Catalyst compositions for selective dimerization and polymerization of ethylene
US-2018133703-A1 · May 17, 2018 · US
US2017174584A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017174584-A1 |
| Application number | US-201514977728-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 22, 2015 |
| Priority date | Dec 22, 2015 |
| Publication date | Jun 22, 2017 |
| Grant date | — |
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Oligomerization processes include the steps of introducing a monomer containing a C 3 to C 30 olefin and a chemically-treated solid oxide into a reaction zone, and oligomerizing the monomer to form an oligomer product in the reaction zone. Fluorided silica-coated alumina and fluorided-chlorided silica-coated alumina are illustrative chemically-treated solid oxides that can be used in the oligomerization processes.
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1 . A process comprising: (i) introducing a monomer comprising a C 3 to C 30 olefin and a chemically-treated solid oxide into a reaction zone, the chemically-treated solid oxide comprising a silica-coated alumina treated with an electron-withdrawing anion; and (ii) oligomerizing the monomer to form an oligomer product in the reaction zone; wherein the oligomerizing step is conducted in the substantial absence of organoaluminum compounds and the absence of metallocene compounds; and wherein the oligomer product comprises at least 30 wt. % dimers. 2 . The process of claim 1 , wherein the chemically-treated solid oxide comprises fluorided silica-coated alumina. 3 . The process of claim 2 , wherein a conversion of the monomer to the oligomer product is greater than that of a comparable process using sulfated alumina, under the same oligomerization conditions. 4 . The process of claim 1 , wherein the chemically-treated solid oxide comprises fluorided-chlorided silica-coated alumina. 5 . The process of claim 4 , wherein a conversion of the monomer to the oligomer product is greater than that of a comparable process using sulfated alumina, under the same oligomerization conditions. 6 . The process of claim 1 , wherein: the silica-coated alumina comprises from 20 to 45 wt. % silica, based on the weight of the silica-coated alumina; and the electron-withdrawing anion comprises sulfate, fluoride, chloride, or any combination thereof. 7 . The process of claim 1 , wherein the monomer comprises at least 75 wt. % C 3 to C 18 alpha olefins. 8 . The process of claim 1 , wherein the monomer comprises propylene, 1-butene, 1-pentene, 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, or any combination thereof. 9 . The process of claim 1 , wherein the monomer comprises propylene, and wherein the oligomer product comprises at least 40 wt. % trimers and/or a weight ratio of trimers to tetramers in the oligomer product is greater than 1:1. 10 . The process of claim 1 , wherein the monomer comprises 1-butene, 1-pentene, 1-hexene, or any combination thereof and wherein the oligomer product comprises at least 40 wt. % trimers and/or a weight ratio of trimers to dimers in the oligomer product is greater than 1:1. 11 . The process of claim 1 , wherein the monomer comprises 1-octene, 1-decene, 1-dodecene, or any combination thereof, and wherein a weight ratio of dimers to trimers in the oligomer product is greater than 1:1. 12 . A process comprising: (i) introducing a monomer comprising a C 12 to C 16 olefin and a chemically-treated solid oxide into a reaction zone, the chemically-treated solid oxide comprising sulfated alumina; and (ii) oligomerizing the monomer to form an oligomer product in the reaction zone; wherein the oligomerizing step is conducted in the substantial absence of organoaluminum compounds and the absence of metallocene compounds; and wherein the oligomer product comprises from 30 to 98 wt. % dimers. 13 . The process of claim 12 , wherein a weight ratio of dimers to trimers in the oligomer product is from 2:1 to 6:1. 14 . The process of claim 12 , wherein the oligomer product comprises from 55 to 95 wt. % dimers and/or a weight ratio of dimers to trimers in the oligomer product is from 1.5:1 to 8:1. 15 . The process of claim 1 , wherein the monomer comprises 1-dodecene. 16 - 20 . (canceled) 21 . A process comprising: (i) introducing a monomer comprising a C 3 to C 8 olefin and a chemically-treated solid oxide into a reaction zone, the chemically-treated solid oxide comprising a silica-coated alumina treated with an electron-withdrawing anion; and (ii) oligomerizing the monomer to form an oligomer product in the reaction zone; wherein the oligomerizing step is conducted in the substantial absence of organoaluminum compounds and the absence of metallocene compounds; and wherein the oligomer product comprises at least 30 wt. % trimers. 22 . The process of claim 21 , wherein the electron-withdrawing anion comprises sulfate, fluoride, chloride, or any combination thereof. 23 . The process of claim 21 , wherein the monomer comprises propylene, and wherein a weight ratio of trimers to tetramers in the oligomer product is in a range from 1.05:1 to 1.6:1. 24 . The process of claim 23 , wherein: the oligomer product comprises from 35 to 60 wt. % trimers; and the chemically-treated solid oxide comprises fluorided silica-coated alumina and/or fluorided-chlorided silica-coated alumina. 25 . The process of claim 21 , wherein the monomer comprises 1-hexene, and wherein a weight ratio of trimers to dimers in the oligomer product is in a range from 1.02:1 to 2:1. 26 . The process of claim 25 , wherein: the oligomer product comprises from 35 to 65 wt. % trimers; and the chemically-treated solid oxide comprises fluorided silica-coated alumina and/or fluorided-chlorided silica-coated alumina.
Alumina · CPC title
Chlorides · CPC title
Fluorides · CPC title
Halogens; Compounds thereof · CPC title
with metal oxides · CPC title
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