solution. The amount is preferably 2 parts by weight or less, more preferably 1 part by weight or less, and substantially no surfactant is preferably used.

<Process (i- (b))>
In the step (i- (b)) of the present invention, the slurry solution and the remaining rubber latex solution are mixed to produce a carbon black-containing rubber latex solution with rubber latex particles attached thereto. The method of mixing the slurry solution and the remaining rubber latex solution in a liquid phase is not particularly limited. For example, the slurry solution and the remaining rubber latex solution may be mixed with, for example, a high shear mixer, a high shear mixer, a homomixer, or a ball mill. And a mixing method using a general disperser such as a bead mill, a high-pressure homogenizer, an ultrasonic homogenizer, and a colloid mill. If necessary, the entire mixing system such as a disperser may be heated during mixing.

  The remaining rubber latex solution preferably has a higher rubber solids concentration than the rubber latex solution added in step (i- (a)) in consideration of dehydration time and labor in the next step (iii). Specifically, the concentration of the rubber solid content is preferably 10 to 60% by weight, and more preferably 20 to 30% by weight.

<(2) Step (ii)>
In the step (ii) of the present invention, the carbon black-containing rubber latex solution is coagulated to produce a carbon black-containing rubber coagulated product. Examples of the coagulation method include a method in which a coagulant is contained in a carbon black-containing rubber latex solution to which rubber latex particles are attached. In this case, as the coagulant, an acid such as formic acid or sulfuric acid usually used for coagulation of the rubber latex solution, or a salt such as sodium chloride can be used. In addition, after the step (ii) and before the step (iii), for the purpose of appropriately reducing the amount of water contained in the carbon black-containing rubber coagulum, if necessary, for example, a centrifugation step or a heating step. A solid-liquid separation step may be provided.

<(3) Step (iii)>
In the step (iii) of the present invention, a rubber wet masterbatch is produced by dehydrating the carbon black-containing rubber coagulum. In the step (iii), for example, a single screw extruder can be used, and dehydration can be performed while applying a shearing force to the carbon black-containing rubber coagulum while heating to 100 to 250 ° C. In the present invention, particularly in the step (iii), the compound represented by the general formula (I) is added to the carbon black-containing rubber coagulum, and the general formula (I) The carbon black-containing rubber coagulum is dehydrated while dispersing the compound represented by Although the moisture content of the carbon black-containing rubber coagulated product before the start of the step (iii) is not particularly limited, the above-mentioned solid-liquid separation step and the like are provided as necessary, and Wa / Wb described later is in an appropriate range. It is preferable to adjust the moisture content so that

  As described above, the dispersibility is significantly improved by dispersing the compound represented by the general formula (I) in the carbon black-containing rubber coagulated product in the presence of moisture. In particular, the water content (Wa) of the carbon black-containing rubber coagulated product when the compound represented by the general formula (I) is added is preferably, for example, 1 part by weight or more with respect to 100 parts by weight of the rubber component during the rubber coagulation. 10 parts by weight or more is more preferable, 800 parts by weight or less is preferable, and 600 parts by weight or less is more preferable. Further, the content (Wb) of the compound represented by the general formula (I) when the compound represented by the general formula (I) is added is, for example, 0 with respect to 100 parts by weight of the rubber component during the rubber coagulation. 1 part by weight or more is preferable, 0.5 part by weight or more is more preferable, 10 parts by weight or less is preferable, and 5 parts by weight or less is more preferable. Further, the ratio of Wa to Wb (Wa / Wb) is preferably 1 ≦ Wa / Wb ≦ 8100. When Wa / Wb is less than 1, the dispersibility of the compound represented by formula (I) in the carbon black-containing rubber coagulated product may not be sufficiently improved. In order to further improve the dispersibility of the compound represented by the general formula (I), Wa / Wb is preferably 1 or more. On the other hand, when Wa / Wb exceeds 8100, water to be dehydrated is remarkably increased, so that the productivity of the rubber wet masterbatch tends to deteriorate. When considering the productivity of the rubber wet masterbatch, Wa / Wb is preferably 7400 or less.

  After the step (iii), if necessary, a separate drying step may be provided to further reduce the moisture content of the rubber wet masterbatch. As a method for drying the rubber wet masterbatch, for example, various drying apparatuses such as a single screw extruder, an oven, a vacuum dryer, and an air dryer can be used.

