Gasoline aromatization and isomerization reforming catalyst and preparation method and applications thereof

A catalyst and aromatization technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of cumbersome catalyst preparation steps and achieve good aromatization effects

Active Publication Date: 2012-06-20
DALIAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The above-mentioned patents developed a catalyst with aromatization function for FCC gasoline upgrading, which showed good oct

Method used

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  • Gasoline aromatization and isomerization reforming catalyst and preparation method and applications thereof
  • Gasoline aromatization and isomerization reforming catalyst and preparation method and applications thereof
  • Gasoline aromatization and isomerization reforming catalyst and preparation method and applications thereof

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0034] Example 1

[0035] ①Preparation of catalyst carrier

[0036] 1) Weigh 3.5kg nano ZSM-5 raw powder, 1.14kg pseudo-boehmite and 120g sesame powder, mix the three evenly, add 2300ml nitric acid solution with a mass concentration of 10%, and knead it in the extruder. forming. Place it at room temperature for 12 hours, then dry at 100°C for 12 hours and calcine at 540°C for 3 hours.

[0037] 2) Put 4 kg of the catalyst carrier prepared in the above step 1) in a 0.4mol / L ammonium nitrate solution at a solid-liquid volume ratio of 1:5, and place it at room temperature for 1 hour. After filtration, wash with deionized water until neutral. Repeat the above operation twice. Dry at 100°C for 12h, calcine at 540°C for 3h, and set aside.

[0038] 3) Put 4 kg of the catalyst carrier prepared in the above step 2) in a 0.6 mol / L nitric acid solution at a solid-liquid ratio of 1:5, and place it at room temperature for 24 hours. After filtering, wash with deionized water. After drying at 1...

Example Embodiment

[0043] Example 2

[0044] ① Preparation of catalyst carrier: the same as in Example 1.

[0045] ②Preparation of catalyst

[0046] 1) Pack 20g of the above catalyst carrier A in the constant temperature section of the fixed bed, at 550℃, space velocity 1h -1 Treat with steam for 2h.

[0047] 2) The catalyst treated in step 1) was immersed in 15ml of solution containing 3.66g zinc nitrate and 0.62g lanthanum nitrate, immersed at room temperature for 24h, filtered, dried at 100°C for 12h, and calcined at 540 for 4h to prepare supported zinc oxide and Lanthanum oxide catalyst.

[0048] 3) The catalyst prepared in step 2) was then immersed in 15 ml of a solution containing 1.48 g of ammonium dihydrogen phosphate, immersed at room temperature for 12 hours, filtered, dried at 100°C for 12 hours, and calcined at 540 for 4 hours to obtain product catalyst E.

Example Embodiment

[0049] Example 3

[0050] ① Preparation of catalyst carrier: the same as in Example 1.

[0051] ②Preparation of catalyst

[0052] 1) Pack 10g of the above catalyst carrier A in the constant temperature section of the fixed bed, at 500℃, space velocity 0.5h -1 Treat with steam for 3h.

[0053] 2) The catalyst treated in step 1) above was immersed in 8ml of solution containing 0.92g zinc nitrate and 0.27g lanthanum nitrate, immersed at room temperature for 24h, filtered, dried at 100°C for 12h, and calcined at 540 for 4h to prepare supported zinc oxide and Lanthanum oxide catalyst.

[0054] 3) The catalyst prepared in step 2) is then immersed in 8 ml of a solution containing 0.74 g of ammonium dihydrogen phosphate, immersed at room temperature for 24 hours, filtered, dried at 100°C for 12 hours, and calcined at 540 for 4 hours to obtain product catalyst F.

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Abstract

The invention discloses a gasoline aromatization and isomerization reforming catalyst. The catalyst comprises the following components by weight percent: 0.1-5% of oxide of the metal in IIB group, 0.1-3% of lanthanide metal oxide, 0.1-5% of oxide of the element in VA group, 50-80% of nanosized HZSM-5 and 20%-40% of alumina. The preparation method comprises the following steps: using a nanosized ZSM-5 molecular sieve to prepare the nanosized HZSM-5 carrier, performing hydrothermal treatment, and adopting the isovolumetric impregnation method to load an active component I and an active component II and obtain the target catalyst. The catalyst provided by the invention has good aromatization activity and isomerization activity and a certain desulfurization capacity; and the olefin content (V) of the gasoline product which is prepared by using the catalyst provided by the invention is no more than 30%, the aromatic content (V) is no more than 35%, the benzene content (V) is no more than 1% and the loss of the octane value is no more than 1.

Description

technical field [0001] The invention relates to a preparation method and application of a gasoline aromatization isomerization catalyst. In particular, it relates to a catalyst preparation method for loading active metal components on nano-scale ZSM-5 molecular sieves. Through the interaction between additives, metal components and molecular sieves, the dispersion of metal active components is improved, and the catalytic performance of the catalyst is improved. . Background technique [0002] With the improvement of gasoline standards, how to hydro-upgrade to reduce the olefin content in gasoline, remove sulfur compounds, and at the same time make the loss of octane number smaller is the key to gasoline upgrading. The octane number of catalytic cracked gasoline (FCC gasoline) raw materials with low olefin content, high aromatic content and sulfur content less than 200ppm is mainly provided by aromatics and isoparaffins. During the upgrading process, by increasing the selec...

Claims

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Application Information

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IPC IPC(8): B01J29/40C10G45/64
Inventor 王祥生龙化云靳凤英
Owner DALIAN UNIV OF TECH
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