Catalyst for hydrogenation of waste solvent in production of anti-aging agent 6PPD and application of catalyst
A technology for catalysts and waste solvents, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, organic chemistry, etc., can solve the problem of generating more impurities, low alcohol content, and conversion of dehydrogenation catalysts Low efficiency and other problems, to achieve the effect of solving the impact of product quality, less types of impurities, and enriching the product chain
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Embodiment 1
[0024] A nickel / cobalt / aluminum catalyst was prepared with alumina as a carrier. Based on the total weight of the catalyst, the nickel content in the catalyst was 11.0%, the cobalt content was 5.4%, and the aluminum content was 10.0%. Pack the nickel / cobalt / aluminum catalyst in the fixed-bed reactor. During the production of anti-aging agent 6PPD, the waste solvent passes through the dehydration tower and the light component removal tower, and the overhead fraction enters the hydrogenation reactor. The reaction temperature is 145°C and the system pressure is 1.5MPa, liquid space velocity 0.10h -1 , the hydrogenation product enters the product tank after condensation. Analyzing the product composition of the product tank, the content of MIBC is 95.2%, and the content of MIBK is 4.3%.
Embodiment 2
[0026] A nickel / manganese / aluminum catalyst was prepared with alumina as a carrier. Based on the total weight of the catalyst, the nickel content in the catalyst was 10.0%, the manganese content was 2.5%, and the aluminum content was 13.7%. The nickel / manganese / aluminum catalyst is packed in the fixed bed reactor, and the waste solvent in the production process of anti-aging agent 6PPD passes through the dehydration tower and the light component removal tower, and the overhead fraction enters the hydrogenation reactor. The reaction temperature is 185°C and the system pressure is 2.5MPa, liquid space velocity 0.15h -1 , the hydrogenation product enters the product tank after condensation. Analyzing the product composition of the product tank, the content of MIBC is 98.2%, and the content of MIBK is 1.4%.
Embodiment 3
[0028] A nickel / zinc catalyst was prepared using silicon oxide as a carrier. Based on the total weight of the catalyst, the nickel content in the catalyst was 40.0%, and the zinc content in the catalyst was 28.0%. Pack the nickel / zinc catalyst in the fixed bed reactor, the waste solvent in the production process of anti-aging agent 6PPD passes through the dehydration tower and light component removal tower, and the overhead fraction enters the hydrogenation reactor, the reaction temperature is 215°C, and the system pressure is 3.5MPa , liquid space velocity 0.12h -1 , the hydrogenation product enters the product tank after condensation. The product composition of the product tank was analyzed, and the content of MIBC was 92.6%, and the content of MIBK was 6.9%.
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