JP2011195632A - Diene rubber suffering from no discoloration with time and method of manufacturing the same - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a simple and low-cost method of manufacturing a diene rubber that is prevented from discoloration caused by conventional method of manufacturing a polybutadiene rubber and has a decreased gel content.SOLUTION: The method of manufacturing the diene rubber suffering from no discoloration with time comprises charging water before polymerization of a monomer to be used so that the molar ratio of an organoaluminum to water (Al/HO) falls within the range of 1.00 to 2.00 and subsequently carrying out polymerization.

Description

In the present invention, in order to prevent discoloration with time due to the conventional method for producing polybutadiene rubber, the molar ratio of water to organic aluminum (Al / H ₂ O) in the production process is 1.00 to 2.00. The present invention relates to a simple and low-cost method in which initial coloring is suppressed so as to be within a range, discoloration with time is also suppressed, and gel content is reduced.

In general, butadiene rubber often adds many compounds such as various catalysts, promoters, and antioxidants in the production process. In particular, the addition of an antioxidant prevents the deterioration of the product, so such an additive is essential. However, when there are many kinds and amounts of additives, side effects such as coloring and odor often occur, and unexpected problems may occur.

In particular, when a side effect of coloring occurs, there are many cases where the product is required to have transparency, which is often a big problem, and many solutions have been attempted so far.

  For example, in Patent Document 1, in the production of a chloroprene polymer, coloring is prevented by using diethylhydroxylamine and a phenolic antioxidant together as a polymerization terminator.

  Moreover, in patent document 2, by superposing | polymerizing 1 or more types of phenolic compounds after superposition | polymerization of a butadiene rubber, adjusting pH value to the range of 4-11, and oxygen content being 0-0.3 ppm. , Providing stable and colorless polybutadiene rubber.

Further, in the prior art document 3, one or more compounds selected from the group consisting of an aryl phosphine compound and a silazane compound are added to a blend comprising an antioxidant or a polymerization inhibitor when polymerizing. To prevent coloring.

However, it is difficult to say that any anti-coloring method is advantageous in terms of cost, such as adding a compound to the additive used in the conventional production process in many cases and making the production process more complicated.

An object of the present invention is to provide a coloring solution method in which the manufacturing process is almost the same as that of the conventional method and the cost increase is suppressed in solving the coloring problem.

JP 06-345832 A Special table 2003-535926 JP 2009-249308 A

An object of the present invention is to provide a colorless diene rubber having high storage stability and a method for producing the same by an industrially simple method.

In the process for producing a diene rubber, the present invention is such that the molar ratio of water to organoaluminum (Al / H ₂ O) is in the range of 1.00 to 2.00 before polymerization of the monomer used. The present invention relates to a method for producing a diene rubber that does not discolor over time, and is polymerized thereafter.

The diene rubber is polybutadiene polymerized by a catalyst system of a cobalt compound and organoaluminum, and relates to a process for producing a diene rubber which does not discolor over time.

The cobalt compound is cobalt octaate, and relates to a method for producing a diene rubber which does not discolor over time.

  The present invention relates to a diene rubber obtained by the above production method and not discolored with time.

  A method for producing a diene rubber that is low in cost, industrially simple and does not discolor over time can be provided.

(1) Polymerization method of the present invention In the polymerization method of the diene rubber of the present invention, (A) a diene monomer is dissolved in (B) an organic solvent, and (C) water is dissolved therein. Next, (D) an organoaluminum cocatalyst is added and aged, and (E) a transition metal catalyst is added and polymerized. In order to stop the polymerization after the reaction, (F) a polymerization terminator is added, and then (G) an antioxidant is added.

(A) Diene-based monomer Examples of the diene-based monomer include 1,3-butadiene, isoprene, 1,3-pentadiene, 2,3-dimethylbutadiene, 2-phenyl-1,3-butadiene, and the like. These may be used individually by 1 type, may mix 2 or more types, and also may be used by copolymerizing with other dienes, such as 1, 3- hexadiene. Of these, 1,3-butadiene is preferred.

(B) Organic solvent As the organic solvent to be used, aromatic hydrocarbons such as toluene, benzene and xylene, aliphatic hydrocarbons such as n-hexane, butane, heptane and pentane, and alicyclic such as cyclopentane and cyclohexane Hydrocarbons such as hydrocarbon, 1-butene, cis-2-butene, trans-2-butene, etc., hydrocarbon solvents such as mineral spirit, solvent naphtha, kerosene, and halogenated hydrocarbon solvents such as methylene chloride Etc. Further, 1,3-butadiene itself may be used as a polymerization solvent.

