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Hydroprocessing catalyst and its uses

A hydrogenation treatment and catalyst technology, applied in refining to remove heteroatoms, etc., can solve the problems of eased operating conditions, reduced stability, expensive precious metals, etc., and achieve less sulfur loss, improved stability, and good stability Effect

Active Publication Date: 2007-04-25
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, precious metal catalysts are generally used in the production of ultra-clean petroleum products, because this type of catalyst has high activity in a relatively "clean" environment, and the operating conditions are relatively mild, but the price of precious metals is very expensive, which greatly restricts its use. Application on industrial equipment
In general, the active phase of non-precious metal catalysts is in the sulfurized state. To maintain the activity of the catalyst, the active phase in the sulfurized state in the catalyst must not be lost. There is an equilibrium between the active phase in the sulfurized state and hydrogen itself, and sulfur is very weak in a low-sulfur environment. It is easy to lose and lead to a decrease in catalyst activity and stability. At present, there is no report on stabilizing the sulfurized active phase in the catalyst to improve catalyst activity and stability.

Method used

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  • Hydroprocessing catalyst and its uses

Examples

Experimental program
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Effect test

Embodiment 1

[0033] A preparation method of the catalyst of the present invention

[0034] Take SB powder and Y zeolite (provided by Wenzhou Catalyst Factory, unit cell parameter is 2.464nm, silicon-aluminum molar ratio is 27, sodium oxide content is 0.08wt%, specific surface area is 692m 2 / g, the pore volume is 0.41ml / g) and zinc oxide powder are thoroughly mixed, impregnated with a solution containing ammonium fluoride, nickel nitrate and ammonium tungstate, dried at 120°C for 8 hours and activated at 500°C for 4 hours. The obtained catalyst powder is pressed into tablets, and crushed into 60-80 mesh particles to obtain a catalyst, numbered E-1. The composition and properties of the catalyst are shown in Table 3, and the results of the micro-reverse evaluation are shown in Table 4.

Embodiment 2

[0036] A preparation method of the catalyst of the present invention

[0037] Take amorphous silicon aluminum dry glue powder (SiO 2 The content is 18wt%), zinc carbonate, ZSM-5 (provided by Nankai University, the molar ratio of silicon to aluminum is 48), SB powder and methylcellulose are thoroughly mixed, and then an appropriate amount of 66wt% of nitric acid and an appropriate amount of water are added for extrusion molding. After drying at 100°C for 12 hours and calcining at 600°C for 3 hours, a catalyst carrier was obtained. Take an appropriate amount of the carrier, first saturated with a solution containing ferric nitrate, dried at 200°C for 6 hours, and then impregnated with a solution containing nickel carbonate, ammonium molybdate and phosphoric acid, dried at 80°C for 6 hours, and calcined at 550°C for 4 hours. A catalyst was obtained, numbered E-2. The composition and properties of the catalyst are shown in Table 3, the conditions and results of the micro-reverse evalu...

Embodiment 3

[0039] A preparation method of the catalyst of the present invention

[0040] Take amorphous titanium aluminum dry rubber powder (TiO 2 The content is 7wt%), zinc chloride powder, SB powder and Sesbania powder are thoroughly mixed, and then extruded with acetic acid, citric acid and an appropriate amount of water as a peptizer, dried at 200°C for 2 hours, and calcined at 550°C for 8 hours to obtain Catalyst carrier. Take an appropriate amount of the carrier, impregnate it with a solution containing cobalt carbonate, ammonium molybdate, phosphoric acid and ferric chloride, then dry at 120°C for 4 hours and calcinate at 480°C for 6 hours to obtain a catalyst, numbered E-3. The composition and properties of the catalyst are shown in Table 3, and the conditions and results of the micro-reverse evaluation are shown in Table 4.

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Abstract

The invention disclosed a hydrogenating catalyst and its application. The catalyst contains not only hydrogenating active metal and alumina, it also contains silicon oxide, titanium oxide and molecular sieve (one kind or many kinds of them) and stabilizing agent iron, magnesium, zinc, gallium, calcium and barium (one kind or many kinds of them). The catalyst can stabilize the sulphur in the catalyst's sulfurized active phase so as to avoid the loss of sulphur in the active phase and improve the catalyst's stability substantially, especially under the conditions of low sulphur content or no sulphur at all. The invention can especially be used in the hydrodesulfurization and hydrogenation de-arene of distillate.

Description

Technical field [0001] The invention relates to a hydroprocessing catalyst. More specifically, the present invention relates to a catalyst capable of stabilizing the sulfided active phase in a low-sulfur or sulfur-free environment, and is particularly suitable for ultra-deep hydrodesulfurization, hydrodenitrogenation and hydrodearomatization of distillate oil. process. Background technique [0002] As the society attaches great importance to the environment and human health, environmental protection laws and regulations have increasingly strict requirements on the sulfur content in petroleum products, especially diesel fractions. The current sulfur content in diesel fractions of 0.05 wt% to 0.10 wt% is acceptable Yes, but soon the sulfur content will be required to be less than 0.05wt%, and the sulfur content will be required to be less than 350μg / g or even lower in the foreseeable future, and the 95% point of diesel fuel will be required to be less than 350℃. Whether this standa...

Claims

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Application Information

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IPC IPC(8): C10G45/04
Inventor 刘全杰方向晨徐会青贾立明王伟
Owner CHINA PETROLEUM & CHEM CORP
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