Methods for operating polyethylene reactor systems
US-2024392119-A1 · Nov 28, 2024 · US
US10745495B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10745495-B2 |
| Application number | US-201716070536-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 19, 2017 |
| Priority date | Jan 21, 2016 |
| Publication date | Aug 18, 2020 |
| Grant date | Aug 18, 2020 |
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The invention relates to a process for the production of polyethylene by gas phase polymerisation of ethylene in the presence of a supported chromium oxide based catalyst which is modified with an amino alcohol wherein the molar ratio of amino alcohol:chromium ranges between 0.5:1 and 1.5:1 wherein the support is silica having a surface area (SA) between 250 m2/g and 400 m2/g and a pore volume (PV) between 1.1 cm3/g and less than 2.0 cm3/g.
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The invention claimed is: 1. A process for the production of polyethylene by gas phase polymerisation of ethylene in the presence of a supported chromium oxide based catalyst composition which is modified with an amino alcohol wherein the molar ratio of amino alcohol: chromium ranges between 0.5:1 and 1.5:1, wherein the support is silica having a surface area (SA) between ≥450 m 2 /g and ≤550 m 2 /g and a pore volume (PV) between ≥1.7 cm 3 /g and ≤2.0 cm 3 /g and wherein the catalyst comprises a titanium compound. 2. The process according to claim 1 characterised in that the amount of chromium in the supported catalyst is ≥0.1% by weight and ≤0.5% by weight. 3. The process according to claim 1 , characterised in that the molar ratio of amino alcohol:chromium ranges between 0.7:1 and 1.5:1. 4. The process according to claim 1 , characterised in that the molar ratio of amino alcohol:chromium ranges between 1:1 and 1.3:1. 5. The process according to claim 1 , characterised in that the amino alcohol has the formula wherein the R groups may be, independently of one other the same or different, a C 1 -C 10 alkyl group, and R 1 is a C 3 -C 8 cycloalkyl group or a C 4 -C 16 alkyl substituted cycloalkyl group. 6. The process according to claim 5 characterised in that the amino alcohol is 4-(cyclohexylamino) pentan-2-ol or 4-[(2-methylcyclohexyl) amino]pentan-2-ol. 7. The process according to claim 1 , characterised in that the titanium compound a compound according to the formulas Ti(OR 1 ) n X 4-n and Ti(R 2 ) n X 4-n , wherein R 1 and R 2 represent an (C 1 -C 20 ) alkyl group, (C 1 -C 20 ) aryl group or (C 1 -C 20 ) cycloalkyl group, X represents a halogen atom, and n represents a number satisfying 0≥n≤4. 8. The process according to claim 1 characterised in that the amount of chromium in the supported catalyst is ≥0.1% by weight and ≤0.5% by weight, the molar ratio of amino alcohol:chromium ranges between 1:1 and 1.3:1, and the amino alcohol has the formula wherein the R groups may be, independently of one other the same or different, a C 1 -C 10 alkyl group, and R 1 is a C 3 -C 8 cycloalkyl group or a C 4 -C 16 alkyl substituted cycloalkyl group. 9. The process according to claim 8 characterised in that the titanium compound is a compound according to the formulas Ti(OR 1 ) n X 4-n and Ti(R 2 ) n X 4-n , wherein R 1 and R 2 represent an (C 1 -C 20 ) alkyl group, (C 1 -C 20 ) aryl group or (C 1 -C 20 ) cycloalkyl group, X represents a halogen atom, and n represents a number satisfying 0≥n≤4.
Ethene · CPC title
Catalyst characterized by its size · CPC title
Dual catalyst, i.e. use of two different catalysts, where none of the catalysts is a metallocene · CPC title
Component of C08F4/64 containing at least two different metals · CPC title
Polymerisation in gaseous state · CPC title
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