Phosphor and rare earth composite modification method of molecular sieve

A rare earth modification, molecular sieve technology, applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of long crystallization time, excessive consumption, and difficulty in forming core/shell molecular sieves

Active Publication Date: 2012-10-24
PETROCHINA CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of this method is that if synthesized at high temperature, AlO 4 -5 grows well on the outer layer of ZSM-5, which easily leads to AlO 4 -5 independent crystallization, it is difficult to form a core / shell molecular sieve in the true sense; if synthesized at low temperature, AlO 4 -5 has a long crystallization time, resulting in excessive consumption
[0034] The above research is to first synthesize binary hydrotalcite, and then prepare a single active component catalyst, but in some reactions that require the simultaneous presence of multiple active components, the above method obviously has shortcomings

Method used

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  • Phosphor and rare earth composite modification method of molecular sieve
  • Phosphor and rare earth composite modification method of molecular sieve
  • Phosphor and rare earth composite modification method of molecular sieve

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0081] Add 5g of USY molecular sieve into 50ml of deionized water, stir evenly at 40°C, add 7.437g of zinc nitrate, 1.84g of lanthanum nitrate, and 3.19g of aluminum nitrate in sequence, mix and stir for 0.5 hours, and add 40g / L of A mixed alkali solution of sodium hydroxide and sodium carbonate, adjust the pH value of the system to 6, stir for 4 hours under this condition, transfer to a high-pressure reactor, crystallize at 85°C for 24 hours, filter, wash and dry to obtain Zn- Al-La-CO 3 / USY Composite.

[0082] Will contain 5g Zn-Al-La-CO 3 / USY composite wet filter cake dissolved in 20mL deionized water to make a slurry, 1g of NaH 2 PO 4 2H 2 O (0.198mol) was dissolved in 10mL water to form a solution. Make NaH under stirring 2 PO 4 The solution was slowly added to the slurry and mixed with dilute HNO 3 The solution adjusts the pH of the system to about 4.5, and refluxes for 1 hour. The product was fully washed with deionized water to pH ≈ 7 and dried to obtain Zn / ...

Embodiment 2

[0084] Add 5g of USY molecular sieve into 50ml of deionized water, stir evenly at 20°C, add 7.437g of zinc nitrate, 2.71g of lanthanum nitrate, and 2.34g of aluminum nitrate in sequence, mix and stir for 0.5 hours, and add 40g / L of hydrogen at a rate of 1ml / min A mixed alkali solution of sodium oxide and sodium carbonate, adjust the pH value of the system to 6, stir for 6 hours under this condition, transfer to a high-pressure reactor, crystallize at 85°C for 24 hours, filter, wash and dry to obtain Zn-Al -La-CO 3 / USY Composite,

[0085] Will contain 10g Zn-Al-La-CO 3 The wet filter cake of the / USY composite was dissolved in 20 mL of deionized water to make a slurry, and 1 g of phosphoric acid was dissolved in 10 mL of water to make a solution. Slowly add orthophosphoric acid solution into the slurry under stirring, and dilute HNO 3 The solution adjusts the pH of the system to about 4.5, and refluxes for 1 hour. The product was fully washed with deionized water to pH ≈ 7...

Embodiment 3

[0087] Add 5g of USY molecular sieve into 50ml of deionized water, stir evenly at 20°C, add 13.73g of zinc nitrate and 2.67g of lanthanum nitrate in turn, mix and stir for 0.5 hours, add 80g / L of sodium hydroxide and carbonic acid at a speed of 0.1ml / min Mixed alkali solution of sodium, adjust the pH value of the system to 6, stir under this condition for 6 hours, transfer to a high-pressure reactor, crystallize at 85°C for 24 hours, filter, wash and dry to obtain Zn-Al-La-CO 3 / USY Composite.

[0088] Will contain 1g Zn-Al-La-CO 3 The wet filter cake of / USY composite material was dissolved in 20 mL of deionized water to make a slurry, and 1 g of phosphorous acid was dissolved in 10 mL of water to make a solution. Slowly add the phosphorous acid solution into the slurry under stirring, and dilute HNO 3 The solution adjusts the pH of the system to about 4.5, and refluxes for 1 hour. The product was thoroughly washed with deionized water to pH 7 and dried to obtain Zn-Al-La-...

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Abstract

A phosphor and rare earth composite modification method of a molecular sieve comprises that an aluminum source on the surface of the molecular sieve is utilized for in situ synthesis of carbonate-ion-pillared Zn (Mg) / Al / La (Ce) ternary hydrotalcite; that dihydrogen-phosphate-ion-pillared hydrotalcite is prepared by employing an ion exchange method; and that a program heating calcination method is used to make P2O5, La2O3 or Ce2O3 be highly dispersed in the surfaces and pores of the molecular sieve, thereby improving the acidity of the molecular sieve. According to the method of the invention, the molecular sieve modified by hydrotalcite precursor method not only realizes high dispersion of active components, but also greatly improves the acidity and the stability of the molecular sieve, thereby providing a material with practical application values for preparing catalyst for catalytic cracking of heavy oil.

Description

technical field [0001] The invention relates to a phosphorus and rare earth compound modification method of molecular sieves, in particular to a modification method in which hydrotalcite precursors are produced in molecular sieves. Background technique [0002] The availability of conventional petroleum resources is decreasing day by day, and the processing of heavy oil and residual oil is receiving more and more attention. Heavy oil is characterized by large molecules and complex molecular structures. Moreover, heavy oil is enriched with most of the sulfur, nitrogen and metal compounds in crude oil. These compounds are not only difficult to crack and easy to form coke, but also deposited on the surface of the catalyst are very easy to poison the catalyst and lose its activity. [0003] Based on the above characteristics of heavy oil, the selection of molecular sieve type and the modification of molecular sieve are very important in heavy oil catalytic cracking, which are d...

Claims

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Application Information

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IPC IPC(8): B01J29/08B01J29/70C10G11/05
Inventor 刘洪涛刘宏海胡清勋石永刚王坤赵红娟张莉王宝杰赵晓争熊晓云高雄厚
Owner PETROCHINA CO LTD
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