Process for the production of polysulfide silane compounds

Details Process for the production of polysulfide silane compounds Process for the production of polysulfide silane compounds

2000-06-30

2001-08-14

Shaver, Paul F. (Department: 1621)

Organic compounds -- part of the class 532-570 series

Organic compounds

Silicon containing

Reexamination Certificate

active

06274755

ABSTRACT:

CROSS-REFERENCE TO RELATED APPLICATION
This application is based on German Application DE 199 30 495.5, filed Jul. 1, 1999, which disclosure is incorporated herein by reference.
FIELD OF THE INVENTION
This invention relates to a process for the production of polysulfide silane compounds.
BACKGROUND OF THE INVENTION
Silica-filled rubber articles are known in the rubber industry. In comparison with prior technology, these rubber articles have various advantages, such as, for example, in the tire sector, inter alia, improved wet skid behavior and lower rolling resistance are provided. Polysulfide silane compounds are used as additives in order to achieve such good characteristics. These compounds act as coupling agents between the filler, silica and the organic polymer and bring about a reduction in the viscosity of the composition during incorporation of the filler.
Various processes for the production of known polysulfide silanes are described in several patent applications. Most methods start from alkoxysilylalkyl halides which are reacted with alkali metal polysulfides produced in various manners.
According to U.S. Pat. No. 5,405,985, an alkali metal polysulfide is produced by reacting alkali metal sulfide with sulfur in an aqueous solution. The polysulfide coupling agents are obtained by reacting the resultant aqueous polysulfide solution with alkoxysilylalkyl halides in a phase-transfer catalyzed system. It is known that both alkoxysilylalkyl halides and the reaction products obtained therefrom are susceptible to hydrolysis. This process accordingly has the disadvantage that the polymers formed after hydrolysis and condensation exhibit no reinforcing action or exhibit a severely reduced reinforcing action when used in a rubber composition.
For this reason, anhydrous systems are used in other known processes. An anhydrous polysulfide may thus, for example, be obtained in an upstream synthesis step from elemental sulfur and elemental sodium (U.S. Pat. No. 4,640,832). Alternative production methods for anhydrous alkali metal polysulfides start from elemental sulfur and alcohols (U.S. Pat. No. 5,399,739) or from alkali metal alkoxides, hydrogen sulfide and sulfur (U.S. Pat. No. 5,596,116). Another variant uses alkali metal hydrogen sulfide and sodium alkoxide in combination with sulfur in order to produce the polysulfide (DE 3311340).
These known processes have the disadvantage that costly starting materials such as alkali metals or alkali metal alkoxides or the toxicologically and ecotoxicologically questionable compound hydrogen sulfide must be used in the production of sodium polysulfide.
It is furthermore known to dry commercially available “anhydrous” sodium sulfide and then to react it with sulfur in organic solvents. The hydrous sodium sulfide is dried both by contact drying under reduced pressure (JP 7228588, DE 19755760, EP 361998) and by azeotropic drying methods (DE 19610281, JP 7228588). These known processes have the disadvantage that sodium sulfide has a strong tendency to melt on heating which means that even slight deviation from optimum conditions causes the material being dried to stick to the container walls with consequent losses of valuable product. Dried sodium sulfide moreover has a tendency to ignite spontaneously, such that elaborate safety precautions are required for drying, which make the process uneconomic for industrial application.
U.S. Pat. No. 5,663,396 discloses a process in which the polysulfide is produced in an aqueous solution from sodium hydroxide solution and sulfur. The resultant polysulfide solution is then in turn reacted with alkoxysilylalkyl halides in a phase-transfer catalyzed system. There is a great risk in this procedure too that some of the starting compound or product will be reacted to yield polymers which are ineffective for practical application.
In view of the above-described disadvantages of the prior art, there was a requirement for a process which is straightforward to perform industrially and is simultaneously economically viable for the production of anhydrous alkali metal polysulfides, which may be used for the production of the stated polysulfide silane compounds.
SUMMARY OF THE INVENTION
The present invention provides a process for the production of polysulfide silane compounds of the general formula (I)
Z-R
1
-S
n
-R
1
-Z,  (I)
in which
R
1
represents branched or unbranched alkyl groups having 1 to 8 C atoms and optionally interrupted by O, N or S atoms or alkylaromatics of the type (CH
2
)
p
Ph(CH
2
)
p
having 8 to 14 C atoms, wherein
p is an integer from 1 to 4 and n is an integer from 1 to 4,
Z represents residues of the type (R
2
O)
3−m
R
2
m
Si, in which the residues R
2
may be identical or different and are branched or unbranched alkyl residues having 1 to 6 C atoms, and
m is 0, 1 or 2,
wherein silylalkyl halides of the general formula (II)
ZR
1
X,  (II)
in which X corresponds to Cl, Br or I and Z and R
1
have the above-stated meanings, are reacted with alkali metal polysulfides of the general formula (III)
M
2
S
n
,  (III)
wherein
M denotes the alkali metals Na and K and n has the above-stated meaning,
which process is characterized in that the
alkali metal polysulfides M
2
S
n
are obtained by reacting alkali metal hydroxides of the general formula (IV)
MOH,  (IV)
in which M has the above-stated meaning, with elemental sulfur in a non-aqueous solvent or without solvent.
The alkali metal polysulfide may be produced under protective gas at standard pressure or under reduced pressure, wherein the resultant water is distilled off. Nitrogen, helium or argon may be used as the protective gas. The pressure range may be from 1 bar to 0.1 mbar. The reaction temperature may be from 50° C. to 250° C., preferably from 80° C. to 150° C. Once the exothermic reaction has subsided, the reaction may be taken to completion by maintaining a temperature of 100° C. to 250° C., preferably 130° C. to 170° C., for a period of 0.5 to 4 hours, preferably 2 to 3 hours.
Non-aqueous solvents which may be used are high-boiling ethers or polyethers, saturated hydrocarbons or aromatics, preferably xylene, mesitylene or naphthalene, or mixtures thereof.
The process according to the invention has the advantage over the prior art that it may be performed in a virtually anhydrous system. Any water arising during the reaction between the alkali metal hydroxide and sulfur is removed from the product during the reaction, such that the alkali metal polysulfide, which is obtained as a solid, may be reacted in an anhydrous system to yield alkoxysilylalkyl polysulfides.


REFERENCES:
patent: 5663396 (1997-09-01), Musleve et al.
patent: 6140524 (2000-10-01), Ichinohe et al.
patent: 6194595 (2001-02-01), Michel et al.

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