Patent Application
20240352200
The present invention relates to a method for producing a rubber composition, a fumed silica for rubber composition, and a rubber composition.
A heavy-duty tire used for a truck, a bus, or the like has a larger load weight and a longer travel distance than those of a passenger car tire and is thus required to have high wear resistance performance. In addition, in recent years, in the heavy-duty tire used for a truck, a bus, or the like, as seen in the labeling systems of Japan and Europe and the Smart Way regulations of North America, it is important to reduce an environmental burden, and in particular, it is required to reduce rolling resistance and improve fuel efficiency.
As an index of rolling resistance of a rubber composition such as a tire, tan δ at 60° C. (hereinafter, referred to as tan δ (60° C.)), which is evaluated as dynamic viscoelastic properties, is generally used. It indicates that, in the rubber composition, the smaller the tan δ (60° C.), the lower the rolling resistance. In addition, it indicates that the smaller the tan δ (60° C.), the lower an exothermic property. Therefore, by reducing the tan δ (60° C.), overheating of the tire during driving can be prevented, and durability can also be improved. In the rubber composition, tan δ at 0° C. (hereinafter, referred to as tan δ (0° C.)) is used as an index for evaluating wet friction (wet grip performance), but is not so important in the heavy-duty tire.
Examples of a method for reducing the tan δ (60° C.) of the rubber composition include reducing a blending amount of carbon black to be blended in the rubber composition and increasing a particle diameter of the carbon black. However, in this method, mechanical properties such as tensile strength at break, tensile elongation at break, and rubber hardness of the rubber composition decrease, and when such a rubber composition is used for the heavy-duty tire, there arises a problem that wear resistance and uneven wear resistance decrease.
Patent Literatures 1 to 3 propose blending a fumed silica in a rubber composition as the method of reducing the rolling resistance tan δ (60° C.) of the rubber composition. However, the fumed silica is easily scattered as a powder having a very small bulk density. Therefore, in a Banbury mixer generally used industrially, it has been difficult to knead the fumed silica into the rubber composition even when the kneading is performed for a long period of time, and for example, it has been difficult to knead the fumed silica to a target amount because the fumed silica is scattered even when the fumed silica is blended into the rubber composition little by little several times. In addition, even when the fumed silica can be kneaded, the fumed silica is easily agglomerated in the rubber composition. Therefore, it has been industrially difficult to favorably disperse the fumed silica in the rubber composition.
Patent Literature 4 proposes that a silicon dioxide fine powder (fumed silica) blended in a silicone rubber is mechanically pulverized until a bulk specific gravity is 80 g/L to 300 g/L. However, since the mechanically pulverized silicon dioxide fine powder (fumed silica) in Patent Literature 4 has a specific surface area of 80 m2/g to 180 m2/g, when the silicon dioxide fine powder is blended into the rubber composition for the heavy-duty tire, the performance required for the rubber composition for the heavy-duty tire such as wear resistance performance cannot be exhibited. Therefore, in order to exhibit the performance required for the rubber composition for the heavy-duty tire, a method for industrially kneading the fumed silica into the rubber composition and a rubber composition blended with the fumed silica are required.
An object of the present invention is to easily produce a rubber composition containing a fumed silica by a mixer type kneading apparatus generally used industrially. In addition, an object of the present invention is to provide a rubber composition containing a fumed silica, which can be easily produced by a mixer type kneading apparatus generally used industrially, and the fumed silica contained therein.
A gist of the present invention is as follows.
(1) A method for producing a rubber composition including:
(2) The method for producing a rubber composition according to (1), in which the diene rubber is a natural rubber or an isoprene rubber.
(3) The method for producing a rubber composition according to (1) or (2), in which a vibration mill or a ball mill is used in the compression process.
(4) The method for producing a rubber composition according to any one of (1) to (3), in which the fumed silica before the compression process is subjected to a heat treatment.
(5) The method for producing a rubber composition according to any one of (1) to (4), in which the step of kneading the compressed fumed silica and the diene rubber is a step of kneading the compressed fumed silica, the diene rubber, and a silane coupling agent.
