PROCESS FOR THE PREPARATION OF PROPANE-1,3-DIOL BY VAPOR PHASE HYDROGENATION OF 3-HYDROXYPROPANAL, BETA-PROPIOLACTONE, OLIGOMERS OF BETA-PROPIOLACTONE, ESTERS OF 3-HYDROXYPROPANOIC ACID OR MIXTURES THEREOF
View Patent ↗A process is described for the production of propane-1,3-diol. The process comprises subjecting a vaporous feed mixture comprising a hydrogen-containing gas and a feedstock selected from 3-hydroxypropanal, β-propiolactone, oligomers of β-propiolactone, esters of 3-hydroxypropanoic acid, and mixtures of two or more thereof to hydrogenation conditions in a hydrogenation zone in the presence of a heterogeneous hydrogenation catalyst, and recovering a reaction product comprising propane-1,3-diol.
1. A process for the production of propane-1,3-diol which comprises
forming a vaporous feed mixture comprising a hydrogen-containing gas and a substantially anhydrous feedstock selected from β-propiolactone, oligomers of β-propiolactone, esters of 3-hydroxypropanoic acid, and mixtures of two or more thereof,
supplying the vaporous feed mixture to a hydrogenation zone containing a heterogeneous hydrogenation catalyst selected from reduced copper oxide/zinc oxide hydrogenation catalysts, reduced manganese-promoted copper catalysts, reduced copper chromite catalysts and reduced promoted copper chromite catalysts at a temperature of from about 130° C. to about 180° C. and a feed pressure to the hydrogenation zone of from about 50 psia (about 344.74 kpa) to about 2000 psia (13789.52 kPa) said hydrogenation conditions effective for hydrogenating feedstock to propane-1,3-diol, and
recovering from the hydrogenation zone a reaction product comprising propane-1,3-diol.
2. The process according to claim 1 , wherein the feedstock comprises an alkyl ester or a hydroxyalkyl ester of 3-hydroxypropanoic acid.
3. The process according to claim 1 wherein the hydrogenation is effected using a fixed bed of a granular hydrogenation catalyst.
4. The process according to claim 1 wherein the hydrogen-containing gas:feedstock molar ratio in the vaporous feed mixture is in the range of from about 50:1 to about 1000:1.
5. The process according to claim 1 , wherein the feed temperature to the hydrogenation zone is from about 135° C. to about 150 ° C.
6. The process according to claim 1 wherein the feed pressure to the hydrogenation zone is from about 350 psia (about 2413.17) to about 1000 psia (about 6894.76 kPa).
7. The process according to claim 1 wherein the feedstock is supplied to the first hydrogenation zone at a rate corresponding to a liquid hourly space velocity of from about 0.05 to about 5.0 h −1 .