Synthetic resins or natural rubbers -- part of the class 520 ser – Synthetic resins – From sulfur-containing reactant
Reexamination Certificate
2002-07-15
2004-06-08
Truong, Duc (Department: 1711)
Synthetic resins or natural rubbers -- part of the class 520 ser
Synthetic resins
From sulfur-containing reactant
C528S373000, C528S389000, C528S486000, C528S492000
Reexamination Certificate
active
06747122
ABSTRACT:
FIELD OF THE INVENTION
The invention relates to a process for the preparation of polymeric sulfur compounds with polythiocyclopentanediyl structural units which are used as vulcanizing agents for diene rubbers.
BACKGROUND OF THE INVENTION
EP-A 258 168 discloses the reaction of olefins with sulfur in water, it being possible for bases to be present as catalysts. Cyclopentadiene and dicyclopentadiene, inter alia, are mentioned as preferred olefins (page 4, lines 14-15). Cyclopentadiene de facto does not occur in the examples according to the present invention. Regarding industrial applicability, it is disclosed on page 7, lines 57-58 and page 8, lines 1-3 that the vulcanizing agents according to the invention lead to vulcanizates which are comparable in their physical properties to the properties obtained with a conventional sulfur vulcanization system. An improved reversion stability of the vulcanizates according to the present invention is not described. In example 1 of the German patent application with the application number DE 100002878.0, it is shown that the products cited therein from dicyclopentadiene and sulfur do not give vulcanizates with improved reversion stability.
U.S. Pat. No. 3,523,926 discloses vulcanizing agents from diolefins, such as e.g. cyclopentadiene and dicyclopentadiene, and sulfur with amines as the catalyst. The additional use of hydrogen sulfide is neither described nor suggested in this reference.
U.S. Pat. No. 2,989,513 discloses polymers of sulfur and an olefin for vulcanization of rubber. In column 3, line 21, cyclopentadiene, inter alia, is mentioned as a useful olefin. The reaction according to this reference is preferably carried out at between 145° and 160° C. The embodiment examples include only copolymers of sulfur and styrene or sulfur and ethylene or isobutylene. At no point in this reference is the additional use of hydrogen sulfide described or suggested.
The German patent application with the application number DE 100002878.0 already describes polymeric sulfur compounds with polythiocyclopentanediyl structural elements which can be employed as crosslinking agents for diene rubbers. According to DE 100002878.0, the polymeric sulfur compounds are obtained by reaction of di-cyclopentenylpolysulfanes, which are known per se, with sulfur and hydrogen sulfide in the presence of amines at temperatures in the range from approx. 100° to 180° C. The di-cyclopentenylpolysulfanes employed can be prepared by (a) addition of sulfanes on to cyclopentadiene and/or methylcyclopentadiene or by (b) reaction of the cyclopentadienes according to the invention with liquid hydrogen sulfide to give (methyl)cyclopent-2-ene-1-thiol and subsequent reaction with elemental sulfur in the presence of amines as a catalyst. In the process according to (a), the preparation and handling of the sulfanes is very complex and expensive from the safety point of view, since sulfanes can decompose spontaneously into hydrogen sulfide and sulfur in contact with rough surfaces. In the process according to (b) the handling of a large amount of liquid hydrogen sulfide is necessary, which requires a gas liquefaction plant. Furthermore, the processes according to (a) and (b) are multi-stage processes.
SUMMARY OF THE INVENTION
The object of the present invention was to provide a one-stage process for the preparation of polymeric sulfur compounds with polythiocyclopentanediyl structural units which is industrially simple and easy to realize.
The object has been achieved by direct reaction of (methyl)cyclopentadiene with sulfur and hydrogen sulfide in the presence of a catalyst.
Therefore, the invention provides a process for the preparation of polymeric sulfur compounds of the formula
wherein the substituents
R
1
and R
2
are identical or different and represent hydrogen or methyl,
n and m denote integers in the range from 2 to 12, and
x denotes an integer in the range from 2 to 500,
wherein (methyl)cyclopentadiene is reacted with sulfur and hydrogen sulfide at 100° to 180° C., in the presence of a catalyst, the molar ratio of sulfur to hydrogen sulfide being 1:0.1 to 1:5, and the molar ratio of (methyl)cyclopentadiene to sulfur being 1:1 to 1:9.