(6) A fumed silica for rubber composition, which is obtained by a surface treatment with a mercapto-thiocarboxylate oligomer, in which a tap density is 200 g/L or more and a BET specific surface area is 200 m2/g or more.
(7) A rubber composition containing: a compressed fumed silica having a tap density of 200 g/L or more and a BET specific surface area of 200 m2/g or more: a natural rubber; and a mercapto-thiocarboxylate oligomer.
According to the present invention, a rubber composition containing a fumed silica can be easily produced by a mixer type kneading apparatus generally used industrially. In addition, according to the present invention, it is possible to provide a rubber composition containing a fumed silica, which can be easily produced by a mixer type kneading apparatus generally used industrially, and the fumed silica contained therein.
First, a method for producing a rubber composition according to the present embodiment will be described in detail.
The method for producing a rubber composition according to the present embodiment includes:
In the present embodiment, the method for producing a rubber composition includes the step of applying the compression process to the fumed silica to obtain the compressed fumed silica. The fumed silica is silicon dioxide in a form of fine particles produced by high temperature hydrolysis of silicon tetrachloride in an oxyhydrogen flame, and may be referred to as a pyrogenic silica. The fine particles of the fumed silica are aggregated and fused into a bead form, and form a bulky agglomerate.
In the present embodiment, the fumed silica having a tap density of 200 g/L or more and a BET specific surface area of 200 m2/g or more is obtained by applying the compression process to the fumed silica (hereinafter, the fumed silica obtained by the compression process may be referred to as the compressed fumed silica).
In the present embodiment, the above fumed silica and compressed fumed silica are used for producing a rubber composition. Therefore, in the present description, the above fumed silica and compressed fumed silica are also referred to as a fumed silica for rubber composition.
In the present embodiment, the BET specific surface area of the fumed silica before the compression process is 200 m2/g or more. The BET specific surface area of the fumed silica before the compression process is preferably 220 m2/g or more, and more preferably 250 m2/g or more. By using the fumed silica having a BET specific surface area within the above range, the number of silanol groups serving as a reaction site with the diene rubber or a silane coupling agent to be described later can be sufficiently secured, and the compressed fumed silica to be described later can be favorably kneaded with the diene rubber. An upper limit of the BET specific surface area of the fumed silica is not particularly limited, and may be 500 m2/g.
In the present embodiment, the tap density of the fumed silica before the compression process may be less than 200 g/L. The tap density of the fumed silica before the compression process may be 100 g/L or less, or 45 g/L or less. The tap density of the fumed silica can be increased by the compression process to be described later. A lower limit of the tap density of the fumed silica before the compression process is not particularly limited, and may be 30 g/L.
In the present embodiment, the compression process refers to a process for increasing the tap density of the fumed silica. An apparatus used for the compression process is not particularly limited as long as it can increase the tap density by pulverizing the fumed silica, and a vibration mill or a ball mill is preferred, and a vibration mill is more preferred. The vibration mill is a vibration type fine pulverizer, and the ball mill is a pulverizer that makes a fine powder by grinding a material by rotating a hard ball in a cylindrical container. In the present embodiment, the fumed silica is subjected to the compression process using a compression process apparatus such as a vibration mill or a ball mill to obtain the compressed fumed silica.
In the compression process, mechanical energy such as impact, friction, or pulverization is applied to the fumed silica. As a result, it is considered that a surface of the fumed silica is activated, the silanol group on the surface of the fumed silica is cleaved, and the number of surface hydroxy groups increases. Then, the increase in the number of the surface hydroxy groups in the fumed silica occurs not only in the outermost surface layer but also in the inner layer. It is known that the surface-activated fumed silica does not lose activity unless the fumed silica is sufficiently heated. That is, the compressed fumed silica obtained by the compression process can stably maintain a state in which the surface is activated and the number of the surface hydroxy groups is increased for a long period of time. Therefore, in the present embodiment, by the compression process, a reaction between the compressed fumed silica and the diene rubber or the silane coupling agent is promoted, and the compressed fumed silica, which can be favorably kneaded with the diene rubber and has excellent storage stability, is obtained.
