Olefin double bond isomerization catalyst with high poison resistance
US-2018273443-A1 · Sep 27, 2018 · US
US9346720B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9346720-B2 |
| Application number | US-201214113829-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 27, 2012 |
| Priority date | Apr 28, 2011 |
| Publication date | May 24, 2016 |
| Grant date | May 24, 2016 |
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The present invention relates to a process for isomerizing linear alpha-olefins having from 4 to 8 carbon atoms over a heterogeneous catalyst, wherein the catalyst comprises a hydrogenation metal and a selectivity promoter selected from among selenium and tellurium on a support, and also a process for preparing 1-olefins by a metathesis reaction of 2-olefins with ethene, wherein the 2-olefins are prepared by the above mentioned isomerization process.
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The invention claimed is: 1. A process for isomerizing linear alpha-olefins having from 4 to 8 carbon atoms over a heterogeneous catalyst, wherein the catalyst comprises a hydrogenation metal selected from the group consisting of palladium, platinum, nickels, and mixtures thereof, and a selectivity promoter selected from the group consisting of selenium and tellurium on a support, wherein the isomerization is carried out at a temperature of from 30 to 120° C. 2. The process according to claim 1 carried out in the presence of hydrogen. 3. The process according to claim 1 , wherein the support comprises aluminum oxide (Al 2 O 3 ), silicon dioxide (SiO 2 ) or a mixture thereof. 4. The process according to claim 1 , wherein a catalyst which comprises palladium and selenium or tellurium, on a support has a surface area of from 80 to 380 m 2 /g, a pore volume of from 0.6 to 0.95 cm 3 /g and a pore diameter of from 3 nm to 300 μm, with from 80 to 95% of the pore volume being in the pore diameter range from 10 to 100 nm, is used. 5. The process according to claim 1 , wherein the catalyst comprises from 0.1 to 0.8% by weight of palladium, from 0.02 to 0.08% by weight of selenium, tellurium or a mixture of selenium and tellurium, based on the total weight of the catalyst. 6. The process according to claim 1 , wherein the isomerization is carried out at a pressure of from 4 to 35 bar. 7. The process according to claim 1 , wherein the hydrogenation metal is palladium. 8. The process according to claim 7 , wherein the palladium is in elemental form. 9. A process comprising: a. preparing a 2-olefin by the process according to claim 1 ; and b. preparing a 1-olefin reacting the 2-olefin with ethane in a metathesis reaction. 10. The process according to claim 9 , wherein the metathesis is carried out in the presence of a catalyst selected from the group consisting of WO 3 /SiO 2 , CoO—MoO 3 /Al 2 O 3 , Re 2 O 7 /Al 2 O 3 and mixtures thereof, or metal-organic catalysts of the Schrock or Grubbs type.
Silica · CPC title
with five carbon atoms · CPC title
Palladium · CPC title
Tungsten · CPC title
and cobalt · CPC title
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