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Hydrogenation catalyst composition and preparation method thereof

A technology of hydrogenation catalyst and composition, applied in the direction of chemical instruments and methods, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc., can solve the problem of affecting catalyst activity, complex preparation process, active metal Aggregation and other issues

Active Publication Date: 2016-08-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are many deficiencies in the preparation process of the catalyst. Firstly, the reaction environment in the process of neutralization and gelation is uneven, the particle size of the prepared alumina particles is small, and the crystallinity is not high; Complex, and high-temperature calcination can easily cause the loss of catalyst specific surface area and pore volume, making the pore structure of the catalyst unsatisfactory; moreover, high-temperature calcination of the catalyst can easily cause active metals to gather and form inactive nickel-aluminum spinel, thus affecting the catalyst. activity and many other issues
[0005] CN101927197A relates to a hydrogenation catalyst and a preparation method in which the concentration of active metals and acidic additives is distributed in a gradient-decreasing manner. By preparing a relatively concentrated active metal solution and acidic additive solution, deionized water or ammonia water is gradually added during the impregnation of the carrier The method of diluting the solution is saturated and sprayed on the carrier; or by preparing at least two active metal solutions and acidic additive solutions with different concentrations, and spraying them on the carrier according to the concentration of the active metal solution and the acidic additive solution from high to low; or using Impregnation with a solution with a higher concentration of acidic additives, gradually adding a solution with a lower concentration of acidic additives during the impregnation process and diluting with deionized water; drying and roasting; impregnation with a solution with a higher concentration of active metals, gradually adding active metals during the impregnation process Impregnation in a solution with a lower metal concentration and dilution with deionized water; or the acidic additive impregnation step is carried out after metal impregnation; drying and roasting; It is easy to cause the blockage of the catalyst pore structure and the destruction of the pores, and the preparation process is complicated, time-consuming and labor-intensive
At present, there are few reports on the preparation method of alumina with gradient distribution of additive concentration

Method used

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  • Hydrogenation catalyst composition and preparation method thereof
  • Hydrogenation catalyst composition and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0060] This example introduces the preparation method of Mo, Ni, P active metal solution. In this example, only one original solution of Mo, Ni, and P with one concentration and ratio is prepared, and solutions with other ratios and concentrations can be prepared according to the method introduced.

[0061] Take 386g of molybdenum oxide and 123g of basic nickel carbonate into a multi-necked flask, add a certain amount of deionized water, stir until the substance in the bottle is slurry, then slowly add 86g of phosphoric acid, and then heat slowly after the initial reaction , keep the solution temperature at 90-110° C. for 1-3 hours, stop heating, filter the resulting solution while it is hot, and then adjust the pH value of the solution to 1.0-4.0 with phosphoric acid to obtain a clear dark green original solution. The solution composition is MoO 3 : 69.27g / 100ml; NiO: 12.49g / 100ml.

[0062] Get 296g ammonium molybdate, 105g nickel nitrate is put into multi-necked flask, aft...

Embodiment 2

[0065] Add bottom water to the bottom of the impingement flow reactor, and heat to 90°C; start the impingement flow reactor, and adjust the frequency of the ultrasonic generator to 20kHz. Adjust the impact direction of the two acceleration tubes to be horizontal, and start the accelerator to inject AlCl with a concentration of 45g / 100mL 3 The solution is injected from the feed port I at a flow rate of 15L / h, and after the liquid is atomized through the pressure atomization nozzle, the acceleration tube at the feed port II level with it is sprayed out through the pressure atomization nozzle and injected into NaAlO at a flow rate of 20L / h 2 Solution (concentration is 20g / 100ml), Na 2 SiO 3 Solution (concentration: 20g / 100ml), alkaline active metal solution (concentration: 30g / 100ml) mixed solution hit each other, react for 30min, stop injecting liquid and bottom ultrasonic generator; Ports III and IV were added with NaAlO at the same time at 15L / h 2 (solution concentration is...

Embodiment 3

[0067] Add bottom water to the bottom of the impingement flow reactor, and heat to 90°C; start the impingement flow reactor, and adjust the frequency of the ultrasonic generator to 30kHz. Adjust the impact direction of the two accelerator tubes to make a horizontal impact, and start the accelerator to inject AlCl 3 solution (30g / 100mL), ZrCl 4 Solution (concentration of 20g / 100ml) and alkaline active metal solution (concentration of 40g / 100mL) are injected from the feed port I at a flow rate of 25L / h, and the liquid is atomized through the pressure atomization nozzle to the level of the liquid The acceleration tube at the feed inlet II is sprayed out through the pressure atomization nozzle and NaAlO is continuously added at the same time at 16L / h 2 The solutions (concentration: 35g / 100mL) collide with each other, react for 25min, stop injecting the liquid and the bottom stirrer; at the same time, feed NaAlO continuously at 16L / h at the feed ports III and IV at the bottom of t...

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Abstract

The invention discloses a hydrogenation catalyst composition and its preparation method. The hydrogenation catalyst composition comprises an alumina carrier, active metal and an auxiliary agent, wherein the active metal is one or more metals selected from VIII group and / or VIB group metallic elements; and the auxiliary agent is one or two elements selected from silicon or zirconium. Concentration of silicon or zirconium in the catalyst is metered according to oxide and gradually decreases from the catalyst granule center to the external surface. Content of silicon and / or zirconium at R of granules is 1.0-3.0 wt%; content of silicon and / or zirconium at 1 / 3 of R is 0.5-1.0 wt%, and content of silicon and / or zirconium at 2 / 3 of R is 0.1-0.5 wt%, wherein R is radius of catalyst granules with the catalyst center as the starting point. The catalyst prepared by an impinging stream co-precipitation gelling mode has the following advantages: particle size distribution is centralized; the catalyst has an ideal pore structure; contents of the auxiliary agent and the active metal in the catalyst are reduced gradiently; inactivation rate of the catalyst can be effectively reduced; and metal-removal and metal-holding capabilities of the catalyst are enhanced.

Description

technical field [0001] The invention relates to a hydrogenation catalyst composition and a preparation method thereof, in particular to a hydrogenation catalyst composition with a gradient distribution of additives and active metal concentrations and a method thereof. Background technique [0002] Crude oil and distillates derived from crude oil contain impurities such as sulfur, nitrogen, oxygen and metals. The existence of these impurities not only affects the stability of the oil, but also emits SO during use. X , NO X and other harmful gases pollute the environment. During the secondary processing of oil products, the presence of impurities such as sulfur, nitrogen, oxygen and metals can poison catalysts. Therefore, removing the above-mentioned impurities is an important process in oil processing. Distillate oil hydrotreating refers to the process of contacting raw oil and hydrogen with a catalyst at a certain temperature and pressure to remove impurities and saturat...

Claims

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Application Information

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IPC IPC(8): B01J23/883C10G45/08
Inventor 吕振辉彭绍忠高玉兰张学辉徐黎明佟佳
Owner CHINA PETROLEUM & CHEM CORP
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