In the present embodiment, the tap density of the fumed silica after the compression process, that is, the compressed fumed silica is 200 g/L or more. The tap density of the compressed fumed silica is preferably 250 g/L or more, and more preferably 300 g/L or more. When the tap density of the compressed fumed silica is within the above range, scattering and floating of particles can be reduced, and the compressed fumed silica can be favorably kneaded with the diene rubber. In addition, the tap density of the compressed fumed silica is preferably 400 g/L or less. When the tap density is too large, the silica is likely to form a mass, and a step is required to loosen the mass before the rubber composition is produced or before the rubber composition is kneaded with the diene rubber. In this case, it is difficult to perform a continuous operation process, and the production cost may increase.
In the present embodiment, the tap density of the compressed fumed silica can be controlled by adjusting compression process conditions. For example, preferred compression process conditions when a ball mill or a vibration mill is used as the compression process apparatus are shown below.
The ball diameter of the ball mill is preferably 15 mm to 30 mm, and more preferably 20 mm to 25 mm. When the ball diameter is too small, there is a concern that the tap density of the compressed fumed silica cannot be increased due to insufficient impact force during pulverization. In addition, when the ball diameter is too small, it is necessary to extend the pulverization time in order to make the tap density of the compressed fumed silica 200 g/L or more, which may decrease productivity and increase production cost. When the ball diameter is too large, since a gap between balls is large and a collision frequency is low, the pulverization time may be extended, and the production cost may increase.
The rotation speed of the ball mill is preferably 50 rpm to 600 rpm, and more preferably 200 rpm to 400 rpm. When the rotation speed is too small, there is a concern that the tap density of the compressed fumed silica cannot be increased due to insufficient impact force during pulverization. In addition, when the rotation speed is too small, it is necessary to extend the pulverization time in order to make the tap density of the compressed fumed silica 200 g/L or more, which may decrease the productivity and increase the production cost. When the rotation speed is too large, the pulverization efficiency may decrease.
The ball filling rate of the ball mill is preferably 10% to 80%, and more preferably 20% to 50%. When the ball filling rate is too small, there is a concern that the tap density of the compressed fumed silica cannot be increased due to insufficient pulverization efficiency. In addition, when the ball filling rate is too small, it is necessary to extend the pulverization time in order to make the tap density of the compressed fumed silica 200 g/L or more, which may decrease the productivity and the production cost. When the ball filling rate is too large, the pulverization efficiency may decrease.
The ball diameter of the vibration mill is preferably 15 mm to 30 mm, and more preferably 20 mm to 25 mm. When the ball diameter is too small, there is a concern that the tap density of the compressed fumed silica cannot be increased due to insufficient impact force during pulverization. In addition, when the ball diameter is too small, it is necessary to extend the pulverization time in order to make the tap density of the compressed fumed silica 200 g/L or more, which may decrease the productivity and the production cost. When the ball diameter is too large, since a gap between the balls is large and a collision frequency is low, the pulverization time may be extended, and the production cost may increase.
The vibration frequency of the vibration mill is preferably 600 CPM to 2000 CPM, and more preferably 800 CPM to 1500 CPM. When the vibration frequency is too small, there is a concern that the tap density of the compressed fumed silica cannot be increased due to insufficient impact force during pulverization. In addition, when the vibration frequency is too small, it is necessary to extend the pulverization time in order to make the tap density of the compressed fumed silica 200 g/L or more, which may decrease the productivity and the production cost. When the vibration frequency is too large, there are concerns that the impact force is increased and stable pulverization cannot be possible.
The ball filling rate of the vibration mill is preferably 30% to 90%, and more preferably 50% to 80%. When the ball filling rate is too small, there is a concern that the tap density of the compressed fumed silica cannot be increased due to insufficient pulverization efficiency. In addition, when the ball filling rate is too small, it is necessary to extend the pulverization time in order to make the tap density of the compressed fumed silica 200 g/L or more, which may decrease the productivity and the production cost. When the ball filling rate is too large, the pulverization efficiency may decrease.
