Chemically-recycled pet fiber, rubber-fiber composite, conveyor belt, hose and tire
US-2024344242-A1 · Oct 17, 2024 · US
US9683088B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9683088-B2 |
| Application number | US-201514635634-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 2, 2015 |
| Priority date | Aug 31, 2012 |
| Publication date | Jun 20, 2017 |
| Grant date | Jun 20, 2017 |
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A process for regenerating sulfur-crosslinked rubber vulcanizates to regenerates, wherein at least one regenerating agent is used in the regeneration. The regenerating agent is selected from the group consisting of dithiophosphoryl polysulfides and/or silanes having a polysulfane group. Regenerates which have been produced by means of the process lead to improved or equal rolling resistance indicators and a lower compression set in vulcanized rubber mixtures compared to regenerates known in the prior art.
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What is claimed is: 1. A process for regenerating sulfur-crosslinked rubber vulcanizates to give regenerates comprising: providing at least one regenerating agent for regenerating sulfur-crosslinked rubber vulcanizates, wherein the regenerating agent is selected from the group consisting of dithiophosphoryl polysulfides and silanes having a polysulfane group, and mixing a mixture of the at least one regenerating agent and sulfur-crosslinked rubber vulcanizates for a period of time of from 5 to 35 minutes. 2. The process as claimed in claim 1 , wherein the dithiophosphoryl polysulfide has the general formula I where R 1 and R 2 are identical or different and are selected from among linear or branched C 3 -C 20 -alkyl radicals and x=1 to 6. 3. The process as claimed in claim 2 , wherein the dithiophosphoryl polysulfide is a bis(O,O-2-ethylhexyl)thiophosphoryl polysulfide. 4. The process as claimed in claim 1 , wherein the silane having a polysulfane group has the general formula II (R 2 O) 3-y R 3 y —Si—R 1 —S x —R 1 —Si—(OR 2 ) 3-z R 3 z (II) where x=1 to 8 and the radicals R 1 in a molecule are identical or different and are selected from among linear or branched C 1 -C 18 -alkyl radicals, the radicals R 2 and R 3 in a molecule are identical or different and are selected from among linear or branched or cyclic saturated C 1 -C 30 -alkyl radicals and y and z are identical or different and are each from 0 to 3, wherein the radicals R 2 and/or R 3 optionally contain from 1 to 10 nitrogen atoms (N) and/or oxygen atoms (O) as heteroatoms in the carbon chain. 5. The process as claimed in claim 4 , wherein the silane having a polysulfane group is a bis(trialkoxysilyl)propyl polysulfane. 6. The process as claimed in claim 4 , wherein the radicals R 2 and/or R 3 additionally contain from 1 to 10 nitrogen atoms (N) and/or oxygen atoms (0) as heteroatoms in the carbon chain. 7. The process as claimed in claim 1 , wherein the silane having a polysulfane group has the general formula V (R 2 O) 3-y R 3y —Si—R 1 —S x —R 1 —Si—(O 2 R 2 )R 3 (V) where x=1 to 8 and the radicals R 1 in a molecule are identical or different and are selected from among linear or branched C 1 -C 18 -alkyl radicals, the radicals R 2 in a molecule are identical or different and are selected from among linear or branched or cyclic saturated C 1 -C 30 -alkyl radicals and y and z are identical or different and are each from 0 to 3 and the radicals R 3 in a molecule are identical or different and are selected from among linear or branched C 1 -C 10 -alkyl or alkoxy radicals. 8. The process as claimed in claim 1 , wherein the silane having a polysulfane group has the general formula VI (R 2 O 2 )R 3 —Si—R 1 —S x —R 1 —Si—(O 2 R 2 )R 3 (VI) where x=1 to 8 and the radicals R 1 in a molecule are identical or different and are selected from among linear or branched C 1 -C 18 -alkyl radicals, the radicals R 2 in a molecule are identical or different and are selected from among linear or branched or cyclic saturated C 1 -C 30 -alkyl radicals and the radicals R 3 in a molecule are identical or different and are selected from among linear or branched C 1 -C 10 -alkyl or alkoxy radicals. 9. A process for regenerating sulfur-crosslinked rubber vulcanizates to give regenerates, comprising: placing the sulfur-crosslinked rubber vulcanizate to be regenerated in amounts of from 68 to 98% by weight in a mechanical mixer; heating the sulfur-crosslinked rubber vulcanizate to be regenerated to a temperature of from 50 to 70° C.; adding at least one dithiophosphoryl polysulfide and/or at least one silane having a polysulfane group in amounts of from 2 to 15% by weight to form a mixture; and, mixing the mixture for a period of time of from 5 to 35 minutes at a temperature of from 80 to 150° C. 10. The process as claimed in claim 1 , wherein the sulfur-crosslinked rubber vulcanizates originate from used tires or conveyor belts or vulcanized waste obtained in the production of industrial rubber articles or pneumatic vehicle tires. 11. A regenerate produced as claimed in the process as claimed in claim 1 . 12. The regenerate as claimed in claim 11 for producing pneumatic vehicle tires. 13. A process of regenerating sulfur-crosslinked rubber vulcanizates comprising adding dithiophosphoryl polysulfides as regenerating agents, and mixing the resulting mixture for a period of time of from 5 to 35 minutes. 14. A process for regenerating sulfur-crosslinked rubber vulcanizates comprising adding silanes having a polysulfane group as regenerating agents, and mixing the resulting mixture for a period of time of from 5 to 35 minutes.
Plastics recycling; Rubber recycling · CPC title
for mixing rubber · CPC title
Cross-Sectional Technologies · mapped topic
by chemically breaking down the molecular chains of polymers or breaking of crosslinks, e.g. devulcanisation (depolymerisation to the original monomer C07) · CPC title
Phosphorus bound to sulfur · CPC title
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