fcc gasoline selective hydrotreating method

A hydrotreating and selective technology, which is applied in the direction of selective hydrofining, hydrocarbon oil treatment products, hydrocarbon oil treatment, etc., can solve problems such as catalyst composition and content, complex preparation process, and difficult to control the quality of catalyst products.

Active Publication Date: 2020-12-11
林雅娟
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The composition and content of the above-mentioned catalysts are relatively large, the preparation process is complicated, and it is difficult to control the quality of catalyst products produced in large quantities

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] 1. Preparation of nickel-doped lanthanum ferrite

[0023] Under stirring conditions, dissolve 2.51mol lanthanum nitrate in 120mL water, add citric acid and stir to dissolve; then add 4.79mol iron nitrate, then add 190g sodium polyacrylate, then add 42g nickel nitrate aqueous solution, continue stirring for 30min, after drying Drying, roasting and grinding to obtain nickel-doped lanthanum ferrite.

[0024] 2. Preparation of silica-alumina carrier

[0025] Dissolve 5g of sodium polyacrylate in nitric acid, then add 38g of microsilica powder and 50g of pseudoboehmite powder, and stir evenly to obtain a mixture of microsilica powder-pseudoboehmite-sodium polyacrylate (abbreviated silicon-aluminum-organic mixture) , take 1 / 8 of the amount for later use, and add citric acid to 4.5g of nickel-doped lanthanum ferrite for later use. Add 300g of pseudo-boehmite powder and 25.0g of fenugreek powder into the kneader, add nitric acid, then add 40.2g of sodium polyacrylate nitric a...

Embodiment 2

[0029] The preparation of nickel-doped lanthanum ferrite is the same as in Example 1, except that 260g of sodium polyacrylate is added, and the preparation of the silica-alumina carrier is the same as in Example 1. The silica-alumina carrier contains 4.4wt% of silicon oxide, 5.7wt% % nickel-doped lanthanum ferrite, 1.6wt% potassium, carrier mesopores accounted for 64.2% of the total pores, and macropores accounted for 25.6% of the total pores. The unit content of sodium polyacrylate in the alumina precursor is 3 times higher than the content of sodium polyacrylate in the silicon source-organic polymer mixture. The preparation method of catalyst 2 is the same as embodiment 1.

Embodiment 3

[0031] The preparation of nickel-doped lanthanum ferrite is the same as in Example 1, except that 220g of polyacrylic acid is added, and the preparation of the silica-alumina carrier is the same as in Example 1. The silica-alumina carrier contains 8.4wt% of silicon oxide, 2.6wt% Nickel-doped lanthanum ferrite, 0.8wt% potassium, the carrier mesopores account for 54.6% of the total pores, and the macropores account for 33.5% of the total pores. The unit content of polyacrylic acid in the alumina precursor is 3.3 times higher than that in the silicon source-organic polymer mixture. The preparation method of catalyst 3 is the same as that of Example 1.

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Abstract

The invention relates to a selective hydrogenation treatment method for FCC gasoline. A fixed bed reactor is adopted, and a catalyst comprises a silicon oxide-aluminum oxide carrier and metallic active ingredients nickel, molybdenum, zinc and lithium which are loaded on the carrier; the reaction process conditions are as follows: the reaction temperature is 100-230 DEG C, the reaction pressure is1.1-5.5 MPa, the volumetric air speed is 1.2-5.0 h<-1>, and the volume ratio of hydrogen to oil is (7-28) to 1. The method is used for selective hydrogenation of the FCC gasoline to remove mercaptan sulfur and alkadiene.

Description

technical field [0001] The invention relates to a method for selective hydrotreating of FCC gasoline. Background technique [0002] With the increasingly stringent environmental protection regulations, countries around the world have put forward more and more stringent requirements on the quality of petroleum processed products, especially the stricter restrictions on the sulfur content of petroleum processed products. The sulfides contained in light petroleum products are mainly mercaptans (RSH), sulfides (RSR), etc. Among them, mercaptans have the greatest impact on product quality, not only have a foul smell, strong corrosiveness, but also affect Product stability. [0003] US6692635B2 discloses a method for producing gasoline with low sulfur content, in which a new sweetening technology is adopted. This technology feeds the whole distillate gasoline raw material into a selective hydrogenation reactor to make mercaptans react with olefins or diolefins in gasoline to gen...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G45/08C10G45/38B01J23/887
CPCB01J23/002B01J23/8873B01J2523/00C10G45/08C10G45/38C10G2300/202C10G2300/305C10G2400/02B01J2523/11B01J2523/27B01J2523/31B01J2523/3706B01J2523/41B01J2523/68B01J2523/842B01J2523/847
Inventor 黄凤玉黄志祥张丽娥张素珍
Owner 林雅娟
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