Methods for making linear internal olefins from mixtures of linear and branched olefins
US-2024051900-A1 · Feb 15, 2024 · US
US12331013B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12331013-B2 |
| Application number | US-202218270921-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 13, 2022 |
| Priority date | Jan 15, 2021 |
| Publication date | Jun 17, 2025 |
| Grant date | Jun 17, 2025 |
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Provided is a production method for indan and hydrindane, including a reaction step of introducing a raw material composition including tetrahydroindene into a continuous reactor including a solid catalyst containing platinum, and bringing the raw material composition into contact with the solid catalyst under the conditions of 150° C. to 350° C. to obtain a reaction product including indan and hydrindane, in which the amount (mol/min) of hydrogen molecules is 5 times or less the amount (mol/min) of tetrahydroindene, and the amount (mol/min) of oxygen molecules is 0.1 times or less the amount (mol/min) of tetrahydroindene.
Opening claim text (preview).
The invention claimed is: 1. A production method for indan and hydrindane, comprising: reacting by introducing a raw material composition including 3a,4,7,7a-tetrahydroindene, optionally hydrogen molecules, and optionally oxygen molecules into a continuous reactor including a solid catalyst containing platinum, and bringing the raw material composition into contact with the solid catalyst under conditions of 150° C. to 350° C. to obtain a reaction product including indan and hydrindane, wherein a ratio (C H2 /C 0 ) of an amount C H2 (mol/min) of the hydrogen molecules introduced into the continuous reactor per unit time with respect to an amount C 0 (mol/min) of the 3a,4,7,7a-tetrahydroindene introduced into the continuous reactor per unit time is 1 or less, and a ratio (C O2 /C 0 ) of an amount C O2 (mol/min) of the oxygen molecules introduced into the continuous reactor per unit time with respect to an amount C 0 of the 3a,4,7,7a-tetrahydroindene introduced into the continuous reactor per unit time is 0.1 or less. 2. The production method according to claim 1 , wherein in the reacting, the raw material composition is brought into contact with the solid catalyst under conditions of 0.1 to 5.0 MPaG. 3. The production method according to claim 1 , wherein the solid catalyst contains a carrier and a supported metal supported on the carrier, and the carrier includes aluminum, while the supported metal includes platinum. 4. The production method according to claim 3 , wherein a proportion occupied by platinum in the supported metal is 80% by mass or more. 5. The production method according to claim 3 , wherein the platinum is supported on the carrier by using a platinum source that includes no chlorine atom. 6. The production method according to claim 1 , wherein a content of 3a,4,7,7a-tetrahydroindene in the raw material composition is 5% by mass or more. 7. The production method according to claim 1 , wherein a mass ratio (C 1 /C 2 ) of a content C 1 of indan with respect to a content C 2 of hydrindane in the reaction product is 1.0 or more and 4.5 or less. 8. The production method according to claim 1 , wherein the reaction product further includes 3a,4,7,7a-tetrahydroindene, and a portion of the reaction product is reused as the raw material composition of the reacting. 9. The production method according to claim 1 , further comprising raw material synthesis by reacting butadiene with at least one selected from the group consisting of cyclopentadiene and dicyclopentadiene to obtain 3a,4,7,7a-tetrahydroindene.
with oxygen as an acceptor · CPC title
Platinum · CPC title
the other ring being five-membered, e.g. indane · CPC title
Indenes; Completely or partially hydrogenated indenes · CPC title
Spheres · CPC title
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