In the present embodiment, the BET specific surface area of the compressed fumed silica is preferably 200 m2/g or more, more preferably 220 m2/g or more, and still more preferably 250 m2/g or more. By setting the BET specific surface area of the compressed fumed silica within the above range, the number of the silanol groups serving as the reaction site with the diene rubber or the silane coupling agent in the compressed fumed silica can be sufficiently secured, and the compressed fumed silica can be favorably kneaded with the diene rubber. An upper limit of the BET specific surface area of the compressed fumed silica is not particularly limited, and may be 500 m2/g.
In the present embodiment, the method for producing a rubber composition includes the step of kneading the compressed fumed silica and the diene rubber. A blending amount of the compressed fumed silica is preferably 5 to 90 parts by weight, and more preferably 10 to 55 parts by weight, with respect to 100 parts by weight of the diene rubber. When the blending amount of the compressed fumed silica is too small, there is a concern that wear resistance performance of the obtained rubber composition cannot be sufficiently improved. When the blending amount of the compressed fumed silica is too large, there is a concern that the silica cannot be sufficiently dispersed in the diene rubber and cannot be favorably kneaded in the diene rubber.
In the present embodiment, examples of the diene rubber include a natural rubber, an isoprene rubber, a butadiene rubber, a styrene-butadiene rubber, an acrylonitrile-butadiene rubber, a butyl rubber, an ethylene-propylene-diene rubber, and a chloroprene rubber. Among them, a natural rubber and an isoprene rubber are preferred, and a natural rubber is most preferred. According to the production method of the present embodiment, even in the case of kneading with a natural rubber derived from agricultural products and having a viscosity or composition likely to vary depending on the season and production area, it is possible to perform the kneading by a mixer type kneading apparatus generally used industrially.
The kneading of the compressed fumed silica and the diene rubber may be performed using a mixer type kneading apparatus generally used industrially in production of the rubber composition, and for example, a Banbury mixer can be used. Operating conditions of the apparatus are not particularly limited as long as the compressed fumed silica and the diene rubber can be sufficiently kneaded.
In the present embodiment, by blending the silane coupling agent to be described later, dispersibility of the compressed fumed silica to the diene rubber can be improved, and a reinforcing property to the rubber can be improved. The silane coupling agent may be blended before the above compression process, or may be blended during or after the compression process. When the silane coupling agent is to be blended before the compression process, for example, the silane coupling agent can be sprayed to the fumed silica using a spray reactor. When the spraying is performed, heating may be performed as necessary. By blending the silane coupling agent to the fumed silica by spraying or the like, the fumed silica can be subjected to a surface treatment (hereinafter, the fumed silica subjected to a surface treatment may be referred to as a surface-treated fumed silica). When the silane coupling agent is to be blended during the compression process, for example, the silane coupling agent can be added into the apparatus when the compression process is applied to the fumed silica by a compression process apparatus such as a vibration mill. When the blending is performed after the compression process, the compressed fumed silica, the diene rubber, and the silane coupling agent may be kneaded in a mixer type kneading apparatus.
In the present embodiment, as described above, the surface treatment is performed by spraying a liquid silane coupling agent to the fumed silica before or after the compression process. The surface-treated fumed silica thus obtained is different from a so-called hydrophobized silica and has a hydrophilic property.
A blending amount of the silane coupling agent is preferably 3 to 30 parts by weight, and more preferably 5 to 20 parts by weight, with respect to 100 parts by weight of the compressed fumed silica or the fumed silica. When the blending amount of the silane coupling agent is too small, the dispersibility of the compressed fumed silica may be insufficient. When the blending amount of the silane coupling agent is too large, there are concerns that silane coupling agents are subjected to condensation and the wear resistance performance of the obtained rubber composition cannot be sufficiently improved.
Kinds of the silane coupling agent are not particularly limited as long as the silane coupling agent can be used in a diene rubber composition, and examples thereof include a sulfur-containing silane coupling agent such as bis-(3-triethoxysilylpropyl) tetrasulfide, bis(3-triethoxysilylpropyl) disulfide, 3-trimethoxysilylpropylbenzothiazole tetrasulfide, γ-mercaptopropyltriethoxysilane, 3-octanoylthiopropyltriethoxysilane, or a mercapto-thiocarboxylate oligomer.
