Linear Alpha Olefin Isomerization Using an Ebullated Bed Reactor
US-2020325085-A1 · Oct 15, 2020 · US
US10329218B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10329218-B2 |
| Application number | US-201615575484-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 27, 2016 |
| Priority date | May 29, 2015 |
| Publication date | Jun 25, 2019 |
| Grant date | Jun 25, 2019 |
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An isomerization catalyst for isomerizing a first straight-chain olefin to a second straight-chain olefin different therefrom in a double bond position in the presence of 20 ppm by volume or more of molecular oxygen and/or water, comprising: Si; and Al.
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The invention claimed is: 1. An isomerization catalyst adapted to isomerize a first straight-chain olefin to a second straight-chain olefin different therefrom in a double bond position in the presence of 20 ppm by volume or more of molecular oxygen, comprising: Si; and Al; wherein an amount A 1 of total acid sites measured by ammonia temperature programmed desorption is 0.11 mmol/g or less wherein a ratio A 2 /A 1 of an amount A 2 of acid sites measured in a temperature range of 600° C. or more to the amount A 1 of the total acid sites measured by ammonia temperature programmed desorption is 0.03 or more. 2. The isomerization catalyst according to claim 1 , wherein a ratio A 2 /A 1 of an amount A 2 of acid sites measured in a temperature range of 600° C. or more to the amount A 1 of the total acid sites measured by ammonia temperature programmed desorption is 0.03 or more. 3. The isomerization catalyst according to claim 1 , comprising a zeolite. 4. The isomerization catalyst according to claim 1 , wherein a molar ratio of Si to Al (Si/Al) is 100 or more. 5. A method for producing a straight-chain olefin, comprising: a step of contacting a raw material compound comprising a first straight-chain olefin with the isomerization catalyst according to claim 1 in the presence of 20 ppm by volume or more of molecular oxygen to isomerize at least a portion of the first straight-chain olefin to the second straight-chain olefin different therefrom in double bond position. 6. The production method according to claim 5 , wherein the numbers of carbon atoms of the first straight-chain olefin and the second straight-chain olefin are 4 to 8. 7. The production method according to claim 5 , wherein the step is performed under conditions for a gas-solid catalytic reaction. 8. A method for producing a compound comprising: a first step of contacting a first raw material compound comprising a first straight-chain olefin with the isomerization catalyst according to claim 1 in the presence of 20 ppm by volume or more of molecular oxygen to isomerize at least a portion of the first straight-chain olefin to a second straight-chain olefin different therefrom in double bond position; and a second step of reacting a second raw material compound comprising the second straight-chain olefin to obtain a compound derived from the second straight-chain olefin. 9. The production method according to claim 8 , wherein the second step is a step of obtaining the compound derived from the second straight-chain olefin and a composition comprising the first straight-chain olefin, and the composition obtained in the second step is reused as a portion or all of the first raw material compound. 10. The production method according to claim 8 , wherein the second step is a step of contacting the second raw material compound with a dehydrogenation catalyst to obtain a conjugated diene by the dehydrogenation reaction of the second straight-chain olefin. 11. The production method according to claim 8 , wherein the second step is a step of contacting the second raw material compound with a hydroformylation catalyst to obtain an aldehyde by the hydroformylation reaction of the second straight-chain olefin. 12. A method for producing a compound, comprising: a step of contacting a raw material compound comprising a first straight-chain olefin with a group of catalysts comprising the isomerization catalyst according to claim 1 in the presence of 20 ppm by volume or more of molecular oxygen to obtain a compound derived from an isomerized product of the first straight-chain olefin. 13. The production method according to claim 12 , wherein the group of catalysts further comprises a dehydrogenation catalyst, and the compound derived from the isomerized product of the first straight-chain olefin is a conjugated diene. 14. The production method according to claim 12 , wherein the group of catalysts further comprises a hydroformylation catalyst, and the compound derived from the isomerized product of the first straight-chain olefin is an aldehyde. 15. The production method according to claim 12 , wherein the step is a step of obtaining the compound derived from the isomerized product of the first straight-chain olefin and an unreacted material comprising the first straight-chain olefin, and the unreacted material obtained in the step is reused as a portion or all of the raw material compound.
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