Heterogeneous catalytic gasification reactor for coal
A technology of gasification reactor and heterogeneous catalysis, which is applied in the direction of gasification process, fuel pre-distillation, petroleum industry, etc., can solve the problems of inefficient and clean utilization, and achieve the effect of ensuring the original state and in situ
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Embodiment 1
[0025] see figure 1 , in this embodiment, a coal heterogeneous catalytic gasification reactor, including a feed system, a gas system, a heating system, a solid-gas reactor 1 and a gas-gas reactor 2, the bottom of the solid-gas reactor 1 is connected with a main gas Intake pipe 1-1, the top of solid-gas reactor 1 is connected with the bottom of gas-gas reactor 2 through connecting pipe 2-3, and the top of gas-gas reactor 2 is connected with outlet pipe 2-2; solid-gas reactor 1 and gas The inside of the gas reactor 2 is equipped with partitions 1-3, and the partitions 1-3 divide the interior of the solid-gas reactor 1 and the gas-gas reactor 2 into several compartments from bottom to top. Several feeding pipes 1-2 are connected to the side wall, and several secondary gas inlet pipes 2-1 are connected to the side wall of the gas-gas reactor 2.
[0026] The feeding pipes 1-2 communicate with different compartments in the solid-gas reactor 1 respectively, and the secondary gas inl...
Embodiment 2
[0034] Experimental objectives: the release of sulfur and nitrogen elements in the volatile matter of bituminous coal during fluidized bed pyrolysis;
[0035] Solid gas reactor 1:
[0036] Form: fluidized bed; bottom bed material: zirconium dioxide (zircon sand);
[0037] Dimensions: Inner diameter Φr = 40mm, height h5 = 180mm;
[0038] Reaction temperature: 900°C;
[0039] Upper compartment 1-5: h4=20mm, no filler;
[0040] Feed: 0.2mm bituminous coal, feed amount 10g, feed flow rate: 100mg / min;
[0041] Fluidizing gas: argon, flow rate 0.9L / min;
[0042] Injection gas blowing: argon, flow rate 0.1L / min;
[0043] Gas reactor 2:
[0044] Form: entrained bed; no bed material; size: inner diameter same as above, height h1+h2=200mm; reaction temperature: 900°C;
[0045] Intake air: oxygen; 0.6L / min;
[0046] Compartment: no padding;
[0047] Detection Systems:
[0048] Use the flue gas composition analyzer to detect the concentration of SOx and NOx at the outlet of gas-ga...
Embodiment 3
[0051] Experimental objectives: During fluidized bed pyrolysis, the release of sulfur and nitrogen elements from the interaction between bituminous coal volatiles and coal char;
[0052] Solid gas reactor 1:
[0053] Form: fluidized bed; bottom bed material: zirconium dioxide (zircon sand);
[0054] Dimensions: Inner diameter Φr = 40mm, height h5 = 180mm;
[0055] Reaction temperature: 900°C;
[0056] Upper compartment 1-5: h4=20mm, 0.2mm particle size bituminous coal 10g;
[0057] Feed material: bituminous coal, feed amount 10g, feed flow rate: 100mg / min;
[0058] Fluidizing gas: argon, flow rate 0.9L / min;
[0059] Injection gas blowing: argon, flow rate 0.1L / min;
[0060] Gas reactor 2:
[0061] Form: entrained bed; no bed material; size: inner diameter same as above, height h1+h2=200mm; reaction temperature: 900°C;
[0062] Intake air: oxygen; 0.6L / min;
[0063] Compartment: no padding;
[0064] Detection Systems:
[0065] Use the flue gas composition analyzer to ...
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