WO2018074569A1

WO2018074569A1 - Masterbatch

Info

Publication number: WO2018074569A1
Application number: PCT/JP2017/037926
Authority: WO
Inventors: 真耶村上; 弘貴山口
Original assignee: 住友精化株式会社
Priority date: 2016-10-21
Filing date: 2017-10-20
Publication date: 2018-04-26
Also published as: JPWO2018074569A1; AR109851A1; TW201825574A

Abstract

The present invention enhances kneading workability and the mechanical characteristics of rubber products by using a masterbatch which includes a sulfide compound (A) and silica (B). The sulfide compound (A) is a compound represented by formula (I) [in formula (I), D represents an oxygen atom or a direct bond, and x represents 3 or 4]. The silica (B) satisfies the following conditions: the BET specific surface area is 0.1–50 m²/g; and the DBP absorption is 150–200 ml/100 g.

Description

Master Badge

The present invention relates to a master batch for a rubber composition, a rubber composition containing the master batch, and a method for producing the same.

In order to improve the performance of rubber products, it is known to use rubber compounding agents such as sulfur. In recent years, there has been a demand for industrial rubber that further improves various mechanical properties such as heat resistance and durability of rubber products. In order to improve these mechanical properties, a polymer rubber compounding agent, for example, a rubber compounding agent containing a cyclic polysulfide is disclosed (Patent Document 1).

JP 2014-210870 A

However, some rubber compounding agents are not solid but high viscosity oily compounds. In particular, since the sulfide rubber compounding agent is an oily compound, if it is kneaded with a rubber component by a roll at the time of rubber production, if it is added in an oily state, a slip phenomenon occurs and workability deteriorates. Furthermore, it is difficult to mix uniformly.

In particular, the sulfide rubber compounding agent has a strong odor, and when kneaded with a rubber component using an open roll generally used at the time of rubber production, the odor leaks, which is disadvantageous in industrial production. There was a case.

As a result of earnestly examining the combination of the sulfide rubber compounding agent and other raw materials, the present inventor is able to solve the above problems by using a masterbatch containing a specific sulfide compound and a specific silica. I found it.
That is, the present invention is a masterbatch containing a sulfide compound (A) and silica (B),
The sulfide compound (A) has the formula (I):

Wherein (I), D represents an oxygen atom or a direct bond, x is shows the 3 or 4. ]
A compound represented by
The silica (B) has the following conditions:
A BET specific surface area of 0.1 to 50 m ² / g, and
DBP oil absorption is 150-200ml / 100g
A masterbatch that satisfies the requirements and a method for manufacturing the same are provided.

The present invention also provides a rubber composition containing the masterbatch and a rubber component, and a method for producing the same.

If the master batch in the present invention is used, the rubber compounding agent can be efficiently and uniformly mixed in the rubber composition. Moreover, the rubber composition to which the master batch of the present invention is added can impart excellent mechanical properties to the resulting rubber product.

<Master batch>
The master batch in the present invention contains at least a sulfide compound and silica. In particular, the master batch of the present invention contains both the sulfide compound (A) and silica (B).

In the production process of the rubber composition, when the master batch of the present invention is used, a slip phenomenon hardly occurs during kneading with a roll. Moreover, the masterbatch of this invention is excellent in the dispersibility in a rubber composition. Further, when the masterbatch of the present invention is used in the production process of the rubber composition, excellent mechanical properties (for example, heat resistance, durability, mechanical properties, vibration resistance, moldability, etc.) are imparted to the rubber product. be able to.

By using the master batch of the present invention, it is possible to obtain the above-described effect superior to the case where the sulfide compound (A) and the silica (B) are added separately.

[Sulphide compounds]
The sulfide compound in the present invention has the formula (I):

[In Formula (I), D represents an oxygen atom or a direct bond, and x represents 3 or 4. ]
It is a sulfide compound (A) shown by these.

In the formula (I), D is preferably an oxygen atom from the viewpoint of improving the mechanical properties of the resulting rubber product.

In the formula (I), x is preferably 3 from the viewpoint of improving the mechanical properties of the resulting rubber product.

In the formula (I), D is an oxygen atom and x is preferably 3 from the viewpoint of improving the mechanical properties of the resulting rubber product.

