Co-selective methanation catalyst
US-9522391-B2 · Dec 20, 2016 · US
US9393554B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9393554-B2 |
| Application number | US-201414654996-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 4, 2014 |
| Priority date | Feb 6, 2013 |
| Publication date | Jul 19, 2016 |
| Grant date | Jul 19, 2016 |
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Provided is a method that produces a saturated aldehyde from a 1,2-alkanediol in high yield. Disclosed is a method for producing a saturated aldehyde from a 1,2-alkanediol in the presence of a regular mesoporous material.
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The invention claimed is: 1. A method for producing a saturated aldehyde, the method comprising contacting a 1,2-alkanediol with a regular mesoporous material to convert the 1,2-alkanediol into a saturated aldehyde, wherein the regular mesoporous material is a regular mesoporous material obtained by reacting a layered silicate with a surfactant. 2. The method according to claim 1 , wherein an average pore size of the regular mesoporous material is 2.0 nm or more and 10.0 nm or less. 3. The method according to claim 1 , wherein an acid quantity of the regular mesoporous material is 1.0 mmol/g or more and 10.0 mmol/g or less. 4. The method according to claim 1 , wherein the layered silicate is selected from kanemite (NaHSi 2 O 5 .3H 2 O), sodium disilicate crystals (α, β, γ, σ-Na 2 Si 2 O 5 ), makatite (Na 2 Si 4 O 9 .5H 2 O), ilerite (Na 2 Si 8 O 17 .xH 2 O), magadiite (Na 2 Si 14 O 29 .xH 2 O), and kenyaite (Na 2 Si 20 O 41 .xH 2 O). 5. The method according to claim 1 , wherein the regular mesoporous material is FSM-16. 6. The method according to claim 1 , wherein the 1,2-alkanediol is 1,2-propanediol. 7. The method according to claim 1 , wherein the saturated aldehyde is propionaldehyde. 8. The method according to claim 1 , wherein the 1,2-alkanediol is contacted with a regular mesoporous material such that W/F is 0.01 g·min/ml or more and 1000 g·min/ml or less. 9. The method according to claim 1 , wherein a temperature of the regular mesoporous material during the contacting is set to 200° C. or higher and 800° C. or lower. 10. The method according to claim 1 , wherein the 1,2-alkanediol is 1,2-propanediol, the saturated aldehyde is propionaldehyde, the 1,2-propanediol is contacted with the regular mesoporous material such that W/F is 0.01 g·min/ml or more and 1000 g·min/ml or less, a temperature of the regular mesoporous material during the contacting is set to 200° C. or higher and 800° C. or lower, and the yield of propionaldehyde is at least 42.5%. 11. The method according to claim 10 , wherein the regular mesoporous material is FSM-16. 12. The method according to claim 10 , wherein the regular mesoporous material is MCM-41. 13. The method according to claim 1 , wherein the yield of saturated aldehyde is at least 42.5%. 14. The method according to claim 1 , wherein the yield of saturated aldehyde is at least 42.5%-63.0%. 15. The method according to claim 10 , wherein the yield of propionaldehyde is 42.5%-63.0%.
Mesoporous materials not having base exchange properties, e.g. Si-MCM-41 · CPC title
Saturated compounds having —CHO groups bound to acyclic carbon atoms or to hydrogen · CPC title
by dehydration and rearrangement involving two hydroxy groups in the same molecule · CPC title
{Microporous crystalline materials not having base exchange properties, such as} silica polymorphs, e.g. silicalites · CPC title
Operations & Transport · mapped topic
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