Combined fluidized bed and fixed bed coal catalytic gasification reaction device and method thereof
A fluidized bed gasification and coal catalytic gasification technology, which is applied in gasification process, manufacture of combustible gas, petroleum industry, etc., can solve the problems of low methane yield, poor operation stability, low carbon conversion rate and gasification intensity, etc. , to increase the methane content, prevent the direct combustion process, and improve the fluidization stability.
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Embodiment 1
[0044] A combined fluidized bed and fixed bed catalytic gasification device, the inner diameter of the fluidized bed gasification section is 1.0m, the height is 12m, the height of the raw material inlet is located at 1 / 3 of the height of the fluidized bed gasification section, and the inlet of the circulating synthesis gas is located at the 1 / 2 of the height of the fluidized bed gasification section, the first-stage return material inlet is located at 1 / 6 of the height of the fluidized bed gasification section, the circulation ratio of the first-stage return material inlet is 5 times, and the inclined surface of the gas distributor is equal to the horizontal plane The included angle is 30°, air holes are arranged on the conical surface of the gas distributor, the air holes are evenly arranged 10 times along the circumference, and the opening rate is 2%. The fixed bed gasification section has an inner diameter of 1.0m and a height of 6m. The grate is located at 1 / 3 of the height...
Embodiment 2
[0047] A combined fluidized bed and fixed bed catalytic gasification device, the inner diameter of the fluidized bed gasification section is 1.0m, the height is 12m, the height of the raw material inlet is located at 1 / 3 of the height of the fluidized bed gasification section, and the inlet of the circulating synthesis gas is located at the 1 / 2 of the height of the fluidized bed gasification section, the first-stage return material inlet is located at 1 / 6 of the height of the fluidized bed gasification section, the circulation ratio of the first-stage return material inlet is 5 times, and the inclined surface of the gas distributor is equal to the horizontal plane The included angle is 30°, air holes are arranged on the conical surface of the gas distributor, the air holes are evenly arranged 10 times along the circumference, and the opening rate is 2%. The inner diameter of the fixed bed gasification section is 1.0m, and the height is 6m. The grate is located at 1 / 3 of the hei...
Embodiment 3
[0050]A combined fluidized bed and fixed bed catalytic gasification device, the inner diameter of the fluidized bed gasification section is 1.0m, the height is 12m, the height of the raw material inlet is located at 1 / 3 of the height of the fluidized bed gasification section, and the inlet of the circulating synthesis gas is located at the 1 / 2 of the height of the fluidized bed gasification section, the first-stage return material inlet is located at 1 / 8 of the height of the fluidized bed gasification section, the circulation rate of the first-stage return material inlet is 5 times, and the inclined surface of the gas distributor is equal to the horizontal plane The included angle is 30°, air holes are arranged on the conical surface of the gas distributor, the air holes are evenly arranged 10 times along the circumference, and the opening rate is 2%. The inner diameter of the fixed bed gasification section is 1.0m, and the height is 6m. The grate is located at 1 / 3 of the heigh...
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