The sulfide compound (A) may be oily, semi-solid, or liquid. The viscosity of the sulfide compound (A) is preferably in the range of 0.1 mPa · s to 1000 mPa · s.

The sulfide compound (A) functions as a vulcanizing agent (crosslinking agent) when blended with a rubber component. When blended, the performance as a vulcanizing agent is improved by combining with the following silica (B).

[silica]
Silica (B) in the present invention has the following conditions:
A BET specific surface area of 0.1 to 50 m ² / g, and
DBP oil absorption is 150-200ml / 100g
Meet.

From the viewpoint of dispersibility in the rubber composition, mechanical properties of the resulting rubber product, etc., the BET specific surface area of silica (B) is 0.1 to 50 m ² / g, and the mechanical properties superior to the resulting rubber product From the viewpoint of imparting characteristics, 10 to 50 m ² / g is preferable, 20 to 50 m ² / g is more preferable, and 30 to 50 m ² / g is more preferable.

The BET specific surface area of silica (B) in the present invention means a nitrogen adsorption amount specific surface area, and is measured in accordance with, for example, JIS Z 8830: 2013.

From the viewpoints of properties, states, dispersibility in the rubber composition, and mechanical properties of the resulting rubber product, the DBP (dibutyl phthalate) oil absorption in silica (B) is 150 to 200 ml / 100 g. From the viewpoint of imparting superior mechanical properties to the resulting rubber product, it is preferably 160 to 200 ml / 100 g, more preferably 170 to 200 ml / 100 g, still more preferably 175 to 200 ml / 100 g, and 175 to 195 ml / 100 g. Is even more preferable.

The DBP oil absorption of silica (B) in the present invention is measured in accordance with JIS K6217-4: 2008.

The silica (B) in the present invention satisfies the above conditions. Specifically, for example, precipitation method silica, gel method silica, dry silica, colloidal silica, amorphous silica, crystalline silica, dry method silica, wet method silica Synthetic silica, natural silica and the like can be used.

The pH of the aqueous dispersion of silica (B) in the present invention at 25 ° C. is preferably 6.0 to 7.0, and more preferably 6.2 to 6.8. When pH is larger than 6.0, the vulcanization time at the time of rubber product manufacture can be shortened. Moreover, when pH is smaller than 7.0, stability of the sulfide compound in a masterbatch improves more.

The pH of the silica (B) aqueous dispersion is a value obtained by measuring an aqueous dispersion at 25 ° C. prepared by adding 4 g of silica to 100 mL of water and stirring for 5 minutes.

[Other ingredients in masterbatch]
Other components to be included in the masterbatch include resin components such as acrylic polymers, vulcanizing agents (crosslinking agents) other than the above, vulcanization accelerators, vulcanization aids, reinforcing agents, fillers, anti-aging agents, and improved heat resistance. Additives such as an agent, a plasticizer, a viscosity modifier, a molecular weight modifier, and a stabilizer can be used as long as the effects of the present invention are not affected.

[Ingredient composition in masterbatch]
The mass ratio of the sulfide compound (A) and silica (B) in the master batch of the present invention is appropriately selected depending on the types of the sulfide compound (A) and silica (B) used. The mass ratio ((A) / (B)) between the sulfide compound (A) and silica (B) may be 20/80 to 80/20, and preferably 30/70 to 70/30. Here, when the mass ratio of the sulfide compound (A) is larger than 20, workability is further improved. When the mass ratio of the sulfide compound (A) is smaller than 80, the handling property of the master batch can be improved such as reducing odor.

In the master batch of the present invention, the sulfide compound (A) is preferably 20% by mass or more. Moreover, it is preferable that a silica (B) is 20 mass% or more in a masterbatch. In the master batch, the total amount of the sulfide compound (A) and silica (B) is preferably 40% by mass or more, more preferably 55% by mass or more, and further preferably 75% by mass or more.

[Manufacturing method of master batch]

The masterbatch production method in the present invention is not particularly limited as long as the components of the masterbatch can be mixed, but the sulfide compound (A), silica (B) and an organic solvent are mixed and the organic solvent is removed. It is preferable to manufacture by doing.