<(4) Step (iv)>
In the step (iv) of the present invention, a tire member is manufactured by adding calcium carbonate surface-treated with an organic material to a rubber wet masterbatch and dry-mixing.

  The organic material of calcium carbonate surface-treated with the organic material is not limited as long as it can suppress agglomeration of calcium carbonate during dry mixing. For example, fatty acid, fatty acid ester, rosin Acid, quaternary ammonium salt, and lignic acid. Of these, fatty acids, fatty acid esters, and rosin acids are preferred from the viewpoint of further improving the tensile product (destructive property) without deteriorating the exothermic property of the vulcanized rubber. Examples of calcium carbonate include synthetic calcium carbonate and heavy calcium carbonate. The calcium carbonate surface-treated with an organic material may be used alone or in combination of two or more.

  The content of calcium carbonate surface-treated with the organic material is preferably 0.5 to 15 parts by weight with respect to 100 parts by weight of the rubber component contained in the tire member. The content of calcium carbonate surface-treated with an organic material is 0.8 weight with respect to 100 parts by weight of the rubber component contained in the tire member from the viewpoint of improving the tensile product (destructive property) of the vulcanized rubber. Part or more, preferably 1 part by weight or more. The content of the calcium carbonate surface-treated with the organic material is 12 parts by weight or less with respect to 100 parts by weight of the rubber component contained in the tire member from the viewpoint of imparting low heat build-up to the vulcanized rubber. Is preferable, and it is more preferable that it is 10 parts weight or less.

  In the step (iv), various compounding agents can be further used. Examples of usable compounding agents include sulfur vulcanizing agents, vulcanization accelerators, anti-aging agents, silica, silane coupling agents, zinc oxide, methylene acceptors and methylene donors, stearic acid, and vulcanization accelerators. Additives, vulcanization retarders, organic peroxides, softeners such as waxes and oils, and compounding agents usually used in the rubber industry such as processing aids.

  The sulfur as the sulfur-based vulcanizing agent may be normal sulfur for rubber, and for example, powdered sulfur, precipitated sulfur, insoluble sulfur, highly dispersible sulfur and the like can be used. A sulfur type vulcanizing agent may be used independently and may use 2 or more types together.

  The sulfur content is preferably 0.3 to 6.5 parts by weight with respect to 100 parts by weight of the rubber component contained in the tire member. If the sulfur content is less than 0.3 parts by weight, the crosslinking density of the vulcanized rubber will be insufficient and the rubber strength will be reduced. If it exceeds 6.5 parts by weight, both heat resistance and durability will be improved. Getting worse. In order to secure the rubber strength of the vulcanized rubber and improve the heat resistance and durability, the sulfur content is 1.0 to 5.5 with respect to 100 parts by weight of the rubber component contained in the tire member. More preferred are parts by weight.

  Examples of the vulcanization accelerator include sulfenamide vulcanization accelerators, thiuram vulcanization accelerators, thiazole vulcanization accelerators, thiourea vulcanization accelerators, and guanidine vulcanization accelerators that are usually used for rubber vulcanization. Examples thereof include vulcanization accelerators such as vulcanization accelerators and dithiocarbamate vulcanization accelerators. A vulcanization accelerator may be used independently and may use two or more sorts together.

  The content of the vulcanization accelerator is preferably 1 to 5 parts by weight with respect to 100 parts by weight of the rubber component contained in the tire member.

  As the anti-aging agent, aromatic amine type anti-aging agent, amine-ketone type anti-aging agent, monophenol type anti-aging agent, bisphenol type anti-aging agent, polyphenol type anti-aging agent, dithiocarbamine, which are usually used for rubber Antiaging agents such as acid salt-based antioxidants and thiourea-based antioxidants may be mentioned. Antiaging agents may be used alone or in combination of two or more.

  The content of the anti-aging agent is preferably 1 to 5 parts by weight with respect to 100 parts by weight of the rubber component contained in the tire member.

The silica is not particularly limited as long as it can be used as a reinforcing filler, but wet silica (hydrous silicic acid) is preferable. Colloidal properties of the silica is also not particularly limited, preferably has a nitrogen adsorption specific surface area (BET) is 150 to 250 ² / g by BET method, and more preferred is a 180~230m ² / g . The BET of silica is measured according to the BET method described in ISO 5794. Silica may be used alone or in combination of two or more.

