Olefin production method
US-2024391852-A1 · Nov 28, 2024 · US
US11041059B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11041059-B2 |
| Application number | US-201716461918-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 17, 2017 |
| Priority date | Nov 18, 2016 |
| Publication date | Jun 22, 2021 |
| Grant date | Jun 22, 2021 |
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A method for reclaiming rubber comprises the steps of: (i) providing a starting material comprising a vulcanized rubber polymer; (ii) subjecting the starting material to mechanical stress and at a temperature of at least 200° C. to achieve at least a partial destruction of the cross-links and the backbone structure of the rubber polymer into fragments; and (iii) reconstituting at least part of the fragments in the presence of a branching/grafting agent to obtain a renewed rubber composition.
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The invention claimed is: 1. A method for reclaiming rubber, comprising the steps of (i) providing a starting material comprising a vulcanized rubber polymer; (ii) subjecting the starting material to mechanical stress and at a temperature of at least 200° C. either in the absence of a fragmentation additive, or in the presence of a fragmentation additive capable of generating radicals at the temperature used, to achieve at least a partial destruction of the cross-links and the backbone structure of the rubber polymer into fragments; and (iii) partially reconstituting the fragments obtained in step (ii) in the presence of a branching/grafting agent to obtain a renewed rubber composition. 2. Method according to claim 1 , wherein said starting material comprises a mixture of two or more distinct rubbers. 3. Method according to claim 1 , wherein said starting material comprises ground tire rubber (GTR) from car tires and/or truck tires. 4. Method according to claim 1 , wherein step (ii) is performed in the presence of a fragmentation additive capable of generating radicals at the temperature used. 5. Method according to claim 4 , wherein the fragmentation additive is a polymer which undergoes thermal degradation above 200° C. 6. Method according to claim 5 , wherein said polymer is a linear triblock copolymer based on styrene and ethylene/butylene (SEBS). 7. Method according to claim 1 , wherein step (ii) is performed in the absence of a fragmentation additive. 8. Method according to claim 1 , wherein step (ii) is performed at a temperature of at least 220° C. 9. Method according to claim 1 , wherein step (ii) is performed under mixing using in high-shear mixing equipment. 10. Method according to claim 1 , wherein said branching/grafting agent comprises a plurality of unsaturated moieties capable of reacting with free radicals. 11. Method according to claim 10 , wherein said branching/grafting agent comprises the general structure F′—R—F″, wherein each of F′ and F″ is an unsaturated moiety capable of reacting with free radicals. 12. Method according to claim 10 , wherein said branching/grafting agent is a bifunctional agent comprising C═C bonds. 13. Method according to claim 12 , wherein said bifunctional branching/grafting agent is selected from the group consisting of substituted or unsubstituted hydroquinone, substituted or unsubstituted divinylbenzene, and substituted or unsubstituted bismaleimide, which bifunctional branching/grafting agent is used under non-crosslinking conditions. 14. Method according to claim 10 , wherein said branching/grafting agent is a polymeric agent comprising multiple F moieties attached to a polymeric backbone, F being an unsaturated moiety capable of reacting with free radicals, preferably independently selected from —C═C— and C═O. 15. Method according to claim 13 , wherein said polymeric branching/grafting agent is a co-polymer of the type A-B-A, wherein each of A and B is independently selected from the group of homo- and or co-polymers of styrene (S), butadiene (B), isoprene (I) and their hydrogenated counterparts. 16. Method according to claim 1 , wherein step (iii) is performed in the presence of about 0.1-20 wt % branching/grafting agent. 17. Method according to claim 1 , wherein steps (ii) and (iii) are performed as a one-pot-process. 18. Method according to claim 17 , wherein SEBS is used. 19. Method according to claim 1 , wherein step (ii) is performed in an extruder and step (iii) is performed in a batch mixer. 20. A renewed rubber composition obtainable by a method according to claim 1 . 21. Method according to claim 1 , wherein the method is used in the manufacture of tires, roofing material, or flooring material, or wherein the method is used in roadbuilding. 22. Method according to claim 9 , wherein the high-shear mixing equipment is an extruder. 23. Method according to claim 9 , wherein the mixing is performed at a speed of at least 50 rpm for a period of 1-60 minutes. 24. Method according to claim 10 , wherein said moieties are selected from —C═C— and C═O. 25. Method according to claim 11 , wherein F′ and F″ are independently selected from —C═C— and C═O, and wherein R is an alkylic or aromatic organic moiety, or any combination thereof. 26. Method according to claim 15 , wherein said polymer is SBS (triblock, styrene-butadiene-styrene), SEBS (linear triblock copolymer based on styrene and ethylene/butylene) or SIS (styrene-isoprene-styrene). 27. Method according to claim 16 , wherein step (iii) is performed in the presence of about 1-7 wt % branching/grafting agent. 28. Method according to claim 17 , wherein steps (ii) and (iii) are performed in an extruder.
Depolymerisation · CPC title
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Plastics recycling; Rubber recycling · CPC title
Flooring (stair treads E04F11/104; coverings not specially adapted for floors E04F13/00; borders, skirtings E04F19/02; {implements for laying flooring E04F21/20;} gratings for cleaning soles of footwear A47L23/24; {built-in gratings E04F19/10; removing floor coverings E04G23/00; carpets A47G27/00;} of similar materials to roads E01C; basic or rough floors {, structural floors} E04B5/00) · CPC title
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