In the present embodiment, when a natural rubber is used as the diene rubber, a mercapto-thiocarboxylate oligomer is preferably used as the silane coupling agent. That is, the fumed silica before or after the compression process is preferably surface-treated with the mercapto-thiocarboxylate oligomer.
The mercapto-thiocarboxylate oligomer is a thiocarboxylate oligomer having a mercapto group, and examples of a molecular structure of the mercapto-thiocarboxylate oligomer are shown below. In the following molecular structure, a sum (x+y) of a repeating number (x) of a linking unit A and a repeating number (y) of a linking unit B is preferably in a range of 3 to 300. Within this range, mercaptosilane of the linking unit B is covered with —C7H15 of the linking unit A, so that a scorch time can be prevented from being shortened and good reactivity with a silica or a rubber component can be secured. As the mercapto-thiocarboxylate oligomer, specifically, “NXT-Z45” manufactured by Momentive can be used.
Therefore, in the present embodiment, a preferred embodiment of the fumed silica for rubber composition is as follows.
A fumed silica for rubber composition, which is obtained by a surface treatment with a mercapto-thiocarboxylate oligomer, in which
The rubber composition according to the present embodiment is produced by the above method. Preferably, the rubber composition is produced by kneading the natural rubber and the fumed silica for rubber composition surface-treated with the mercapto-thiocarboxylate oligomer.
When the above silane coupling agent is to be blended after the compression process of the fumed silica, the rubber composition is produced by kneading the fumed silica for rubber composition, the diene rubber, and the silane coupling agent. As described above, the silane coupling agent is preferably the mercapto-thiocarboxylate oligomer.
Therefore, in the present embodiment, a preferred embodiment of the rubber composition is as follows.
A rubber composition, which is obtained by blending:
In the present embodiment, the rubber composition is preferably a rubber composition used for a tire, particularly a tire tread, and more preferably a rubber composition used for a heavy-duty tire or a tire tread thereof.
In the present embodiment, the method for producing a rubber composition may include a step of adding an oil. That is, the oil may be blended into the rubber composition. Examples of the oil include an aromatic oil, a paraffin oil, and a naphthenic oil. These may be used alone, or may be used in a combination of two or more kinds. A blending amount of the oil is preferably 2 to 10 parts by weight, and more preferably 4 to 8 parts by weight, with respect to 100 parts by weight of the diene rubber.
The above step of adding the oil may be performed before a step of kneading with the diene rubber, and for example, the above oil may be preliminarily mixed with the compressed fumed silica. Alternatively, the above oil may be added in the step of kneading the compressed fumed silica and the diene rubber.
In the present embodiment, the method for producing a rubber composition may include a step of adding a reinforcing filler. That is, the reinforcing filler may be blended into the rubber composition. Examples of the reinforcing filler include carbon black, clay, mica, talc, calcium carbonate, aluminum hydroxide, aluminum oxide, and titanium oxide. When the rubber composition used for a tire or a tire tread is to be produced, such a reinforcing filler may be blended. Further, when the reinforcing filler is to be blended, a filler coupling agent can also be blended in an appropriate amount. A blending amount of these reinforcing fillers may be a general blending amount in the related art as long as it does not violate the object of the present invention.
In the present embodiment, the method for producing a rubber composition may include a step of adding various additives such as a vulcanization or crosslinking agent, a vulcanization accelerator, sulfur, zinc oxide, stearic acid, an antioxidant, a plasticizer other than those described above, a processing aid, a liquid polymer, and a thermosetting resin. That is, the above various additives may be blended into the rubber composition. Such additives can be blended before or after kneading the diene rubber, and assist in vulcanization or crosslinking of the rubber composition. When the rubber composition used for a tire or a tire tread is to be produced, such additives may be blended. A blending amount of these additives may be a conventional general blending amount as long as it does not violate the object of the present invention.
