Apparatus and method for preparing metal nitride catalytic material
A technology for catalytic materials and nitrides, applied in chemical instruments and methods, physical/chemical process catalysts, chemical/physical processes, etc., can solve the problems of product purity and quality decline, avoid product quality decline, and eliminate operations. Hazardous and environmental pollution, the effect of eliminating temperature gradient problems
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[0022] γ-Mo 2 The preparation technology of N is described in detail. In the present invention, the room temperature generally refers to 16-30°C.
[0023] In view of the preparation of high specific surface area γ-Mo 2 The research experience of N, the present invention adopts the approach of temperature-programmed gradual reaction, utilizes N 2Reduction of MoO as a reducing gas 3 . By controlling the heating rate and increasing the gas flow rate, the accumulation of product moisture is prevented; in order to reduce gas consumption, a gas circulation device is designed in the system to reduce production costs.
[0024] The reaction device for preparing molybdenum nitride in a fluidized bed is shown in Figure 1.
[0025] 1. Gas
[0026] 1 nitrogen - high-purity nitrogen (volume concentration of 99.999%), nitriding raw material, from steel cylinders, to the mixer;
[0027] 2 Hydrogen - high-purity hydrogen (volume concentration 99.999%), nitriding raw material, from steel ...
Embodiment 1
[0149] The temperature programming system that the present invention adopts is as figure 2 As shown, the optimal temperature programming regime is:
Embodiment 25
[0150] 1. Rapid heating from room temperature to 673K, the heating rate is 1-50K / min (25K / min in this embodiment);
[0151] 2.673-933K adopts 0.6-1K / min (this embodiment 0.6K / min) speed to heat up;
[0152] 3. 933K constant temperature 0.5-1hr (this embodiment 1hr);
[0153] 4. Cool to room temperature in a fluidized bed reactor;
[0154] 5. React N at room temperature 2 -H 2 The mixed gas is switched to volume ratio 99%Ar-1%O 2 Mixed gas (ie passivation treatment), time 12-24hr, 24hr in this embodiment.
[0155] γ-Mo of the present invention 2 The N-supported catalyst was prepared as follows:
[0156] According to the above process, the MoO 3 / TiO 2 、MoO 3 / NiO-TiO 2 、MoO 3 / Al 2 o 3 -TiO 2 or MoO 3 / Al 2 o 3 Put into fluidized bed reactor of the present invention, carry out N 2 -H 2 Reductive replacement of MoO 3 reaction to produce Mo 2 N / TiO 2 、Mo 2 N / NiO-TiO 2 、Mo 2 N / Al 2 o 3 -TiO 2 or Mo 2 N / Al 2 o 3 Supported metal nitride catalyst. N 2...
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