Synthetic resins or natural rubbers -- part of the class 520 ser – Synthetic resins – Polymers from only ethylenic monomers or processes of...
Reexamination Certificate
1999-01-21
2003-05-20
Carone, Michael J. (Department: 3641)
Synthetic resins or natural rubbers -- part of the class 520 ser
Synthetic resins
Polymers from only ethylenic monomers or processes of...
C252S182130
Reexamination Certificate
active
06566467
ABSTRACT:
BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates to an inhibitor for the emulsion polymerization of chloroprene and a process for making a discoloration-resistant polychloroprene using such inhibitor.
2. Background Art
Chloroprene is a highly reactive monomer. Spontaneous free-radical polymerization is expected for uninhibited chloroprene monomer at ordinary temperatures (Encyclopedia of Polymer Science and Engineering, Volume 3, second edition, p. 442 (1985)).
Emulsion polymerization is the preferred way to accommodate the high polymerization rates of chloroprene and achieve high molecular weight. In order to control the polymerization reaction and prevent additional reactions after the desired molecular weight is reached, the polymerization reaction is usually not taken to full conversion of the chloroprene monomer. Rather, the reaction mixture is treated with an inhibitor, often referred to as a shortstop, which effectively stops the polymerization at less than 100% conversion. The residual chloroprene monomer is then removed.
Known effective shortstops for the emulsion polymerization of chloroprene such as phenothiazine and para-tert-butyl catechol, are usually highly colored or photosensitizers. They lead to polychloroprenes which discolor quickly under sunlight. Other materials disclosed as a shortstop or stabilizer for the emulsion polymerization of chloroprene include a class of bis(phenol)methane compounds which are substituted with alkyl radicals in the positions ortho and para to each of the hydroxy groups (the “Rosahl compounds”), which are disclosed by Rosahl et al. in U.S. Pat. No. 3,074,899. While the “Rosahl” compounds do yield polymers with a low tendency to discolor, Applicant has found that they do not safely and effectively shortstop chloroprene polymerization when the “Rosahl” compounds are used as the sole inhibitor. Further in U.S. Pat. No. 4,481,313, Banta et al. disclose that the emulsion polymerization of chloroprene can be shortstopped using phenolic antioxidants such as hydroquinone, 2,5-di-tert-amylhydroquinone, 4-tert-butyl-pyrocatechol, 4,4′-thiobis(6-tert-butyl-o-cresol) and 2,6-di-tert-butyl-4-phenylphenol. The phenolic antioxidants disclosed in U.S. Pat. No. 4,481,313 either cause discoloration or have been found by Applicant to be ineffective shortstops.
SUMMARY OF THE INVENTION
The invention is directed to a polymerization inhibitor composition for the emulsion polymerization of chloroprene comprising a 4-(C
1
-C
3
alkoxy)phenol and a hindered bis(phenol)methane of the formula
wherein each R
1
is independently selected from the group consisting of C
1
-C
12
alkyl radicals and each R
2
is independently selected from the group consisting of H and C
1
-C
12
alkyl radicals, the molar ratio of the alkoxyphenol to the hindered bis(phenol)methane being 0.5/1-2.5/1.
Further, the invention is directed to a process for making a discoloration-resistant polychloroprene comprising the steps of polymerizing chloroprene monomer in an aqueous emulsion and shortstopping the polymerization step by adding the above inhibitor composition. A minimum of 0.0003% of the total of alkoxyphenol and bis(phenol)methane are required for an effective shortstop, based on the weight of total initial monomer in the polymerization process.
DETAILED DESCRIPTION OF THE INVENTION
Applicant has found that 4-(C
1
-C
3
alkoxy)phenol compounds (sometimes referred to as hydroquinone mono(C
1
-C
3
alkyl)ether compounds) are about as effective as the Rosahl compounds for shortstopping the emulsion polymerization of chloroprene and that neither completely halts polymerization when used as the sole inhibitor. More importantly, Applicant has further discovered that a composition containing both types of compounds is a surprisingly more effective shortstop than either one alone and the combination can completely halt polymerization.
