초록 ▼

A commercially available anatase titania catalyst is shown to be catalytically active towards the formation of methacrolein from formaldehyde and propionaldehyde with conversions and selectivities close to 90%. This titania catalyst is readily available, non-toxic, and can be used with formaldehyde

A commercially available anatase titania catalyst is shown to be catalytically active towards the formation of methacrolein from formaldehyde and propionaldehyde with conversions and selectivities close to 90%. This titania catalyst is readily available, non-toxic, and can be used with formaldehyde and a variety of other aldehyde compounds to make α,β-unsaturated aldehyde compounds. This process benefits from low raw material costs and is economically advantaged due to the elimination of catalyst separation. An additional advantage of this method involves the ability of the catalyst to be fully regenerated after a calcination step at 450° C. in air. This process shows promising stability and selectivity during lifetime studies, particularly when performed in the presence of a hydrogen carrier gas.

대표청구항 ▼

1. A process for preparing an α,β-unsaturated aldehyde compound, comprising: contacting a formaldehyde source, a hydrogen containing diluent gas, and an aldehyde with a heterogeneous anatase titania catalyst under vapor-phase condensation conditions to obtain the α,β-unsaturated aldehyde compound;wh

1. A process for preparing an α,β-unsaturated aldehyde compound, comprising: contacting a formaldehyde source, a hydrogen containing diluent gas, and an aldehyde with a heterogeneous anatase titania catalyst under vapor-phase condensation conditions to obtain the α,β-unsaturated aldehyde compound;wherein the α,β-unsaturated aldehyde compound has the general formula (I): wherein R is a hydrogen or a hydrocarbon group having 1-12 carbons wherein the molar ratio of the formaldehyde to aldehyde reagents is from 0.2 to 5. 2. The process according to claim 1, wherein the formaldehyde source and the aldehyde are contacted with the heterogeneous anatase titania catalyst at a temperature of about 100° C. to about 500° C. 3. The process according to claim 1, wherein the formaldehyde source and the aldehyde are contacted with the heterogeneous anatase titania catalyst at a temperature of about 100° C. to about 300° C. 4. The process according to claim 1, wherein the formaldehyde source comprises trioxane, formaldehyde, formalin, or a combination thereof. 5. The process of claim 1, wherein the aldehyde comprises acetaldehyde, propionaldehyde, n-butyraldehyde, pentanal, hexanal, heptanal, octanal, nonanal, decanal, undecanal, dodecanal, 3-methylbutyraldehyde, 3-ethylbutyraldehyde and 3-ethylpentanal, but-3-enal, pent-3-enal, 2-cyclohexylacetaldehyde, 2-phenylacetaldehyde, or a combination thereof. 6. The process according to claim 1, wherein the aldehyde is a linear saturated aldehyde comprising acetaldehyde, propionaldehyde, n-butyraldehyde, pentanal, hexanal, heptanal, octanal, nonanal, decanal, undecanal, dodecanal, or a combination thereof. 7. The process according to claim 1, wherein the aldehyde is a branched saturated aldehyde comprising 3-methylbutyraldehyde, 3-ethylbutyraldehyde and 3-ethylpentanal, or a combination thereof. 8. The process according to claim 1, wherein the aldehyde is a cyclic or an aromatic substituted aldehyde comprising 2-cyclohexylacetaldehyde, 2-phenylacetaldehyde, or a combination thereof. 9. The process according to claim 1, wherein the heterogeneous anatase titania catalyst is regenerated with a calcination step at 450° C. in air. 10. The process according to claim 1, wherein the α,β-unsaturated aldehyde compound is produced with a space time yield greater than 8 moles aldehyde/kg catalyst/hr. 11. A process for preparing methacrolein, comprising: contacting a formaldehyde source, a hydrogen containing diluent gas, and a propionaldehyde with a heterogeneous anatase titania catalyst under vapor-phase condensation conditions to obtain methacrolein;wherein methacrolein has the general formula (I): 12. The process according to claim 11, wherein the formaldehyde source comprises trioxane, formaldehyde, formalin, or a combination thereof. 13. The process according to claim 11, wherein the methacrolein is produced with a space time yield greater than 8 moles methacrolein/kg catalyst/hr. 14. The process according to claim 11, wherein the methacrolein is used to produce isobutyraldehyde, methacrylonitrile, methacrylic acid, methyl methacrylate, poly(methyl methacrylate), or a combination thereof. 15. A process for preparing an α,β-unsaturated aldehyde compound, comprising: contacting an aqueous formaldehyde source, a hydrogen containing diluent gas, and an aldehyde with a heterogeneous anatase titania catalyst under vapor-phase condensation conditions to obtain the α,β-unsaturated aldehyde compound;wherein the α,β-unsaturated aldehyde compound has the general formula (I): wherein R is a hydrogen or a hydrocarbon group having 1-12 carbons; wherein the molar ratio of the formaldehyde to aldehyde reagents is from 0.2 to 5. 16. The process according to claim 15, wherein the α,β-unsaturated aldehyde compound is produced with a space time yield greater than 8 moles aldehyde/kg catalyst/hr. 17. The process according to claim 11, wherein the concentration of hydrogen in the diluent gas is within a range of 10 to 90 mole %. 18. The process according to claim 15, wherein the concentration of hydrogen in the diluent gas is within a range of 10 to 90 mole %.