The solvent is preferably a non-aromatic hydrocarbon, particularly cyclohexane.

(E) Transition metal catalysts that can be used include cobalt-based catalysts.

As the cobalt-based catalyst, a cobalt salt or complex is preferably used. Particularly preferred are cobalt salts such as cobalt octaate, cobalt chloride, cobalt bromide, cobalt nitrate, cobalt octylate (ethylhexanoate), cobalt naphthenate, cobalt acetate and cobalt malonate, and cobalt bisacetylacetonate. And trisacetylacetonate, ethyl acetoacetate cobalt, organic base complexes such as pyridine complexes and picoline complexes of cobalt salts, or ethyl alcohol complexes.

  Of these, cobalt octaate is particularly preferred.

(E) The amount of the cobalt compound used is usually in the range of 1 × 10 ⁻⁷ to 1 × 10 ⁻⁴ mol, preferably 1 × 10 ⁻⁶ to 1 × 10 ⁻⁵ mol, with respect to 1 mol of butadiene. It is.

The above polybutadiene can also be produced with a catalyst other than cobalt.
Examples of catalysts other than cobalt-based catalysts include nickel-based, neodymium-based, and vanadium-based catalysts.

Examples of the nickel-based catalyst include a catalyst system composed of a nickel compound-organoaluminum compound.

Nickel compounds include nickel naphthenate, nickel formate, nickel octylate, nickel stearate, nickel citrate, nickel benzoate and nickel toluate, organic complex compounds such as nickel acetylacetonate, and alkylbenzene sulfonic acid. Examples thereof include nickel and nickel oxyborate.

Among these, nickel octylate is preferable.

  Furthermore, as the form of the diene polymer corresponding to the type of metal catalyst, lithium catalyst polymerization-polybutadiene (Li-BR), cobalt catalyst polymerization-polybutadiene (Co-BR), neodymium catalyst polymerization-polybutadiene (Nd-BR), nickel Catalytic polymerization-polybutadiene (Ni-BR), titanium catalytic polymerization-polybutadiene (Ti-BR), styrene-butadiene block copolymer (SB, SBS, SEBS), random styrene-butadiene-copolymer (L-SBR), butadiene-isoprene -Copolymer (BI), styrene-butadiene-isoprene-terpolymer (SIB) and the like.

  In particular, cobalt-catalyzed polymerization-polybutadiene (Co-BR) is particularly suitable for the method of the present invention.

(D) Organoaluminum promoter The usable organoaluminum promoter includes trialkylaluminum, dialkylaluminum chloride, dialkylaluminum bromide, alkylaluminum sesquichloride, alkylaluminum sesquibromide, alkylaluminum dichloride, and the like.

Specific examples of the compound include trialkylaluminum such as trimethylaluminum, triethylaluminum, triisobutylaluminum, trihexylaluminum, trioctylaluminum, and tridecylaluminum.

In addition, dialkylaluminum chlorides such as dimethylaluminum chloride and diethylaluminum chloride, organoaluminum halogen compounds such as sesquiethylaluminum chloride and ethylaluminum dichloride, hydrogenated organics such as diethylaluminum hydride, diisobutylaluminum hydride and sesquiethylaluminum hydride Aluminum compounds are also included. These organoaluminum compounds may be used alone or in combination of two or more.

  Of these, triethylaluminum, diethylaluminum chloride and the like are particularly preferable.

(D) The usage-amount of organoaluminum is the range of 50-2000 mol with respect to 1 mol of (E) transition metal catalysts (for example, cobalt-type catalyst).

(C) The amount of water added is important to balance the molar ratio with (D) the organoaluminum promoter. (D) When the molar ratio of the aluminum aluminum promoter to water (Al / H ₂ O) is in the range of 1.00 to 2.00, the initial coloration is suppressed, and the color change with time is also suppressed. Not only can the content be reduced, but also a significant decrease in polymerization activity can be prevented, so the molar ratio is also important in terms of productivity.

  Here, the initial coloring is defined as a coloring state for one week after the production.

(D) The organoaluminum promoter is good if the molar ratio with water (Al / H ₂ O) is 1.00 to 2.00, more preferably 1.05 to 1.90, It is especially preferable that it is 1.10-1.50, and 1.20-1.40 is the most preferable.

(D) If the molar ratio (Al / H ₂ O) of the organic aluminum promoter to water is less than 1.00 or more than 2.00, initial coloration and color change with time are likely to occur, and the gel content also increases. Therefore, it is not preferable.

