Continuous process for producing halogenated isoolefin copolymer
US-2022025084-A1 · Jan 27, 2022 · US
US11919977B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11919977-B2 |
| Application number | US-201917311297-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 12, 2019 |
| Priority date | Dec 27, 2018 |
| Publication date | Mar 5, 2024 |
| Grant date | Mar 5, 2024 |
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The invention relates to an energy efficient, fast and environmentally favourable process for the preparation of chlorinated butyl rubbers, that uses hypochlorous acid (HOCl) and/or dichlorine monoxide (Cl 2 O) as halogenating agent. The process comprises reacting a copolymer with hypochlorous acid and/or dichlorine oxide. The copolymer comprises units derived from an isoolefin monomer and units derived from a multiolefin monomer. A preferred isoolefin is isobutene and a preferred multiolefin is isoprene.
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What is claimed is: 1. A process for the preparation of a chlorinated copolymer comprising at least the steps of: polymerizing a copolymer from a reaction medium comprising: an aliphatic medium including at least 50 weight percent of one or more aliphatic hydrocarbons, and a monomer mixture comprising at least one isoolefin monomer and at least one multiolefin monomer, in the presence of an initiator to form a product comprising the copolymer, the aliphatic medium, and residual monomers of the monomer mixture; removing the residual monomer to obtain an organic phase comprising the copolymer and the aliphatic medium; contacting the organic phase with hypochloric acid, dichlorine oxide, or an aqueous phase containing hypochloric acid or dichlorine oxide; and reacting the copolymer in the organic phase with hypochloric acid and or dichlorine oxide. 2. The process according to claim 1 , wherein the isoolefin monomer is selected from those having from 4 to 16 carbon atoms. 3. The process according to claim 1 , wherein the isoolefin monomer is isobutene. 4. The process according to claim 1 , wherein the multiolefin is selected from the group consisting of isoprene, butadiene, 2-methylbutadiene, 2,4-dimethylbutadiene, piperyline, 3-methyl-1,3-pentadiene, 2,4-hexadiene, 2-neopentylbutadiene, 2-methyl-1,5-hexadiene, 2,5-dimethyl-2,4-hexadiene, 2-methyl-1,4-pentadiene, 4-butyl-1,3-pentadiene, 2,3-dimethyl-1,3-pentadiene, 2,3-dibutyl-1,3-pentadiene, 2-ethyl-1,3-pentadiene, 2-ethyl-1,3-butadiene, 2-methyl-1,6-heptadiene, cyclopentadiene, methylcyclopentadiene, cyclohexadiene and 1-vinyl-cyclohexadiene. 5. The process according to claim 1 , wherein the multiolefin is isoprene. 6. The process according to claim 4 , wherein the copolymers further comprise further structural units derived from olefins selected from the group consisting of β-pinene, styrene, divinylbenzene, diisopropenylbenzene, and o-, m- and p-alkylstyrenes. 7. The process according to claim 1 , wherein the reacting includes a chlorination reaction and is carried out by contacting the aqueous phase with the organic. 8. The process according to claim 1 , wherein hypochloric acid and/or dichlorine oxide are prepared by reacting one or more hypochlorites with acidic compounds having a pKa of 0.00 to 7.60, as measured at standard conditions. 9. The process according claim 8 , wherein the acidic compounds are carboxylic acids. 10. The process according claim 8 , wherein the one or more hypochlorites is sodium hypochlorite. 11. The process according to claim 7 , wherein the aqueous phase comprising hypochloric acid and/or dichlorine oxide exhibits a pH value of from 2.0 to 7.4 under reaction conditions. 12. The process of claim 1 , wherein the reaction is carried out in the presence of an antioxidant. 13. The process of claim 1 , wherein the isoolefin monomer is selected from those having 4 to 7 carbon atoms. 14. The process of claim 1 , wherein the isoolefin monomer is selected from the group consisting of isobutene, 2-methyl-1-butene, 3-methyl-1-butene, and 2-methyl-2-butene. 15. A process for the preparation of a chlorinated copolymer comprising at least the step of reacting a copolymer comprising i) structural units derived from at least one isoolefin monomer and ii) structural units derived from at least one multiolefin monomer with hypochloric acid and or dichlorine oxide; wherein the chlorinated copolymer has a chlorine content from 0.1 to 4 wt.