Patent ID: 7161014

Claim:
A process for preparing a reaction product comprising an alpha-methylene lactone of the Formula II, said process comprising reacting a lactone of the Formula I with formaldehyde wherein R is selected from the group consisting of hydrogen, methyl, ethyl, and straight or branched C 3 –C 5 alkyl; at a temperature in the range of from about 150° C. to about 450° C. in the presence of a grafted catalyst; said grafted catalyst being made by a process comprising: (a) contacting (i) porous silica, optionally containing a first element, said first element being one, two or three members selected from the group consisting of aluminum, zirconium, and titanium, said silica having a pore volume of at least 0.4 cc/g attributable to pores having pore diameters between 65 and 3200 Angstroms, with (ii) a solution comprising a solvent and an organic compound of a second element, said second element being one, two or three members selected from the group consisting of potassium, barium and rubidium; (b) drying the product of step (a) to remove at least a portion of said solvent; (c) heating the product of step (b) to a temperature in the range of 350° C. to 550° C. to produce a catalyst precursor; (d) flushing at a preselected flow rate an oxygen-containing gas over said catalyst precursor either during step (c), or after step (c) while the temperature is still in the range of 350° C. to 550° C. to produce a catalyst candidate in which the second element is present in said catalyst candidate in an amount from about 0.1% to about 40% by weight of the combined weight of the catalyst candidate and the second element; (e) determining by porosimetry whether said catalyst candidate has a pore volume of at least about 0.3 cubic centimeters per gram of catalyst attributable to pores having a diameter between 65 and 3200 Angstroms; and (f) if said catalyst candidate does not have a pore volume of at least about 0.3 cubic centimeters per gram of catalyst attributable to pores having a diameter between 65 and 3200 Angstroms, repeating, optionally more than once, steps (a) through (e) using in step (d) flow rates successively greater than said preselected flow rate until the catalyst candidate has a pore volume of at least about 0.3 cubic centimeters per gram of catalyst attributable to pores having a diameter between 65 and 3200 Angstroms; (g) contacting the material produced in step (f) with a second solution of zirconium, aluminum or titanium alkoxides dissolved in a second solvent, said alkoxides containing from one to 20 carbon atoms; (h) filtering the material of step (g); (i) drying the product of step (h) to remove at least a portion of said second solvent; (j) heating the product of step (b) to a temperature in the range of 350° C. to 550° C.; and (k) flushing at a preselected flow rate an oxygen-containing gas over the product of step (j) either during step (j), or after step (j) while the temperature is still in the range of 350° C. to 550° C. to produce the grafted catalyst.