Hydrocarbon desulfurizer
A desulfurizer and hydrocarbon oil technology, which is applied in the field of hydrocarbon oil desulfurizers, can solve problems such as long time, and achieve the effects of cracking inhibition, high acid density, and high hydrothermal stability
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preparation example Construction
[0018] The preparation method of the desulfurizing agent provided by the present invention is as follows: mix the precursor of the inorganic oxide with the clay according to a predetermined amount and prepare it into a slurry with a solid content of 10-50% by weight with decationized water, and adjust its pH with an inorganic acid And maintain it to 2-4, after standing and aging at 20-80°C for 0-2 hours, add a predetermined amount of zeolite, homogenize, spray molding, and wash to remove free Na + ,dry.
[0019] Wherein the precursor of the inorganic oxide is selected from: alumina sol, pseudo-boehmite, silica sol and mixtures thereof and silica-alumina sol or gel, preferably a mixture of aged pseudo-boehmite and alumina sol, aging The weight ratio of the pseudo-boehmite to the alumina sol binder (calculated as alumina) is 0.1-10, preferably 0.5-7.0.
[0020] The aged pseudo-boehmite slurry can be prepared by a conventional method, such as beating pseudo-boehmite and water, s...
Embodiment 1-2
[0034] These examples illustrate: the preparation of the monozeolite desulfurizers provided by the present invention with clay as the matrix and pseudo-boehmite as the binder and the performance of these desulfurizers on a continuous micro-reactor device.
[0035] Using heavy gasoline with a distillation range of 90-202°C (with a sulfur content of 1844.9mg / L) as the reaction raw material, the evaluation tests were carried out on the desulfurizers PDS2 and APDS2 on the continuous micro-reactor device, and the test conditions were 5.0 grams of desulfurizer. , reaction temperature 350°C, weight hourly space velocity 4 hours -1 , The weight ratio of agent to oil is 10. Table 1 lists the reaction results.
Embodiment 3-4
[0040] Using heavy gasoline with a distillation range of 90-202°C (with a sulfur content of 1844.9mg / L) as the reaction raw material, the evaluation tests were carried out on the desulfurizers PDS1 and PDS3 on the continuous micro-reactor device, and the test conditions were 5.0 grams of desulfurizers. , reaction temperature 350°C, weight hourly space velocity 4 hours -1 , The weight ratio of agent to oil is 10. Table 2 lists the reaction results.
[0041] It can be seen from Table 2 that the desulfurization agent contains an appropriate amount of phosphorus compounds, which is beneficial to the desulfurization effect.
[0042] gasoline feedstock
[0043] gasoline feedstock
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