Fluidizable catalyst for oxidative dehydrogenation of alkanes to olefins in an oxygen free environment
Fluidizable catalysts for the oxygen-free oxidative dehydrogenation of alkanes to corresponding olefins. The catalysts comprise 10-20% by weight per total catalyst weight of one or more vanadium oxides (VO x ) such as V 2 O 5 as well as 1-5% by weight per total catalyst weight of niobium as a promoter. The dehydrogenation catalysts are mounted on an alumina support that is modified with lanthanum to stabilize bulk phase transformation of the alumina. Various methods of preparing and characterizing the catalysts as well as methods for the oxygen-free oxidative dehydrogenation of alkanes to corresponding olefins with improved alkane conversion and olefin selectivity are also disclosed.
1. A method for producing a dehydrogenation catalyst comprising
a support material comprising alumina modified by lanthanum, and
a catalytic material disposed on the support material,
wherein the catalytic material comprises one or more vanadium oxides and niobium as a promoter, and
wherein the dehydrogenation catalyst comprises 10-20% of the one or more vanadium oxides by weight relative to the total weight of the dehydrogenation catalyst,
the method comprising:
mixing lanthanum with alumina to form the support material comprising alumina modified by lanthanum;
mixing the support material with a solution comprising a vanadium salt and a niobium salt in a solvent to form loaded catalyst precursors;
reducing the loaded catalyst precursors with H 2 gas to form reduced catalyst precursors; and
oxidizing the reduced catalyst precursors with oxygen to form the dehydrogenation catalyst.
2. A method for dehydrogenating an alkane to a corresponding olefin, comprising:
flowing the alkane through a reactor comprising a catalyst chamber loaded with a dehydrogenation catalyst at a temperature in the range of 400-800 ° C. to form the corresponding olefin and a reduced catalyst;
oxidizing the reduced catalyst in an oxygen environment separated from the catalyst chamber to regenerate the dehydrogenation catalyst; and
repeating the flowing and the oxidizing at least once without a loss in percent conversion of the alkane, a loss in selectivity for the olefin, or both;
wherein the dehydrogenation catalyst comprises:
a support material comprising alumina modified by lanthanum, and
a catalytic material disposed on the support material,
wherein the catalytic material comprises one or more vanadium oxides and niobium as a promoter, and
wherein the dehydrogenation catalyst comprises 10-20% of the one or more vanadium oxides by weight relative to the total weight of the dehydrogenation catalyst.
3. A method for dehydrogenating an alkane to a corresponding olefin comprising
flowing the alkane through a reactor comprising a catalyst chamber loaded with a dehydrogenation catalyst at a temperature in the range of 400-800 ° C. to form the corresponding olefin and a reduced catalyst,
wherein the reactor is a fluidized bed reactor and the dehydrogenating is performed in an oxygen free environment, and
wherein the dehydrogenation catalyst comprises:
a support material comprising alumina modified by lanthanum, and
a catalytic material disposed on the support material,
wherein the catalytic material comprises one or more vanadium oxides and niobium as a promoter, and
wherein the dehydrogenation catalyst comprises 10-20% of the one or more vanadium oxides by weight relative to the total weight of the dehydrogenation catalyst.
4. The method of claim 3 , wherein the dehydrogenation catalyst is present at an amount in the range of 0.01-0.5 g per mL of the alkane.
5. The method of claim 3 , wherein the alkane is ethane and the method has an ethane conversion of 5-35% at a reaction time of 5-60 seconds and a temperature of 500-600 ° C.
6. The method of claim 3 , wherein the alkane is ethane and the method has an ethylene selectivity of 60-90% at a reaction time of 5-60 seconds and a temperature of 500-600 ° C.
7. The method of claim 3 , wherein the dehydrogenation catalyst comprises 1-5% of niobium by weight relative to the total weight of the dehydrogenation catalyst.
8. The method of claim 3 , wherein the dehydrogenation catalyst comprises 0.1-3% of lanthanum by weight relative to the total weight of the dehydrogenation catalyst.
9. The method of claim 3 , wherein the dehydrogenation catalyst comprises 30-50% of alumina by weight relative to the total weight of the dehydrogenation catalyst.
10. The method of claim 3 , wherein the one or more vanadium oxides have the general formula of V n O 2n+1 , the general formula of V n O 2n−1 , or both;
wherein n is a whole number greater than zero.
11. The method of claim 3 , wherein the one or more vanadium oxides are at least one selected from the group consisting of V 2 O 5 , VO 2 , and V 2 O 3 .
12. The method of claim 3 , wherein the dehydrogenation catalyst comprises at least 50% of V 2 O 5 by weight relative to the total weight of the one or more vanadium oxides.
13. The method of claim 3 , wherein the one or more vanadium oxides form a crystalline phase on the surface of the support material.
14. The method of claim 3 , wherein the dehydrogenation catalyst has a BET surface area in the range of 10-50 m 2 /g.
15. The method of claim 3 , wherein the dehydrogenation catalyst has an average particle size in the range of 30-150 μm.
16. The method of claim 3 , wherein the dehydrogenation catalyst has an apparent particle density in the range of 1-5 g/cm 3 .
17. The method of claim 3 , wherein the dehydrogenation catalyst has a total acidity in the range of 6-11 mL of NH 3 per gram of catalyst.
18. The method of claim 3 , wherein the dehydrogenation catalyst is fluidizable and has Class B powder properties in accordance with Geldart particle classification.