Apparatus and method for producing methane-rich synthesis gas through efficient coal catalytic gasification
A technology of coal catalytic gasification and methane synthesis gas, which is applied in gasification process, granular/powdered fuel gasification, and combustible gas production, etc. It can solve the problems of low carbon conversion rate and gasification intensity, poor operation stability, and methane yield Low-level problems, to achieve the effect of improving carbon conversion rate, reducing load, and high methane production rate
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Embodiment 1
[0042] A high-efficiency coal catalytic gasification device for producing methane-rich synthesis gas. The inner diameter of the fluidized bed pyrolysis methanation furnace is 1.0m, the height is 12m, and the height of the raw material inlet is located at 2 / 3 of the height of the fluidized bed pyrolysis methanation furnace. The inner diameter of the fluidized bed gasifier is 0.8m, and the height is 15m. The semi-coke inlet is located at 1 / 8 of the height of the fluidized bed gasifier, and the return inlet is located at 1 / 4 of the height of the fluidized bed gasifier. The length of the bed pyrolysis methanation furnace is 9m, accounting for 3 / 4 of the height of the methanation furnace.
[0043] In the experiment, Inner Mongolia lignite and 10% K 2 CO 3 +5% CaO catalyst mixed, put into the fluidized bed pyrolysis methanation furnace from the raw material inlet, nitrogen gas is passed into the fluidizing air gas distributor to make the raw material turbulent and fluidized in the ...
Embodiment 2
[0045] A high-efficiency coal catalytic gasification device for producing methane-rich synthesis gas. The inner diameter of the fluidized bed pyrolysis methanation furnace is 1.0m, the height is 12m, and the height of the raw material inlet is located at 2 / 3 of the height of the fluidized bed pyrolysis methanation furnace. The inner diameter of the fluidized bed gasifier is 0.8m, and the height is 15m. The semi-coke inlet is located at 1 / 8 of the height of the fluidized bed gasifier, and the return inlet is located at 1 / 4 of the height of the fluidized bed gasifier. The length of the bed pyrolysis methanation furnace is 10m, accounting for 5 / 6 of the height of the methanation furnace.
[0046] In the experiment, Inner Mongolia lignite and 10% K 2 CO 3 +5% CaO catalyst mixed, put into the fluidized bed pyrolysis methanation furnace from the raw material inlet, nitrogen gas is passed into the fluidizing air gas distributor to make the raw material turbulent and fluidized in the...
Embodiment 3
[0048] A high-efficiency coal catalytic gasification device for producing methane-rich synthesis gas. The inner diameter of the fluidized bed pyrolysis methanation furnace is 1.0m, the height is 12m, and the height of the raw material inlet is located at 2 / 3 of the height of the fluidized bed pyrolysis methanation furnace. The inner diameter of the fluidized bed gasifier is 0.8m, and the height is 15m. The semi-coke inlet is located at 1 / 8 of the height of the fluidized bed gasifier, and the return inlet is located at 1 / 4 of the height of the fluidized bed gasifier. The length of the bed pyrolysis methanation furnace is 9m, accounting for 3 / 4 of the height of the methanation furnace.
[0049] In the experiment, Inner Mongolia lignite and 10% K 2 CO 3 +10%CaO catalyst mixed, put into the fluidized bed pyrolysis methanation furnace from the raw material inlet, nitrogen gas is passed into the fluidized air gas distributor to make the raw material turbulent and fluidized in the f...
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