A kind of molecular sieve containing phosphorus and loaded metal imf structure and preparation method thereof

A technology for supporting metals and molecular sieves, applied in molecular sieve catalysts, chemical instruments and methods, hydrocarbon cracking to produce hydrocarbons, etc. and diffusion, suppressing non-selective side reactions, and improving reactivity

Active Publication Date: 2020-03-24
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Although IM-5 molecular sieve can have high alkane cracking ability, it is the same as other ten-membered ring molecular sieves. Due to its narrow pore structure, it is difficult for larger reactant molecules such as polycyclic hydrocarbons to enter the crystal pore for reaction, reducing the The effective reaction area of ​​the molecular sieve reduces the reactivity of the molecular sieve; on the other hand, larger product molecules such as isoparaffins and aromatics are not easy to diffuse out of the pores of the molecular sieve, which causes secondary reactions such as excessive hydrogen transfer and coking, which lead to Molecular sieve deactivation, reduced reaction selectivity

Method used

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preparation example Construction

[0031] The present invention also provides a method for preparing the phosphorus-containing and loaded metal-containing IMF structure molecular sieve provided by the present invention. The preparation method includes: a. Desiliconizing the sodium type IMF structure molecular sieve in an alkaline solution to obtain a desiliconization molecular sieve B. The desiliconization molecular sieve obtained in step a is subjected to ammonium exchange to obtain an ammonium exchange molecular sieve; wherein, based on sodium oxide and based on the total dry weight of the ammonium exchange molecular sieve, the sodium content of the ammonium exchange molecular sieve is less than 0.2 weight %; c. The ammonium exchange molecular sieve obtained in step b is dealuminated in a composite acid dealumination agent solution composed of fluorosilicic acid, organic acid and inorganic acid, and filtered and washed to obtain dealumination molecular sieve; d After the dealumination molecular sieve obtained i...

Embodiment 1

[0059] The crystallized IM-5 molecular sieve (produced by Changling Catalyst Factory) is filtered to remove the mother liquor, washed with water, filtered and dried; the dried molecular sieve is roasted in the air for 6 hours at a roasting temperature of 550°C to remove the template agent Take 100g of the above molecular sieve (dry basis) and add it to 1000g of 2.4% by weight NaOH solution, raise the temperature to 65°C, react for 30 minutes, quickly cool to room temperature, filter, and wash until the filtrate is neutral. Then, add 800g of water to the filter cake and add 40g of NH 4 Cl, heated to 75°C, exchanged for 1h, to Na 2 The O content is less than 0.2% by weight, filtered and washed to obtain a molecular sieve filter cake; take 50g (dry basis) of the above molecular sieve filter cake and add water to prepare a molecular sieve slurry with a solid content of 10% by weight, add 5g of oxalic acid during stirring, and then add 35g of hydrochloric acid ( Mass fraction 10%) an...

Embodiment 2

[0075] The crystallized IM-5 molecular sieve (produced by Changling Catalyst Factory) is filtered to remove the mother liquor, washed with water, filtered and dried; the dried molecular sieve is roasted in air for 8 hours at a roasting temperature of 550°C to remove the template agent Take 100g (dry basis) of the above molecular sieve and add it to 1500g 2.3% by weight NaOH solution, raise the temperature to 60°C, react for 45min, quickly cool to room temperature, filter and wash until the filtrate is neutral. Then, add 800g of water to the filter cake and add 40g of NH 4 Cl, heated to 75°C, exchanged for 1h, to Na 2 The O content is less than 0.2% by weight, filtered and washed to obtain a molecular sieve filter cake; take 50g of the above molecular sieve filter cake (dry basis) and add water to prepare a molecular sieve slurry with a solid content of 10% by weight. Add 4g of citric acid and then 10g of sulfuric acid ( Mass fraction 10%) and 45g fluorosilicic acid (mass fractio...

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Abstract

The invention discloses a phosphorus-containing and supported-metal-containing IMF structure molecular sieve and a preparation method thereof, wherein the Al distribution parameter D of the molecularsieve is more than or equal to 0.6 and is less than or equal to 0.85, the volume of the mesopores of the molecular sieve accounts for 50-80% of the total pore volume, the volume of the mesopores withthe pore size of 2-20 nm accounts for more than 85% of the total mesopore volume, the amount of the strong acid of the molecular sieve accounts for 50-80% of the total acid amount, a ratio of the acidB to the acid L is 7-30, the phosphorus content (calculated as P2O5) of the molecular sieve is 0.1-15 wt% by using the dry base weight of the molecular sieve as the reference, and the supported metalcontent (calculated as the oxide of the supported metal) of the molecular sieve is 0.1-5 wt% by using the dry base weight of the molecular sieve as the reference. According to the present invention,the phosphorus-containing and supported-metal-containing IMF structure molecular sieve has advantages of high propylene yield, good propylene selectivity, high ethylene yield and high BTX yield in thecatalytic cracking reaction of petroleum hydrocarbons.

Description

Technical field [0001] The invention relates to a molecular sieve containing phosphorus and a loaded metal IMF structure and a preparation method thereof. Background technique [0002] For a long time, ethylene, propylene and butene have been the basic organic chemical raw materials for synthetic resins, synthetic fibers and synthetic rubber. Among them, propylene is an important raw material for the manufacture of petrochemical products after ethylene. At present, the largest source of propylene at home and abroad is the main by-product of thermal cracking of ethylene. Almost all of the second largest source of propylene comes from FCC units, which provide about 30% of the demand. In the United States, FCC units provide petrochemical products to propylene. About half of the demand. [0003] Due to the rapidly growing demand for polypropylene, petrochemicals require propylene faster than ethylene, and the construction of ethylene plants is limited by the demand for ethylene. There...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/70B01J29/76C10G11/05C07C4/06C07C11/04C07C11/06
CPCB01J29/70B01J29/7049B01J29/76B01J2229/16B01J2229/186B01J2229/37C07C4/06C10G11/05C07C11/04C07C11/06Y02P20/52
Inventor 欧阳颖庄立罗一斌刘建强舒兴田
Owner CHINA PETROLEUM & CHEM CORP
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