-%, wherein the structural units derived from isoprene are at least partially chlorinated to form exo-methylene and endo-Cl and cis-endo and trans-endo and microstructure units such that the microstructure Index X being the ratio of mol-% (exo-methylene+endo-Cl)/mol-% (cis-endo and trans-endo) as measured by 1H-NMR is from 1.50 to 3.30. 16. The process of claim 15 , wherein the chlorine content of the copolymer is from 1.1 to 2.2 wt.-%, and the microstructure Index X is from 2.20 to 2.80. 17. A process for the preparation of a chlorinated copolymer comprising at least the step of reacting a copolymer comprising i) structural units derived from at least one isoolefin monomer and ii) structural units derived from at least one multiolefin monomer with hypochloric acid and or dichlorine oxide; wherein the multi-olefin includes isoprene; wherein the chlorinated copolymer comprises 1-(1-chloromethylethenyl)-2,2,4,4-tetramethylcyclohexane (C1-C13) and 1,1,5,5-tetramethyl-2-(1-chloromethylethenyl)-3-(2,2,4-trimethylpentyl)-cyclohexane (C1-C21) in a ratio (C1-C13)/(C1-C21) of 0.60 or more. 18. A process for the preparation of a chlorinated copolymer comprising at least the steps of: polymerizing a copolymer from a reaction medium comprising: an aliphatic medium including at least 50 weight percent of one or more aliphatic hydrocarbons, and a monomer mixture comprising at least one isoolefin monomer and at least one multiolefin monomer, in the presence of an initiator to form a product comprising the copolymer, the aliphatic medium, and residual monomers of the monomer mixture; removing the residual monomer to obtain an organic phase; contacting the organic phase with hypochloric acid, dichlorine oxide, or an aqueous phase containing hypochloric acid or dichlorine oxide; and reacting the copolymer in the organic phase with hypochloric acid and or dichlorine oxide; wherein the chlorinated copolymer comprises 1-(1-chloromethylethenyl)-2,2,4,4-tetramethylcyclohexane (C1-C13) and 1,1,5,5-tetramethyl-2-(1-chloromethylethenyl)-3-(2,2,4-trimethylpentyl)-cyclohexane (C1-C21) in a ratio (C1-C13)/(C1-C21) of 1.50 to 5.00. 19. A process for the preparation of a chlorinated copolymer comprising at least the step of reacting a copolymer comprising i) structural units derived from at least one isoolefin monomer and ii) structural units derived from at least one multiolefin monomer with dichlorine oxide; wherein the chlorinated copolymer comprises 1-(1-chloromethylethenyl)-2,2,4,4-tetramethylcyclohexane (C1-C13) and 1,1,5,5-tetramethyl-2-(1-chloromethylethenyl)-3-(2,2,4-trimethylpentyl)-cyclohexane (C1-C21) in a ratio (C1-C13)/(C1-C21) of 0.60 or more. 20. The process of claim 15 , wherein the reaction is carried out by contacting an aqueous phase comprising hypochloric acid and/or dichlorine oxide with an organic phase comprising the copolymer and an organic diluent wherein the organic diluent is hexane. 21. The process of claim 15 , wherein the isoolefin monomer is selected from those having from 4 to 16 carbon atoms, optionally wherein the isoolefin monomer is isobutene. 22. The process of claim 15 , wherein the multiolefin monomer is selected from the group consisting of isoprene, butadiene, 2-methylbutadiene, 2,4-dimethylbutadiene, piperyline, 3-methyl-1,3-pentadiene, 2,4-hexadiene, 2-neopentylbutadiene, 2-methyl-1,5-hexadiene, 2,5-dimethyl-2,4-hexadiene, 2-methyl-1,4-pentadiene, 4-butyl-1,3-pentadiene, 2,3-dimethyl-1,3-pentadiene, 2,3-dibutyl-1,3-pentadiene, 2-ethyl-1,3-pentadiene, 2-ethyl-1,3-butadiene, 2-methyl-1,6-heptadiene, cyclopentadiene, methylcyclopentadiene, cyclohexadiene and 1-vinyl-cyclohexadiene. 23. The process of claim 15 , wherein the method includes preparing the hypochloric acid and/or dichlorine oxide by reacting hypochlorites with acidic compounds having a pKa of 0.00 to 7.60 as measured at standard conditions; optionally, wherein the acidic compounds are carboxylic acids; optionally, wherein the hypochlorite is sodium
Incorporating halogen atoms into the molecule · CPC title
Halogenation · CPC title
with conjugated diolefins, e.g. butyl rubber · CPC title
as molar percentages · CPC title
wherein the polymer is a copolymer and the modification is taking place only on one or more of the monomers present in minority · CPC title
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