초록 ▼

Disclosed is a process for the production of higher aldehydes from lower alcohols using a two-stage vapor phase heterogeneous catalyst system. Ethanol feeds afford aldehydes such as butyraldehyde and crotonaldehyde while butanol feeds yield 2-ethylhexanal and 2-ethylhexenal. Higher product selectivi

Disclosed is a process for the production of higher aldehydes from lower alcohols using a two-stage vapor phase heterogeneous catalyst system. Ethanol feeds afford aldehydes such as butyraldehyde and crotonaldehyde while butanol feeds yield 2-ethylhexanal and 2-ethylhexenal. Higher product selectivities are obtained when the alcohol is first dehydrogenated in the upper catalyst stage followed by aldol condensation of the resulting lower aldehyde to a higher aldehyde.

대표청구항 ▼

1. A process for the preparation of a higher-molecular-weight alcohol comprising (A) feeding a lower-molecular-weight alcohol to a first reactor zone comprising a heterogeneous dehydrogenation catalyst to produce a lower-molecular-weight aldehyde containing stream;(B) feeding said lower-molecular-we

1. A process for the preparation of a higher-molecular-weight alcohol comprising (A) feeding a lower-molecular-weight alcohol to a first reactor zone comprising a heterogeneous dehydrogenation catalyst to produce a lower-molecular-weight aldehyde containing stream;(B) feeding said lower-molecular-weight aldehyde containing stream to a second reactor zone comprising a heterogeneous aldol condensation catalyst to produce a higher-molecular-weight aldehyde containing stream; and(C) feeding said higher-molecular-weight aldehyde containing stream and hydrogen to a third reactor zone comprising a heterogeneous hydrogenation catalyst to produce an effluent comprising a higher-molecular-weight alcohol;wherein said process is conducted in the vapor phase. 2. The process according to claim 1, wherein said heterogeneous aldol condensation catalyst comprises V2O5 modified anatase. 3. The process according to claim 1, wherein said lower-molecular-weight alcohol is selected from the group consisting of methanol, ethanol, n-propanol, n-butanol, and i-butanol. 4. The process according to claim 1, wherein the temperature ranges from 100° C. to 500° C., the pressure ranges from 0 psig to 250 psig; and further comprising feeding a diluent gas selected from at least one of the group consisting of nitrogen, argon, oxygen, air, hydrogen, and helium to said first reactor zone. 5. The process according to claim 1, wherein the single-pass yield of lower-molecular-weight alcohol to higher-molecular-weight alcohol ranges from 5 percent to 60 percent. 6. A process for the preparation of 2-EH compounds comprising (A) feeding n-butanol to a first reactor zone comprising a heterogeneous dehydrogenation catalyst and a heterogeneous aldol condensation catalyst; and(B) producing a reactor effluent comprising at least one compound selected from the group consisting of 2-ethylhexanal (2-EH-anal) and 2-ethylhexenal (2-EH-enal);wherein said process is conducted in the vapor phase. 7. The process according to claim 6, wherein said heterogeneous dehydrogenation catalyst and said heterogeneous aldol condensation catalyst are commingled in a catalyst bed. 8. The process according to claim 6, wherein said heterogeneous dehydrogenation catalyst is in a first catalyst bed and said heterogeneous aldol condensation catalyst is in a second catalyst bed. 9. The process according to claim 6, further comprising (C) feeding said reactor effluent to a second reactor zone comprising a heterogeneous hydrogenation catalyst to produce a crude product comprising of 2-ethylhexanal and/or 2-ethylhexanol. 10. The process according to claim 6, wherein said heterogeneous aldol condensation catalyst comprises V2O5 modified anatase. 11. The process according to claim 10, wherein said heterogeneous aldol condensation catalyst comprises V2O5 modified anatase, wherein the amount of V2O5 ranges from 1 weight percent to 30 weight percent based upon the total weight of said V2O5 modified anatase. 