  The content of the silica is more preferably 1 to 50 parts by weight and further preferably 10 to 30 parts by weight with respect to 100 parts by weight of the rubber component contained in the tire member.

  The silane coupling agent is not particularly limited as long as it is usually used for rubber. For example, bis (3-triethoxysilylpropyl) tetrasulfide, bis (3-triethoxysilylpropyl) disulfide, bis (2-tri Sulfide silanes such as ethoxysilylethyl) tetrasulfide, bis (4-triethoxysilylbutyl) disulfide, bis (3-trimethoxysilylpropyl) tetrasulfide, bis (2-trimethoxysilylethyl) disulfide; 3-mercaptopropyltri Mercaptosilanes such as methoxysilane, 3-mercaptopropyltriethoxysilane, 3-mercaptopropylmethyldimethoxysilane, 3-mercaptopropyldimethylmethoxysilane, mercaptoethyltriethoxysilane; Tanoiruchio -1-propyltriethoxysilane, and protection mercaptosilane such as 3-propionylthio trimethoxy silane. A silane coupling agent may be used independently and may use 2 or more types together.

  The content of the silane coupling agent is more preferably 2 to 20% by weight of the silica weight, and further preferably 4 to 15% by weight.

  In the step (iv), rubber can be used to adjust the content of the rubber component contained in the tire member. Examples of the rubber include diene rubbers known to those skilled in the art, such as natural rubber (NR), polyisoprene rubber (IR), polystyrene butadiene rubber (SBR), polybutadiene rubber (BR), chloroprene rubber (CR), nitrile rubber ( NBR) can be used.

  In the step (iv), the method of blending each raw material (each component) is not particularly limited. For example, components other than vulcanized components such as a sulfur vulcanizing agent and a vulcanization accelerator are added in any order. And kneading method, simultaneously adding and kneading, and adding all components simultaneously and kneading.

  Examples of the dry mixing include a kneading method using a kneader used in a normal rubber industry such as a Banbury mixer, a kneader, and a roll. The number of times of kneading may be one or more times. The kneading time varies depending on the size of the kneader to be used, but is usually about 2 to 5 minutes. Moreover, when the tire member does not contain the vulcanization component, the discharge temperature of the kneader is preferably 120 to 170 ° C, and more preferably 120 to 150 ° C. When the tire member contains the vulcanization component, the discharge temperature of the kneader is preferably 80 to 110 ° C, more preferably 80 to 100 ° C.

  In the present invention, instead of the steps (i) to (iii), a mixture of carbon black and rubber is added to the compound represented by the general formula (I) and water (1 to 100 parts by weight of the rubber component). (About 10 parts by weight) is added to obtain a rubber masterbatch in which the compound represented by the general formula (I) is dispersed, and then in the step (iv), the rubber masterbatch obtained above is used as the rubber wetbatch. A tire member can be manufactured by using it instead of a masterbatch. In the said manufacturing method, since the dispersibility of the compound represented by general formula (I) can be improved in the rubber masterbatch manufactured in the manufacturing intermediate stage of a tire member, the tire member obtained from the rubber masterbatch Becomes excellent in dispersibility of the compound represented by the general formula (I).

  The same carbon black as that used in the method for producing the rubber wet masterbatch can be used. The rubber is a diene rubber known to those skilled in the art, for example, natural rubber (NR), polyisoprene rubber (IR), polystyrene butadiene rubber (SBR), polybutadiene rubber (BR), chloroprene rubber (CR), nitrile rubber ( NBR) can be used.

  Since the vulcanized rubber obtained from the tire member of the present invention has low heat build-up and high tensile product (destructive property), it is suitable as a tread rubber for heavy load tires.

  EXAMPLES The present invention will be described below with reference to examples, but the present invention is not limited to these examples.

