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

A molecular sieve and IMF technology, which is applied in the field of phosphorus-containing IMF structure molecular sieves and its preparation, can solve the problems of reducing the effective reaction area of ​​molecular sieves, reducing the reactivity of molecular sieves, and reducing reaction selectivity, so as to facilitate the formation and diffusion and suppress non-selectivity. Sexual side effects, the effect of improving reactivity

Active Publication Date: 2019-11-15
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

[0028] The present invention also provides a preparation method of the phosphorus-containing IMF structure molecular sieve provided by the present invention, the preparation method comprising: a, the sodium type IMF structure molecular sieve is desiliconized in an alkaline solution to obtain a desiliconization molecular sieve; b, the steps The desiliconized molecular sieve obtained in a is subjected to ammonium exchange treatment to obtain an ammonium exchanged molecular sieve; wherein, the sodium content of the ammonium exchanged molecular sieve is less than 0.2% by weight in terms of sodium oxide and based on the total dry weight of the ammonium exchanged molecular sieve; c, The ammonium-exchanged molecular sieve obtained in step b is dealuminated in a complex acid dealumination agent solution composed of fluosilicic acid, organic acid and inorganic acid, and after filtering and washing, the dealuminated molecular sieve is obtained; d, step c After the dealuminated molecular ...

Embodiment 1

[0055] Filter the mother liquor from the crystallized IM-5 molecular sieve (produced by Changling Catalyst Factory), wash with water, filter and dry; roast the dried molecular sieve in the air for 6 hours at a roasting temperature of 550°C to remove the templating agent therein Get the above-mentioned molecular sieve 100g (dry basis) and add in 1000g 2.4% by weight of NaOH solution, heat up to 65°C, react for 30min, cool to room temperature rapidly, filter, wash until the filtrate is neutral. Then, add 800g water to the filter cake to make a slurry, add 40g NH 4 Cl, heated to 75°C, exchanged for 1h, to Na 2 O content is lower than 0.2% by weight, filters, washes, and obtains molecular sieve filter cake; Get above-mentioned molecular sieve filter cake 50g (dry basis) and add water and be mixed with the molecular sieve slurry of solid content 10% by weight, add oxalic acid 5g in stirring, then 35g hydrochloric acid ( Mass fraction 10%) and 28g fluosilicic acid (mass fraction 3%...

Embodiment 2

[0071] Filter the mother liquor from the crystallized IM-5 molecular sieve (produced by Changling Catalyst Factory), wash with water, filter and dry; roast the above-mentioned dried molecular sieve in air for 8 hours at a roasting temperature of 550°C to remove the templating agent therein Take 100g (dry basis) of the above-mentioned molecular sieve and add it to 1500g 2.3% by weight of NaOH solution, heat up to 60°C, react for 45min, cool to room temperature rapidly, filter, and wash until the filtrate is neutral. Then, add 800g water to the filter cake to make a slurry, add 40g NH 4 Cl, heated to 75°C, exchanged for 1h, to Na 2O content is lower than 0.2% by weight, filters, washes, obtains molecular sieve filter cake; Get above-mentioned molecular sieve filter cake 50g (dry basis) and add water and be mixed with the molecular sieve slurry of solid content 10% by weight, add citric acid 4g in stirring, then 10g sulfuric acid ( Mass fraction 10%) and 45g fluosilicic acid (ma...

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PUM

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Abstract

The invention discloses a phosphorus-containing IMF structure molecular sieve and a preparation method thereof, wherein the Al distribution parameter D of the molecular sieve is more than or equal to0.6 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 with the 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 acid B to the acid L is 7-30, and 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. According to the present invention, the phosphorus-containing IMF structure molecular sieve has advantages of high propylene yield, good propylene selectivity, high ethylene yield and high BTX yield in the catalytic cracking reaction of petroleum hydrocarbons.

Description

technical field [0001] The invention relates to a phosphorus-containing IMF structure molecular sieve 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 resin, synthetic fiber and synthetic rubber, among which 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 to produce ethylene. The second largest source of propylene is almost all from FCC units, which provide about 30% of the demand. In the United States, FCC units provide petrochemical products for propylene. About half of the demand. [0003] Due to the rapidly growing demand for polypropylene, the demand for propylene in the petrochemical industry is faster than that for ethylene, and the construction of ethylene plants is limited by the dem...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B39/02B01J29/04
CPCB01J29/041C01B39/026C01P2006/12C01P2006/14C01P2006/16C01P2006/17
Inventor 庄立欧阳颖罗一斌刘建强舒兴田
Owner CHINA PETROLEUM & CHEM CORP
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