A sSelective hydrogenation method for pyrolysis gasoline
A pyrolysis gasoline, selective hydrogenation technology, applied in C6-C9 fractions, pyrolysis gasoline C5-C9 field, can solve the problem of catalyst activity decline
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[0074] The preparation of embodiment with catalyst C1-C6:
[0075] Preparation of Catalyst C1:
[0076] Concentrate 5L to 60g Al 2 o 3 / L of sodium metaaluminate solution is put into a stainless steel container with a stirrer and the bottom of the tank can be fed with gas, and then a certain concentration of nickel nitrate solution is put into a high-position container, and the flow rate of the nickel nitrate is controlled by a peristaltic pump. The solution is added to the sodium metaaluminate solution, and a mixed gas of carbon dioxide and air is introduced into the stainless steel container at the same time, the concentration of carbon dioxide in the mixed gas is 70v%, and the flow rate is 3Nm 3 / h, the gelling temperature is 45°C, the pH value of the gelling is 9.5, after the gelling is completed, stop feeding carbon dioxide, age for 50 minutes, and the aging temperature is 45°C, filter and separate the mother liquor, wash, and dry at 120°C for 6h to obtain nickel-contai...
Embodiment 1
[0105] Put the catalyst 1 into a 250mL adiabatic fixed-bed reaction device, first carry out the reduction and activation of the catalyst, and maintain it for 8 hours under the conditions of a pressure of 2.8MPa, a bed temperature of 110°C, and a hydrogen flow rate of 125L / h to complete the reduction and activation of the catalyst.
[0106] After the restore is complete, use C 5 -C 9 The distillate is the raw material, at an inlet temperature of 70°C, a reaction pressure of 3.0MPa, and a liquid hourly space velocity of 2.0h -1 1. Run for 200 hours under the condition of hydrogen oil volume ratio 400:1, sample and analyze the diene value and bromine value in the product every 24 hours, and the average value of the analysis results is shown in Table 3.
Embodiment 2
[0110] Catalyst 2 was loaded into a 250mL adiabatic fixed-bed reactor, and the catalyst reduction and activation treatment method was the same as in Example 1.
[0111] After the restore is complete, use C 5 -C 9 The distillate is the raw material, at an inlet temperature of 70°C, a reaction pressure of 2.6MPa, and a liquid hourly space velocity of 2.0h -1 1. Run for 200 hours under the condition of hydrogen oil volume ratio 300:1, sample and analyze the diene value and bromine value in the product every 24 hours, and the average value of the analysis results is shown in Table 3.
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