L molecular sieve-containing catalytic gasoline selective hydrodesulfurization modification catalyst

A technology for catalytic cracking gasoline and hydrodesulfurization, which is used in molecular sieve catalysts, physical/chemical process catalysts, petroleum industry and other directions, can solve the problems of poor comprehensive performance of catalytic cracking gasoline upgrading catalysts, and achieve the effect of improving product quality

Active Publication Date: 2010-12-01
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] The purpose of the present invention is to develop a catalyst containing L molecular sieve, so that it has balanced hydrodesulfurization, olefin reduction, and octane n

Method used

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  • L molecular sieve-containing catalytic gasoline selective hydrodesulfurization modification catalyst
  • L molecular sieve-containing catalytic gasoline selective hydrodesulfurization modification catalyst
  • L molecular sieve-containing catalytic gasoline selective hydrodesulfurization modification catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0035] 6g of synthesized KL powder (skeleton SiO 2 / Al 2 o 3 =6~7, relative crystallinity 93%) after drying at 110 ℃ for 2 hours and cooling, after mixing with 25.9g of pseudo-boehmite dry base powder and 1g of turnip powder, add dropwise 1g of concentrated nitric acid, 0.4g of phosphoric acid and Appropriate amount of water; after fully back-mixing in the extruder, extrude into a cylindrical shape with a diameter of 1.5mm; then dry at 110°C for 4 hours; then roast at 550°C for 4 hours to obtain γ-Al 2 o 3 -L molecular sieve composite carrier, the prepared composite carrier is denoted as S8. Dissolve 9g of ammonium molybdate in 40g of water to impregnate the composite carrier, then ultrasonically disperse it for 20 minutes, stir for 5 minutes, dry at 110°C for 4h, roast at 550°C for 4 hours, and cool to room temperature; then use 0.6g of nitric acid Cobalt and 0.1g of nickel nitrate were dissolved in 40g of water, and the molybdenum-loaded composite carrier was co-impregna...

Embodiment 2

[0037] KL molecular sieves were subjected to ammonium exchange to obtain L-1 zeolite with an alkalinity lower than KL, and the 6 g of KL powder in Example 1 was replaced with 6 g of L-1 zeolite, and the following preparation was the same as in Example 1. The prepared composite carrier is denoted as S9, and the corresponding catalyst is denoted as Cat9.

Embodiment 3

[0039] The L-1 zeolite in Example 2 is carried out ammonium exchange again to obtain the L-2 zeolite whose basicity is lower than L-1, and the KL former powder of 6g in Example 1 is replaced with the L-2 zeolite of 6g, and the following preparation With embodiment 1.

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Abstract

The invention relates to an L molecular sieve-containing catalytic gasoline selective hydrodesulfurization modification catalyst. A carrier is a composite carrier consisting of alumina and an L molecular sieve; Co or/and Ni metal and Mo or/and W metal active components are loaded; alkali metals, alkaline-earth metals, rare-earth elements, transition metals and non-metals are compounded to obtain a modifier; the L molecular sieve accounts for 10 to 70 percent of the total weight of the carrier; and based on the total weight of 100 percent of the catalyst, the active component Mo or/and W accounts for 2.0 to 30 percent of the total weight of the catalyst based on the weight percentage of an oxide, the active component Co or/and Ni accounts for 0.1 to 10.0 percent of the total weight of the catalyst based on the weight percentage of the oxide, the modifier accounts for 1 to 10 percent of the total weight of the catalyst and the carrier accounts for 60 to 93 percent of the total weight of the catalyst. Therefore, the desulfurization degree of catalytic gasoline is no less than 80 percent, the volume content of olefin is lowered to be less than 25 percent and the octane number of a product is no less than 1.5 units compared with that of raw oil.

Description

technical field [0001] The invention relates to a catalytic cracking (FCC) gasoline selective hydrodesulfurization and upgrading catalyst used in the production of clean gasoline in the petroleum refining process. Background technique [0002] At present, urban air pollution caused by vehicle exhaust emissions is becoming more and more serious. For example, the "contribution rate" of vehicle emissions to air pollution in Beijing has reached 40-50%. In order to control the air pollution caused by automobile exhaust emissions, countries all over the world have formulated strict gasoline standards (as shown in Table 1). In order to adapt to WTO rules, my country's automotive gasoline standards are also constantly in line with international standards. The newly launched National IV gasoline vehicle emission standards require that the sulfur content be less than 50 μg·g -1 , the volume content of olefins is lower than 25.0%, and gradually approaches the European oil standard IV....

Claims

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Application Information

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IPC IPC(8): B01J29/64C10G49/08
Inventor 兰玲段爱军高镇甬张振莉鞠雅娜霍全赵震潘慧芳
Owner PETROCHINA CO LTD
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