Emulsion polymerization of chloroprene is well known. It is used conventionally to produce a variety of chloroprene rubbers. The term “polymers of chloroprene” or “chloroprene rubbers” encompasses polymers in which chloroprene is the major or predominant monomer and include chloroprene dipolymers, terpolymers and higher copolymers. Organic comonomers such as 2,3-dichloro-1,3-butadiene; acrylonitrile, methacrylonitrile, lower alkyl acrylates, lower alkyl methacrylates, acrylamides, methacrylamides, lower alkyl maleates and fumarates, acrylic acid, methacrylic acid, fumaric acid and maleic acid may be employed.
Usually, the total amount of comonomers will represent no greater than 25 mole percent of the total monomers and preferably will constitute less than 15 mole percent of the total monomers including chloroprene. The term “monomer” as used is understood to include all polymerizable monomer excluding any elemental sulfur that may be incorporated into the polymer. The total amount of monomers is generally at least 50 mole percent chloroprene, preferably less than 25 mole percent comonomer and more preferably less than 15 mole percent comonomer.
Any process for polymerizing chloroprene in aqueous emulsion which does not interfere with the novel characteristics of this invention can be employed. Processes and methods for the polymerization and recovery of chloroprene are disclosed, for example, in the “Encyclopedia of Polymer Science and Technology,” supra, and in numerous patents such as U.S. Pat. Nos. 2,264,173 and 2,264,191 both issued on Nov. 25, 1941 and Whitby, “Synthetic Rubber”, 1954, p. 770. The polymerization may be conducted either batchwise or continuously.
A typical process begins with a recipe which calls for an emulsifier, water, chloroprene, comonomer as appropriate, either elemental sulfur or a chain-transfer agent, and other additives for colloidal stability.
Conventional emulsifiers may be employed such as the salts of rosins and rosin derivatives such as tall oil rosin (or resin), wood rosin, disproportionated rosins and salts thereof. Rosin base emulsifiers are well known to the art. A particularly preferred rosin emulsifier is wood rosin (unmodified except for clean-up and sold by the Reichhold Chemicals as Nancy-Wood Rosin).
In general practice, chloroprene is polymerized in the presence of either elemental sulfur or a sulfur-containing chain-transfer agent. Elemental sulfur is incorporated into the backbone of the polymer. Polysulfide bonds are subsequently cleaved by a peptizing agent. The amount of sulfur can range from as low as 0.1% or less based on polymerizable compounds (monomer) up to the maximum proportion soluble in the non-aqueous phase under the conditions of the polymerization, ordinarily about 0.2 to 2.5%, preferably in the range of 0.2 to 0.8 parts of sulfur per 100 parts of monomer, more preferably 0.3 to 0.65 parts thereof.
In contrast to elemental sulfur, chain transfer agents react with growing polymer chain ends resulting in termination and end-capping. Conventional chain-transfer agents include mercaptans such as dodecyl mercaptan and disulfides such as alkylxanthogen disulfides. Generally, at least 0.05 parts, preferably 0.05-0.8 parts and most preferably 0.1-0.25 parts, chain transfer agent are used per 100 parts monomer.
The usual methods may be employed to prepare the aqueous emulsion of monomers, either elemental sulfur or chain-transfer agent, emulsifier and water. A stabilizer for the emulsion, such as a sodium salt of a naphthalensulfonic acid-formaldehyde condensation product is generally added to the aqueous phase as well. The proportions in the aqueous emulsion are not critical but generally the monomer will be present in an amount such as from 30 to 60 percent by weight based on the total weight of the composition.
The pH of the aqueous emulsion for polymerization may be varied depending upon the particular emulsification system employed and can be acidic, neutral or alkaline; however, it is preferred to have a pH in the range of about 7 to 13.5.
An initiator is added to the emulsion. Conventional initiators for chloroprene polymerization may be employed. Preferre
Baker Aileen J.
Carone Michael J.
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