In the present embodiment, the method for producing a rubber composition may include a step of adding a precipitated silica. That is, the precipitated silica can be blended into the rubber composition. The precipitated silica is a silica synthesized by a neutralization reaction between generally sodium silicate and a mineral acid (usually sulfuric acid). The precipitated silica is generally classified into a precipitated silica and a gel silica. In the present embodiment, the precipitated silica is preferably blended. A blending amount of the precipitated silica is preferably 0 to 100 parts by weight, and more preferably 0 to 60 parts by weight, with respect to 100 parts by weight of the diene rubber. The precipitated silica may be mixed with the compressed fumed silica before the step of kneading with the diene rubber, or may be added in the step of kneading the compressed fumed silica and the diene rubber. By blending the precipitated silica, a blending amount of an expensive fumed silica can be reduced. When the blending amount of the precipitated silica is too small, the obtained rubber composition may be expensive. When the blending amount of the precipitated silica is too large, there is a concern that the wear resistance performance of the rubber composition cannot be sufficiently improved. A ratio of the blending amount of the fumed silica to the blending amount of the precipitated silica is not particularly limited as long as it does not violate the object of the present invention.
Hereinafter, the present invention will be described with reference to Examples, but the present invention is not limited to the following Examples.
The fumed silica was subjected to a surface treatment. That is, 10.0 kg of a fumed silica (QS-30C manufactured by Tokuyama Corporation, nitrogen adsorption specific surface area: 300 m2/g) was stirred and mixed in a mixer having an internal volume of 300 L, and the atmosphere was replaced with a nitrogen atmosphere. At a reaction temperature of 25° C., 2 parts by weight of water was added to the fumed silica by using a single fluid nozzle. Thereafter, a silane coupling agent (mercapto-thiocarboxylate oligomer (NXT-Z45 manufactured by Momentive)) was added to the fumed silica by using the single fluid nozzle such that a blending amount thereof was 8 parts by weight with respect to 100 parts by weight of the fumed silica. The temperature was raised to 200° C. at a rising temperature of 100° C./hr, and nitrogen was supplied at a supply rate of 40 L/min to remove an unreacted material and a reaction by-product. The surface-treated fumed silica was obtained.
The obtained surface-treated fumed silica was subjected to a compression process. That is, 200 g of the surface-treated fumed silica was charged into a 7 L ball mill (ball diameter φ: 25 mm, ball filling: 30%, 300 rpm), and was pulverized at room temperature for 5 hours. A compressed fumed silica I was obtained.
Tap densities and specific surface areas of the fumed silica, the surface-treated fumed silica, and the compressed fumed silica after the compression process were evaluated according to the following methods. Results are shown in Table 1. The expression “after compression process” refers to a case where the fumed silica and the surface-treated fumed silica were subjected to the compression process, respectively, under the above conditions.
A 1 L resin-made graduated cylinder was placed on an electronic balance, tared, and filled with about 1 L of the fumed silica, and a weight M (g) was recorded. Thereafter, tapping was manually performed 30 times from a height of about 10 cm, then a volume V (ml) was measured, and a tap density p was calculated according to the following equation. The same calculation was performed on the surface-treated fumed silica. In addition, the same calculation was performed on the fumed silica and the surface-treated fumed silica after the compression process, respectively.
A specific surface area of the fumed silica was measured by a nitrogen adsorption BET one-point method using a BET specific surface area measuring apparatus SA-1000 manufactured by SIBATA Scientific Technology Ltd. The same measurement was performed on the surface-treated fumed silica. In addition, the same measurement was performed on the fumed silica and the surface-treated fumed silica after the compression process, respectively.
A surface-treated fumed silica was obtained in the same manner as in Example 1-1. The obtained surface-treated fumed silica was subjected to the compression process. That is, the surface-treated fumed silica was supplied to a 1 m3 continuous vibration mill (ball diameter Q: 25 mm, silica supply rate: 100 g/min, ball filling amount: 80%, vibration frequency: 1200 CPM, amplitude: 8 mm) and pulverized. A compressed fumed silica II was obtained. The tap density and the specific surface area were evaluated in the same manner as in Example 1-1.
