Thermally integrated process for the production of ethylene oxide from a flow of ethanol
US-2015376151-A1 · Dec 31, 2015 · US
US9688647B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9688647-B2 |
| Application number | US-201415034742-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 4, 2014 |
| Priority date | Nov 15, 2013 |
| Publication date | Jun 27, 2017 |
| Grant date | Jun 27, 2017 |
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Direct epoxidation of propene is carried out on electrochemically tuned mixed oxide catalyst surfaces in a single chamber reactor with mixed reaction gas of hydrocarbon and oxygen. Yield and selectivity improvement compared to platinum- or silver-based noble metal catalysts have been demonstrated for the same reactor set up. Increase in propylene oxide yield has been demonstrated when a cell voltage is applied.
Opening claim text (preview).
What is claimed is: 1. A method for producing propylene oxide, comprising: reacting oxygen and propene in the presence of a mixed metal oxide catalyst to produce propylene oxide, wherein the mixed metal oxide catalyst serves as an electrode of an electrochemical cell, wherein the mixed metal oxide catalyst comprises a perovskite catalyst, wherein the ratio of propene to oxygen is about 0.5:1 or greater, applying a voltage to the electrochemical cell, and wherein the voltage is applied to the electrochemical cell such that the mixed metal oxide catalyst electrode is anodic. 2. The method of claim 1 , wherein an anodic potential is from about 0.1V to about 0.7V. 3. The method of claim 1 , wherein the electrochemical cell comprises an oxygen ion conducting electrolyte. 4. The method of claim 1 , wherein the oxygen ion conducting electrolyte comprises doped zirconia. 5. The method of claim 1 , wherein the mixed metal oxide catalyst is a noble metal-free catalyst. 6. The method of claim 1 , wherein the mixed metal oxide catalyst comprises a transition metal. 7. The method of claim 1 , wherein the perovskite catalyst comprises a Fe or a Mn catalyst. 8. The method of claim 1 , wherein the temperature is from about 400° C. to about 650° C. 9. The method of claim 1 , wherein the temperature is about 500° C. 10. The method of claim 1 , wherein the ratio of propene to oxygen is about 1:1 or greater. 11. The method of claim 1 , wherein the ratio of propene to oxygen is about 2:1 or greater. 12. A method for producing propylene oxide, comprising: reacting oxygen and propene in the presence of a mixed metal oxide catalyst free of a noble metal to produce propylene oxide, wherein the mixed metal oxide catalyst serves as an electrode of an electrochemical cell, wherein the metal oxide catalyst comprises a perovskite catalyst, wherein the ratio of propene to oxygen is about 0.5:1 or greater, tuning the electrochemical cell by injecting charge carriers and oxygen into the catalyst. 13. The method of claim 12 , wherein the metal oxide catalyst comprises a transition metal. 14. The method of claim 12 , wherein the perovskite catalyst comprises a Fe or a Mn catalyst. 15. The method of claim 12 , wherein the temperature is from about 400° C. to about 650° C. 16. The method of claim 12 , wherein the ratio of propene to oxygen is about 1:1 or greater. 17. The method of claim 1 , wherein the ratio of propene to oxygen is from about 1:1 to about 50:1.
with air or molecular oxygen · CPC title
with rare earths or actinides · CPC title
Chemistry & Metallurgy · mapped topic
with catalysts containing silver or gold · CPC title
characterised by the material · CPC title
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