A kind of prolific gasoline catalytic cracking catalyst and preparation method thereof

A catalytic cracking and catalyst technology, applied in catalytic cracking, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve the problems of high energy consumption, cumbersome preparation process and high catalyst preparation cost

Active Publication Date: 2021-07-30
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the above patented molecular sieve modification process must go through a roasting process, the preparation process is cumbersome, consumes a lot of energy, and requires a large number of modifications to existing production equipment to achieve industrial production, resulting in high catalyst preparation costs and difficult operations.

Method used

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  • A kind of prolific gasoline catalytic cracking catalyst and preparation method thereof
  • A kind of prolific gasoline catalytic cracking catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] (1) Preparation of the Y-type molecular sieve modified by phosphorus and magnesium: get 922 grams of rare earth ultra-stable Y (dry basis), after beating with 1956 grams of deionized water, add 9.2 grams of diammonium hydrogen phosphate (in terms of phosphorus), and react 2 hours, then 7.1 g of magnesium chloride (calculated as magnesium) was added to the above slurry for mixing and beating, and reacted at 95° C. for 1 hour to obtain phosphorus and magnesium modified molecular sieve Y1.

[0042] (2) Preparation of modified matrix material: 872 grams of kaolin, 560 grams of halloysite, 976 grams of aluminum sol, 1056 grams of pseudoboehmite and 3257 grams of deionized water were mixed and beaten, stirred for 30 minutes, and 10 grams of phosphoric acid was added (calculated as phosphorus), and stirred evenly to prepare the modified matrix material M1.

[0043] The above phosphorus and magnesium modified molecular sieve Y1 and modified matrix material M1 were mixed and bea...

Embodiment 2

[0045] (1) Preparation of Y-type molecular sieve modified by phosphorus and magnesium: get 1210 grams of rare earth Y (dry basis), after beating with 6200 grams of deionized water, add 1.3 grams of phosphoric acid (calculated as phosphorus), react for 1 hour, and then add to the above-mentioned Add 61 grams of magnesium nitrate (calculated as magnesium) to the slurry for mixing and beating, and react at 110° C. for 0.5 hour to obtain phosphorus and magnesium modified molecular sieve Y2.

[0046] (2) Preparation of modified matrix material: 150 grams of kaolin, 62 grams of aluminum sol, 160 grams of rare earth solution, 83 mL of hydrochloric acid, 607 grams of pseudoboehmite and 2000 grams of deionized water were mixed and beaten, stirred for 20 minutes, and 1 gram of Phosphoric acid (calculated as phosphorus), stirred evenly to prepare the modified matrix material M2.

[0047] The above-mentioned phosphorus and magnesium modified molecular sieve Y2 and modified matrix material...

Embodiment 3

[0049] (1) Preparation of the Y-type molecular sieve modified by phosphorus and magnesium: get 516 grams of hydrogen Y (dry basis) and 385 grams of ultra-stable Y (dry basis), after beating with 3308 grams of deionized water, add 2.3 grams of ammonium phosphate (with Phosphorus) and 2 grams of phosphoric acid (calculated as phosphorus), reacted for 3 hours, then added 0.7 gram of magnesium sulfate (calculated as magnesium) and 0.2 gram of magnesium chloride (calculated as magnesium) to the above slurry, mixed and beaten, and reacted at 60 ° C for 2 hours, phosphorus and magnesium modified molecular sieve Y3 was obtained.

[0050] (2) Preparation of modified matrix material: 1203 grams of kaolin, 121 grams of aluminum sol, 83 mL of hydrochloric acid, 176 grams of pseudoboehmite and 2000 grams of deionized water were mixed and beaten, stirred for 45 minutes, and 5 grams of diammonium hydrogen phosphate ( Calculated as phosphorus), and stirred evenly to prepare the modified matri...

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Abstract

The invention provides a prolific gasoline catalytic cracking catalyst and a preparation method thereof. The catalyst comprises 15-70wt% molecular sieve, 15-60wt% clay, 8-30wt% pseudo-boehmite, 3-20wt% binder, and 0.01-2wt% phosphorus in terms of phosphorus, and 0.01-3wt% magnesium in terms of magnesium. The preparation method is as follows: (1) Preparation of Y-type molecular sieve modified by phosphorus and magnesium: mixing Y-type molecular sieve and phosphorus-containing compound for beating reaction, and then adding magnesium-containing compound to raise the temperature for reaction. (2) Preparation of modified matrix material: mix clay, pseudo-boehmite, binder and water for beating, add phosphorus-containing compound and stir evenly. (3) mixing and beating the above-mentioned phosphorus and magnesium modified Y-type molecular sieves and modified matrix materials, followed by successive steps of spray drying, washing, filtering and drying. The catalyst prepared by the invention has strong heavy oil conversion ability, good coke and gasoline selectivity, simple preparation process and easy industrial production.

Description

technical field [0001] The invention relates to a catalytic cracking catalyst and a preparation method thereof, in particular to a prolific gasoline catalytic cracking catalyst and a preparation method thereof. Background technique [0002] In recent years, with the adjustment of China's economic structure, the growth rate of domestic diesel demand has slowed down. Refineries adjust the structure of oil products by reducing the ratio of diesel to gasoline produced to adapt to changes in market demand and ensure the balance between supply and demand in my country's refined oil market. FCC gasoline accounts for 75% of the domestic gasoline pool. Therefore, it is most effective to increase gasoline production and reduce diesel-gasoline ratio around optimizing FCC scheme. Aiming at this, people have done a lot of research on molecular sieve modification, catalyst manufacturing and process design (Liu Tao, Zhang Zhongdong, Zhang Haitao, etc. Sinoforeign Energy. 2009, 14(1): 71-7...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/08C10G11/05
CPCB01J29/084B01J29/088C10G11/05C10G2300/1037C10G2300/70C10G2400/02
Inventor 谭争国潘志爽袁程远张海涛高雄厚张忠东李雪礼段宏昌黄校亮黄世英郑云锋孙书红崔文广
Owner PETROCHINA CO LTD
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