Copper aluminum catalyst used for 1,4-butynediol production
The present invention is generally related to a novel catalytic composition and a method for the production of 1,4 -butynediol by catalytic ethynylation of formaldehyde, the said method is known as the Reppe reaction. The invented catalyst with lower copper content would provide an advantageous combination of improved utilization efficiency of copper, reduced copper leaching and enhanced filterability, and has minimal to no impact on catalytic activity.
1 . A catalytic composition, comprising:
5% to 35% by weight of Cu, calculated as CuO;
0.1% to 7% by weight of Bi, calculated as Bi 2 O 3 ; and
60% to 95% by weight of Al, calculated as Al 2 O 3 .
2 . The catalytic composition according to claim 1 , wherein a Cu to Bi molar ratio is 55-300:1.
3 . The catalytic composition according to claim 2 , wherein a Cu to Bi molar ratio is 80-200:1.
4 . The catalytic composition according to claim 1 , wherein the catalytic composition comprises 10% to 30% by weight of Cu, calculated as CuO.
5 . The catalytic composition according to claim 1 , wherein the catalytic composition comprises 0.2% to 4% by weight of Bi, calculated as Bi 2 O 3 .
6 . The catalytic composition according to claim 1 , wherein the catalytic composition comprises 70% to 90% by weight of Al, calculated as Al 2 O 3 .
7 . The catalytic composition according to claim 1 , wherein the Al 2 O 3 has a D 50 of 0.1 to 20 μm.
8 . The catalytic composition according to claim 6 , wherein the Al 2 O 3 has a D 50 of 0.2 to 15 μm.
9 . The catalytic composition according to claim 1 , wherein the catalytic composition has a D 50 of 0.5 to 40 μm.
10 . The catalytic composition according to claim 9 , wherein the catalytic composition has a D 50 of 1 to 30 μm.
11 . A process for producing a catalytic composition according to claim 1 comprising:
1) precipitating an acidic copper-containing aqueous solution with precipitation agent, on a particulate carrier; and
2) drying the treated particulate carrier and calcining at 300 to 800° C. to form the catalytic composition;
wherein the particulate carrier comprises alumina.
12 . A process for hydrogenation, dehydrogenation, hydrogenolysis, or ethynylation comprising reacting in the presence of the catalytic composition according to claim 1 .