A method for catalytic gasification and methane enrichment of gasification coke

A technology of methanation and coke particles, which is applied in gasification process, coke oven, and combustible gas production, can solve the problems of high hydrogen cost, large equipment investment, and low methane yield, and achieve good gasification reaction activity and low Catalyst cost, effect of high methanation activity

Active Publication Date: 2020-10-13
TAIYUAN UNIV OF TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, large-scale industrial gasification coke production has just started in my country, and there is no precedent in the field of clean coal technology in foreign countries, and most of the existing research focuses on coal gasification technology for high-efficiency methane production, and there are few studies on gasification coke gasification methane production
Patent document CN101906339A couples coal gasification and methanation technology to produce substitute natural gas in an integrated way, but the subsequent equipment investment of this process is large, and a large amount of carbon dioxide will be produced in the process of producing syngas
Patent CN102021037B provides a method and device for catalytic methane production from coal, which realizes coal cracking while producing natural gas, but this technology consumes a lot of water and has low carbon utilization rate
Patent CN102242006A provides a process for direct coal hydrogenation to methane, but the methane yield of this process is low, the cost of hydrogen used is high, and the economic benefit is poor

Method used

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  • A method for catalytic gasification and methane enrichment of gasification coke

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Experimental program
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Effect test

Embodiment 1

[0023] Dry-grind laterite nickel ore with initial Ni and Fe contents of 1.34wt% and 30.2wt%, respectively, to obtain mineral powder with a particle size of ≤3mm, and add 15wt% of Na to the crushed mineral powder. 2 CO 3 , After mixing uniformly, in a stirred reactor at 800 ℃, water gas (gas composition is H 2 50vol%, CO 40vol%, CO 2 9vol%, the other 1vol%) was reduced and burned for 120min under the condition of 160L / (g·h) space velocity to prepare the required additives.

[0024] After that, the lignite, gas coal, and fat coal are respectively sent to the crusher for preliminary crushing. After crushing, additives are added for mixing. The mass ratio of lignite, gas coal, fat coal and additives is 3:5:1:0.25. After mixing, enter the counterattack The crusher is used for crushing and mixing, and the content of coal with a size of less than 3 mm in the crushed coal reaches 93 wt%.

[0025] The crushed coal is tamped to form a cylindrical coal cake, and then the coal cake is put int...

Embodiment 2

[0030] The initial Ni and Fe content of 1.02wt% and 29.8wt% laterite nickel ore were dry-grinded to obtain mineral powder with a particle size of ≤3mm, and 10wt% Na was added to the crushed mineral powder. 2 CO 3 And 5wt% of CaO, mixed uniformly, in a stirred reactor at 1000 ℃, water gas (gas composition is H 2 50vol%, CO 40vol%, CO 2 9 vol%, the other 1 vol%) was reduced and burned for 80 minutes at a space velocity of 120L / (g·h) to prepare the required additives.

[0031] After that, the lignite, gas coal, and fat coal are respectively sent to the crusher for preliminary crushing. After crushing, additives are added for mixing. The mass ratio of lignite, gas coal, fat coal and additives is 1:5:1:0.25. After mixing, enter the counterattack The crusher is used for crushing and mixing, and the content of coal with a size of less than 3mm in the crushed coal reaches 95wt%.

[0032] The crushed coal is tamped to form a cylindrical coal cake, and then the coal cake is put into a high-...

Embodiment 3

[0037] The laterite nickel ore with initial Ni and Fe contents of 1.98wt% and 31.2wt%, respectively, was dry-milled to obtain mineral powder with a particle size of ≤3mm. Add 20wt% CaO to the crushed mineral powder, and mix it evenly. In a stirred reactor at 900℃, coke oven gas (gas composition is CH 4 25.3vol%, H 2 60.5vol%, CO 6.2vol%, C 2+ Unsaturated hydrocarbon 3.0vol%, CO 2 2.0vol%, O 2 0.5 vol%, other 2.5 vol%) at a space velocity of 140L / (g·h), reduced and burned for 90 minutes to prepare the required additives.

[0038] After that, the lignite, gas coal, and fat coal are respectively sent to the crusher for preliminary crushing. After crushing, additives are added for mixing. The mass ratio of lignite, gas coal, fat coal and additives is 3:2:1:0.25. After mixing, enter the counterattack The crusher is used for crushing and mixing, and the content of coal with a size of less than 3mm in the crushed coal reaches 91wt%.

[0039] The crushed coal is tamped to form a cylind...

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Abstract

The invention relates to a method for catalyzing gasification and rich methanation by virtue of gasifying coke. The method comprises the following steps: adding at least one of 10wt%-20wt% of Na2CO3 or CaO into red clay nickel mineral powder, uniformly mixing, respectively putting brown coal, gas coal and rich coal into a crusher, carrying out primary crushing, adding an additive, mixing to obtain a mixture, putting the mixture into a reaction crusher, crushing, and mixing, so as to obtain crushed coal; and carrying out tamping formation and coking on the crushed coal, crushing gasifying coke, and gasifying coke particles under the actions of temperature, pressure and a gasifying agent. The method has the advantages of high carbon utilization rate, low cost and high methane yield.

Description

Technical field [0001] The invention belongs to the field of coal coke catalytic preparation of natural gas, and specifically relates to a coke for gasification and a method for gasification and methanization. Background technique [0002] Coking belongs to the traditional coal chemical industry. China's coke production capacity is severely surplus, with a production capacity of approximately 680 million tons and a capacity utilization rate of approximately 65%, of which approximately 90% of the coke is used in the smelting industry. Therefore, the use of existing equipment to produce gasified coke and expand the use of coke is of positive significance for resolving excess coke production capacity in my country and promoting the development of the industry. [0003] Gasified coke is a kind of coke used for gas production. It requires low ash content, high ash melting point, appropriate and uniform lumpness. Although the existing metallurgical coke can be used as gasified coke, it i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10B57/06C10B53/08C10B57/00C10J3/64
CPCC10B53/08C10B57/005C10B57/06C10J3/64C10J2300/0943C10J2300/0976Y02P20/52
Inventor 杨颂刘守军杜文广闫志中郝志强
Owner TAIYUAN UNIV OF TECH
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