Production of Higher Alcohols with Minimum Methanol Content from the Gasification of Carbonaceous Materials
US-2015361015-A1 · Dec 17, 2015 · US
US9745235B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9745235-B2 |
| Application number | US-201415034937-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 6, 2014 |
| Priority date | Nov 11, 2013 |
| Publication date | Aug 29, 2017 |
| Grant date | Aug 29, 2017 |
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In an embodiment: a method of making syngas in a metal reactor can comprise introducing carbon dioxide and hydrogen to the metal reactor in the presence of a catalyst to form the syngas, wherein the metal reactor comprises nickel and wherein the carbon dioxide and the hydrogen are in physical contact with a wall of the metal reactor; and passivating the nickel with a sulfur containing compound.
Opening claim text (preview).
We claim: 1. A method of making syngas in a metal reactor comprising: introducing carbon dioxide and hydrogen to the metal reactor in the presence of a catalyst to form the syngas, wherein a wall of the metal reactor comprises nickel and wherein the carbon dioxide and the hydrogen are in physical contact with the wall of the metal reactor; and passivating the nickel in the reactor walls with a sulfur containing compound. 2. The method of claim 1 , wherein the passivating comprises an initial passivating that occurs prior to the introducing of the carbon dioxide and hydrogen and/or an intermittent passivating that occurs after the introducing of the carbon dioxide and hydrogen. 3. The method of claim 2 , wherein the initial passivating and/or the intermittent passivating occurs for 4 to 24 hours. 4. The method of claim 2 , wherein the passivating comprises initial passivating and the method further comprises adding the catalyst to the metal reactor after the initial passivating. 5. The method of claim 2 , wherein the intermittent passivating occurs after a pressure in the metal reactor is less than or equal to 0.1 MPa. 6. The method of claim 2 , further comprising introducing an oxygen stream at a temperature of greater than or equal to 500° C. during or after the intermittent passivating. 7. The method of claim 2 , further comprising removing the catalyst prior to the intermittent passivating. 8. The method claim 1 , wherein the passivating comprises a continuous passivating that occurs simultaneously with the introducing of the carbon dioxide and hydrogen by introducing the sulfur containing compound to the reactor in a sulfur stream. 9. The method of claim 8 , wherein the passivating comprises an initial passivating that occurs prior to the introducing of the carbon dioxide and hydrogen. 10. The method of claim 9 , further comprising adding the catalyst to the metal reactor after the initial passivating. 11. The method of claim 8 , wherein the sulfur containing compound is introduced in an amount of 0.1 to 8 vol % based on the total volume introduced to the reactor. 12. The method of claim 1 , wherein the reactor is an adiabatic reactor. 13. The method of claim 1 , wherein the reactor comprises stainless steel. 14. The method of claim 1 , wherein reactor comprises 0.1 to 20 wt % nickel. 15. The method of claim 1 , wherein the carbon dioxide and the hydrogen are introduced at a CO 2 :H 2 ratio of 1:1 to 1:10. 16. The method of claim 1 , wherein the syngas has a H 2 :CO ratio of 0.1 to 10. 17. The method of claim 1 , wherein the catalyst comprises a metal oxide catalyst. 18. The method of claim 1 , wherein the metal comprises Cr, Mn, Sn, W, V, Mo, La, Ce, Pb, Mg, Ca, K, W, Cu, or a combination comprising one or more of the foregoing. 19. The method of claim 1 , further comprising using the syngas in a methanol production reaction. 20. The method of claim 1 , further comprising combining the syngas with a second syngas from a different syngas source.
Sulfiding · CPC title
Chromium, molybdenum or tungsten · CPC title
Apparatus characterised by being constructed of material selected for its chemically-resistant properties · CPC title
using catalysts, e.g. selective catalysts · CPC title
one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis · CPC title
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