Y molecular sieve high in silica alumina ratio and abundant in secondary holes and preparation method therefor

A secondary pore, silicon-aluminum ratio technology, applied in the direction of crystalline aluminosilicate zeolite, octahedral crystalline aluminosilicate zeolite, etc., can solve the problems of limiting the range of molecular sieve raw materials, increasing hydrothermal dealumination to create mesopores, etc., to achieve The effect of widening the selection range of raw materials, low reagent cost, and enriching the secondary pore structure

A secondary pore, silicon-aluminum ratio technology, applied in the direction of crystalline aluminosilicate zeolite, octahedral crystalline aluminosilicate zeolite, etc., can solve the problems of limiting the range of molecular sieve raw materials, increasing hydrothermal dealumination to create mesopores, etc., to achieve The effect of widening the selection range of raw materials, low reagent cost, and enriching the secondary pore structure

CN104843736AInactive Publication Date: 2015-08-19BC P INC CHINA NAT PETROLEUM CORP +1

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  • Y molecular sieve high in silica alumina ratio and abundant in secondary holes and preparation method therefor
  • Y molecular sieve high in silica alumina ratio and abundant in secondary holes and preparation method therefor

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] This example provides a Y molecular sieve with a high silicon-aluminum ratio and abundant secondary pores, which is prepared by the following steps:

[0046] Weigh 20.0g of the NaY zeolite sample that was dried overnight and place it in a quartz reaction tube, pass nitrogen gas into it, and do a good job of leak detection. Furnace heating program: From the initial temperature of 30°C to 500°C for 100 minutes, keep it for 120 minutes, then stop heating, when the temperature naturally drops to 270°C, pass through the 4 saturated N 2 At the same time, the temperature was raised to 430°C at a heating rate of 4°C / min for 40 minutes. After the reaction was completed, the SiCl 4 saturated N 2 , N 2 Continue purging for 120 minutes, then stop heating and cool down naturally, take out the sample and wash and dry to obtain the crude product;

[0047] Take 10 g of the crude product, add it to 200 mL of sodium hydroxide solution with a concentration of 0.1 mol / L, heat it in a w...

Embodiment 2

[0053] This example provides a Y molecular sieve with a high silicon-aluminum ratio and abundant secondary pores, which is prepared by the following steps:

[0054] Weigh 20.0g of the NaY zeolite sample that was dried overnight and place it in a quartz reaction tube, pass nitrogen gas into it, and do a good job of leak detection. Furnace heating program: From the initial temperature of 30°C to 500°C for 100 minutes, keep it for 120 minutes, then stop heating, when the temperature naturally drops to 270°C, pass through the 4 saturated N 2 At the same time, the temperature was raised to 510°C at a heating rate of 4°C / min for 1h. After the reaction was completed, the SiCl 4 saturated N 2 , alone N 2 Continue purging for 120 minutes, then stop heating and cool down naturally, take out the sample and wash and dry to obtain the crude product;

[0055] Take 10 g of the crude product, add it to 200 g of sodium hydroxide solution (concentration: 0.15 mol / L), heat in a water bath at...

Embodiment 3

[0061] This example provides a Y molecular sieve with a high silicon-aluminum ratio and abundant secondary pores, which is prepared by the following steps:

[0062] Weigh 20.0g of the NaY zeolite sample that was dried overnight and place it in a quartz reaction tube, pass nitrogen gas into it, and do a good job of leak detection. Furnace heating program: From the initial temperature of 30°C to 500°C for 100 minutes, keep it for 120 minutes, then stop heating, when the temperature naturally drops to 270°C, pass through the 4 saturated N 2 At the same time, the temperature was raised to 510°C at a heating rate of 3°C / min for 80 minutes. After the reaction was completed, the SiCl 4 saturated N 2 , N 2 Continue purging for 120 minutes, then stop heating and cool down naturally, take out the sample and wash and dry to obtain the crude product;

[0063] Take 10 g of the crude product, add it to 200 g of sodium hydroxide solution (concentration: 0.2 mol / L), heat it in a water bat...

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Abstract

The invention provides a Y molecular sieve high in silica alumina ratio and abundant in secondary holes and a preparation method therefor. The preparation method comprises steps of: Y-type zeolite is processed for 1-5 hours at 300-600 DEG C to obtain dry Y-type zeolite, and calculated by SiO2 and Al2O3, the silica alumina mole ratio of the Y-type zeolite is (3-6):1;the temperature is lowered to 200-600 DEG C;in a waterless dry environment, dry air saturated by a dealuminated siliceous reinforcing agent is introduced to the dry Y-type zeolite to react for 0.5h-7h, or in a waterless dry environment, the temperature is raised to 500-700 DEG C at a constant speed, at the same time, the dry air saturated by a dealuminated siliceous reinforcing agent is introduced to the dry Y-type zeolite to react for 0.5h-7h, and a rough product is obtained; the rough product is subjected to alkali treatment for 10min-5h at 30-100 DEG C, solid-liquid mass ratio for the alkali treatment is (1-50):1, and a Y molecule sieve high in silica alumina ratio and abundant in secondary holes is obtained. The invention further provides the Y molecule sieve high in the silica alumina ratio and abundant in secondary holes, obtained by adopting the preparation method and has high silica aluminum ratio and abundant secondary hole structures.

Description

technical field [0001] The invention relates to a Y molecular sieve with a high silicon-aluminum ratio and abundant secondary pores and a preparation method thereof, belonging to the technical field of molecular sieve preparation. Background technique [0002] Since the first industrial fluidized catalytic cracking unit was put into operation in 1942, it has developed into a core processing technology in the oil refining industry. Moreover, due to the characteristics of my country's own crude oil, the status of catalytic cracking technology is even more important. The importance of Y-type molecular sieve as the main active component of cracking catalyst is self-evident. [0003] Since Break's successful synthesis of Y-type molecular sieves, the world's energy structure and chemical composition have changed, triggering a revolution in petrochemicals. Today, after decades of changes, although synthetic materials emerge in endlessly, no one can shake the monopoly position of Y...

Claims

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Application Information

Patent Timeline
19 Aug 2015
Publication
CN104843736A
IPC
C01B39/24
Inventors
申宝剑; 袁德林