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ZSM-35 molecular sieve preparation method

A ZSM-35 and molecular sieve technology, applied in the field of ZSM-35 molecular sieve preparation, can solve the problems of inability to guarantee the stability of isobutene-selective catalysts, long residence time in pores, poor diffusion performance, etc., and achieve excellent catalytic performance and voids between molecular sieves. The effect of large, small thickness and particle size

Active Publication Date: 2019-01-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the residence time of the ZSM-35 molecular sieve prepared by this method is too long, the diffusion performance of reactants and products in the molecular sieve is not good, and under the condition of too many acid sites, n-butene dimerization easily occurs to form octane Cracking of ene and octene into propylene and pentene, hydrogen transfer and coking and other side reactions
Once carbon deposits are formed in the catalytic reaction, the selectivity of isobutene and the stability of the catalyst cannot be guaranteed

Method used

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  • ZSM-35 molecular sieve preparation method
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  • ZSM-35 molecular sieve preparation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] Step A, under the condition of 40 ℃, 600g silica sol (SiO 2 content is 25%) and 0.28g sodium hydroxide join in 1440g distilled water, add 31.9g aluminum sulfate (Al 2 o 3 content is 16%), continue to stir for a period of time until the solution is uniform, slowly add 114.7g of pyridine, and then add 21g of ethylenediamine to obtain a ZSM-35 molecular sieve mixture;

[0046] The molar ratio of the obtained ZSM-35 molecular sieve mixture is Al 2 o 3 : 50SiO 2 : 1600H 2 O: 7 organic template agent I + 29 organic template agent II: 0.14OH - ;

[0047] Step B, heating the ZSM-35 molecular sieve mixture at a stirring speed of 300 rpm to 180° C., and crystallizing at a constant temperature for 20 hours to obtain a crystallized ZSM-35 molecular sieve mixture;

[0048] Step C, filter, wash and dry the crystallized ZSM-35 molecular sieve mixture at 120°C, transfer the dried molecular sieve to a muffle furnace for calcination at 400°C, and finally obtain nanosheets ZSM-35 ...

Embodiment 2

[0051] The difference from Example 1 is that the gelling temperature is changed to 50°C, the amount of sodium hydroxide is changed to 0.32g, the amount of distilled water is changed to 1620g, the amount of pyridine is changed to 102.8g, and the first organic template is changed to cyclo Hexylamine, the dosage is 29.7g, the order of adding the first organic template agent and the second organic template agent is changed to be added at the same time, the crystallization temperature is changed to 190°C, the constant temperature crystallization time is changed to 24h, and the drying temperature is changed to 130°C , the calcination temperature was changed to 450°C, and the rest of the components and conditions remained unchanged;

[0052] The molar ratio of the obtained ZSM-35 molecular sieve mixture is Al 2 o 3 : 50SiO 2 : 1800H 2 O: 6 organic template agent I + 26 organic template agent II: 0.16OH - .

[0053] The obtained sample is analyzed by BET, and the specific surface...

Embodiment 3

[0055] The difference from Example 1 is that the gel forming temperature is changed to 30° C., the amount of silica sol is changed to 720 g, the amount of sodium hydroxide is changed to 0.3 g, the amount of distilled water is changed to 1350 g, and the second organic template is changed to piperin Pyridine, the consumption is 102.2g, the order of adding the first organic template agent and the second organic template agent is changed to first add the first organic template agent and then the second organic template agent, the constant temperature crystallization time is changed to 24h, and the drying temperature is changed to 24h. is 140°C, the calcination temperature is changed to 450°C, and the rest of the components and conditions remain unchanged;

[0056] The molar ratio of the obtained ZSM-35 molecular sieve mixture is Al 2 o 3 : 60SiO 2 : 1500H 2 O: 7 organic template agent I + 24 organic template agent II: 0.15OH - .

[0057] The obtained sample was analyzed by BE...

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Abstract

The invention relates to a ZSM-35 molecular sieve and a preparation method thereof. The method comprises: carrying out mixing gelling on a silicon source, an aluminum source, an alkali, water, an organic template agent I and an organic template agent II, carrying out hydrothermal crystallization, filtering, washing, drying, and roasting to obtain a ZSM-35 molecular sieve, wherein the ZSM-35 molecular sieve has a sheet-like structure along the c-axis direction. According to the present invention, through the synergistic action of the organic template agent I and the organic template agent II, the prepared nano-sheet-like ZSM-35 molecular sieve has characteristics of small particle size and high specific surface area, wherein the diffusion rate is obviously improved through the small particle size, such that the reactant molecules and the product molecules can rapidly enter and exit the molecular sieve pore channels so as to reduce the occurrence probability of carbon deposition, the gapbetween the molecular sieves is large, and the thickness and the particle size are small so as to prolong the regeneration cycle of the catalyst and improve the selectivity of the product.

Description

technical field [0001] The invention belongs to the technical field of ZSM-35 molecular sieve preparation, and relates to a ZSM-35 molecular sieve and a preparation method thereof. Background technique [0002] ZSM-35 molecular sieve is a medium-porous zeolite developed by Mobil Corporation, with a FER-type framework structure. Naturally occurring FER zeolite is a silicon-rich crystalline zeolite whose crystal structure belongs to the orthorhombic system. It has a two-dimensional channel structure perpendicular to each other, that is, a ten-membered ring channel (0.42×0.54nm) parallel to the (001) plane and an eight-membered ring channel (0.35×0.48nm) parallel to the (010) plane. The ring channel and the six-membered ring channel intersect in the C direction to form a spherical cage (FER cage). [0003] The catalytic performance of molecular sieves is closely related to the crystal structure and morphology of molecular sieves. With its unique ten-membered ring structure, ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B39/44B82Y30/00B01J29/65B01J35/10
CPCB82Y30/00C01B39/445B01J29/65C01P2004/62C01P2004/64C01P2006/12C01P2004/03C01P2002/72B01J35/40B01J35/615Y02P20/584
Inventor 吴凯任行涛贾志光杨怀军裴庆君杨光刘艳惠
Owner CHINA PETROLEUM & CHEM CORP
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