Modification method of small-grain NaY-type molecular sieve

A molecular sieve and small-grain technology, applied in molecular sieve catalysts, chemical instruments and methods, crystalline aluminosilicate zeolites, etc., can solve the problem of poor hydrothermal stability of small-grain NaY molecular sieves and fine-grain Y-type molecular sieves. Poor performance, complex process steps and other problems, to achieve the effect of excellent selectivity of heavy naphtha, improved accessibility, and conducive to diffusion

Active Publication Date: 2015-05-06
CHINA PETROLEUM & CHEM CORP +1
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The method for preparing fine-grained Y-type molecular sieves proposed in CN1081425A is to precrystallize the NaY synthesis solution at 80°C to 180°C for 1 to 10 hours, then add the directing agent after cooling to room temperature, and then add the directing agent at 80°C to 100°C. Continue to crystallize for 5 to 25 hours, the process steps are more complicated and difficult to control, and the hydrothermal stability of the fine-grained Y-type molecular sieve obtained is poor
[0014] At present, due to the poor hydrothermal stability and unstable structure of small-grain NaY molecular sieves, small-grain Y-type molecular sieves with complete structure, high crystallinity and many secondary pores cannot be obtained after subsequent modification.

Method used

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  • Modification method of small-grain NaY-type molecular sieve

Examples

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Embodiment 1

[0047] This example is to prepare the raw material small grain NaY molecular sieve

[0048] Preparation of NY-1

[0049] (1) Preparation of directing agent: dissolve 10 g of solid sodium hydroxide in 80 g of water, add 2 g of sodium metaaluminate (Al 2 O 3 The content is 45wt%, Na 2 O content is 41wt%), and then add 36g water glass (SiO 2 The content is 28wt%, Na 2 The O content is 8 wt%), after mixing uniformly, it was stirred and aged at 15 °C for 4 hours to prepare the directing agent.

[0050] (2) Preparation of amorphous silicon-alumina precursors

[0051] The solid sodium aluminate is formulated into a concentration of 40gAl 2 O 3 / L sodium aluminate working solution, take SiO containing 2 28wt% sodium silicate solution, then diluted to a concentration of 100g SiO 2 / L sodium silicate working solution. Take 1L of sodium aluminate working solution and put it in the gel-forming tank, then add 0.2L of sodium silicate working solution, control the reaction tempera...

Embodiment 2

[0065] Firstly, the raw material small-grain NaY molecular sieve was alkali-treated, 1000 grams of NY-1 was mixed with 5L of NaOH solution with a concentration of 1 mol / L, and the temperature was maintained at 80 °C for 2 hours. Nearly neutral; contact the filter cake with 10 liters of 0.5 mol / L ammonium nitrate aqueous solution, the stirring speed is 300 rpm, and stir at a constant temperature of 90 ° C for 1 hour, then filter the molecular sieve, and leave a small sample for analysis of Na 2 O content; repeat the above operation until Na in the molecular sieve 2 When the O content reaches 2.5 wt %, the dried sample number is NNY-1.

Embodiment 3

[0067] Firstly, the raw material small-grained NaY molecular sieve was alkali-treated, 1000 grams of NY-2 and 5L of KOH solution with a concentration of 0.8 mol / L were beaten and mixed evenly, and the temperature was maintained at 80 °C for 2 hours of stirring treatment, filtered and washed with water until the solution was obtained. Nearly neutral; contact the filter cake with 10 liters of 0.5 mol / L ammonium nitrate aqueous solution, stir at 300 rpm, and stir at a constant temperature of 95 °C for 1 hour, then filter the molecular sieve, and leave a small sample for analysis of Na 2 O content; repeat the above operation until Na in the molecular sieve 2 The content of O reaches 2.5 wt %, and the obtained sample after drying is numbered NNY-2.

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Abstract

The invention discloses a modification method of a small-grain NaY-type molecular sieve. According to the invention, the NaY-type molecular sieve raw material with relatively high silica-to-alumina ratio, high crystallinity and good stability is adopted. Through sequential steps of alkali wash, ammonium exchange, hydrothermal treatment, and acid and ammonium salt mixed solution treatment, the obtained small-grain Y-type molecular sieve has relatively high SiO2 / A12O3 molar ratio as well as relatively high secondary pore proportion. Also, the stability of the Y-type molecular sieve is maintained. The molecular sieve has relatively high specific surface area and relatively high crystallinity. The Y-type molecular sieve provided by the invention is suitable to be used as a cracking component of a light oil hydrocracking catalyst. With the Y-type molecular sieve, the catalyst has the advantages of good activity, good heavy naphtha selectivity and excellent product quality.

Description

technical field [0001] The invention relates to a modification method of a NaY type molecular sieve, in particular to a modification method of a small grain NaY type molecular sieve. Background technique [0002] Y-type molecular sieve is the most common cracking active component in the field of heavy oil cracking. The grain size is generally about 1000nm, the grain size is relatively large, the channel is relatively long, the diffusion resistance is large, and it is difficult for macromolecules to enter the channel for reaction. The product after the reaction is also difficult to diffuse out, so its cracking activity and the selectivity of the target product are restricted. Compared with the conventional Y-type molecular sieve, the small-grained Y-type molecular sieve has a larger external surface area and more active centers on the external surface, which is conducive to improving the cracking capacity of macromolecular hydrocarbons, so it has more superior catalytic react...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B39/24B01J29/08
CPCB01J29/084C01B39/24C01P2002/72C01P2004/03C01P2004/62C01P2006/12C01P2006/14
Inventor 王占宇孙晓艳樊宏飞
Owner CHINA PETROLEUM & CHEM CORP
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