A kind of dimethyl terephthalate (DMT) hydrogenation catalyst and preparation method thereof
A technology of dimethyl cyclohexanedicarboxylate and catalyst, which is applied in the field of catalysis, can solve problems such as low yield, high equipment cost and operating cost, and reduce reaction pressure, and achieve high reaction efficiency, low cost, and improved hydrogenation activity Effect
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Embodiment 1
[0032] Take by weighing 50.0g process and dry pine activated carbon (400 mesh, specific surface area 1200m 2 / g, pore volume 0.8ml / g), added to 200mL ammonium tungstate solution containing tungsten mass fraction of 10%, stirred and impregnated for 2h, filtered, and the filter cake was dried in an oven at 120°C for 5h to obtain ammonium tungstate loaded Activated carbon precursor. Put the precursor in a tube furnace, under a hydrogen atmosphere, the gas flow rate is 5ml / g min, the furnace temperature is raised to 400°C at 5°C / min, and the carbonization is kept for 6h. After the end, it is lowered to room temperature, and a small amount of air is introduced. passivation to obtain a tungsten carbide-activated carbon composite carrier with a mass fraction of tungsten carbide of 5%.
[0033] According to the mass content of metal ruthenium in the catalyst as 5%, the equal volume impregnation method is used to impregnate the ruthenium trichloride hydrochloric acid solution on the t...
Embodiment 2
[0035] Take by weighing 50.0g process and dry pine activated carbon (400 mesh, specific surface area 1200m 2 / g, pore volume 0.8ml / g), join in the ammonium paramolybdate solution that 200mL contains molybdenum mass fraction and be 5%, stir and impregnate 4h, filter, and filter cake is dried 5h in 120 ℃ oven and obtains loaded with paramolybdate Ammonium activated carbon precursor. Put the precursor in a tube furnace, under a hydrogen atmosphere, the gas flow rate is 5ml / g min, the furnace temperature is raised to 400°C at 5°C / min, and the carbonization is kept for 6h. After the end, it is lowered to room temperature, and a small amount of air is introduced. passivation to obtain a molybdenum carbide-activated carbon composite carrier with a molybdenum carbide mass fraction of 3%.
[0036] According to the mass content of metal ruthenium in the catalyst as 5%, the equal volume impregnation method is used to impregnate the ruthenium trichloride hydrochloric acid solution on the...
Embodiment 3
[0038] Take by weighing 50.0g process and dry pine activated carbon (400 mesh, specific surface area 1200m 2 / g, pore volume 0.8ml / g), added to 200mL ammonium paratungstate solution containing 10% tungsten mass fraction, stirred and impregnated for 2h, filtered, and the filter cake was dried in an oven at 120°C for 5h to obtain an activated carbon precursor loaded with ammonium paratungstate. Put the precursor in a tube furnace, under a hydrogen atmosphere, the gas flow rate is 5ml / g min, the furnace temperature is raised to 400°C at 5°C / min, and the carbonization is kept for 6h. After the end, it is lowered to room temperature, and a small amount of air is introduced. passivation to obtain a tungsten carbide-activated carbon composite carrier with a mass fraction of tungsten carbide of 5%.
[0039] According to the mass content of metal ruthenium in the catalyst as 3%, the equal volume impregnation method is used to impregnate the ruthenium trichloride hydrochloric acid solut...
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