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Anti-basic nitrogen gasoline yield increase catalysis cracking catalyst and preparation method thereof

A cracking catalyst and gasoline technology, applied in catalytic cracking, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve the problems of product distribution deterioration, no cracking catalysts found, low activity, etc., and achieve high conversion rate and high catalytic cracking Effect of Activity and High Gasoline Yield

Active Publication Date: 2013-05-08
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the existing cracking catalysts still have the problems of low activity and poor product distribution when used in base-nitrogen-containing feedstocks, and no cracking catalysts related to base-nitrogen-resistant and prolific gasoline have been found.

Method used

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  • Anti-basic nitrogen gasoline yield increase catalysis cracking catalyst and preparation method thereof
  • Anti-basic nitrogen gasoline yield increase catalysis cracking catalyst and preparation method thereof
  • Anti-basic nitrogen gasoline yield increase catalysis cracking catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 5、6 and 8

[0027] The second Y-type molecular sieve is a gas-phase ultra-stable Y-type molecular sieve containing rare earths, and its preparation method includes: contacting the Y-type molecular sieves containing rare earths with silicon tetrachloride under stirring, and the contact temperature is 100-500 ° C, The contact time is 0.1-10 hours, and the weight ratio of the rare earth-containing Y-type molecular sieve to silicon tetrachloride is 1:0.05-0.5. The specific preparation method of the second Y-type molecular sieve can refer to the patent application CN1683244A, especially the examples 5, 6 and 8;

[0028] The third Y-type molecular sieve is a rare earth-containing acid-treated hydrothermal ultra-stable Y-type molecular sieve, and its preparation method includes: mixing the ultra-stable Y-type molecular sieve and an acid solution with a concentration of 0.01-2N at a liquid-solid ratio (weight) The ratio of 4-20 is fully mixed at 20-100 ° C, treated for 10-300 minutes, washed, fil...

Embodiment 1

[0049] This example is used to illustrate the catalytic cracking catalyst provided by the present invention.

[0050] (1) Preparation of modified Y-type molecular sieve

[0051] In the reactor, add 5.0 kilograms of NaY molecular sieves on a dry basis (Changling Catalyst Factory provides, crystallinity 86%, skeleton silicon-aluminum ratio (SiO 2 / Al 2 o 3molar ratio) 5.2) and 4 kg of deionized water, slowly add 4.0 liters of rare earth chloride solution (provided by Qilu Catalyst Factory, RE 2 o 3 content of 222.5 grams per liter), adjust the system pH=3.5 with 4% by weight dilute hydrochloric acid, heat up to 90°C and stir for 1.5 hours, filter, wash, and dry; then bake at 650°C and 100% steam atmosphere for 2 hours, The "cross-baked" rare earth sodium Y was obtained, which was recorded as modified molecular sieve ABY-1A.

[0052] Take 2.0 kg of modified molecular sieve ABY-1A dry basis and put it into the reaction kettle, add 1.6 kg of deionized water, and slowly add 0.5...

Embodiment 2-7

[0059] This example is used to illustrate the catalytic cracking catalyst provided by the present invention.

[0060] Prepare catalytic cracking catalyst according to the method of embodiment 1 respectively, difference is, in step (2), mesoporous silicon aluminum material, kaolin, described modified Y-type molecular sieve ABY-1, described second rare earth-containing Y-type molecular sieve (S1), the third rare earth-containing Y-type molecular sieve (S2), pseudo-boehmite and alumina sol are shown in Table 1 below in terms of dry basis, and the dosage of each component is In parts by weight, catalytic cracking catalysts C2-C7 are prepared respectively.

[0061] Table 1

[0062]

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Abstract

The invention relates to an anti-basic nitrogen gasoline yield increase catalysis cracking catalyst and a preparation method thereof. The catalyst comprises a cracking activity component, a mesoporous silicon-aluminum material, an adhesive and clay, wherein the cracking activity component comprises a first Y type molecular sieve and a rare earth-containing ultra-stable Y type molecular sieve, rare earth content in the first Y type molecular sieve is 8-23 wt% (calculated as rare earth oxide), iron content in the first Y type molecular sieve is 0.1-3.0 wt% (calculated as Fe2O3), copper content in the first Y type molecular sieve is 0-3.0 wt% (calculated as CuO), phosphorus content in the first Y type molecular sieve is 0-2.0 wt% (calculated as P2O5), and sodium oxide content in the first Y type molecular sieve is 0.1-2.5 wt%. The catalyst preparation method comprises: carrying out pulping on a cracking activity component, a mesoporous silicon-aluminum material, an adhesive and clay, and carrying out spray drying, washing, filtering and drying. With application of the catalyst in catalytic cracking of high basic nitrogen content hydrocarbon oil, high conversion rate and high gasoline yield are provided.

Description

technical field [0001] The present invention relates to a kind of catalytic cracking catalyst, more specifically relates to a kind of cracking catalyst of anti-alkaline nitrogen and prolific gasoline. Background technique [0002] Catalytic cracking (FCC) is an important secondary processing process of crude oil and occupies a pivotal position in the oil refining industry. In the catalytic cracking process, heavy fractions such as vacuum distillate oil or residues of heavier components react in the presence of catalysts and are converted into high value-added products such as liquefied gas, gasoline, and diesel oil. In this process, it is usually necessary to use Catalytic material with high cracking activity. Microporous zeolite catalytic materials are widely used in petroleum refining and processing industries due to their excellent shape-selective catalytic performance and high cracking reactivity. With the depletion of petroleum resources and the requirements of enviro...

Claims

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Application Information

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IPC IPC(8): B01J29/80B01J29/14B01J29/08C10G11/05
Inventor 朱玉霞罗一斌邓景辉欧阳颖王维家任飞杨雪唐立文郑金玉许明德
Owner CHINA PETROLEUM & CHEM CORP