Conversion of 2,3-butanediol to butadiene
A composition comprising 2,3-butanediol is dehydrated to methyl vinyl carbinol and/or 1,3-butadiene by exposure to a catalyst comprising (a) M x O y wherein M is a rare earth metal, a group IIIA metal, Zr, or a combination thereof, and x and y are based upon an oxidation state of M, or (b) M 3 a (PO 4 ) b where M 3 is a group IA, a group IIA metal, a group IIIA metal, or a combination thereof, and a and b are based upon the oxidation state of M 3 . Embodiments of the catalyst comprising M x O y may further include M 2 , wherein M 2 is a rare earth metal, a group IIA metal, Zr, Al, or a combination thereof. In some embodiments, 2,3-butanediol is dehydrated to methyl vinyl carbinol and/or 1,3-butadiene by a catalyst comprising M x O y , and the methyl vinyl carbinol is subsequently dehydrated to 1,3-butadiene by exposure to a solid acid catalyst.
1. A method, comprising:
converting 2,3-butanediol to methyl vinyl carbinol, 1,3-butadiene, or a mixture thereof by
contacting a feed stream comprising 2,3-butanediol with a catalyst comprising (a) M x O y where M is a rare earth metal, a group IIIA metal, Zr, or a combination thereof, and x and y have values based upon an oxidation state of M, and wherein the catalyst is not CeO 2 , or (b) M 3 a (PO 4 ) b where M 3 is a group IA metal, a group IIA metal, a group IIIA metal, or a combination thereof, and a and b have values based upon the oxidation state of M 3 ; and
dehydrating at least a portion of the 2,3-butanediol to form a product comprising methyl vinyl carbinol, 1,3-butadiene, or a combination thereof.
2. The method of claim 1 , wherein the catalyst has a methyl vinyl carbinol selectivity of at least 20%, a 1,3-butadiene selectivity of at least 20%, or a combined 1,3-butadiene and methyl vinyl carbinol selectivity of at least 20%.
3. The method of claim 1 , wherein M is In, Sc, La, Tm, or a combination thereof.
4. The method of claim 1 , wherein the catalyst further comprises a dopant M 2 , wherein M 2 is a rare earth metal, a group IA metal, a group IIA metal, a group IIIA metal, Zr, or a combination thereof, and wherein M 2 is different than M or M 3 .
5. The method of claim 4 , wherein M is Zr.
6. The method of claim 1 , wherein the catalyst is (i) an oxide of In, Al, La, and Zr, (ii) an oxide of Al and Zr, (iii) an oxide of Zr and Ca, (iv) Tm 2 O 3 , (v) ZrO 2 , (vi) Sc 2 O 3 , or (vii) In 2 O 3 .
7. The method of claim 1 , wherein the catalyst is In 2 O 3 .
8. The method of claim 1 , wherein the feed stream is contacted with the catalyst at a temperature within a range of 250° C. to 700° C. and atmospheric pressure.
9. The method of claim 1 , wherein the feed stream is contacted with the catalyst at a flow rate effective to produce a W/F (catalyst weight (g)/feed flow rate (mol/h)) value within a range of 0.5 to 100 g catalyst·h/mol feed stream.
10. The method of claim 9 , wherein the W/F value is from 1 to 10 g catalyst·h/mol feed stream.
11. The method of claim 1 , wherein at least 5% of the 2,3-butanediol is dehydrated.
12. The method of claim 1 , wherein the catalyst is disposed within a column, and the method further comprises flowing the feed stream through the column at a weight hourly space velocity from 0.3 to 12 h −1 .
13. The method of claim 1 , wherein the product comprises methyl vinyl carbinol, and the method further comprises:
contacting the product comprising methyl vinyl carbinol with a solid acid catalyst; and
dehydrating at least a portion of the methyl vinyl carbinol to 1,3-butadiene.
14. The method of claim 13 , wherein the solid acid catalyst is an aluminosilicate, alumina, sulfated zirconia, or a mixture thereof.
15. A method, comprising:
converting 2,3-butanediol to 1,3-butadiene by
contacting a feed stream comprising 2,3-butanediol with a first catalyst at a temperature within a range of 250° C. to 700° C., wherein the first catalyst comprises M x O y where M is a rare earth metal, a group IIIA metal, Zr, or a combination thereof, and x and y have values based upon an oxidation state of M, and wherein the catalyst is not CeO 2 ;
dehydrating at least 5% of the 2,3-butanediol in the feed stream with the first catalyst to form a first product comprising methyl vinyl carbinol, 1,3-butadiene, or a combination thereof;
contacting the first product with a second catalyst comprising a solid acid catalyst at a temperature from about 250° C. to about 700° C.; and
dehydrating at least 5 wt % of the methyl vinyl carbinol to form a second product comprising 1,3-butadiene.
16. The method of claim 15 , wherein M is In, Sc, La, Tm, or a combination thereof.
17. The method of claim 15 , wherein the first catalyst further comprises M 2 , wherein M 2 is a rare earth metal, a group IA metal, a group IIA metal, a group IIIA metal, Zr, or a combination thereof, and wherein M 2 is different than M.
18. The method of claim 15 , wherein the first catalyst is In 2 O 3 .
19. The method of claim 15 , wherein at least 50% of the 2,3-butanediol in the feed stream is dehydrated with the first catalyst.
20. The method of claim 19 , wherein the solid acid catalyst is an aluminosilicate, alumina, sulfated zirconia, or a mixture thereof.