초록 ▼

The invention relates to a catalyst composition comprising a mixed oxide of vanadium, titanium, and phosphorus. The titanium component is derived from a water-soluble, redox-active organo-titanium compound. The catalyst composition is highly effective at facilitating the vapor-phase condensation of

The invention relates to a catalyst composition comprising a mixed oxide of vanadium, titanium, and phosphorus. The titanium component is derived from a water-soluble, redox-active organo-titanium compound. The catalyst composition is highly effective at facilitating the vapor-phase condensation of formaldehyde with acetic acid to generate acrylic acid, particularly using an industrially relevant aqueous liquid feed. Additionally, the catalyst composition is catalytically active towards the formation of acrylic acid from methylene diacetate and methacrylic acid from methylene dipropionate; both reactions are carried out with high space time yields.

대표청구항 ▼

1. A process for preparing a 2,3-unsaturated carboxylic acid comprising: contacting a formaldehyde source, a carboxylic acid, and a diluent gas with a condensation catalyst under vapor-phase condensation conditions to obtain the 2,3-unsaturated carboxylic acid;wherein the condensation catalyst compr

1. A process for preparing a 2,3-unsaturated carboxylic acid comprising: contacting a formaldehyde source, a carboxylic acid, and a diluent gas with a condensation catalyst under vapor-phase condensation conditions to obtain the 2,3-unsaturated carboxylic acid;wherein the condensation catalyst comprises a mixed oxide of vanadium (V), titanium (Ti), and phosphorus (P);wherein the diluent gas comprises from about 3 mol % to about 5 mol ° le oxygen, based on the total moles of feed; andwherein the process has a selectivity of greater than about 40% and a conversion of greater than about 40%;wherein the formaldehyde source is a methylene dicarboxylate having the general formula (I): and wherein R is selected from the group consisting of a hydrogen, methyl, ethyl, propyl, iso-propyl, and an alkyl group having 1 to 8 carbons. 2. The process according to claim 1, wherein the diluent gas comprises from about 3 mol % to about 4 mol % oxygen, based on the total moles of feed. 3. The process according to claim 1, wherein the diluent gas comprises from about 3.5 mol % to about 4 mol % oxygen, based on the total moles of feed. 4. The process according to claim 1, wherein the process has a selectivity of greater than about 60% and a conversion of greater than about 50%. 5. The process according to claim 1, wherein the condensation catalyst has the formula VTiaPbOc, wherein a is a number from 0.3 to 6.0, b is a number from 2.0 to 13.0, and c is the number of atoms required to satisfy the valences of the components other than oxygen. 6. The process according to claim 1, wherein the titanium component is the residue of a water-soluble, redox-active organo-titanium compound. 7. The process according to claim 6, wherein the organo-titanium compound comprises titanium(IV) bis(ammonium lactate) dihydroxide. 8. The process according to claim 1, wherein the condensation reaction has a total space feed velocity of from 50 to 400 moles of feed/(kg catalyst·hr). 9. The process according to claim 1, wherein the space time yield of the 2,3 unsaturated carboxylic acid is from about A to about 200 moles of 2,3 unsaturated carboxylic acid per kg catalyst per hour. 10. A process for preparing acrylic acid comprising: contacting a formaldehyde source, acetic acid, and a diluent gas with a condensation catalyst under vapor-phase condensation conditions to obtain the acrylic acid;wherein the condensation catalyst comprises a mixed oxide of vanadium (V), titanium (Ti), and phosphorus (P);wherein the diluent gas comprises from about 3 mol % to about 5 mol % oxygen, based on the total moles of feed (liquids and diluent gas); andwherein the process has a selectivity of greater than 40% and a conversion of greater than 40%wherein the formaldehyde source comprises a methylene diacetate having the general formula (I): and wherein R is a hydrogen. 11. The process according to claim 10, wherein the diluent gas comprises from about 3.5 mol % to about 4 mol % oxygen, based on the total moles of feed (liquids and diluent gas). 12. The process according to claim 10, wherein the process has a selectivity of greater than 60% and a conversion of greater than 50%. 13. The process according to claim 10, wherein the titanium component is the residue of a water-soluble, redox-active organo-titanium compound and wherein the organo-titanium compound comprises titanium(IV) bis(ammonium lactate) dihydroxide. 14. A process for preparing methacrylic acid comprising: contacting a formaldehyde source, propionic acid, and a diluent gas with a condensation catalyst under vapor-phase condensation conditions to obtain the methacrylic acid;wherein the condensation catalyst comprises a mixed oxide of vanadium (V), titanium (Ti), and phosphorus (P);wherein the diluent gas comprises from about 3 mol % to about 5 mol % oxygen, based on the total moles of feed (liquids and diluent gas); andwherein the process has a selectivity of greater than 40% and a conversion of greater than 40%wherein the formaldehyde source comprises a methylene dipropionate having the general formula (I): and wherein R is a methyl group. 15. The process according to claim 14, wherein the diluent gas comprises from about 3.5 mol % to about 4 mol % oxygen, based on the total moles of feed (liquids and diluent gas). 16. The process according to claim 14, wherein the process has a selectivity of greater than 60% and a conversion of greater than 50%. 17. The process according to claim 14, wherein the titanium component is the residue of a water-soluble, redox-active organo-titanium compound and wherein the organo-titanium compound comprises titanium(IV) bis(ammonium lactate) dihydroxide.