Production of tetrahydrofuran

Claim 2

A process for converting acrolein into tetrahydrofuran which comprises (1) forming 2-vinyl-5-methyl-1,3-dioxane by the acid-catalyzed condensation of acrolein with 2-methyl-1,3-propanediol; (2) hydroformylation of the 2-vinyl-5-methyl-1,3-dioxane with carbon monoxide and hydrogen in the presence of a hydroformylation catalyst at a temperature between about 25° and 200° C and a pressure between about 15 and 300 psi to produce a mixture of 2-(5'-methyl-1',3'-dioxane)propionaldehyde and 3-(5'-methyl-1',3'-dioxane)propionaldehyde; and (3) hydrogenating said mixture of propionaldehydes with hydrogen in the presence of a hydrogenation catalyst at a temperature between about 180° and 225° C and a pressure between about 100 and 1000 psi in an aqueous medium maintained at a pH between about 0.2 and 3 with a water-soluble acid to produce a product mixture of tetrahydrofuran and 2-methyl-1,3-propanediol, and recovering the tetrahydrofuran from the product mixture.

Claim 3

A process for producing tetrahydrofuran which comprises (1) continuously feeding and reacting 2-methyl-1,3-propanediol and acrolein to form 2-vinyl-5-methyl-1,3-dioxane in a condensation reaction zone; (2) continuously withdrawing the 2-vinyl-5-methyl-1,3-dioxane from said condensation reaction zone and continuously feeding the 2-vinyl-5-methyl-1,3-dioxane into a hydroformylation reaction zone to produce a mixture of 2-(5-methyl-1',3'-dioxane)propionaldehyde and 3-(5'-methyl-1',3'-dioxane)propionaldehyde in the presence of a hydroformylation catalyst at a temperature between about 25° and 200° C and a pressure between about 15 and 300 psi; (3) continuously withdrawing the propionaldehyde mixture and catalyst from the hydroformylation reaction zone; (4) continuously separating and recycling the hydroformylation catalyst to the hydroformylation reaction zone; (5) continuously feeding and contacting the propionaldehyde mixture with hydrogen in a hydrogenation zone in the presence of a hydrogenation catalyst at a temperature between about 180° and 225° C and a pressure between about 100 and 1000 psi in an aqueous medium maintained at a pH between about 0.2 and 3 with a water-soluble acid to produce a product mixture of tetrahydrofuran and 2-methyl-1,3-propanediol; (6) continuously recovering the tetrahydrofuran and 2-methyl-1,3-propanediol as separate components; and (7) continuously recycling the 2-methyl-1,3-propanediol to the first step condensation reaction zone.

Claim 4

A process for producing tetrahydrofuran which comprises (1) continuously feeding and reacting 2-methyl-1,3-propanediol and acrolein to form 2-vinyl-5-methyl-1,3-dioxane in a condensation reaction zone; (2) continuously withdrawing the 2-vinyl-5-methyl-1,3-dioxane from said condensation reaction zone and continuously feeding the 2-vinyl-5-methyl-1,3-dioxane into a hydroformylation reaction zone to produce a mixture of 2-(5-methyl-1',3'-dioxane)propionaldehyde and 3-(5'-methyl-1',3'-dioxane)propionaldehyde in the presence of a hydroformylation catalyst at a temperature between about 25° and 200° C and a pressure between about 15 and 300 psi; (3) continuously withdrawing the propionaldehyde mixture and catalyst from the hydroformylation reaction zone; (4) continuously separating and recycling the hydroformylation catalyst to the hydroformylation reaction zone; (5) continuously feeding and contacting the propionaldehyde mixture with hydrogen in a hydrogenation zone in the presence of a hydrogenation catalyst at a temperature between about 180° and 225° C and a pressure between about 100 and 1000 psi in an aqueous medium maintained at a pH between about 0.2 and 3 with a water-soluble acid to produce a product mixture of tetrahydrofuran and 2-methyl-1,3-propanediol; (6) continuously recovering the tetrahydrofuran and 2-methyl-1,3-propanediol as separate components; and (7) continuously recycling the 2-methyl-1,3-propanediol to the first step condensation reaction zone.

Claim 5

A process for converting acrolein into tetrahydrofuran which comprises (1) forming 2-vinyl-5-methyl-1,3-dioxane by the acid-catalyzed condensation of acrolein with 2-methyl-1,3-propanediol; (2) hydroformylation of the 2-vinyl-5-methyl-1,3-dioxane with carbon monoxide and hydrogen in the presence of a hydroformylation catalyst at a temperature between about 80° and 120° C and a pressure between about 300 and 3000 psi to produce a mixture of 2-(5'-methyl-1',3'-dioxane)propionaldehyde and 3-(5'-methyl-1',3'-dioxane)propionaldehyde, and increasing the temperature into the range between about 150° and 225° C to convert the propionaldehydes into a mixture of 2-(5'-methyl-1',3'-dioxane)propanol and 3-(5'-methyl-1',3'-dioxane)propanol; and (3) hydrogenating said mixture of propanols with hydrogen in the presence of a hydrogenation catalyst at a temperature between about 180° and 225° C and a pressure between about 100 and 1000 psi in an aqueous medium maintained at a pH between about 0.2 and 3 with a water-soluble acid to produce a product mixture of tetrahydrofuran and 2-methyl-1,3-propanediol, and recovering the tetrahydrofuran from the product mixture.

Claim 6

A process for converting acrolein into tetrahydrofuran which comprises (1) forming 2-vinyl-5-methyl-1,3-dioxane by the acid-catalyzed condensation of acrolein with 2-methyl-1,3-propanediol; (2) hydroformylation of the 2-vinyl-5-methyl-1,3-dioxane with carbon monoxide and hydrogen in the presence of a hydroformylation catalyst at a temperature between about 80° and 120° C and a pressure between about 300 and 3000 psi to produce a mixture of 2-(5'-methyl-1',3'-dioxane)propionaldehyde and 3-(5'-methyl-1',3'-dioxane)propionaldehyde, and increasing the temperature into the range between about 150° and 225° C to convert the propionaldehydes into a mixture of 2-(5'-methyl-1',3'-dioxane)propanol and 3-(5'-methyl-1',3'-dioxane)propanol; and (3) hydrogenating said mixture of propanols with hydrogen in the presence of a hydrogenation catalyst at a temperature between about 180° and 225° C and a pressure between about 100 and 1000 psi in an aqueous medium maintained at a pH between about 0.2 and 3 with a water-soluble acid to produce a product mixture of tetrahydrofuran and 2-methyl-1,3-propanediol, and recovering the tetrahydrofuran from the product mixture.