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Catalytic cracking light gasoline desulfurization adsorbent and preparation method thereof

A catalytic cracking and adsorbent technology, applied in chemical instruments and methods, hydrocarbon oil treatment, refined hydrocarbon oil, etc., can solve the problems of unsatisfactory effect and high saturation of tertiary olefins, and achieve good low temperature and low pressure activity, enhanced dispersion, Weaken the effect of the interaction

Active Publication Date: 2021-06-04
PETROCHINA CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0009] The main purpose of the present invention is to provide a kind of catalytic cracking light gasoline desulfurization adsorbent and preparation method thereof, to overcome the desulfurization adsorbent in the prior art when applying to catalytic cracking light gasoline with lower sulfur content and higher olefin content. High carbon olefin saturation, the defect of unsatisfactory effect

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  • Catalytic cracking light gasoline desulfurization adsorbent and preparation method thereof
  • Catalytic cracking light gasoline desulfurization adsorbent and preparation method thereof

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preparation example Construction

[0036] Further, the present invention also provides the preparation method of the catalytic cracking light gasoline desulfurization adsorbent, including the steps of:

[0037] Step 1, prepare ZnO-TiO 2 Composite oxide;

[0038] Step 2, use tin precursor solution to ZnO-TiO 2 Composite oxide is modified;

[0039] Step 3, the modified ZnO-Tio obtained by step 2 2 The composite oxide impregnates the impregnation liquid comprising the active component precursor to obtain a catalytic cracking light gasoline desulfurization adsorbent.

[0040] Among them, the present invention is for ZnO-TiO 2 The preparation of the composite oxide is not particularly limited, and is a preferred technical solution, the preparation process is: mixed the alkali-type carbonate, metallite-based acid, and the ground is uniformly added to 2 to 6% by weight of nitric acid and 3 to 6% by weight of Tianjing powder. After the stirring is mixed, the mold is extruded, and after 12 h, it is dried in 120 to 150 ° C f...

Embodiment 1

[0054] It is weighing the alkali-type carbonate (25%, the same as the same) 90g, 51g of ketchlate, 4g of the fields, mixed with mixed grinding, and then adding the amount of 2% nitric acid, stirring is mixed and squeezed. After 12 h, it was dried at 120 ° C for 6 h, and then it was taken at 500 ° C for 7 hours to obtain ZnO-TiO. 2 Carrier A. Then, it is called 0.98 g of tinyl chloride dissolve in 51 ml no water ethanol, and ZnO-TiO 2 The volume of the carrier A is immersed for 6 h, dried at 120 ° C, baked for 6 h at 400 ° C, and modified ZnO-TiO 2 Carrier B. Zno-TiO 2 Zno and TiO 2 The mass ratio is 6: 4, SN accounts for Zno-TiO 2 The mass percentage of composite oxides is 0.6%, and the carrier hole is 0.36cm. 3 / g, the specific surface area is 31.6m 2 / g, the deposit density is 0.96 g / ml (the pore area of ​​the carrier, the surface area, the density of the density and the like is substantially the same as the corresponding catalyst, so the corresponding catalyst is not indica...

Embodiment 2

[0056] It is weighing 104g of alkali-type carbonate, 38g of metanton acid, 5g of Tianjing powder, uniform, then adding a proper amount of 3% nitric acid, stirring is mixed and squeezed, placed in 12 h, after 120 ° C drying 4h, Get ZnO-TiO after calcination at 450 ° C for 8 h 2 Carrier. Then, 2.0 g of tin chloride dissolve is dissolved in 56 ml of anhydrous ethanol, and ZnO-TiO 2 The vectors of the carrier are impregnated at 7 h, dried at 120 ° C, baked at 400 ° C for 5 h, and modified Al 2 O 3 -Tio 2 Carry C. Zno-TiO 2 Zno and TiO 2 The mass ratio is 7: 3, SN accounts for Zno-TiO 2 The mass percentage of composite oxides is 1.1%, and the carrier hole is 0.31cm. 3 / g, the specific surface area is 32.9m 2 / g, the stacked density is 0.98 g / ml.

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Abstract

The invention provides a catalytic cracking light gasoline desulfurization adsorbent and a preparation method thereof, wherein the adsorbent comprises a carrier and an active component, the carrier is a Sn modified ZnO-TiO2 composite oxide, and the active component is nickel and / or cobalt. The preparation method of the adsorbent comprises a process of preparing a modified ZnO-TiO2 composite oxide carrier and a process of preparing a catalytic cracking light gasoline desulfurization adsorbent by an impregnation method. The adsorbent has the desulfurization activity advantage of a traditional Ni / ZnO adsorbent, is good in low-temperature and low-pressure activity, can effectively reduce the olefin saturation, and is high in breakthrough sulfur capacity.

Description

Technical field [0001] The present invention relates to the field of desulfurization adsorbent, and is particularly suitable for catalytic cracking light gasoline and hydrocarbon-containing sulfur-containing compound removal of the desired adsorbent and the preparation method thereof. Background technique [0002] With the implementation of China's protection of environmental policy and the attention of environmental protection, China's control of sulfur content in gasoline is more stringent. On January 1, 2017, the country V standards were implemented in the country in the country. When my country's car gasoline products are large, the FCC gasoline must be performed in order to obtain low sulfur gasoline. Desulfurization. Fcc gasoline desulfurization is generally preferred to perform cutting separation based on the characteristics of FCC gasoline, heavy two components, and the cut light gasoline components are mainly enriched in large quantities of C5 ~ C6 tertiary carboxide, wh...

Claims

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Application Information

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IPC IPC(8): B01J20/06B01J20/30C10G25/00
CPCB01J20/06B01J20/02C10G25/003C10G2300/202B01J2220/42Y02A50/20
Inventor 肖寒李芹刘飞王玫周红军周广林李长明翟莉慧马应海李修仪卜婷婷景媛媛李世龙
Owner PETROCHINA CO LTD