A surface-treated fumed silica was obtained in the same manner as in Example 1-1 except that a silane coupling agent (mercapto-thiocarboxylate oligomer (NXT-Z45 manufactured by Momentive)) was added such that a blending amount thereof was 4 parts by weight with respect to 100 parts by weight of the fumed silica in the preparation of the surface-treated fumed silica. A compressed fumed silica III was obtained in the same manner as in Example 1-1. The tap density and the specific surface area were evaluated in the same manner as in Example 1-1.
The fumed silica was subjected to the compression process without a surface treatment. That is, the fumed silica (QS-30C manufactured by Tokuyama Corporation, nitrogen adsorption specific surface area: 300 m2/g) was supplied to a 1 m3 continuous vibration mill (ball diameter q: 25 mm, silica supply rate: 100 g/min, ball filling amount: 80%, vibration frequency: 1200 CPM, amplitude: 8 mm) and pulverized. A compressed fumed silica IV was obtained. The tap density and the specific surface area were evaluated in the same manner as in Example 1-1.
The fumed silica was subjected to the compression process without a surface treatment. That is, 200 g of the fumed silica (QS-30C manufactured by Tokuyama Corporation, nitrogen adsorption specific surface area: 300 m2/g) was charged into a 7 L ball mill (ball diameter q: 25 mm, ball filling: 30%, 300 rpm), and was pulverized at room temperature for 5 hours. A compressed fumed silica V was obtained. The tap density and the specific surface area were evaluated in the same manner as in Example 1-1.
The fumed silica was subjected to the compression process without a surface treatment. That is, a compressed fumed silica VI was obtained in the same manner as in Example 1-5 except that the fumed silica (QS-25 manufactured by Tokuyama Corporation, nitrogen adsorption specific surface area: 250 m2/g) was used. The tap density and the specific surface area were evaluated in the same manner as in Example 1-1.
The above compressed fumed silica I, a natural rubber, a butadiene rubber, a precipitated silica, a silane coupling agent (mercapto-thiocarboxylate oligomer (NXT-Z45 manufactured by Momentive)), and carbon black were charged into a 1.7 L closed Banbury mixer so as to have blending amounts shown in Table 3, and compounding agents (zinc oxide, stearic acid, an antioxidant, and an oil) were charged into the closed Banbury mixer so as to have blending amounts shown in Table 2. The above mixture was kneaded for 6 minutes and cooled to room temperature to obtain a master batch. The master batch was returned to the 1.7 L closed Banbury mixer, and the remaining compounding agents (1.5 parts by weight of sulfur and a vulcanization accelerator) were added and mixed to prepare a rubber composition.
Kinds of the above raw materials used in the preparation of the rubber composition are shown below.
Kinds of the compounding agents shown in Table 2 are shown below.
The obtained rubber composition was press-vulcanized at 150° C. for 10 minutes to prepare a test piece made of the rubber composition. The following physical properties were evaluated by using the obtained test piece. Results are shown in Table 3.
An FPS wear amount of the obtained test piece made of the rubber composition was measured using an FPS wear tester (AB-2012 manufactured by Ueshima Seisakusho Co., Ltd.) under conditions including a temperature of 20° C., a load of 40 N, a slip ratio of 10%, and a test time of 2 minutes. A volume loss was calculated based on the FPS wear amount, and was expressed as an index according to the following calculation equation with a loss amount in Standard Example 1 being 100. The larger the index, the better the wear resistance.
<Fuel efficiency: Tan δ (60° C.)>
The obtained test piece made of the rubber composition was measured in accordance with JIS K6394 using a dynamic viscoelastic tester (VR-7130 manufactured by Ueshima Seisakusho Co., Ltd.) under the following conditions. The tan δ (60° C.) was calculated based on a measured value at 60° C.
An index was calculated according to the following equation with a measured value in Standard Example 1 being 100. The larger the index, the better the rolling resistance.
The hardness of the obtained test piece made of the rubber composition was measured in accordance with Type A in JIS K6253.
A Mooney viscosity (ML1+4, 100° C.) of the obtained test piece made of the rubber composition at 100° C. was measured in accordance with JIS K6300-1 using a Mooney viscosity meter (VR-1132 manufactured by Ueshima Seisakusho Co., Ltd.).