(F) Polymerization Terminator The polymerization of the diene rubber is terminated by adding water, alcohol, organic acid or inorganic acid and / or phenol by a usual method.

Among these, dispersibility is good, and preferred polymerization terminators include water and lower alcohols, and the amount of water used is 1.38 × 10 ^{−8 to} 9.9 vol% with respect to the total raw material mixed solution. Preferably, it is 2.76 × 10 ^{−8 to 5} vol%, more preferably 4.14 × 10 ^{−8 to 3} vol%. The total raw material mixed solution is the total amount of a mixed solution of butadiene which is a raw material charged into the reactor, a solvent cyclohexane and butene, and a raw material mixed solution added before modification.

The lower alcohol preferably has 5 or less carbon atoms, and specifically includes methanol, ethanol, propanol, isopropanol, butanol, ter-butyl alcohol, pentanol and isomers thereof. These may be used alone or in combination.

In the present invention, the order of adding (G) antioxidant is added after (F) polymerization terminator, but the order of adding (G) antioxidant and (F) polymerization terminator is reversed. May be.
Moreover, (F) addition of a polymerization terminator can be omitted. (Changed the expression slightly)

(G) Antioxidant As a polymerization terminator, 4,6-bis (octylmethyl) -o-cresol (CAS-No. 110553-27-0) and octadecyl-3- (3) are used as phenolic antioxidants. , 5-Ditertbutyl 4-hydroxyphenyl) propionate (CAS-No. 2082-79-3) and pentaerythritol tetrakis [3 (3,5 ditertbutyl 4-hydroxyphenyl) propionate] (CAS-No. 6683-19-) 8) and the like. Other examples include phosphorus antioxidants.

Among these, 4,6-bis (octylmethyl) -o-cresol is preferable.

(G) The necessary amount of the antioxidant used is added depending on the period to be stabilized, but is preferably 5 × 10 ^{−6 to} 3 × 10 ⁻⁴ moles relative to 1 mole of butadiene. ^{−5 to} 2 × 10 ⁻⁴ mol is more preferable. If the amount of the antioxidant is too small, the anti-deterioration function cannot be obtained, and if it is too much, it causes coloring.

In the present invention, known molecular weight regulators at the time of polymerization, for example, non-conjugated dienes such as cyclooctadiene and allene, or α-olefins such as ethylene, propylene and butene-1 can be used.

The polymerization temperature is preferably in the range of -30 to 100 ° C, particularly preferably in the range of 30 to 80 ° C. The polymerization time is preferably in the range of 5 minutes to 12 hours, particularly preferably 10 minutes to 6 hours. The polymerization pressure is carried out under normal pressure or up to about 10 atm (gauge pressure).

The toluene solution viscosity (Tcp) of polybutadiene that can be produced according to the present invention is 10 to 300, more preferably 20 to 200, still more preferably 25 to 150, and most preferably 30 to 130.

According to the present invention, the polybutadiene that can be produced has a Mooney viscosity (ML _{1 + 4} , 100 ° C.) at 100 ° C. of 10 to 200. 20-150 are more preferable, 25-100 are still more preferable, and 29-60 are the most preferable.

According to the present invention, the ratio (Tcp / ML _{1 + 4} ) of toluene solution viscosity (Tcp) to Mooney viscosity (ML _{1 + 4} , 100 ° C.) at 100 ° C. is 1 or more and the gel content is 0.01 wt% or less. Polybutadiene can be produced.

The ratio (Tcp / ML _{1 + 4} ) of the toluene solution viscosity (Tcp) to the Mooney viscosity (ML _{1 + 4} , 100 ° C.) at 100 ° C. is an index of the linearity (linear) of the polymer, and the larger this value is It means a polymer with high linearity. On the other hand, the lower the value, the more branched the polymer.
A preferable value of Tcp / ML _{1 + 4} is preferably 1.0 or more, more preferably 1.2 or more, and particularly preferably 1.7 or more.

The gel content is desirably 0.01 wt% or less, but is more preferably 0.003 wt% or less, and particularly preferably 0.002 wt% or less. When the amount exceeding 0.01 wt% is generated, not only the appearance of the product is deteriorated, but also a fish eye problem is likely to occur when used as a resin film modifier.

The stable colorless diene rubber produced according to the present invention is used to produce all types of vulcanizates, for example, tires, hoses, footwear members, industrial belts, medical rubber, sporting goods, crawlers or packings. As well as for impact modification of polymers based on vinyl aromatic compounds such as polystyrene and bulk polymers produced by bulk processes.

