A method for preparing lubricating oil base oil by cocatalytic conversion of waste plastics and naphthenes
A technology of lubricating oil base oil and naphthenes, which is applied in the field of co-catalytic conversion of waste plastics and naphthenes to prepare lubricating oil base oils, can solve the problems of harsh reaction conditions, complex processes, and environmental pollution, and achieve easy industrial production and simple process Effect
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Embodiment 1
[0018] Example 1 Rh / Nb 2 o 5 Catalyst preparation
[0019] First, the Nb was measured by the incipient wetness method 2 o 5 The zero charge point of is about 2.5, prepare 500mL 200mg·L -1 of [(NH 4 ) 3 Rh] 6+ , in order to achieve the highest adsorption capacity of Rh ions, adjust the pH value of the solution to 10 with ammonia water, and Nb 2 o 5 The precursors were mixed and shaken in a shaker for 1 h. Filtrate after the end, use ICP to measure the Rh ion content of the filtrate, and combine the Rh ion content of the initial ammonium hexachlororhodium acid triammonium solution, calculate the Rh content on the adsorption precursor to be 1.5 μ mol / m 2 . The solid was dried overnight at room temperature and then reduced at 400°C under a hydrogen atmosphere to obtain Rh / Nb 2 o 5 Catalyst, its X-ray diffraction pattern is as follows figure 1 shown.
Embodiment 2
[0020] The preparation of embodiment 2 Pt / HZSM-5 catalyst
[0021] First, the zero charge point of HZSM-5 was measured to be about 3.0 by incipient wetness method, and 500mL of 100mg L was prepared -1 of [(NH 4 ) 3 Pt] 2+ , in order to achieve the highest Pt ion adsorption, the pH of the solution was adjusted to 9.5, mixed with the HZSM-5 precursor and shaken in a shaker for 1 h. After filtering, use ICP to measure the Pt ion content of the filtrate, combined with the Pt ion content of the initial ammonium chloroplatinate solution, calculate the Pt content on the adsorption precursor to be 1.0 μmol / m 2 . The solid was dried overnight at room temperature, and then reduced at 400°C under a hydrogen atmosphere to prepare the Pt / HZSM-5 catalyst.
Embodiment 3
[0022] Example 3 Rh / Nb in autoclave reactor 2 o 5 Catalytic co-catalytic conversion of waste plastics and decahydronaphthalene derived from low-density polyethylene
[0023] The prepared Rh / Nb in the autoclave reactor 2 o 5 The catalyst was tested for its activity in the cocatalytic conversion of waste plastics and decahydronaphthalene derived from low-density polyethylene. Weigh 0.05g of catalyst, 1.0g of waste plastic, 20mL of decahydronaphthalene, and continuously stir and react at 300°C and 2.0MPa hydrogen pressure for 36h. After cooling down, separate the catalyst to obtain 2.0% C1-C5 low-carbon alkane gas, 95% C6-C35 long-chain naphthenic liquids and waxes, and 3% plastic residue. The obtained liquid product is separated, and it is analyzed by chromatography-mass spectrometry and time-of-flight mass spectrometry respectively, and it is found that lubricating oil base oil is obtained with a yield of 90%. The specific process is as follows figure 2 shown.
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