Tantalum-based catalyst deposited on silica for the transformation of ethanol into butadiene
US-2018208522-A1 · Jul 26, 2018 · US
US10647625B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10647625-B2 |
| Application number | US-201715837382-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 11, 2017 |
| Priority date | Feb 7, 2017 |
| Publication date | May 12, 2020 |
| Grant date | May 12, 2020 |
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A process for producing 1,3-butadiene (BD) from ethanol in a single step by s7passing a mixture containing ethanol in a gas phase over a multifunctional catalyst having a transition metal dispersion of at least 30% on a silica metal oxide support. In some examples the multifunctional catalyst comprises a silica metal oxide having a surface area of at least 200 m{circumflex over ( )}2/g. The multifunctional catalyst can include a transition metal oxide, a silica metal oxide made from a high purity silica gel, mesoporous silica and fumed silica, such as high purity SBA16, SBA15, or Davisil grade 646.
Opening claim text (preview).
What is claimed is: 1. A method for producing 1,3-butadiene (BI)) from ethanol the method comprising: passing a gaseous feed containing the ethanol over a multi-functional catalyst to produce the 1,3-butadiene (BD); wherein the multifunctional catalyst comprises a silica support, said silica support comprises 1-10 wt % ZrO2 and has a Lewis Acid site concentration of 10-35 μmole/gram; and the multifunctional catalyst comprises silver (Ag) or copper (Cu) having a dispersion of at least 40% on the silica metal oxide support. 2. The process of claim 1 wherein the silica ZrO2 support comprises a silica selected from the group consisting of a high purity silica gel, mesoporous silica and fumed silica. 3. The process of claim 2 wherein the silica ZrO2 is a high purity SBA16. 4. The process of claim 2 wherein the silica ZrO2 is high purity SBA15. 5. The process of claim 2 wherein the silica ZrO2 is Davisil grade 646. 6. The process of claim 1 wherein hydrogen is added to the feed. 7. The process of claim 1 wherein the feed is 100% ethanol. 8. The process of claim 1 wherein the feed is a mixture containing at least 30% ethanol and includes water and wherein the process produces a yield that is at least 30% butadiene. 9. The process of claim 1 wherein the step of passing the feed containing ethanol in a gas phase is performed at a temperature between 200° C. and 375° C. 10. A process for producing 1,3-butadiene (BD) from ethanol in a single step, comprising the step of passing a feed containing ethanol in gas phase over a 1% Ag/4% ZrO 2 /SiO 2 -SBA-16 catalyst having a Ag dispersion of at least 40% on the SiO 2 -SBA-16 support. 11. The process of claim 10 wherein the step of passing a feed containing ethanol is performed in operating conditions including a temperature of 325° C., pressure of 1 atm, and a flow rate of 0.23 hr −1 . 12. The process of claim 10 wherein the feed contains at east 30 percent water by weight.
Silica · CPC title
Platinum · CPC title
Ruthenium, rhodium, osmium or iridium · CPC title
Silver · CPC title
Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof · CPC title
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