(Raw materials used)
a) Carbon black:
Carbon black “N234” (nitrogen adsorption specific surface area 126 m ² / g), “Seast 7HM” (manufactured by Tokai Carbon Co., Ltd.)
b) Dispersion solvent: water c) Rubber latex solution:
Natural rubber latex solution “NR Field Latex” (Golden Hope) (DRC = 31.2%)
d) Compound represented by general formula (I):
(2Z) -4-[(4-Aminophenyl) amino] -4-oxo-2-butenoic acid sodium (manufactured by Sumitomo Chemical Co., Ltd.)
e) Coagulant: Formic acid (primary 85%, 10% solution diluted to pH 1.2), (produced by Nacalai Tesque)
f) Silica: “Nip seal AQ” (BET = 205 m ² / g) (Nippon Silica Kogyo Co., Ltd.)
g) Silane coupling agent: bis (3-triethoxysilylpropyl) disulfide, “Si75” (manufactured by Degussa)
h) Zinc Hana: “Zinc Hana 3” (Mitsui Metals)
i) Stearic acid: “Lunac S-20” (manufactured by Kao Corporation)
j) Calcium carbonate “Brilliant-1500” (manufactured by Shiroishi Calcium Industry Co., Ltd.)
k) Calcium carbonate surface-treated with an organic material:
Fatty acid-treated calcium carbonate: “Shiroka Hana CC” (manufactured by Shiroishi Calcium Industry Co., Ltd.)
Rosin acid-treated calcium carbonate: “Hakuen Hana DD” (manufactured by Shiroishi Calcium Industry Co., Ltd.)
l) Sulfur: “5% oil-filled fine powder sulfur” (manufactured by Tsurumi Chemical Co., Ltd.)
m) Vulcanization accelerator:
(A): N-cyclohexyl-2-benzothiazolesulfenamide, “Sunseller CM”: (manufactured by Sanshin Chemical Industry Co., Ltd.)
(B) 1,3-diphenylguanidine, “Noxeller D” (Ouchi Shinsei Chemical Co., Ltd.)
n) Natural rubber (NR): “RSS # 3”
o) Polybutadiene: “JSR BR01” (manufactured by JSR)

<Example 1>
Carbon black was added to the natural rubber diluted latex aqueous solution adjusted to a concentration of 0.52% by weight so as to achieve the blending amount shown in Table 1 (the concentration of carbon black with respect to water was 5% by weight), and this was made by PRIMIX. Carbon black was dispersed using Robomix (conditions of the Robomix: 9000 rpm, 30 minutes) to produce a carbon black-containing slurry solution to which the natural rubber latex particles described in Table 1 were attached (Step (i )-(A)). Next, the natural rubber latex solution (28% by weight) is added to the carbon black-containing slurry solution to which the natural rubber latex particles produced in the step (i- (a)) are attached so as to have the blending amounts shown in Table 1. And then mixed using a SANYO household mixer SM-L56 type (mixer conditions 11300 rpm, 30 minutes) to produce a carbon black-containing rubber latex solution with natural rubber latex particles attached thereto (step (i) )).

  Formic acid as a coagulant was added to the carbon black-containing natural rubber latex solution to which the natural rubber latex particles produced in step (i) were adhered until the entire solution reached pH 4, thereby producing a carbon black-containing natural rubber coagulated product. (Step (ii)). The obtained carbon black-containing natural rubber coagulated product is subjected to a solid-liquid separation process as necessary, and the carbon black-containing natural rubber coagulated product adjusted to have the moisture content shown in Table 1 and the general formula The compound represented by (I) is introduced into a screw press V-01 type manufactured by Suehiro EPM, and the carbon black-containing natural rubber coagulate is dispersed while the compound represented by the general formula (I) is dispersed. The natural rubber coagulum was dehydrated to produce a rubber wet masterbatch (step (iii)). Table 1 shows the values of Wa / Wb in the step (iii).

  The rubber wet masterbatch obtained above and the raw materials listed in Table 1 (components excluding sulfur and vulcanization accelerator) are dry-mixed using a Banbury mixer (kneading time: 3 minutes, discharge temperature: 150). The tire member was manufactured. Next, sulfur, a vulcanization accelerator (A) and a vulcanization accelerator (B) shown in Table 1 were added to the obtained tire member, and dry mixing (kneading time: 1 minute, discharged using a Banbury mixer) (Temperature: 90 ° C.) to produce an unvulcanized tire member (step (iv)). In addition, the compounding ratio of Table 1 is shown by weight part (phr) when the whole quantity of the rubber component contained in a rubber latex composition is 100 weight part.

<Examples 2 to 7>
An unvulcanized tire member was produced in the same manner as in Example 1 except that each raw material and its blending amount were changed as shown in Table 1.