DETAILED DESCRIPTION OF THE INVENTION
Therefore, the present invention provides a process for the preparation of polymeric sulfur compounds of the formula
wherein the substituents
R
1
and R
2
are identical or different and represent hydrogen or methyl,
n and m denote integers in the range from 2 to 12, preferably 2 to 7, and
x denotes an integer in the range from 2 to 500, preferably 2 to 300, in particular 2 to 100,
wherein (methyl)cyclopentadiene is reacted with sulfur and hydrogen sulfide at 100° to 180° C., preferably at 130° to 150° C., in the presence of a catalyst, the molar ratio of sulfur to hydrogen sulfide being 1:0.1 to 1:5, preferably 1:0.5 to 1:2, and the molar ratio of (methyl)cyclopentadiene to sulfur being 1:1 to 1:9, preferably 1:2 to 1:5.
The numbers of the sulfur atoms n and m in the polymer chain are of course, in each case integers. Fractions can also result for the sulfur chain length averaged over all the polymer molecules, due to the formation of a mean value.
The number x for the recurring unit in a specific polymer molecule is an integer. Fractions can also result for the average recurring unit of the total number of polymers, due to the formation of a mean value.
Brönsted acids, Lewis acids or amines are possible as the catalyst for the process according to the present invention. Phosphoric acid, perchloric acid or trifluoromethanesulfonic acid or also mixtures thereof are preferably employed as Brönsted acids. Anhydrous aluminum chloride and in particular, boron trifluoride-etherate are preferably employed as Lewis acids. Possible amines are primary, secondary or tertiary, aliphatic, cycloaliphatic or aromatic or heterocyclic amines or mixtures thereof. Secondary or tertiary aliphatic amines with C
1
- to C
4
-alkyl radicals, such as e.g. dimethylamine, diethylamine, di-n-propylamine, di-i-propylamine, di-n-butylamine, trimethylamine, triethylamine, tri-n-propylamine, tri-i-propylamine or tri-n-butylamine are preferably employed. Triethylamine is more preferred. The catalyst is, in general, employed in an amount of 0.001 to 10 parts by wt., preferably 0.1 to 5 parts by wt., based on 100 parts by wt. of sulfur.
The reaction according to the present invention takes place under pressure, this usually establishing itself in a range from approx. 1 to 500 bar, preferably approx. 1 to 250 bar, depending on the nature of the starting substances and the amount thereof and depending on the temperature used.
The process according to the present invention can be carried out e.g. by a discontinuous or continuous process. In the discontinuous process (methyl)cyclopentadiene is initially introduced into a pressure reactor together with sulfur, hydrogen sulfide and the catalyst and the mixture is then heated up to a temperature of 100° to 180° C., while stirring, and reacted, or (methyl)cyclopentadiene is pumped into the stirred mixture which has been heated up to the temperature according to the invention (feed process). In the continuous process the educts can be added to the reactor individually or also as a mixture and reacted at the reaction temperatures according to the invention.
In an embodiment of the present invention, sulfur, hydrogen sulfide and the catalyst are initially introduced into an autoclave and the (methyl)cyclopentadiene is then added at the reaction temperature according to the present invention (feed process).
The reaction according to the present invention can also be carried out in solvent. Possible suitable solvents are aliphatic C
5
- to C
12
-hydrocarbons, such as e.g. pentane, hexane, heptane or octane, or corresponding hydrocarbon mixtures, such as e.g. petroleum ether with a boiling point of 40° to 70° C., light petroleum with a boiling point of 70° to 90° C. or middle petroleum with a boiling point of 90° to 180° C., C
5
- to C
10
-cycloalkanes, such as e.g. cyclopentane, methylcyclopentan
Buding Hartmuth
Hahn Josef
Runk Marco
Weidenhaupt Hermann-Josef
Bayer Aktiengesellschaft
Gil Joseph C.
Seng Jennifer R.
Truong Duc
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