A kind of nickel-based selective hydrogenation catalyst initial activation hydrothermal passivation method
A hydrogenation catalyst and selective technology, which can be used in catalyst activation/preparation, selective hydrorefining, chemical instruments and methods, etc., can solve the problems of long start-up period and impact on stable performance, and achieve a shortened start-up period. Effect
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Embodiment 1
[0021] Raw materials: Lanzhou Petrochemical C 6 -C 7 Distillation pyrolysis gasoline is used as a raw material, and the properties of the raw material are shown in Table 1:
[0022] Table 1 Raw material properties
[0023]
[0024] Catalyst reduction treatment
[0025] On a 100ml fixed-bed reactor, the catalyst loading amount is 100ml (mass 76g), and the catalyst reduction process is completed according to the following process conditions.
[0026] (1) Reduction pressure 0.5MPa;
[0027] (2) The amount of reduced hydrogen is 800 times the volume of the catalyst;
[0028] (3) Reduction process: raise the bed temperature to 150°C at a heating rate of 50°C / h and keep the temperature constant for 4 hours; raise the bed temperature to 250°C at a heating rate of 30°C / h and keep the temperature constant for 8 hours; Raise the bed temperature to 370°C at a heating rate of 30°C / h, and keep the temperature constant for 8 hours; raise the bed temperature to 430°C at a heating rate ...
Embodiment 2
[0044] The catalyst reduction process was carried out according to Example 1. The restoration conditions are as follows:
[0045] 1) Reducing pressure. 3.5MPa;
[0046] 2) The amount of hydrogen to be reduced is 550 times the volume of the catalyst;
[0047] 3) Reduction process: raise the bed temperature to 130°C at a heating rate of 20°C / h, and keep the temperature constant for 6 hours;
[0048] Raise the bed temperature to 230°C at a heating rate of 40°C / h and keep the temperature constant for 5 hours; raise the bed temperature to 350°C at a heating rate of 20°C / h and keep the temperature constant for 5 hours; Raise the bed temperature to 460°C, keep the temperature constant for 5 hours, and lower the bed temperature below 40°C to complete the reduction.
[0049] After the reduced catalyst is discharged from the reactor, the initial activity of the catalyst is deactivated in the moving bed, the temperature of the bed is raised to 380°C, and the water vapor temperature is...
Embodiment 3
[0058] The catalyst reduction process and process conditions were carried out according to Example 1.
[0059] The passivation treatment conditions are as follows:
[0060] (1) The steam treatment temperature is 470°C;
[0061] (2) The steam treatment time is 1 hour;
[0062] (3) The water vapor consumption per hour is 152g / h.
[0063] Table 4 catalyst passivation effect
[0064]
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