<Comparative Examples 1-3>
Each raw material shown in Table 2 (components excluding sulfur and vulcanization accelerator) was dry-mixed (kneading time: 3 minutes, discharge temperature: 150 ° C.) using a Banbury mixer to produce a tire member. Next, sulfur, a vulcanization accelerator (A) and a vulcanization accelerator (B) shown in Table 2 were added to the obtained tire member, and dry mixing (kneading time: 1 minute, discharged using a Banbury mixer) (Temperature: 90 ° C.) to produce an unvulcanized tire member.

<Comparative Example 4>
In the step (iii) of Example 1, the rubber wet masterbatch was produced without adding the compound represented by the general formula (I). 1 was used to produce an unvulcanized tire member.

<Comparative Example 5>
Before the step (iii) of Example 1, the carbon black-containing natural rubber coagulated product was dried until the moisture content was 0%, and a carbon black-containing natural rubber coagulated product in a dry state containing no moisture was used. Using the raw materials shown in Table 2, an unvulcanized tire member was produced in the same manner as in Example 1.

  Vulcanized rubber was produced by vulcanizing the unvulcanized tire members obtained in the above examples and comparative examples under the conditions of 150 ° C. and 30 minutes. The following evaluation was performed about the obtained vulcanized rubber. The evaluation results are shown in Tables 1 and 2.

<Evaluation of heat generation>
The exothermic evaluation was carried out using a viscoelasticity tester manufactured by Toyo Seiki Co., Ltd., measuring the loss factor tanδ under the conditions of static strain 10%, dynamic strain ± 2%, frequency 50Hz, and temperature 60 ° C. In Examples 1 to 5 and Comparative Examples 4 and 5, the value of Comparative Example 1 was set to 100 and displayed as an index. In Example 6, the value of Comparative Example 2 was displayed as an index with 100, and in Example 7, the value of Comparative Example 3 was displayed as 100 with an index. Moreover, it shows that it is hard to generate | occur | produce heat and it is excellent in low exothermic property, so that an index | exponent is small.

<Evaluation of tensile product>
The tensile product was evaluated by performing a tensile test in accordance with JIS K6251 on a sample obtained by punching the obtained vulcanized rubber with a dumbbell-shaped No. 3 shape to obtain a tensile product (TB (tensile strength) × EB (elongation at break)) was determined, and Examples 1 to 5 and Comparative Examples 4 and 5 were expressed as indexes with the value of Comparative Example 1 being 100. In Example 6, the value of Comparative Example 2 was displayed as an index with 100, and in Example 7, the value of Comparative Example 3 was displayed as 100 with an index. The larger the value, the better the reinforcement and fracture characteristics.

Claims (4)

A method for producing a tire member obtained using at least carbon black, a dispersion solvent, and a rubber latex solution as a raw material,
Mixing the carbon black, the dispersion solvent, and the rubber latex solution to produce a carbon black-containing rubber latex solution (i);
Coagulating the resulting carbon black-containing rubber latex solution to produce a carbon black-containing rubber coagulum (ii);
The resulting carbon black-containing rubber coagulated product has the general formula (I):

(In Formula (I), R ¹ and R ² represent a hydrogen atom and an alkyl group, alkenyl group or alkynyl group having 1 to 20 carbon atoms, and R ¹ and R ² may be the same or different. M ⁺ represents a sodium ion, a potassium ion or a lithium ion.) And a compound represented by the general formula (I) in the carbon black-containing rubber coagulated material containing water. A step (iii) of producing a rubber wet masterbatch by dehydrating the carbon black-containing rubber coagulum while dispersing
A method for producing a tire member comprising a step (iv) of adding calcium carbonate surface-treated with an organic material to the obtained rubber wet masterbatch and dry-mixing.   In the step (iii), the water content in the carbon black-containing rubber coagulated product when the compound represented by the general formula (I) is added is Wa, and the content of the compound represented by the general formula (I) is The tire member manufacturing method according to claim 1, wherein when Wb is satisfied, 1 ≦ Wa / Wb ≦ 8100.   The method for manufacturing a tire member according to claim 1 or 2, wherein the organic material is at least one selected from the group consisting of fatty acids, fatty acid esters, and rosin acid.   The calcium carbonate surface-treated with the organic material is 0.5 to 15 parts by weight with respect to 100 parts by weight of the rubber component contained in the tire member. Tire member manufacturing method.