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Small crystal grain molecular sieve preparation method

A technology of molecular sieve and small grain, applied in the direction of crystalline aluminosilicate zeolite, octahedral crystalline aluminosilicate zeolite, etc.

Active Publication Date: 2006-06-21
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0040] The above-mentioned methods for synthesizing small-grain faujasite can often only synthesize X-type molecular sieves or SiO 2 / Al 2 o 3 Y-type molecular sieve with lower silicon-aluminum ratio <5

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0058] This example illustrates the implementation of the method provided by the present invention.

[0059] The directing agent was prepared as described in Comparative Example 1.

[0060] NaY molecular sieve according to 2.76Na 2 O:Al 2 o 3 : 8.4SiO2 2 :209H 2 O ratio synthesis. Under stirring, add 450ml of deionized water, 200.4g of directing agent, 300ml of aluminum sulfate solution and 243ml of low sodium metaaluminate solution into 949ml of water glass in sequence, continue to stir vigorously for 30min after the addition, and then statically age at 60°C for 23h , add 248ml water glass, make the total feeding ratio be 3.37Na 2 O:Al 2 o 3 : 10.4SiO 2 :233H 2 O, continue the crystallization for 15 hours to obtain the small-grain high-silicon NaY molecular sieve prepared by the method of the present invention.

[0061] Gained sample measures its relative crystallinity by X-ray diffraction method to be 97%, SiO 2 / Al 2 o 3 is 5.90. The grain size measured by th...

Embodiment 2

[0071] This example illustrates the implementation of the method provided by the present invention.

[0072] According to the NaY molecular sieve synthesis gel prepared in Example 1, after static aging at 80°C for 20h, add 74ml of water glass, heat up to 100°C and continue crystallization for 15h to obtain the small-grain high-silicon NaY molecular sieve prepared by the method of the present invention .

[0073] Gained sample measures its relative crystallinity by X-ray diffraction method to be 102%, SiO 2 / Al 2 o 3 It is 5.72, and the grain size measured by the scanning electron microscope is 100-200nm.

Embodiment 3

[0075] This example illustrates the implementation of the method provided by the present invention.

[0076] According to the NaY molecular sieve synthesis gel prepared in Example 1, after static aging at 70°C for 6h, add 320ml of water glass, heat up to 100°C and continue crystallization for 25h to obtain the small-grain high-silicon NaY molecular sieve prepared by the method of the present invention .

[0077] Gained sample measures its relative crystallinity by X-ray diffraction method to be 108%, SiO 2 / Al 2 o 3 It is 6.10, and the grain size measured by scanning electron microscope is 300-600nm.

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PUM

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Abstract

The invention discloses a method for preparing the NaY molecular screen of high alumina silica ratio and fine grain, firstly synthesizing NaY molecular screen guilding agent according to current technology, then producing gel with sodium silicate, guilding agent, acid aluminium salt and sodium metaaluminate, blooming the gei under the temperature of 50-100 Deg C for 0-70 hours, adding some silicon, then blooming continuously under temperature of 90-120 Deg C for 0.5-50 hours, finally filtering, washing and drying. The NaY molecular screen with the alumina silica ratio being 5.2-7.0, and fine grain being 100-400 nm can be prepared by using the method in this invention.

Description

technical field [0001] The invention relates to a preparation method of NaY molecular sieve. More specifically, it relates to a preparation method of a small-grain high-silicon NaY molecular sieve. Background technique [0002] As the core technology of the oil refining industry, catalytic cracking and its catalysts have attracted much attention. As the catalytic cracking feedstock becomes heavier, the proportion of macromolecular hydrocarbons with an average size above 2nm in the feedstock continues to increase. The Y-type molecular sieve, which is the main active component of the catalytic cracking catalyst, has a pore size of only 0.7nm. Obviously, a large number of raw material molecules cannot enter the channels of the Y-type molecular sieve for reaction. Although the macromolecules in the feedstock can be precracked on the catalyst substrate, the diffusion effect still has a significant impact on the catalytic cracking reaction. The small-grain Y-type molecular siev...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B39/02C01B39/24
Inventor 刘中清舒兴田罗一斌崇奇宗保宁慕旭宏何鸣元
Owner CHINA PETROLEUM & CHEM CORP
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