Process for production of alkenediols

Claim 2

A process for production of alkenediol comprising (A) contacting conjugated diene of 4 to about 12 carbon atoms with cupric bromide under bromination conditions; (B) contacting a product from (A) comprising dibromoalkene containing 4 to about 12 carbon atoms corresponding to the formula R 2 BrCCR:CRCBrR 2 or R 2 C:CRCBrRCBrR 2 wherein each R is independently hydrogen or an alkyl radical of 1 to about 8 carbon atoms consistent with the conjugated diene employed in (A), or a mixture of dibromoalkenes of said formulae wherein the R groups are identical, with alkali metal formate under hydrolysis conditions; (C) separating alkenediol from the product of (B); and (D) contacting cuprous bromide, alkali metal bromide and formic acid by-products from steps (A) and (B) with molecular oxygen under conditions effective to regenerate cupric bromide and alkali metal formate.

Claim 3

The process of claim 1 wherein the alkali metal formate is sodium formate.

Claim 4

The process of claim 1 wherein the conjugated diene is 1,3-butadiene.

Claim 5

The process of claim 3 wherein the alkali metal formate is sodium formate.

Claim 6

The process of claim 1 wherein a major portion of the dibromoalkene employed in (B) corresponds to the formula R 2 BrCCR:CRCBrR 2 .

Claim 7

The process of claim 1 wherein at least 75 mole % of the dibromoalkene employed in (B) corresponds to the formula R 2 BrCCR:CRCBrR 2 .

Claim 8

The process of either of claims 5 or 6 wherein said dibromoalkene corresponding to the formula R 2 BrCCR:CRCBrR 2 is 1,4-dibromo-2-butene.

Claim 9

The process of claim 1 wherein the dibromoalkene employed in (B) is 1,4-dibromo-2-butene.

Claim 10

A process for production of alkenediol comprising: (A) contacting conjugated diene of 4 to about 12 carbon atoms with cupric bromide under bromination conditions in an inert liquid medium; (B) contacting the product from (A) with alkali metal formate under hydrolysis conditions; (C) separating alkenediol from the product of (B); and (D) contacting solid cuprous bromide, alkali metal bromide and formic acid remaining after separation in (C) with molecular oxygen under conditions effective to regenerate cupric bromide and alkali metal formate.

Claim 11

A process for production of alkenediol comprising: (A) contacting conjugated diene of 4 to about 12 carbon atoms with cupric bromide under bromination conditions in an inert liquid medium; (B) contacting the product from (A) with alkali metal formate under hydrolysis conditions; (C) separating alkenediol from the product of (B); and (D) contacting solid cuprous bromide, alkali metal bromide and formic acid remaining after separation in (C) with molecular oxygen under conditions effective to regenerate cupric bromide and alkali metal formate.

Claim 12

The process of claim 9 wherein the conditions in (A) comprise a conjugated diene to cupric bromide molar ratio of about 0.52:1 to about 5:1 and a temperature of about 75° to about 150° C.

Claim 13

The process of claim 9 wherein the conditions in (B) comprise an alkali metal formate to dibromoalkene molar ratio of at least about 2:1, a concentration of alkali metal formate in water of about 5 to about 30 wt. %, and a temperature of about 80° to about 150° C.

Claim 14

The process of claim 9 wherein the conditions in (D) comprise a molecular oxygen partial pressure of about 20 to about 40 psig., a formic acid to alkali metal bromide molar ratio of about 0.5:1 to about 5:1 and a temperature of about 80° to about 120° C.

Claim 15

The process of claim 9 wherein alkali metal formate is present in (A).

Claim 16

The process of claim 9 wherein cupric bromide and alkali metal formate from (D) are recycled to (A).

Claim 17

The process of claim 9 wherein the conjugated diene is 1,3-butadiene.

Claim 18

A process for production of 2-butene-1,4-diol comprising the steps: (A) contacting 1,3-butadiene and cupric bromide in the presence of alkali metal formate and an inert liquid solvent for 1,3-butadiene under bromination conditions to form a reaction mixture comprising dibromobutenes, cuprous bromide and alkali metal formate; (B) substantially separating inert hydrocarbon solvent from the reaction mixture of (A); (C) combining the product remaining after separation in (B) with a solution of formic acid in water under hydrolysis conditions to form a reaction mixture comprising water, formic acid, 2-butene-1,4-diol, alkali metal formate, alkali metal bromide and cuprous bromide; (D) separating formic acid, water and a major portion of 2-butene-1,4-diol from the reaction mixture of (C) to form a concentrated slurry comprising alkali metal formate, alkali metal bromide, cuprous bromide and 2-butene-1,4-diol; (E) separating 2-butene-1,4-diol from the formic acid and water of (D); (F) contacting alkali metal formate, alkali metal bromide and cuprous bromide from (D) with molecular oxygen in the presence of formic acid and water under conditions effective to regenerate cupric bromide and alkali metal formate; (G) recycling cupric bromide and alkali metal formate from (F) to (A).

Claim 19

A process for production of 2-butene-1,4-diol comprising the steps: (A) contacting 1,3-butadiene and cupric bromide in the presence of alkali metal formate and an inert liquid solvent for 1,3-butadiene under bromination conditions to form a reaction mixture comprising dibromobutenes, cuprous bromide and alkali metal formate; (B) substantially separating inert hydrocarbon solvent from the reaction mixture of (A); (C) combining the product remaining after separation in (B) with a solution of formic acid in water under hydrolysis conditions to form a reaction mixture comprising water, formic acid, 2-butene-1,4-diol, alkali metal formate, alkali metal bromide and cuprous bromide; (D) separating formic acid, water and a major portion of 2-butene-1,4-diol from the reaction mixture of (C) to form a concentrated slurry comprising alkali metal formate, alkali metal bromide, cuprous bromide and 2-butene-1,4-diol; (E) separating 2-butene-1,4-diol from the formic acid and water of (D); (F) contacting alkali metal formate, alkali metal bromide and cuprous bromide from (D) with molecular oxygen in the presence of formic acid and water under conditions effective to regenerate cupric bromide and alkali metal formate; (G) recycling cupric bromide and alkali metal formate from (F) to (A).

Claim 20

The process of claim 16 wherein the concentrated slurry in (D) is washed with water and formic acid from (E) prior to contacting with molecular oxygen in (F).

Claim 21

The process of claim 17 wherein the formic acid and water in (F) are supplied by the water and formic acid recovered in (E).

Claim 22

The process of claim 16 wherein the formic acid and water in (F) are supplied by the water and formic acid recovered in (E).

Claim 23

The process of claim 16 wherein cupric bromide and alkali metal formate from (F) are recycled to (A) in an inert liquid medium which is the same as the inert liquid medium in (A).

Claim 24

The process of claim 16 wherein the alkali metal formate is sodium formate.