Methods for operating polyethylene reactor systems
US-2024392119-A1 · Nov 28, 2024 · US
US10093643B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10093643-B2 |
| Application number | US-201715812437-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 14, 2017 |
| Priority date | May 27, 2015 |
| Publication date | Oct 9, 2018 |
| Grant date | Oct 9, 2018 |
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The present invention relates to a method for synthesizing cyclocarbonates by reacting an epoxy compound and carbon dioxide at atmospheric pressure and elevated temperature in the presence of a heterogeneous catalyst system comprising an alkali metal halide and silica as well as the use of said catalyst system for the synthesis of cyclocarbonates.
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The invention claimed is: 1. A method for synthesizing a cyclocarbonate, comprising: providing at least one epoxy compound; providing carbon dioxide; providing a heterogeneous catalyst system; reacting the at least one epoxy compound and the carbon dioxide at atmospheric pressure and a temperature in the range of 100 to 150° C. in the presence of the heterogeneous catalyst system, wherein the catalyst system comprises (a) at least one alkali metal halide selected from the group consisting of alkali metal iodides and alkali metal bromides, and (b) silica (SiO 2 ). 2. The method according to claim 1 , wherein the at least one alkali metal halide is selected from the group consisting of lithium iodide (LiI), sodium iodide (NaI), potassium iodide (KI), lithium bromide (LiBr), sodium bromide (NaBr), potassium bromide (KBr) and combinations thereof. 3. The method according to claim 1 , wherein the at least one epoxy compound (a) is a multifunctional epoxy resin; and/or (b) is a liquid epoxy resin; and/or (c) is an aliphatic epoxy resin; and/or (d) has a molecular weight of 200 to 1000 g/mol. 4. The method according to claim 3 , wherein the at least one epoxy compound (d) has a molecular weight of 400 to 600 g/mol. 5. The method according to claim 1 , wherein the reaction temperature is in the range of 120 to 140° C. 6. The method according to claim 1 , wherein the carbon dioxide is provided in form of carbon dioxide gas, wherein the reaction is carried out under a carbon dioxide atmosphere. 7. The method according to claim 4 , wherein the carbon dioxide is provided in solid form (dry ice) and the method further comprises allowing the solid carbon dioxide to sublimate to gas in the reaction. 8. The method according to claim 1 , wherein the heterogeneous catalyst system comprises 0.5 to 5% by weight of the alkali metal halide relative to the epoxy compound and 0.5 to 5% by weight of the silica relative to the epoxy compound. 9. The method according to claim 1 , wherein the heterogeneous catalyst system comprises 1.5 to 2.5% by weight of the alkali metal halide relative to the epoxy compound and 1.5 to 2.5% by weight of the silica relative to the epoxy compound. 10. The method according to claim 1 , wherein the silica is in form of silica gel particles having a mean diameter of 35 to 70 μm. 11. The method according to claim 3 , wherein the at least one epoxy compound is a liquid epoxy resin having a viscosity of less than 110 mPas at 25° C. 12. The method according to claim 1 wherein the at least one epoxy compound comprises at least one terminal 1,2-epoxy group. 13. The method according to claim 1 wherein the at least one epoxy compound is selected from: formula (1) wherein Z represents hydrogen, methyl or ethyl, and X represents a halogen atom or an —OH group; or formula (2) wherein Z represents hydrogen, methyl or ethyl; or the at least one epoxy compound is a glycidyl ester of saturated or ethylenically unsaturated carboxylic acids with at least one substituted or unsubstituted glycidylester group of formula (3) wherein Z represents hydrogen, methyl or ethyl.
Halides · CPC title
Silica · CPC title
Alkali metals · CPC title
Alkylene carbonates; Substituted alkylene carbonates · CPC title
and cyclic ethers · CPC title
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