A method for producing lubricating oil base oil by combining catalyst and hydrocracking tail oil

A combination catalyst and catalyst technology, applied in chemical instruments and methods, catalyst activation/preparation, molecular sieve catalysts, etc., can solve the problems of mesopores without structure, reduce interaction, etc. effect of effect

Active Publication Date: 2020-11-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The seed crystal selected in this invention is a microporous molecular sieve, which is added to the preparation system after silanization, and its hydrophobicity is used to increase its effect on the hydrophobic end of the surfactant micelle, thereby reducing the interaction between the two directing agents. However, the formed mesopores still do not have a regular structure, and whether the addition of seed crystals reduces the amount of templating agent has not been reported.

Method used

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  • A method for producing lubricating oil base oil by combining catalyst and hydrocracking tail oil
  • A method for producing lubricating oil base oil by combining catalyst and hydrocracking tail oil
  • A method for producing lubricating oil base oil by combining catalyst and hydrocracking tail oil

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preparation example Construction

[0032] 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 molecular sieve is ZSM-22 molecular sieve, the preparation method of the mother liquor after crystallization can refer to document O. Muraza et al., Microporous and Mesoporous Materials 206 (2015) 136–143. When the ten-membered ring silica-alumina molecular sieve is ZSM-48 molecular sieve, the preparation method of the crystallized mother liquor can refer to the literature P. Me´ riaudeau et al / Journal of Catalysis, 1999 (185), 435-444, or refer to the United States Patent application US5961951. In one embodiment, the preparation process of the crystallized mother liquor includes: preparing a silicon-containing solution, an aluminum-containing solution, and an alkaline liquid, mixing the above-mentioned liquids to form a gel, and then performing crystallization at a certain temperature.

[0033] In the ...

preparation example 1

[0053] (1) Preparation of crystallized mother liquor

[0054]Take 36.3 grams of SiO containing 40% by weight 2 silica sol, 1.77 g of analytically pure Al 2 (SO 4 ) 3 18H 2 O, 3.94 grams of analytically pure KOH and 8.44 grams of hexamethylenediamine are ready for use. Hexamethylenediamine was mixed with silica sol, KOH and Al 2 (SO 4 ) 3 18H 2 O and 89.4 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.

[0055] (2) Preparation of filter cake

[0056] Filter the crystallized mother liquor prepared in step (1), and continue suction filtration for 5 minutes when there is no filtrate on the filter cake. The filter cake F-1 obtained has a dry basis content of 11.2 % by weight, the silica / alumina molar ratio is 60.

[0057] (3) Preparation of molecular sieve precursor

[0058] The filter cake F-1 was raised from room temperature to 450° C. at a ...

preparation example 2

[0066] (1) Preparation of crystallized mother liquor

[0067] 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.

[0068] (2) Preparation of filter cake

[0069] Filter the crystallized mother liquor prepared in step (1), and continue suction filtration for 5 minutes when there is no filtrate on the filter cake. The filter cake F-2 obtained has a dry basis content of 11.2 % by weight, the silica / alumina molar ratio is 60.

[0070] (3) Preparation of molecular sieve precursor

[0071] The filter cake F-2 was raised from room temperature to 450° C. at a he...

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Abstract

The invention relates to the field of hydrocracking tail oil and particularly relates to a composite catalyst and method of using hydrocracking tail oil to produce lubricant base oil. The composite catalyst includes a first catalyst and a second catalyst. The first catalyst contains a ten-membered ring molecular sieve M1 and the second catalyst contains a ten-membered ring molecular sieve M2, wherein the molar ratio of silicon oxide to aluminum oxide in the ten-membered ring silicon-aluminum molecular sieves M1 and / or M2 is 120-300. The molecular sieves contain mesoporous structures; a closedhysteresis 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.The composite catalyst is used for hydrocracking of tail oil to produce lubricant base oil, great pour point declining effect can be achieved. The lubricant base oil is high in yield and viscosity index.

Description

technical field [0001] The invention relates to the field of hydrotreating of hydrocracking tail oil, in particular to a method for producing lubricating oil base oil by combining a catalyst and hydrocracking tail oil. Background technique [0002] Molecular sieve material has high acidity and high specific surface area, and is an excellent acidic catalyst. At the same time, molecular sieve materials have strong chemical stability and hydrothermal stability, and are difficult to be destroyed by corrosion and dissolution of reactants. Compared with commonly used homogeneous catalysts, molecular sieve material catalysts can be directly reused without separation, and will not pollute the environment and products. The specific surface area and other pore structure parameters of molecular sieve materials have an important influence on the catalytic performance of molecular sieves. Therefore, the preparation of molecular sieves with special channels is an important research direc...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/74B01J35/10B01J37/08B01J37/10B01J37/18C10G49/08
Inventor 毕云飞夏国富杨清河龙湘云黄卫国郭庆洲方文秀
Owner CHINA PETROLEUM & CHEM CORP
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