12. The process according to claim 6, wherein the temperature ranges from 100° C. to 500° C. 13. The process according to claim 6, wherein the temperature ranges from 100° C. to 350° C. 14. The process according to claim 6, wherein the pressure ranges from 0 psig to 250 psig. 15. The process according to claim 6, wherein the pressure ranges from 0 psig to 100 psig. 16. The process according to claim 6, further comprising feeding a diluent gas selected from at least one of the group consisting of nitrogen, argon, oxygen, air, hydrogen, and helium to said first reactor zone. 17. The process according to claim 6, wherein the single-pass yield of said n-butanol to said 2-ethylhexanal and/or said 2-ethylhexenal ranges from 10 percent to 60 percent. 18. The process according to claim 9, wherein the single-pass yield of said n-butanol to said 2-ethylhexanal and/or said 2-ethylhexanol ranges from 5 percent to 40 percent. 19. A process for the preparation of 2-ethylhexanol comprising (A) feeding n-butanol to a first reactor zone comprising a heterogeneous dehydrogenation catalyst to produce a butyraldehyde containing stream;(B) feeding said butyraldehyde containing stream to a second reactor zone comprising a heterogeneous aldol condensation catalyst to produce a 2-ethylhexanal and/or 2-ethylhexenal containing stream; and(C) hydrogenating said 2-ethylhexanal and/or 2-ethylhexenal containing stream to form a crude product comprising 2-ethylhexanal and/or 2-ethylhexanolwherein said process is conducted in the vapor phase. 20. The process according to claim 19, wherein said heterogeneous aldol condensation catalyst comprises V2O5 modified anatase. 21. The process according to claim 19, wherein said heterogeneous aldol condensation catalyst comprises V2O5 modified anatase, wherein the amount of V2O5 ranges from 1 weight percent to 30 weight percent based upon the total weight of said V2O5 modified anatase. 22. The process according to claim 19, wherein said aldol condensation catalyst comprises V2O5 modified anatase, wherein the surface area of said V2O5 modified anatase ranges from 10 m2/g to 150 m2/g. 23. The process according to claim 19, wherein the temperature ranges from 100° C. to 500° C. and the pressure ranges from 0 psig to 250 psig. 24. The process according to claim 19, wherein the temperature ranges from 100° C. to 350° C. and the pressure ranges from 0 psig to 100 psig. 25. The process according to claim 19, further comprising feeding a diluent gas selected from at least one of the group consisting of nitrogen, argon, oxygen, air, hydrogen, and helium to said first reactor zone, and wherein the molar ratio of said diluent gas to said n-butanol ranges from 0.1:1 to 20:1. 26. The process according to claim 19, wherein the single-pass yield of said n-butanol to said 2-ethylhexanal and said 2-ethylhexanol ranges from 5 percent to 60 percent. 27. A process for the preparation of 2-ethylhexanol comprising (A) feeding ethanol to a first reactor zone comprising a first heterogeneous dehydrogenation catalyst to produce an acetaldehyde containing stream;(B) feeding said acetaldehyde containing stream to a second reactor zone comprising a first heterogeneous aldol condensation catalyst to produce a crotonaldehyde containing stream;(C) feeding said crotonaldehyde containing stream to a third reactor zone comprising a first hydrogenation catalyst to produce a n-butanol containing stream;(D) feeding said n-butanol containing stream to a fourth reactor zone comprising a second heterogeneous dehydrogenation catalyst to produce a butyraldehyde containing stream;(E) feeding said butyraldehyde containing stream to a fifth reactor zone comprising a second heterogeneous aldol condensation catalyst to produce a 2-ethylhexanal and/or 2-ethylhexenal containing stream; and(F) feeding said 2-ethylhexanal and/or 2-ethylhexenal containing stream to a sixth reactor zone comprising a second hydrogenation catalyst to produce a crude product comprising 2-ethylhexanolwherein said process is conducted in the vapor phase.