Method for raising gasification reactivity of petroleum coke

A gasification reaction, petroleum coke technology, applied in gasification process, petroleum industry, fixed bed gasification, etc., can solve the problems of low carbon conversion rate and difficult to deal with carbon residue, so as to reduce corrosion, improve reaction activity, widen The effect of using the way

Inactive Publication Date: 2018-09-11
NORTHEASTERN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The biggest problem in petroleum coke gasification engineering is the low carbon co

Method used

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  • Method for raising gasification reactivity of petroleum coke

Examples

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Example Embodiment

[0030] Example 1: Weigh 2.5g FeCl 3 Put it into a beaker, add 50g of water, stir well to get FeCl 3 Solution, then weigh 50g of petroleum coke with a particle size less than 0.074mm, and mix it with FeCl 3 The solution is mixed together and stirred with a magnetic stirrer for 24 hours; finally, the stirred petroleum coke is dried in a drying oven at 105°C for 12 hours to obtain a catalyst-supported petroleum coke prepared by the impregnation method. It is put into a fluidized bed gasifier for reaction, and the gasification agent uses air and water vapor. Gasifier working conditions: pressure is 0.1MPa, temperature is 700℃, mass flow ratio of water vapor to petroleum coke is 1, air to petroleum coke mass flow ratio is 2, and the time required for complete reaction of petroleum coke is shown in Table 1.

Example Embodiment

[0031] Example 2: Weigh 2.5g FeSO 4 Put it into a beaker and add 50g of water, stir well to obtain FeSO 4 Solution, then weigh 50g of petroleum coke with a particle size of less than 0.074mm, and mix it with FeSO 4 The solution is mixed together and stirred with a magnetic stirrer for 24 hours; finally, the stirred petroleum coke is dried in a drying oven at 105°C for 12 hours to obtain a catalyst-supported petroleum coke prepared by the impregnation method. It is put into a fluidized bed gasifier for reaction, and the gasification agent uses air and water vapor. Gasifier working conditions: pressure is 0.1MPa, temperature is 700℃, mass flow ratio of water vapor to petroleum coke is 1, air to petroleum coke mass flow ratio is 2, and the time required for complete reaction of petroleum coke is shown in Table 1.

Example Embodiment

[0032] Example 3: Weigh 1.25g FeSO 4 And 1.25gFeCl 3 Put it into a beaker and add 50g of water, stir well to obtain FeSO 4 And FeCl 3 Solution, then weigh 50g of petroleum coke with a particle size of less than 0.074mm, and mix it with FeSO 4 And FeCl 3 The solution is mixed together and stirred with a magnetic stirrer for 24 hours; finally, the stirred petroleum coke is dried in a drying oven at 105°C for 12 hours to obtain a catalyst-supported petroleum coke prepared by the impregnation method. It is put into a fluidized bed gasifier for reaction, and the gasification agent uses air and water vapor. Gasifier working conditions: pressure is 0.1MPa, temperature is 700℃, mass flow ratio of water vapor to petroleum coke is 1, air to petroleum coke mass flow ratio is 2, and the time required for complete reaction of petroleum coke is shown in Table 1.

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Abstract

The invention relates to the field of petroleum coke gasification, specifically to a method for raising gasification reactivity of petroleum coke. By a dry-mixing and impregnation method, a catalyst and petroleum coke are mixed to obtain a catalyst-supported petroleum coke; and at gasification temperature of 700-1250 DEG C and at the gasification pressure of 0.1-10 MPa, the catalyst-supported petroleum coke is introduced into a gasifier to carry out a gasification reaction. By the use of the catalyst for catalytic gasification of petroleum coke, gasification rate can be greatly increased, timefor gasification is shortened, and resource utilization of petroleum coke is realized. In addition, the catalyst of the invention is low-cost and is convenient to recover.

Description

technical field [0001] The invention relates to the field of petroleum coke gasification, in particular to a method for improving the reaction activity of petroleum coke gasification. Background technique [0002] Petroleum coke is a solid by-product produced by the coking unit of an oil refinery. At present, with the development of the global oil refining industry, the output of petroleum coke is gradually increasing. [0003] Global petcoke production is expected to increase to 170 million tons, with China and India accounting for a third of it. Petroleum coke From 2007 to 2016, the annual output of petroleum coke in my country was more than 12 million tons, and it showed an increasing trend year by year. By the end of 2017, the output of petroleum coke in China exceeded 20 million tons. With the steady growth of my country's economy, especially the continuous development of industries such as steel, cement production and electrolytic aluminum, with the continuous growth...

Claims

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Application Information

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IPC IPC(8): C10J3/02C10J3/46C10J3/54C10J3/72
CPCC10J3/02C10J3/466C10J3/54C10J3/72C10J2300/0903C10J2300/0913C10J2300/0953C10J2300/0956C10J2300/0976C10J2300/0986
Inventor 阎富生梁容真田伟史金星王越吴智勇
Owner NORTHEASTERN UNIV
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