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The present invention provides methods, reactor systems, and catalysts for increasing the yield of aromatic hydrocarbons produced while converting alkanols to hydrocarbons. The invention includes methods of using catalysts to increase the yield of benzene, toluene, and mixed xylenes in the hydrocarb

The present invention provides methods, reactor systems, and catalysts for increasing the yield of aromatic hydrocarbons produced while converting alkanols to hydrocarbons. The invention includes methods of using catalysts to increase the yield of benzene, toluene, and mixed xylenes in the hydrocarbon product.

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1. A method of converting alkanols to aromatic hydrocarbons, the method comprising: partially dehydrogenating a C1-C6 alkanol feedstock in the presence of a dehydrogenation catalyst at an effective dehydrogenation temperature and an effective dehydrogenation pressure to produce a mixture of oxygenat

1. A method of converting alkanols to aromatic hydrocarbons, the method comprising: partially dehydrogenating a C1-C6 alkanol feedstock in the presence of a dehydrogenation catalyst at an effective dehydrogenation temperature and an effective dehydrogenation pressure to produce a mixture of oxygenate components comprising (a) an unreacted C1-C6 alkanol and (b) a carboxylic acid, an aldehyde, an ester, or any combination thereof, wherein at least a portion of the oxygenate components in the mixture have a hydrogen to carbon effective ratio of less than 1.6, and wherein the feedstock is dehydrogenated to an extent sufficient to result in the mixture of oxygenate components having a total hydrogen to carbon effective ratio of between 1.2 and 1.6; andexposing the mixture of oxygenate components to an oxygenate conversion catalyst at an oxygenate conversion temperature and an oxygenate conversion pressure to produce aromatic hydrocarbons. 2. The method of claim 1, wherein the mixture of oxygenate components comprises the carboxylic acid and wherein the carboxylic acid has a hydrogen to carbon effective ratio of less than 1.6. 3. The method of claim 2, wherein the carboxylic acid is acetic acid. 4. The method of claim 1, wherein the mixture of oxygenate components comprises the ester and wherein the ester has a hydrogen to carbon effective ratio of less than 1.6. 5. The method of claim 4, wherein ester is ethyl acetate. 6. The method of claim 1, wherein the mixture of oxygenate components comprises the aldehyde and wherein the aldehyde has a hydrogen to carbon effective ratio of less than 1.6. 7. The method of claim 6, wherein the aldehyde is acetaladehyde. 8. The method of claim 1, wherein the C1-C6 alkanol feedstock comprises two or more C1-C6 alkanols. 9. The method of claim 1, wherein the C1-C6 alkanol feedstock comprises methanol, ethanol, propanol, butanol, or combinations thereof. 10. The method of claim 1, wherein the C1-C6 alkanol feedstock comprises ethanol. 11. The method of claim 1, wherein the total hydrogen to carbon effective ratio is less than 1.5. 12. The method of claim 11, wherein the dehydrogenation catalyst comprises: (i) a metal selected from the group consisting of Cu, Ru, Ag, CuCr, CuZn, Co, Raney copper, copper-zinc-aluminate, alloys thereof, and combinations thereof; and/or(ii) a support selected from the group consisting of alumina, silica, silica-alumina, titania, carbon, zirconia, zinc aluminate, and mixtures thereof. 13. The method of claim 1, wherein: (i) the dehydrogenation temperature is between about 80° C. and 500° C.; and/or(ii) the dehydrogenation pressure ranges from below atmospheric pressure to about 1000 psig. 14. The method of claim 1, wherein the oxygenate conversion catalyst comprises a zeolite. 15. The method of claim 14, wherein the oxygenate conversion catalyst: (i) is ZSM-5;(ii) is modified by a material selected from the group consisting of phosphorous, gallium, zinc, nickel, tungsten, and mixtures thereof; and/or(iii) contains a binder selected from the group consisting of alumina, silica, silica-alumina, titania, zirconia, aluminum phosphate, and mixtures thereof. 16. The method of claim 1, wherein: (i) the oxygenate conversion temperature is between about 250° C. and 550° C.; and/or(ii) the oxygenate conversion pressure ranges from less than atmospheric pressure to about 1000 psig. 17. A method of converting alkanols to aromatic hydrocarbons, the method comprising: partially dehydrogenating a C1-C6 alkanol feedstock in the presence of a dehydrogenation catalyst at an effective dehydrogenation temperature and an effective dehydrogenation pressure to produce a mixture of oxygenate components comprising a C1-C6 alkanol, a carboxylic acid, an aldehyde, and an ester, wherein the carboxylic acid, the aldehyde, and the ester has a hydrogen to carbon effective ratio of less than 1.6, and wherein the feedstock is dehydrogenated to an extent sufficient to result in the mixture of oxygenate components having a total hydrogen to carbon effective ratio of between 1.2 and 1.6; andexposing the mixture of oxygenate components to an oxygenate conversion catalyst at an oxygenate conversion temperature and an oxygenate conversion pressure to produce aromatic hydrocarbons. 18. The method of claim 17, wherein the C1-C6 alkanol feedstock comprises ethanol, the carboxylic acid comprises acetic acid, the aldehyde comprises acetaladehyde, and the ester comprises ethyl acetate. 19. The method of claim 17, wherein the mixture of oxygenates further comprises a ketone, an ether, or both a ketone and an ether. 20. The method of claim 17, wherein the mixture of oxygenates consists essentially of the C1-C6 alkanol, the carboxylic acid, the aldehyde, and the ester. 21. The method of claim 17, wherein the mixture of oxygenates consists essentially of (i) the C1-C6 alkanol, the carboxylic acid, the aldehyde, the ester, and (ii) a ketone, an ether, or both a ketone and an ether. 22. The method of claim 17, wherein the total hydrogen to carbon effective ratio is less than 1.5.