Process for treating dregs, treated dregs, use thereof, process for vulcanizing rubber, and vulcanized rubber
AssigneeOxitec ParticipaçãO E GestãO De Ativos NãO Financeiros Ltda.
InventorSandro Antônio Scodro
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AssigneeOxitec ParticipaçãO E GestãO De Ativos NãO Financeiros Ltda.
InventorSandro Antônio Scodro
Estimating the term…
Provided herein is a process for treating dregs for the application thereof as vulcanization activator of rubbers, putting an end to this residue generated in the cellulose industry and providing vulcanized rubbers with similar or enhanced properties in relation to those already known. The process for treating dregs includes the steps of: (a) drying the dregs; and (b) micronization of the dry dregs to an average particle size (d50) from 2 to 45 micrometers. Further provided herein are treated dregs, a use of treated dregs as vulcanization activator, and a process for vulcanizing rubber and the vulcanized rubber.
1-23. (canceled)
A rubber vulcanization process, comprising the step of adding a vulcanization activator to the rubber to be vulcanized, wherein the vulcanization activator is treated dregs that comprise an average particle size (d50) from 2 to 45 micrometers, preferably, 10 to 15 micrometers, and more preferably, 10 micrometers, and comprise, in % by mass based on the treated dregs:
The rubber vulcanization process according to claim 1, wherein the rubber is natural rubber, styrene butadiene rubber (SBR), ethylene-propylene dimer rubber (EPDM), polybutadiene rubber (BR), or nitrile rubber (NBR).
The rubber vulcanization process according to claim 1, wherein 1 to 5 parts of the treated dregs are added per 100 parts of the rubber to be vulcanized.
Vulcanized rubber obtained according to the process defined in claim 1, comprising, in % by mass based on the mass of the vulcanized rubber:
Means for carrying out the rubber vulcanization process defined in claim 1, wherein the means comprise
Means for carrying out the rubber vulcanization process, according to claim 5, wherein the drying capacity is from 60 to 6,000 kg H2O/hour.
Means for carrying out the rubber vulcanization process, according to claim 5, wherein the operating power of the drying is from 11 to 700 kW.
Means for carrying out the rubber vulcanization process, according to claim 5, wherein the drier speed is 20 to 6,000 rpm for integrated dryers and from 10 to 500 rpm for drum dryers.
Means for carrying out the rubber vulcanization process, according to claim 5, wherein the air flow of the dryer is from 500 to 15,000 Nm3/hour.
Means for carrying out the rubber vulcanization process, according to claim 5, wherein he micronization capacity is 1,000 to 15,000 kg/hour.
Means for carrying out the rubber vulcanization process, according to claim 5, wherein the power consumption of the mill is from 100 to 1500 kWh.
Dependencies are inferred from the claim text.