Alkyne-containing C4 fraction selective hydrogenation method
A technology for selective hydrogenation and carbon four fractions, applied in the fields of hydrocarbons, chemical instruments and methods, hydrogenation to hydrocarbons, etc., which can solve the problems of easy agglomeration, poisoning and deactivation of active components
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[0054] Embodiment uses the preparation of catalyst 1~6
[0055] Preparation of Catalyst C1:
[0056] Concentrate 4L to 50g Al 2 o 3 / L of sodium metaaluminate solution is placed in a stainless steel container with a stirrer and gas can be introduced into the bottom of the tank, the nickel nitrate solution is prepared and placed in a high-position container, a mixed gas of carbon dioxide and air is introduced, and the peristaltic pump is started at the same time Control the flow rate and drop the prepared nickel nitrate solution, the carbon dioxide concentration in the mixed gas is 70v%, and the flow rate is 4Nm 3 / h, the reaction temperature is 40°C, the pH value at the end of the reaction is 10, stop feeding carbon dioxide, age for 30 minutes, filter and separate the mother liquor, wash, and dry at 120°C for 5 hours to obtain nickel-containing pseudo-boehmite.
[0057] Mix and knead nickel-containing pseudo-boehmite with nitric acid and water, extrude into strips, dry at 1...
Embodiment 1
[0084] The C4 fraction rich in alkynes is diluted with the C4 raffinate, and the weight ratio of the C4 fraction rich in alkynes to the C4 raffinate is 1:1. The isothermal reactor adopts single-stage isothermal bubbling bed, adopts catalyst C1, and the catalyst is reduced under hydrogen atmosphere at 120°C for 6h. The reaction inlet temperature is 50°C, the reaction pressure is 1.5MPa, and the liquid space velocity is 7h -1 , the molar ratio of hydrogen to alkyne is 3.5, Table 2 is the composition of materials before and after the reaction.
[0085] Material composition before and after table 2 reaction
[0086]
Embodiment 2
[0088] Dilute the alkyne-rich C4 fraction with raffinate C4 and cracked C4, the weight ratio of the alkyne-rich C4 fraction to (raffinate + cracked C4) is 1:6. The isothermal reactor adopts single-stage isothermal bubbling bed, adopts catalyst C2, and the catalyst is reduced at 120°C for 6 hours under hydrogen atmosphere. The reaction inlet temperature is 60°C, the reaction pressure is 2.0MPa, and the liquid space velocity is 12h -1 , the molar ratio of hydrogen to alkyne is 2.5, Table 3 is the composition of materials before and after the reaction.
[0089] Table 3 Composition of materials before and after reaction
[0090]
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