Used in the preparation of quinone and p-benzoquinone in sio 2 Catalyst loaded with cuo and preparation method thereof
A p-benzoquinone and catalyst technology, applied in the field of CuO/SiO2 catalyst preparation, can solve the problems of low conversion rate of raw materials, many side reactions, expensive raw materials, etc., and achieve high catalytic activity, simple preparation method, and easy recovery.
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Embodiment 1
[0032] Weigh about 0.524g of copper acetylacetonate (Cu(acac) 2 ) was placed in a sublimator in a chemical vapor deposition device, and 2.0 g of nanoscale SiO 2 The particles are placed in the fluidized bed reactor, the chemical vapor deposition device is turned on, the vacuum degree is adjusted to 0.08MPa, and N 2 The carrier gas was 80 mL / min, the temperature of the fluidized bed reactor was adjusted to 200 °C, and the SiO 2 After the particles were dried for 2 hours, air was introduced into the sublimator at a flow rate of 80-100 standard ml / min, the temperature of the sublimator was adjusted to 190 °C, and the fluidized bed reactor was re-adjusted to 260 °C. ) 2 After the complete sublimation, the temperature of the fluidized bed reactor was maintained for 2h, and the vapor deposition device was closed, so that the CuO / SiO 2 (1 mmol / g) catalyst preparation was completed.
Embodiment 2
[0036] Weigh about 0.263g of copper acetylacetonate (Cu(acac) 2 ) was placed in a sublimator in a chemical vapor deposition device, and 2.0 g of nanoscale SiO 2 The particles were placed in the fluidized bed reactor, the chemical vapor deposition device was turned on, the vacuum degree was adjusted to 0.08MPa, and N 2 The carrier gas was 80 mL / min, the temperature of the fluidized bed reactor was adjusted to 200 °C, and the SiO 2 After the particles were dried for 2 hours, air was introduced into the sublimator at a flow rate of 80-100 standard ml / min, the temperature of the sublimator was adjusted to 190 °C, and the fluidized bed reactor was re-adjusted to 300 °C. ) 2 After the complete sublimation, the temperature of the fluidized bed reactor was maintained for 2h, and the vapor deposition device was closed, so that the CuO / SiO 2 (0.5 mmol / g) catalyst preparation was completed.
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