Unlock instant, AI-driven research and patent intelligence for your innovation.

Heavy oil hydrotreating catalyst and its preparation method

A heavy oil hydrogenation and catalyst technology, which is applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, catalyst carrier, etc., can solve the problem of low specific surface area of ​​carrier alumina, unfavorable dispersion of active components, incomplete vulcanization of active metals, etc. problems, to achieve the effect of improving anti-carbon deposition capacity, high capacity, and reducing reaction coking

Active Publication Date: 2022-06-07
CHINA PETROLEUM & CHEM CORP +1
View PDF9 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Although the catalysts disclosed in the above patents all have high pore volume, the specific surface area of ​​the carrier alumina is relatively low, which is not conducive to improving the dispersion of the active components, and has a strong interaction with the active components, resulting in Active metal sulfidation is not complete, these factors limit the further improvement of its catalytic performance in heavy oil hydrogenation

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Heavy oil hydrotreating catalyst and its preparation method
  • Heavy oil hydrotreating catalyst and its preparation method
  • Heavy oil hydrotreating catalyst and its preparation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0050] (1) Catalyst preparation

[0051] Weigh 600g of ammonium phosphate, dissolve in 2000mL deionized water, to give solution A; Grind 1000g of petcoke to a powder, then add to solution A, place for 1.5h, then filter, and the resulting solid sample is placed in an oven and dried at 110 °C for 5h. At 200 °C, the above-mentioned dried solid samples are pretreated with water vapor for 3 h (the volume air velocity of water vapor gas is 1200 h -1 The temperature is then raised to 400 °C, the pretreatment is continued for 3 h, and then cooled to 60 °C under nitrogen protection to obtain pretreatment petcoke.

[0052] The 1000g of the above obtained pretreatment petroleum coke, 57.1g of quasi-thin aluminumite powder and 2000g of potassium hydroxide were mixed evenly, placed in a microwave heating furnace with a microwave frequency of 2450MHz, vacuumed, under the condition of microwave power of 0.3kw, heated to 500 °C, constant for 40 min, and then passed nitrogen to atmospheric pressur...

Embodiment 2

[0059] (1) Catalyst preparation

[0060] Weigh 500g of diammonium hydrogen phosphate, dissolve in 2000mL deionized water, to give solution A; Grind 1000g of petcoke to a powder, then add to solution A, place for 1.5h, then filter, and the resulting solid sample is placed in an oven and dried at 110 °C for 5h. At 200 °C, the above-mentioned dried solid samples are pretreated with water vapor for 3 h (the volume air velocity of water vapor gas is 1000 h -1 The temperature is then raised to 400 °C, the pretreatment is continued for 3 h, and then cooled to 60 °C under nitrogen protection to obtain pretreatment petcoke.

[0061]The 1000g of the above obtained pretreatment petroleum coke, 85.7g of pseudo-thin aluminum powder and 3000g of potassium hydroxide were mixed evenly, placed in a microwave heating furnace with a microwave frequency of 2450MHz, vacuumed, under the condition of microwave power of 0.3kw, heated to 600 °C, constant for 20 min, and then passed nitrogen to atmospheric...

Embodiment 3

[0068] (1) Catalyst preparation

[0069] Weigh 400g of ammonium dihydrogen phosphate, dissolve in 2000mL deionized water, to give solution A; Grind 1000g of petcoke to a powder, then add to solution A, place for 1.5h, then filter, and the resulting solid sample is placed in an oven and dried at 110 °C for 5h. At 200°C, the above-mentioned dried solid samples are pretreated with water vapor for 3 h (the volume air velocity of water vapor gas is 800 h -1The temperature is then raised to 400 °C, the pretreatment is continued for 3 h, and then cooled to 60 °C under nitrogen protection to obtain pretreatment petcoke.

[0070] The 1000g of the above obtained pretreatment petroleum coke, 114.3g of pseudo-thin aluminum powder and 4000g of potassium hydroxide were mixed evenly, placed in a microwave heating furnace with a microwave frequency of 2450MHz, vacuumed, under the condition of microwave power of 0.3kw, heated to 400 ° C, constant 60min, and then passed nitrogen to atmospheric pres...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
specific surface areaaaaaaaaaaa
diameteraaaaaaaaaa
specific surface areaaaaaaaaaaa
Login to View More

Abstract

The invention discloses a heavy oil hydrotreating catalyst and a preparation method thereof. The preparation method comprises mixing petroleum coke, pseudo-boehmite powder and an activator, and activating after mixing uniformly; the obtained sample is firstly treated with an acid solution, and then washed , drying; then introducing active metal components into the obtained solid sample, followed by drying and roasting to obtain a heavy oil hydrotreating catalyst. The present invention also provides a heavy oil hydrotreating catalyst prepared by the method. In the catalyst, the weaker interaction between the carrier and the active component can ensure more complete sulfuration, and more centers with high hydrogenation activity are easy to be formed, so that the catalyst has higher hydrogenation activity.

Description

Technical field [0001] The present invention belongs to the field of refining chemical technology, relates to a catalytic material and a preparation method thereof, in particular to a heavy oil hydrotreatment catalyst and a preparation method thereof. Background [0002] In recent years, the quality of crude oil is getting worse and worse, but the demand for light oil products is increasing year by year, so it is of great practical significance to develop deep processing of heavy oil and increase the added value of products. Hydrogenation technology as the main processing method is facing great challenges, and there is an urgent need to develop a better hydrogenation process and a more active hydrogenation catalyst. The reaction performance of the heavy oil hydrogenation catalyst depends on both the inherent catalytic properties of the active component and the properties of the catalyst carrier. The specific surface area, pore structure, surface acidity, etc. of the support have ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/19B01J32/00B01J35/10B01J37/10B01J37/28C10G49/04
CPCB01J37/10B01J27/19B01J37/28B01J23/002C10G49/04B01J2523/00B01J35/617B01J35/638B01J2523/51B01J2523/68B01J2523/847
Inventor 杨涛金浩朱慧红杨光刘璐姜巧
Owner CHINA PETROLEUM & CHEM CORP