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Hydrogenation catalyst, preparation method thereof, and hydrotreating method of aromatic hydrocarbon-containing oil

A hydrogenation catalyst and catalyst technology, applied in molecular sieve catalysts, chemical instruments and methods, hydrogenation and refining of aromatics, etc., can solve the problems of low saturation of aromatics, poor thermal and hydrothermal stability, and low proportion of secondary pores, etc. problem, to achieve high aromatic saturation

Active Publication Date: 2019-05-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

CN1382632A discloses a super-stabilizing method of small-grain Y-type zeolite, which is obtained by contacting the dry gas of silicon tetrachloride with small-grain NaY zeolite and washing it. The stability is poor, and the inventive method adopts gas-phase dealumination to supplement silicon to process molecular sieves, which makes the thermal and hydrothermal stability of the product worse, and the activity is low
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

Method used

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  • Hydrogenation catalyst, preparation method thereof, and hydrotreating method of aromatic hydrocarbon-containing oil
  • Hydrogenation catalyst, preparation method thereof, and hydrotreating method of aromatic hydrocarbon-containing oil
  • Hydrogenation catalyst, preparation method thereof, and hydrotreating method of aromatic hydrocarbon-containing oil

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preparation example Construction

[0044] In the present invention, the mother liquor after crystallization can be prepared according to conventional methods in the art, for example, when the ten-membered ring silica-alumina molecular sieve is ZSM-22 molecular sieve, the preparation method of the mother liquor after crystallization can refer to the literature O.Muraza et al., Microporous and Mesoporous Materials 206 (2015) 136-143; when the ten-membered ring silicon aluminum molecular sieve is ZSM-48 molecular sieve, the preparation method of the mother liquor after crystallization can refer to the literature P.Me'riaudeau et al / Journal of Catalysis, 1999(185), 435-444, or refer to US Patent Application US5961951. In one embodiment, the preparation process of the crystallization mother liquor of the ten-membered ring silica-alumina molecular sieve includes: preparing a silicon-containing solution, an aluminum-containing solution, and an alkaline liquid, mixing the above-mentioned liquids to form gels, and then ...

preparation example 1

[0077] (1) Preparation of mother liquor after crystallization

[0078] Get 45 grams of white carbon black, 1.25 grams of analytically pure Al 2 (SO 4 ) 3 18H 2 O, 1.88 grams of analytically pure NaOH and 39.3 grams of hexamethylenediamine are ready for use. Mix hexamethylenediamine with silica and 200 g of deionized water, NaOH and Al 2 (SO 4 ) 3 18H 2 O and 272 grams of deionized water were mixed, and then the two solutions were mixed, stirred for 1 hour, then transferred to a reaction kettle, and crystallized at 160° C. for 72 hours.

[0079] (2) Preparation of filter cake

[0080] Filter the mother liquor after crystallization prepared in the operation (1), and continue suction filtration for 5 minutes when there is no filtrate on the filter cake, and obtain the filter cake F-1, which has a dry basis content of 11.2 %, the silica / alumina molar ratio is 30.2.

[0081] (3) Preparation of molecular sieve precursor

[0082] The filter cake F-1 was raised from room te...

preparation example 2

[0089] The ZSM-48 molecular sieve was prepared according to the method of Preparation Example 1, except that in step (3), the filter cake F-1 was raised from room temperature to 350°C at a heating rate of 5°C / min, and kept at a constant temperature for 14 hours. During the heating process, the roasting furnace is a closed roasting furnace to obtain the molecular sieve precursor C-2. The finished product H-2 of ZSM-48 molecular sieve was obtained.

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Abstract

The invention relates to the field of hydrotreating of aromatic hydrocarbon-containing oil and particularly provides a hydrogenation catalyst, a preparation method thereof, and a hydrotreating methodof aromatic hydrocarbon-containing oil. The catalyst contains a supporter and an active metal component supported on the supporter. The active metal component is at least one selected from metal elements in VIB group and non-noble metal element in the VIII group. The supporter contains a ten-membered silicon-aluminum molecular sieve of which the molar ratio of silicon oxide to aluminum oxide is 120-300. The supporter has mesoporous structure; a closed hysteresis loop exists at the position P / P0 = 0.4-0.99 on a low temperature nitrogen adsorption-desorption curve, the start position of the closed hysteresis loop being at the position P / P0 = 0.4-0.7. When the hydrogenation catalyst is used for hydrotreating of the aromatic hydrocarbon-containing oil, a target product is high in aromatic hydrocarbon saturation degree.

Description

technical field [0001] The invention relates to the field of hydrogenation treatment of oil containing aromatics, in particular to a hydrogenation catalyst, a preparation method thereof and a method for hydrogenation of oils containing 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, good biological performance, in line with environmental protection requirements. [0003] To solve the above problems,...

Claims

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Application Information

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IPC IPC(8): B01J29/78C10G45/54C01B39/46
Inventor 毕云飞夏国富李明丰杨清河张乐李洪宝郭庆洲王鲁强方文秀
Owner CHINA PETROLEUM & CHEM CORP
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