Preparation method of hydrodearomatization catalyst

A technology for hydrodearomatization and catalysts, which is applied in molecular sieve catalysts, chemical instruments and methods, and hydrogenation refining of aromatic hydrocarbons, etc. It can solve the problems of small-grain NaY molecular sieves such as poor hydrothermal stability, low silicon utilization rate, and complete structure.

Active Publication Date: 2016-10-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In this method, the raw material needs to be treated with ammonium hexafluorosilicate for dealumination of silicon, and then undergo hydrothermal treatment and other treatments, so as to reduce the collapse of the molecular sieve skeleton structure and improve the crystallization retention of the molecular sieve. After treatment with ammonium hexafluorosilicate for dealumination and silicon supplementation, due to the isomorphic substitution of silicon and aluminum, the molecular sieve silicon oxide aluminum structure is relatively complete, and then hydrothermal treatment will form less secondary pores, and the proportion of secondary pores is low. Facilitate the diffusion of reaction products, low saturation of aromatics
[0007] 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.
[0008] In the preparation process of the existing method, small-grain NaY molecular sieves, silicon and aluminum are easily lost, the utilization rate of silicon is low, and the distribution of silicon and aluminum is not uniform, and it is easy to appear agglomeration, so the existing methods still cannot prepare small-grain NaY molecular sieves with high silicon-aluminum ratio and good thermal stability and hydrothermal stability

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0049] This embodiment is to prepare raw material small grain NaY type molecular sieve

[0050] Preparation of NY-1

[0051] (1) Preparation of directing agent: Dissolve 8 g of sodium hydroxide solid in 80 g of water, add 2.5 g of sodium metaaluminate (Al 2 o 3 Content is 45wt%, Na 2 O content is 41wt%), then add 40g water glass (SiO 2 Content is 28wt%, Na 2 The O content is 8wt%), mixed evenly, and aged at 18° C. for 4 hours to prepare the directing agent.

[0052] (2) Preparation of amorphous silicon-aluminum precursor

[0053] Prepare solid sodium aluminate to a concentration of 0.3L for 100g A1 2 o 3 / L sodium aluminate working solution (a). Dilute the concentrated ammonia water with an appropriate amount of distilled water to obtain about 10wt% dilute ammonia water (b). SiO 2 28wt% sodium silicate solution, then diluted to 0.5L concentration is 140g SiO 2 / L sodium silicate working solution (c). Take a 5-liter steel reaction tank, add 0.5 liter of distilled w...

Embodiment 2

[0067] Firstly, ammonium exchange is carried out on the raw material small grain NaY molecular sieve NY-1. Formulated with NH 4 + and H + Concentrations of 1.0mol / L and 0.02mol / L solution (ammonium chloride and hydrochloric acid mixed solution) 10 liters. Weigh 1,000 grams of small-grain NaY molecular sieves, add them to the above mixed solution, stir at 300 rpm, and stir at a constant temperature of 90°C for 1 hour, then filter the molecular sieves, and leave a small sample for analysis of NaY 2 O content; repeat the above operation until Na in the molecular sieve 2 The content of O reached 1.5wt%, and the sample number after drying was NNY-1.

Embodiment 3

[0069] Firstly, ammonium exchange is carried out on the raw material small grain NaY molecular sieve NY-2. Formulated with NH 4 + and H + 10 liters of solutions (mixed solution of ammonium nitrate and nitric acid) with concentrations of 0.8.0mol / L and 0.01mol / L respectively. Weigh 1,000 grams of small-grain NaY molecular sieves, add them to the above mixed solution, stir at 300 rpm, and stir at a constant temperature of 95°C for 1 hour, then filter the molecular sieves, and leave a small sample for analysis of NaY 2 O content; repeat the above operation until Na in the molecular sieve 2 The O content reached 1.5wt%, and the sample number after drying was NNY-2.

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Abstract

The invention discloses a preparation method for a hydrogenation dearomatization catalyst. According to the method, a NaY type molecular sieve raw material with a high silica-alumina ratio, a high degree of crystallization and good stability is employed and successively undergoes ammonium exchange, primary hydro-thermal treatment, treatment with an alkali-containing solution, secondary hydro-thermal treatment and treatment with a mixed solution of acid and an ammonium salt, so a small-grain Y type molecular sieve is obtained. The small-grain Y type molecular sieve is used as an acidic component and cooperates with amorphous silicon-aluminum, active components and auxiliary components; and the obtained hydrogenation dearomatization catalyst has higher hydrogenation dearomatization activity and is especially applicable to hydrogenation dearomatization and decoloring of high-viscosity cycloalkyl white oil and solvent naphtha containing heavy aromatics.

Description

technical field [0001] The invention relates to a preparation method of a hydrogenation refining catalyst, in particular to a preparation method of a hydrogenation dearomatization catalyst. The catalyst is suitable for the hydrogenation process of aromatics, especially for the hydrogenation and dearomatization process of naphthenic oil containing heavy aromatics. Background technique [0002] Under aerobic conditions, the oil produced by hydroprocessing (such as high-grade lubricating oil, food-grade white oil, etc.) is very sensitive to sunlight and ultraviolet radiation. Exposure to sunlight and air will cause the appearance and performance of the oil to be unstable, and the color of the oil will deepen , in severe cases, precipitation occurs. This type of oil requires low viscosity, high flash point and boiling point, and low volatility. Colorless, odorless, low aromatics content, non-corrosive, good thermal stability and oxidation stability, not easy to cause gelation,...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/12B01J35/10C10G45/54
Inventor 樊宏飞孙晓艳王继锋王占宇
Owner CHINA PETROLEUM & CHEM CORP
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