EXAMPLES The present invention will be specifically described below with reference to examples, but the scope of the present invention is not limited to these examples. The Mooney viscosity (ML _{1 + 4} , 100 ° C.), the toluene solution viscosity (Tcp), the color measurement method, and the gel content measurement are as follows.

Mooney viscosity (ML _{1 + 4} , 100 ° C.) was measured in accordance with JIS K 6300.

Toluene solution viscosity (Tcp) was obtained by dissolving 2.28 g of polymer in 50 ml of toluene, using a standard solution for calibrating viscometer (JIS Z 8809) as a standard solution, and using a Canon Fenceke viscometer No. 400 was used and measured at 25 ° C.

(Coloring measurement)
In addition to visual observation, the coloration was quantitatively measured with a yellow index (YI value) using NDJ-300A manufactured by Nippon Denshoku Industries Co., Ltd.

(Measurement of gel content)
The gel content (toluene insoluble matter) is 10 g of sample rubber and 400 ml of toluene placed in an Erlenmeyer flask and completely dissolved at room temperature (25 ° C.), and then filtered using a filter equipped with a 200 mesh wire mesh. The gel content adhered to the wire mesh after filtration is a value measured by vacuum-drying the wire mesh attached with the gel and measuring the amount of adhesion, and as a percentage of the sample rubber.

Example 1
The inside of the polymerization autoclave having an internal volume of 1.5 L is purged with nitrogen, and 1 L of a raw material mixed solution (cyclohexane 20 wt%, butadiene 40 wt%, butene 40 wt%) is charged and stirred. Next, 4 mmol of water was added and stirring was continued for 30 minutes. Next, 3 mmol of diethylaluminum chloride (DEAC) and 1 mmol of triethylaluminum (TEA) were added, and the mixture was aged by stirring for 5 minutes. The molar ratio (Al / H ₂ O) between the total organoaluminum catalyst (4 mmol / l) and water is 1.00. Thereafter, 11 mmol of 1,5-cyclooctadiene (COD) is added as a molecular weight regulator, the temperature of the solution is 50 ° C., 7.8 μmol of cobalt octylate (Co (Oct) ₂ ) is added, and polymerization is started. Polymerization was carried out for 30 minutes. After the reaction, 0.2355 mmol of 4.6-bis (octylmethyl) -O-cresol (cas-number 110553-27-0) was added as an antioxidant in an ethanol solution and stirred for 1 minute.
Next, polybutadiene was obtained from the recovered polybutadiene solution by vacuum drying the solvent at 100 ° C. for 1 hour.
The color measurement was carried out after 1 week, 2 weeks, 1 month and 2 months after production.

(Example 2)
The same procedure as in Example 1 was carried out except that the amount of water was 3.64 mmol and the molar ratio of the total organoaluminum catalyst (4 mmol / l) to water (Al / H ₂ O) was 1.10. .

(Example 3)
The same procedure as in Example 1 was carried out except that the water was adjusted to 3.08 mmol, and the molar ratio (Al / H ₂ O) of the total organoaluminum catalyst (4 mmol / l) to water was 1.30. .

Example 4
The same procedure as in Example 1 was carried out except that the amount of water was 2.67 mmol, and the molar ratio of the total organoaluminum catalyst (4 mmol / l) to water (Al / H ₂ O) was 1.50. .

(Comparative Example 1)
The same procedure as in Example 1 was carried out except that the amount of water was 4.44 mmol and the molar ratio (Al / H ₂ O) of the total organoaluminum catalyst (4 mmol / l) to water was 0.90. .

(Comparative Example 2)
This was carried out in the same manner as in Example 1 except that water was adjusted to 2.5 mmol, and the molar ratio (Al / H ₂ O) between the total organoaluminum catalyst (4 mmol / l) and water was 1.60. .

  From the results of Table 1, Examples 1 to 4 of the present invention have lower initial coloring, lower color change with time (change in YI per elapsed day), and lower gel content than Comparative Examples 1 and 2. I understand that. That is, it can be seen that the polybutadiene prepared by the method of the present invention suppresses initial coloration (YI at the time of 1 week in the table), suppresses discoloration with time, and further reduces the gel content.

Claims (2)

In the production process of diene rubber, polybutadiene polymerized by a catalyst system with a cobalt compound and organoaluminum, and before the polymerization of the monomer used, the molar ratio of water to organoaluminum (Al / H ₂ O) is A method for producing a diene rubber that does not discolor over time, characterized by being charged so as to be in the range of 1.00 to 2.00 and then polymerized.   A diene rubber which is obtained by the production method according to claim 1 and does not discolor over time.