Hereinafter, the manufacturing method of the master batch will be described. As the organic solvent, an organic solvent inert to the sulfide compound (A) and silica (B) is used as the organic solvent. For example, hydrocarbon solvents such as hexane, pentane, benzene, toluene, xylene, etc. Examples include organic solvents, ether organic solvents such as diethyl ether, tetrahydrofuran, and dioxane, halogenated hydrocarbon organic solvents such as dichloromethane, chloroform, and monochlorobenzene, and polar organic solvents such as methanol, ethanol, ethyl acetate, acetone, and acetonitrile. . From the viewpoint of efficiency when removing the solvent, a solvent having a boiling point of 200 ° C. or lower is preferable, and a solvent having a boiling point of 150 ° C. or lower is more preferable. From the viewpoints of workability and solubility of the sulfide compound, it is preferable to use a halogenated hydrocarbon organic solvent.

In addition to the sulfide compound (A) and silica (B), other components are added to the organic solvent as necessary, and mixed. Mixing can be performed using well-known mixers, such as a homogenizer, a propeller-type stirring apparatus, a rotary-type stirring apparatus, for example.

A master batch can be obtained by removing the organic solvent from the mixed solution thus obtained. For example, the solvent may be removed from the mixed solution by a general method such as reduced pressure drying (reduced pressure distillation), natural drying, heat drying, spray drying, freeze drying and the like. Preferably, drying is performed under reduced pressure, and a master batch in which the components are uniformly dispersed can be obtained. The drying temperature may be 0 ° C. to 200 ° C., and preferably 40 ° C. to 100 ° C. When the drying temperature is lower than 200 ° C., the sulfide compound becomes stable, and when it is higher than 0 ° C., the drying becomes efficient.

The master batch in the present invention may be, for example, a powder, a pellet, a paste, or the like, but is preferably a powder or a pellet from the viewpoint of handleability.

<Rubber composition>
The rubber composition in the present invention contains at least a master batch containing a sulfide compound (A) and silica (B), and a rubber component.

[Rubber component]
As the rubber component, natural rubber (NR) and / or synthetic rubber (SR) are preferably used. The synthetic rubber is preferably a diene synthetic rubber. Examples of the diene-based synthetic rubber include polyisoprene synthetic rubber (IR), polybutadiene rubber (BR), styrene-butadiene copolymer rubber (SBR), acrylonitrile-butadiene copolymer rubber (NBR), chloroprene rubber (CR), Examples thereof include butyl rubber (IIR). These rubber components may be used alone or in combination of two or more.

[Other additives in rubber composition]
The rubber composition of the present invention can contain other additives in addition to the masterbatch containing the sulfide compound (A) and silica (B), and the rubber component.

Other additives known in the art can be used, for example, vulcanizing agents, vulcanization accelerators, anti-aging agents, plasticizers, viscosity modifiers, stabilizers, processing aids, vulcanization acceleration aids. Agents, fillers, colorants and the like.

[Ingredient composition in rubber composition]

In the rubber composition, the master batch may be 0.5 to 60 parts by mass, preferably 0.5 to 40 parts by mass, and 0.5 to 30 parts by mass with respect to 100 parts by mass of the rubber component. More preferred is 0.5 to 20 parts by mass.

In the rubber composition, the sulfide compound (A) in the master batch may be 0.1 to 30 parts by weight, for example 0.1 to 20 parts by weight, based on 100 parts by weight of the rubber component. 1 to 10 parts by mass is preferred.

In the rubber composition, the silica (B) in the master batch may be 0.1 to 30 parts by weight, preferably 0.1 to 20 parts by weight, based on 100 parts by weight of the rubber component. 1 to 10 parts by mass is more preferable.

In the rubber composition, the other additives may be 0.1 to 160 parts by mass in total with respect to 100 parts by mass of the rubber component, and preferably 1 to 120 parts by mass.

[Method for producing rubber composition]
The rubber composition in the present invention can be produced by mixing the masterbatch, natural rubber and / or synthetic rubber, and, if necessary, other additives by a known method. The rubber composition is preferably produced by mixing in the range of 20 to 100 ° C., more preferably in the range of 20 to 80 ° C. By mixing the components in such a temperature range for 5 to 60 minutes, for example, 10 to 30 minutes, a rubber composition can be prepared without proceeding with the vulcanization reaction.

