Water-forming hydrogenation reactions utilizing enhanced catalyst supports and methods of use
View Patent ↗Improved reaction efficiencies are achieved by the incorporation of enhanced hydrothermally stable catalyst supports in various water-forming hydrogenation reactions or reactions having water-containing feeds. Examples of water-forming hydrogenation reactions that may incorporate the enhanced hydrothermally stable catalyst supports include alcohol synthesis reactions, dehydration reactions, hydrodeoxygenation reactions, methanation reactions, catalytic combustion reaction, hydrocondensation reactions, and sulfur dioxide hydrogenation reactions. Advantages of the methods disclosed herein include an improved resistance of the catalyst support to water poisoning and a consequent lower rate of catalyst attrition and deactivation due to hydrothermal instability. Accordingly, higher efficiencies and yields may be achieved by extension of the enhanced catalyst supports to one or more of the aforementioned reactions.
1. A hydrogenation reaction process comprising the steps of:
providing a hydrothermally stable alumina support, the hydrothermally stable alumina support produced by the process comprising:
(a) forming a mixture of a crystalline hydrous alumina precursor and a first structural stabilizer, wherein the crystalline hydrous alumina precursor comprises two or more crystalline boehmites having different average crystallite sizes differing by at least about 1 nm;
(b) drying the mixture to form a dried material, wherein the step of drying comprises spray-drying;
(c) impregnating the dried material with a second structural stabilizer to form a support precursor; and
(d) heat treating said support precursor to form a stabilized support, wherein the step of heat treating comprises calcining at a temperature between about 450° C. and about 900° C. to convert the two or more crystalline boehmites to a hydrothermally stable alumina support;
reacting a plurality of reactants under conversion promoting conditions in the presence of a catalyst supported by the hydrothermally stable alumina support to produce a plurality of products through a water-forming hydrogenation reaction;
wherein the step of reacting comprises allowing the water-forming hydrogenation reaction to occur wherein the water-forming hydrogenation reaction is selected the group consisting of:
an alcohol synthesis reaction;
a dehydration reaction;
a hydrodeoxygenation reaction;
a catalytic combustion reaction;
a hydrocondensation reaction; and
a sulfur dioxide hydrogenation reaction; and
allowing a plurality of products to be formed according to the water-forming hydrogenation reaction.
2. The method of claim 1 further comprising the step of low-temperature treating the dried mixture from step (b) to form a partially-stabilized support, wherein said low-temperature treating comprises exposing said dried mixture to a temperature of about 350° C. or less to substantially retain said two or more crystalline boehmites.
3. The method of claim 1 wherein the water-forming hydrogenation reaction is the alcohol synthesis reaction.
4. The method of claim 1 wherein the water-forming hydrogenation reaction is the dehydration reaction.
5. The method of claim 1 wherein the water-forming hydrogenation reaction is the hydrodeoxygenation reaction.
6. The method of claim 1 wherein the water-forming hydrogenation reaction is the catalytic combustion reaction.
7. The method of claim 1 wherein the water-forming hydrogenation reaction is the hydrocondensation reaction.
8. The method of claim 1 wherein the water-forming hydrogenation reaction is the sulfur dioxide hydrogenation reaction.
9. The method of claim 1 wherein the first structural stabilizer is the same composition as the second structural stabilizer.
10. A reaction process comprising the steps of:
providing a hydrothermally stable alumina support, the hydrothermally stable alumina support produced by the process comprising:
(a) forming a mixture of a crystalline hydrous alumina precursor and a first structural stabilizer, wherein the crystalline hydrous alumina precursor comprises two or more crystalline boehmites having different average crystallite sizes differing by at least about 1 nm;
(b) drying the mixture to form a dried material, wherein the step of drying comprises spray-drying;
(c) impregnating the dried material with a second structural stabilizer to form a support precursor; and
(d) heat treating said support precursor to form a stabilized support, wherein the step of heat treating comprises calcining at a temperature between about 450° C. and about 900° C. to convert the two or more crystalline boehmites to a hydrothermally stable alumina support;
reacting a plurality of reactants under conversion promoting conditions in the presence of a catalyst supported by the hydrothermally stable alumina support to produce a plurality of products in a reactor;
wherein the step of reacting comprises introducing water as feed to the reactor; and
allowing a plurality of products to be formed according to the reaction.