Process for making crosslinked cable insulation using high melt strength ethylene-based polymer made in a tubular reactor and optionally modified with a branching agent
US-11912852-B2 · Feb 27, 2024 · US
US10208192B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10208192-B2 |
| Application number | US-201515119144-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 16, 2015 |
| Priority date | Feb 18, 2014 |
| Publication date | Feb 19, 2019 |
| Grant date | Feb 19, 2019 |
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Copolymers comprising ethylene, vinyl esters, in particular vinyl acetate and esters of (meth)acrylic acid, selected from esters comprising branched alkyl, cyclic alkyl or optionally alkyl substituted aryl moieties and having a weight average molecular weight of 35,000 g/mol to 150,000 g/mol, formulations of such copolymers in organic solvents and their use as pour point depressant, wax inhibitor and flow enhancer for crude oils.
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The invention claimed is: 1. A method comprising adding a pour point depressant for crude oil comprising a copolymer (A) to the crude oil; wherein the copolymer (A) comprises (M1) 83.5 mol % to 96.5 mol % of ethylene, (M2) 3 mol % to 11.5 mol % of at least one vinyl ester of the formula H 2 C═CH—O—(O)C—R 1 (I) where R 1 is H or a C 1 - to C 4 alkyl moiety, and M3) 0.5 mol % to 5 mol % of a (meth)acrylate of the formula H 2 C═C(R 2 )—COOR 3 wherein R 2 is H or methyl, and R 3 is selected from the group consisting of R 3a : branched alkyl moieties having 4 to 18 carbon atoms, R 3b : cyclic alkyl moieties having 5 to 12 carbon atoms, and R 3c : aryl moieties having 6 to 12 carbon atoms which are optionally alkyl substituted, and wherein the copolymer (A) has a weight average molecular weight M w of 35,000 g/mol to 150,000 g/mol. 2. The method according to claim 1 , wherein R 1 is a methyl moiety. 3. The method according to claim 1 , wherein R 3a has 5 to 11 carbon atoms. 4. The method according to claim 1 , wherein R 3a has 8 to 10 carbon atoms. 5. The method according to claim 1 , wherein R 3b has 6 to 10 carbon atoms. 6. The method according to claim 1 , wherein R 3 is selected from the group consisting of R 3a and R 3b . 7. The method according to claim 1 , wherein R 3 is R 3a . 8. The method according to claim 1 , wherein the weight average molecular weight M w of the copolymer (A) is 50,000 g/mol to 120,000 g/mol. 9. The method according to claim 1 , wherein an emulsion or dispersion of at least one copolymer (A) in a solvent or solvent mixture to the crude oil. 10. A method comprising adding a formulation comprising at least one copolymer (A) and an organic solvent to crude oil; wherein the copolymer (A) comprises (M1) 83.5 mol % to 96.5 mol % of ethylene, (M2) 3 mol % to 11.5 mol % of at least one vinyl ester of the formula H 2 C═CH—O—(O)C—R 1 (I) where R 1 is H or a C 1 - to C 4 alkyl moiety, and (M3) 0.5 mol % to 5 mol % of a (meth)acrylate of the formula H 2 C═C(R 2 )—COOR 3 wherein R 2 is H or methyl, and R 3 is selected from the group consisting of R 3a : branched alkyl moieties having 4 to 18 carbon atoms, R 3b : cyclic alkyl moieties having 5 to 12 carbon atoms, and R 3c : aryl moieties having 6 to 12 carbon atoms which are optionally alkyl substituted, and wherein the copolymer (A) has a weight average molecular weight M w of 35,000 g/mol to 150,000 g/mol. 11. The method according to claim 10 , wherein the formulation comprises a composition (X) comprising the at least one copolymer (A), and the at least one organic solvent (B), wherein the concentration of the copolymer (A) is 5 to 25% by weight with respect to the sum of all components of the composition (X). 12. The method according to claim 10 , wherein the formulation used additionally comprises at least one wax dispersant. 13. The method according to claim 12 , wherein the wax dispersant is at least one selected from the group consisting of alkylphenols, alkylphenol-formaldehyde resins, and dodecylbenzenesulfonic acid. 14. The method according to claim 11 , wherein the organic solvent (B) comprises a hydrocarbon or a hydrocarbon mixture. 15. The method according to claim 11 , wherein the solvent (B) comprises saturated aliphatic hydrocarbons having a flashpoint≥60° C. 16. The method according to claim 11 , wherein the concentration of the copolymer (A) is 10 to 20% by weight. 17. The method according to claim 10 , wherein the amount of copolymer (A) added is 50 to 3000 ppm of the copolymer (A) based on the crude oil. 18. The method according to claim 10 , wherein the formulation is injected into a crude oil pipeline. 19. The method according to claim 10 , wherein the formulation is injected into a production well. 20. A method comprising adding a rheology modifier comprising at least one formulation comprising a copolymer (A) and an inorganic solvent to crude oil; wherein the copolymer (A) comprises (M1) 83.5 mol % to 96.5 mol % of ethylene, (M2) 3 mol % to 11.5 mol % of at least one vinyl ester of the formula H 2 C═CH—O—(O)C—R 1 (I) where R 1 is H or a C 1 - to C 4 alkyl moiety, and (M3) 0.5 mol % to 5 mol % of a (meth)acrylate of the formula H 2 C═C(R 2 )—COOR 3 wherein R 2 is H or methyl, and R 3 is selected from the group consisting of R 3a : branched alkyl moieties having 4 to 18 carbon atoms, R 3b : cyclic alkyl moieties having 5 to 12 carbon atoms, and R 3c : aryl moieties having 6 to 12 carbon atoms which are optionally alkyl substituted , and wherein the copolymer (A) has a weight average molecular weight M w of 35,000 g/mol to 150,000 g/mol. 21. The method according to claim 20 , wherein the formulation comprises a composition (X) comprising the at least one copolymer (A), and the at least one organic solvent (B), wherein the concentration of the copolymer (A) is 5 to 25% by weight with respect to the sum of all components of the composition (X).
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