<Rubber products>
By pressing the rubber composition at a high temperature (for example, 120 to 200 ° C., preferably 130 to 170 ° C.) for 5 to 30 minutes, for example, 10 to 20 minutes, to advance the vulcanization reaction You can get a rubber product. This method can be referred to, for example, JIS K 6299: 2012. Rubber products include, for example, anti-vibration rubber; anti-vibration materials such as engine mounts, stabilizer bushes, suspension bushes, etc. used in automobile vehicles; control dampers for computer hard disks, damping dampers for general household appliances such as washing machines; Building walls in the building / housing field; Damping (damping) devices such as damping (damping) dampers and seismic isolation devices; Automotive parts, tires, footwear, hoses, belts, air springs, non-slip sheets, etc. General or industrial products. A rubber product using the rubber composition of the present invention can have excellent aging resistance, heat resistance and mechanical properties.

The following examples further illustrate one embodiment of the present invention. In the examples, “parts” and “%” are based on mass unless otherwise specified.

<Synthesis Example 1, 4, 5, 6-oxatrithiocan>
In a 100 mL four-necked flask, 80 g of sulfur monochloride and 0.02 g of iron powder were added, and the liquid temperature was set to 20 ° C. Next, 43 g of chlorine gas was further blown in over 3 hours while maintaining the liquid temperature at 20 ° C. Then, 118 g of sulfur dichloride was obtained by removing the iron powder. Next, a 5000 mL four-necked flask was charged with 150 g of bis (2-mercaptoethyl) ether, 3700 g of toluene, and 112 g of synthesized sulfur dichloride, and the resulting reaction solution was maintained while maintaining the liquid temperature at 20 ° C. By purification by distillation under reduced pressure, 182 g of 1,4,5,6-oxatrithiocan was obtained. The structure was confirmed by ¹ H-NMR.

<Example 1, Comparative Examples 1-3: Production and evaluation of masterbatch>
[Manufacture of master batch (make master batch)]
In a 1000 mL four-necked flask, 100 g of the sulfide compound obtained in the synthesis example, 300 g of monochlorobenzene, and 100 g of silica having the properties shown in Table 2 were added and stirred at room temperature. Monochlorobenzene in the obtained mixture was removed by distillation under reduced pressure to obtain 200 g of a master batch. The mass ratio of sulfide compound / silica in each example and comparative example is shown in Table 2.
In addition, in the manufactured masterbatch, what was in powder form was “◯”, and what was in the form of dumpling or oil and could not be manufactured as a good masterbatch was “x”.

[Stability of sulfide compounds in masterbatch]
The stability of the sulfide compound (A) in the master batch obtained in Example 1 and Comparative Examples 1 to 3 was evaluated.
In the stability evaluation, the sulfide compound (A) was extracted from the master batches obtained in each Example and Comparative Example, and the change in the weight average molecular weight of the sulfide compound (A) before and after the master batch was measured. Shimadzu GPC (LC10A) was used for the measurement of molecular weight.
The extraction of the sulfide compound (A) after the masterbatch was obtained by adding 100 g of dichloromethane to 5 g of the masterbatch, stirring the mixture at 25 ° C. for 30 minutes, and filtering the silica.
The stability evaluation shown in Table 2 was performed as follows.
Molecular weight change rate (%) = [(weight average molecular weight of sulfide compound (A) before masterbatch formation) − (weight average molecular weight of sulfide compound (A) after masterbatch formation)] / (sulfide before masterbatch formation) Weight average molecular weight of compound (A)) × 100
○: Molecular weight change rate ≦ 10%
Δ: 10% <Molecular weight change rate ≦ 20%
×: Molecular weight change rate> 20%