A test piece was obtained by preparing a rubber composition in the same manner as in Example 2-1 except that blending amounts of the compressed fumed silica I and the precipitated silica were changed as shown in Table 3 in preparation of the rubber composition. Physical properties were evaluated in the same manner as in Example 2-1.
The above compressed fumed silica V, a silane coupling agent (mercapto-thiocarboxylate oligomer (NXT-Z45 manufactured by Momentive)), a natural rubber, a butadiene rubber, a precipitated silica, and carbon black were charged into a 1.7 L closed Banbury mixer so as to have the blending amounts shown in Table 3, and the compounding agents (zinc oxide, stearic acid, am antioxidant, and an oil) were charged into the closed Banbury mixer so as to have the blending amounts shown in Table 2. The above mixture was kneaded for 6 minutes and cooled to room temperature to obtain a master batch. The master batch was returned to the 1.7 L closed Banbury mixer, and the remaining compounding agents (1.5 parts by weight of sulfur and a vulcanization accelerator) were added and mixed to prepare a rubber composition. Kinds of the above raw materials and the compounding agents are the same as those in Example 2-1.
A test piece made of the rubber composition was obtained in the same manner as in Example 2-1. Physical properties were evaluated in the same manner as in Example 2-1.
A test piece was obtained by preparing a rubber composition in the same manner as in Example 2-3 except that blending amounts of the compressed fumed silica V and the precipitated silica were changed as shown in Table 3 in preparation of the rubber composition. Physical properties were evaluated in the same manner as in Example 2-1.
A test piece was obtained by preparing a rubber composition in the same manner as in Example 2-3 except that the precipitated silica was not blended and a blending amount of the compressed fumed silica V was changed as shown in Table 3 in preparation of the rubber composition. Physical properties were evaluated in the same manner as in Example 2-1.
A test piece was obtained by preparing a rubber composition in the same manner as in Example 2-4 except that the butadiene rubber was not blended and a filler coupling agent (SUMILINK 200 manufactured by Sumitomo Chemical Co., Ltd.) was blended in the preparation of the rubber composition. Physical properties were evaluated in the same manner as in Example 2-1 except that a loss amount in Standard Example 2 was set to 100 in the wear resistance and a measured value in Standard Example 2 was set to 100 in the fuel efficiency and the indexes were calculated.
A test piece was obtained by preparing a rubber composition in the same manner as in Example 2-4 except that a natural rubber (SVR made in Vietnam) was used and a blending amount of sulfur was set to 1.9 parts by weight in the preparation of the rubber composition. Physical properties were evaluated in the same manner as in Example 2-1 except that a loss amount in Standard Example 3 was set to 100 in the wear resistance and a measured value in Standard Example 3 was set to 100 in the fuel efficiency and the indexes were calculated.
A natural rubber, a butadiene rubber, carbon black, and compounding agents (zinc oxide, stearic acid, an antioxidant, and an oil) were charged into a 1.7 L closed Banbury mixer so as to have the blending amounts shown in Table 3, and the above mixture was kneaded for 6 minutes and cooled to room temperature to obtain a master batch. The master batch was returned to the 1.7 L closed Banbury mixer, and the remaining compounding agents (1.5 parts by weight of sulfur and a vulcanization accelerator) were added and mixed to prepare a silica-free rubber composition. Blending amounts of the compounding agents are shown in Table 2. Kinds of the above raw materials and the compounding agents are the same as those in Example 2-1.
A test piece made of the rubber composition was obtained in the same manner as in Example 2-1. Physical properties were evaluated in the same manner as in Example 2-1.
A test piece was obtained by preparing a rubber composition in the same manner as in Standard Example 1 except that the butadiene rubber was not blended in the preparation of the rubber composition. Physical properties were evaluated in the same manner as in Example 2-1.
A test piece was obtained by preparing a rubber composition in the same manner as in Standard Example 2 except that a natural rubber (SVR made in Vietnam) was used and a blending amount of sulfur was set to 2.3 parts by weight in the preparation of the rubber composition. Physical properties were evaluated in the same manner as in Example 2-1.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2020-182461 | Oct 2020 | JP | national |
| 2020-187020 | Nov 2020 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2021/038997 | 10/21/2021 | WO |
