Regeneration method of aluminum nitride loaded metal oxide catalyst
A technology for supporting metals and catalysts is applied in the field of regeneration of metal oxide catalysts, which can solve the problems of reducing catalytic performance and destroying catalyst structure, and achieves the effects of low regeneration temperature, improved reaction performance, and avoidance of catalyst structure damage.
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Embodiment 1
[0029] The catalyst adopts the method of CN 112642455 A Example 1 to prepare aluminum nitride-supported zinc oxide catalyst, fill 10g of 40-60 mesh extruded catalyst into a fixed-bed reactor and heat up to the reaction temperature, and the phthalate The phenol-methanol reaction raw material liquid is brought to the reactor, and the reaction conditions are: the molar ratio of catechol to methanol is 0.4:1, and the feeding space velocity of catechol is 0.25h -1 , the reaction temperature is 230°C, and the catalyst is regenerated after running for 4000 hours.
[0030] The catalyst regeneration conditions are:
[0031] (1) The catalyst is regenerated in a mixed gas atmosphere of hydrogen and argon, where the mass fraction of hydrogen in the mixed gas is 20%, the regeneration pressure is 2MPa, the regeneration temperature is 220°C, and the mass space velocity of hydrogen is 0.5h -1 , the regeneration time is 2h.
[0032] (2) The catalyst is washed under pure benzene solvent, and ...
Embodiment 2
[0039] The catalyst adopts the method of CN 112642455 A Example 2 to prepare aluminum nitride-supported ferric oxide catalyst. 10 g of 40-60 mesh extruded catalyst is packed into a fixed-bed reactor and heated to the reaction temperature. The catechol-methanol reaction raw material solution is brought to the reactor, the reaction conditions are: the molar ratio of catechol to methanol is 0.3:1, and the feed space velocity of catechol is 0.2h -1 , the reaction temperature is 250°C, and the catalyst is regenerated after running for 3500h.
[0040] The catalyst regeneration conditions are:
[0041] (1) The catalyst is regenerated in a mixed gas atmosphere of hydrogen and argon, where the mass fraction of hydrogen in the mixed gas is 40%, the regeneration pressure is 3MPa, the regeneration temperature is 260°C, and the mass space velocity of hydrogen is 1.0h -1 , The regeneration time is 3h.
[0042] (2) The catalyst is washed under pure benzene solvent, and the mass space veloc...
Embodiment 3
[0049]The catalyst adopts the method of CN 112642455 A Example 3 to prepare aluminum nitride-supported lanthanum oxide catalyst. Pack 10g of 40-60 mesh extruded catalyst into a fixed-bed reactor and heat up to the reaction temperature. The catechol-methanol reaction raw material solution is brought to the reactor by the feed pump. The reaction conditions are: catechol and The molar ratio of methanol is 0.2:1, and the feed space velocity of catechol is 0.3h -1 , the reaction temperature is 220°C, and the catalyst is regenerated after running for 4000 hours.
[0050] The catalyst regeneration conditions are:
[0051] (1) The catalyst is regenerated in a mixed gas atmosphere of hydrogen and argon, where the mass fraction of hydrogen in the mixed gas is 60%, the regeneration pressure is 4MPa, the regeneration temperature is 300°C, and the mass space velocity of hydrogen is 2.0h -1 , The regeneration time is 3.5h.
[0052] (2) The catalyst is washed under pure benzene solvent, a...
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