<Example 2, Comparative Examples 4 to 5: Production and evaluation of rubber composition>
[Production of rubber composition]
Rubber compositions were produced by mixing the master batches obtained in Example 1 and Comparative Example 1 with unvulcanized rubber compositions, respectively (Example 2 and Comparative Example 4 respectively). Specifically, the master batch and the unvulcanized rubber composition were kneaded at a constant kneading time (15 minutes) using an open roll. The unvulcanized rubber composition is an A-kneaded rubber compound in which a compounding agent other than the vulcanizing agent is kneaded in advance, and a rubber composition was produced by mixing a master batch with the rubber compound. The kneading was performed according to the method described in JIS K 6299-2001. The open roll used was a 6-inch mixing roll manufactured by Yasuda Seiki Seisakusho. The sulfide compound used in Example 1 and silica were added separately at the same mass ratio ((A) / (B) = 50/50) as in Example 1 without making a master batch, and the rubber composition Production was also performed (Comparative Example 5). In addition, each compounding quantity is as having shown in Table 1.

[Kneading workability, vulcanization characteristics of rubber composition and heat resistance of rubber]
The kneading workability during the production of the rubber composition, the vulcanization characteristics of the rubber composition, and the heat resistance of the rubber (vulcanized rubber) were measured.
Vulcanization characteristics were evaluated by a vulcanization test according to JIS K 6300-2-2001. The vulcanization tester used was a CURLAST METER V type manufactured by Orientec Co., Ltd., a crosslinking curve was determined, and the T90 value (optimum crosslinking time) was determined from the change in torque.
The heat resistance of rubber was evaluated by measuring the change in rubber hardness by a heat aging test. The heat aging test was performed according to JIS K 6257-1993. The rubber hardness was measured according to JIS K 6253-1997. A rubber test piece was prepared in accordance with JIS K 6299-2012.
The results are shown in Table 3. The criteria for evaluation are as follows.

(Kneading workability)
The state of the rubber composition obtained by kneading the master batch and the unvulcanized rubber composition for 10 minutes was visually confirmed.
○: Uniformly distributed △: Non-uniform, free of sulfide compound or silica on the rubber surface ×: Sulfide compound or silica is not kneaded into the rubber composition and adheres to the roll

(Vulcanization time)
The difference with respect to the value of T90 of the rubber sample using the masterbatch described in Example 1 was confirmed.
○: T90 difference ≦ 1 min
×: T90 difference> 1 min

(Heat-resistant)
The change in hardness of the rubber sample before and after heat aging was measured. The heat aging test was carried out at 100 ° C. for 72 hours.
○: Change in hardness ≦ 5
×: Change in hardness> 5
The change in hardness was calculated by the following formula with reference to JIS K 6257-1993.
A _H = H ₁ -H ₀
A _H : Change in hardness H ₀ : Hardness before aging H ₁ : Hardness after aging

Claims

A masterbatch comprising a sulfide compound (A) and silica (B),
The sulfide compound (A) has the formula (I):

[In the formula (I), D represents an oxygen atom or a direct bond, and x represents 3 or 4]
A compound represented by
The silica (B) has the following conditions:
BET specific surface area is 0.1 to 50 m 2 / g, and DBP oil absorption is 150 to 200 ml / 100 g.
Satisfy the masterbatch.
The master batch according to claim 1, wherein the aqueous dispersion of silica (B) has a pH of 6.0 to 7.0 at 25 ° C.
The master batch according to claim 1 or 2, wherein a mass ratio ((A) / (B)) of the sulfide compound (A) to the silica (B) is 20/80 to 80/20.
A method for producing a masterbatch comprising a sulfide compound (A) and silica (B), wherein the sulfide compound (A) has the formula (I):

[In Formula (I), D represents an oxygen atom or a direct bond, and x represents 3 or 4. ]
A compound represented by
The silica (B) has the following conditions:
A BET specific surface area of 0.1 to 50 m 2 / g, and
DBP oil absorption is 150-200ml / 100g
The filling,
The manufacturing method of a masterbatch which mixes the said sulfide compound (A), the said silica (B), and an organic solvent, and removes the said organic solvent.
A rubber composition comprising the masterbatch according to any one of claims 1 to 3, and natural rubber and / or synthetic rubber.
A masterbatch according to any one of claims 1 to 3, and a method for producing a rubber composition containing natural rubber and / or synthetic rubber,
A method for producing a rubber composition, comprising mixing 0.5 to 60 parts by mass of the masterbatch with 100 parts by mass of the natural rubber and / or synthetic rubber.