Anti-agglomerants for the rubber industry
a technology for rubber and agglomerates, applied in the field of anti-agglomerants for the rubber industry, can solve the problems of fatty acid salts of mono- or multivalent metal ions, rapid formation of non-dispersed mass of rubber in process water, fouling and plugging of process,
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examples 1 to 4a
Elastomer Particle Formation:
[0427]In an experiment to demonstrate the ability of methyl cellulose to form an aqueous slurry the following experiments were carried out. Isoprene (0.41 g) and isobutylene (13.50 g) were combined with methyl chloride (200 g at −95° C. under an inert atmosphere. A solution of aluminium trichloride (3 g / l) as a lewis acid in methyl chloride (3 mL at −95° C.) was then added with agitation to the reaction mixture to initiate polymerization. Residual traces of water of around 25 ppm within the organic diluent served as initiator. This reaction produced 10 g of butyl rubber with an isoprene level of 2 mol-% in form of finely dispersed particles in methyl chloride and comprising no anti-agglomerants of any kind.
[0428]The resulting mixture was then poured into a 2 L vessel comprising 1 L of water as the aqueous medium and maintained at 85° C. agitated with an impeller at 1000 RPM. The hot water caused the flashing of diluent and residual monomers, leaving behi...
examples 4d
) and 4e)
Continuous Elastomer Particle Formation:
[0432]Isobutylene and isoprene were combined with methyl chloride to prepare a polymerization feedstock such that the total concentration of the monomers was from approximately 10-40 wt.-%. This feedstock stream was cooled to approximately −100° C. and was fed continuously into an agitated reaction vessel, also maintained at −100° C. In the reaction vessel the feedstock was mixed with a continuously added the initiator system stream, a solution of 0.05-0.5 wt.-% aluminium trichloride in methyl chloride as diluent which is typically activated by traces of water from the diluent. The addition rates of the feedstock stream and the initiator system stream were adjusted to provide an isobutylene isoprene elastomer with a mooney viscosity of approximately 34 and an unsaturation level of approximately 1 mol-%. Typically, the wt.-ratio of monomers in the feedstream to aluminum trichloride was held within a range of 500 to 10000, preferably 50...
example 4d
Total unsaturation: 0.9 mol-%
Mw: 436,000
Polydispersity (Mw / Mn): 3.28
Mooney viscosity (ML 1+8 at 125° C., ASTM D 1646): 34
Calcium stearate content: 0.73 wt.-% (GC-FID, FTIR)
Irganox® 1010: 0.035 wt.-%
Volatiles: 0.09 wt.-%
Other antiagglomerants, surfactants, emulsifiers: see above
Ions: (ICP-AES)
Aluminum (from catalyst): 70 ppm
Magnesium: 32 ppm
Other multivalent metal ions (Mn, Pb, Cu, Cr, Ba, Fe, Zn): 4 ppm
Monovalent metal ions (Na, K): 22 ppm
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