Dehydrogenation process of dimethylnaphthalene using metal catalyst
Disclosed herein is a process of producing high purity and high yield dimethylnaphthalene by dehydrogenating a dimethyltetralin isomer using a metal catalyst for dehydrogenation. The metal catalyst contains a carrier selected from alumina (Al 2 O 3 ), silica (SiO 2 ), a silica-alumina mixture and zeolite. The metal catalyst also contains 0.05 to 2.5% by weight of platinum (Pt), 0.1 to 3.0% by weight of tin (Sn) or indium (In), 0.5 to 15.0% by weight of at least one selected from the group consisting of potassium (K), magnesium (Mg) and cesium (Cs), 0.3 to 3.0% by weight of chlorine, and 0.01 to 3.0 % by weight of zinc (Zn) or gallium (Ga) as active components based on an element weight of the final catalyst.
1. A process of producing dimethylnaphthalene comprising:
dehydrogenating a dimethyltetralin isomer to produce dimethylnaphthalene in the presence of a metal catalyst for dehydrogenation,
wherein the carrier of the metal catalyst is alumina (Al 2 O 3 ), silica (SiO 2 ), a silica-alumina mixture, or zeolite, and
the metal catalyst also contains 0.05 to 2.5% by weight of platinum (Pt), 0.1 to 3.0% by weight of tin (Sn) or indium (In), 0.5 to 15.0% by weight of at least one selected from the group consisting of potassium (K), magnesium (Mg), and cesium (Cs), 0.3 to 3.0% by weight of chlorine, and 0.01 to 3.0% by weight of zinc (Zn) or gallium (Ga) as active components based on a weight of the resulting catalyst.
2. The process of producing dimethylnaphthalene according to claim 1 , wherein the metal catalyst further contains 0 to 4.0% by weight of sulfur based on the element weight of the final catalyst.
3. The process of producing dimethylnaphthalene according to claim 1 , wherein a pressure is 10 to 30 kgf/cm 2 during the dehydrogenating.
4. The process of producing dimethylnaphthalene according to claim 1 , wherein a weight hourly space velocity is 2 to 30 hr −1 during the dehydrogenating.
5. The process of producing dimethylnaphthalene according to claim 1 , wherein a temperature is 300 to 450° C. during the dehydrogenating.