Hydrogenation catalyst, preparation method and applications thereof
A hydrogenation catalyst and catalyst technology, which are used in chemical instruments and methods, preparation of hydroxyl compounds, preparation of organic compounds, etc., can solve the problem that copper species cannot be converted into active center acetylene copper complexes, active components have poor dispersion, and The problem of easy loss of components, etc., achieves the effects of concentrated distribution, slow heating rate, and improved catalyst activity
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Embodiment 1
[0041] (1) Weigh 252.5g Cu(NO 3 ) 2 . 3H 2 O, 7.3g Bi(NO 3 ) 2 . 5H 2 O and 10g polyethylene glycol are mixed with 200mL solution;
[0042] (2) Weigh 100g of self-made alumina carrier (specific surface 230, pore volume 0.86);
[0043](3) Weigh 80mL solution to impregnate the alumina carrier for one stage. After impregnation, the catalyst is dried at 120°C for 4 hours, and then weigh 40mL solution for two stage impregnation. After impregnation, the catalyst is dried at 110°C for 5 hours; After the end, roasting is carried out, wherein the heating rate of 0~130°C is 1.5°C / min, the heating rate of 130~180°C is 0.7°C / min, the heating rate of 180~260°C is 5°C / min, and the heating rate of 260~500°C 2.5°C / min, 500°C constant temperature for 3 hours to obtain catalyst A, whose physical and chemical properties are shown in Table 1.
Embodiment 2
[0045] Other conditions are the same as in Example 1, except that the quality of polyethylene glycol in the prepared solution is 8g. During the catalyst roasting process, the heating rate at 0~130°C is 1.6°C / min, the heating rate at 130~180°C is 0.9°C / min, and the heating rate at 180~180°C The heating rate at 260°C was 5.5°C / min, and the heating rate at 260-500°C was 2.3°C / min. Catalyst B was obtained, and its physical and chemical properties are shown in Table 1.
Embodiment 3
[0047] Other conditions are the same as in Example 1, except that the quality of polyethylene glycol in the prepared solution is changed to 12g. During the catalyst roasting process, the heating rate at 0~130°C is 1.4°C / min, and the heating rate at 130~180°C is 0.6°C / min. The heating rate was 4.5 °C / min at 180-260 °C, and 2.6 °C / min at 260-500 °C. Catalyst C was obtained, and its physical and chemical properties are shown in Table 1.
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