A kind of preparation method of nay molecular sieve

A technology of molecular sieve and silica-alumina gel, which is applied in the direction of crystalline aluminosilicate zeolite and octahedral crystalline aluminosilicate zeolite, etc., can solve the problems of long time-consuming depolymerization of silica gel, low utilization rate of silicon source, and high feeding water volume. Achieve clean production, save energy consumption, and improve the effect of solid content

Active Publication Date: 2019-09-24
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, most of the industry adopts the method proposed in US3671191 to produce NaY molecular sieves, but there are problems in that the amount of feed water is high, the ratio of feed silicon to aluminum is high, and the utilization rate of silicon sources is low, which makes the single-pot yield of the product low.
However, this method takes a long time to depolymerize silica gel, and the preparation process of synthetic gel is relatively complicated, and the synthesized NaY crystal grains are relatively small, only 200nm-400nm

Method used

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  • A kind of preparation method of nay molecular sieve
  • A kind of preparation method of nay molecular sieve

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preparation example Construction

[0024] The present invention provides a method for preparing NaY molecular sieves, the method comprising: a. uniformly mixing a directing agent, a silicon source, an aluminum source and water to obtain a silica-alumina gel mixture, wherein, in terms of oxides and moles, the The composition of the silica-alumina gel mixture is Na 2 O: Al 2 o 3 : SiO 2 :H 2 O=(1.5-10):1:(5-18):(100-500), preferably Na 2 O: Al 2 o 3 : SiO 2 :H 2O=(2-6):1:(6-10):(150-400); b, filter the silica-alumina gel mixture obtained in step a to obtain a gel filter cake; c, filter the silica-alumina gel mixture obtained in step b The obtained gel filter cake is subjected to crystallization treatment to obtain a crystallized product; d. Washing and drying the crystallized product obtained in step c to obtain NaY molecular sieve. It should be noted that in the process of preparing the silica-alumina gel mixture in the method of the present invention, the addition of water is not particularly strictly ...

Embodiment 1

[0042] This example illustrates the preparation method of the directing agent used in the present invention.

[0043] With 378 water glass (Qilu Catalyst Company provides, SiO 2 251.5g / L, modulus 3.3, density 1260g / L) is put into the beaker, add 282g perbasic sodium metaaluminate (provided by Qilu Catalyst Company, Al 2 o 3 41g / L, Na 2 (297g / L, density 1353g / L) and 38g of water, aged at 30°C for 18 hours to obtain the directing agent. The molar ratio of the directing agent is 16.5Na 2 O: Al 2 o 3 :15SiO2 2 :350H 2 O.

Embodiment 2

[0045] This example illustrates the preparation method of the NaY molecular sieve provided by the invention.

[0046] Under stirring state, to 126g water glass (provided by Qilu Catalyst Company, SiO 2 251.5g / L, modulus 3.3, density 1260g / L) add the directing agent that 25g embodiment 1 prepares, 20g aluminum sulfate solution (Qilu Catalyst Company provides, Al 2 o 3 90g / L, H 2 SO 4 259g / L, density 1277g / L), 32g low-alkali sodium metaaluminate solution (provided by Qilu Catalyst Company, Al 2 o 3 186.7g / L, Na 2 (280.8g / L, density 1405g / L) and 100g water are mixed homogeneously, and the silica-alumina gel mixture of gained is filtered in suction filter, and with the water rinse of 10 times of filter cake volume, drain, will obtain 204g gel filter cake (dry basis is 24.0%) is directly packed in the stainless steel reactor and is crystallized at 100 ℃ for 26h, and the crystallized product is through filtering, washing, and 120 ℃ of drying overnights in oven, obtains NaY...

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Abstract

The invention discloses a method for preparing a NaY molecular sieve. The method comprises the following steps: a, uniformly mixing a guiding agent, a silicon source, an aluminum source and water so as to obtain a silicon-aluminum gel mixture, wherein the silicon-aluminum gel mixture contains Na2O, Al2O3, SiO2 and H2O in a mole ratio of oxides of (1.5-10):1:(5-18):(100-500); b, filtering the silicon-aluminum gel mixture obtained in the step a so as to obtain gel filter cakes; c, performing crystallization treatment on the gel filter cakes obtained in the step b so as to obtain a crystallization product; and d, washing and drying the crystallization product obtained in the step c, thereby obtaining the NaY molecular sieve. As the silicon-aluminum gel is filtered and washed before crystallization, the single kettle yield of synthesis of the NaY molecular sieve is increased, the energy consumption in heating for synthesizing gel is reduced, impurity ions in synthesized gel can be removed, direct recycling of crystallization mother liquor is facilitated, and clean production of the NaY molecular sieve is achieved.

Description

technical field [0001] The invention relates to a preparation method of NaY molecular sieve. Background technique [0002] As a catalyst active component or catalyst carrier, Y-type molecular sieve can be widely used in refining and chemical processes such as catalytic cracking, hydrocracking and isomerization, and is currently the most used zeolite material. NaY molecular sieve, as the raw material of petroleum cracking catalyst, generally requires its silicon-aluminum ratio to be greater than 5.0 in order to maintain sufficient hydrothermal stability during use. At present, the method for industrially producing NaY molecular sieves basically adopts the directing agent method proposed by the U.S. GRACE company (U.S. Patent No. NaY molecular sieves were prepared by thermal crystallization. The preparation method that US3639099 proposes is because the feeding basicity is bigger, and the silicon-aluminum ratio of the prepared NaY molecular sieve is generally 4.0-4.5; And whe...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B39/24
Inventor 王维家罗一斌
Owner CHINA PETROLEUM & CHEM CORP
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