A kind of preparation method of cobalt-based catalyst for reforming hydrogen production with CO reduction modification
A cobalt-based catalyst, reforming hydrogen production technology, applied in catalyst activation/preparation, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of large particle size of cobalt species
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Embodiment 1
[0027] 1.H 2 Reduction treatment: Weigh 500 mg of the ground catalyst precursor, put it into the reactor, and control the introduction of H 2 The flow rate is 20ml / min, the reduction treatment is carried out at 500°C for 200min, and the hydrogen is cut off. The particle size and dispersion of metal cobalt particles are shown in Table 1.
[0028] 2. Hydrogen production by steam reforming of ethanol: Introduce nitrogen, the flow rate of nitrogen gas is controlled at 80ml / min, and the aqueous ethanol solution with a molar ratio of water to ethanol of 9:1 is pumped into the reactor at a flow rate of 0.2ml / min at 500°C Under the conditions of the reaction to produce hydrogen. The reaction results are shown in Table 2.
Embodiment 2
[0030] 1.H 2 Reduction treatment: Weigh 500 mg of the ground catalyst precursor, put it into the reactor, and control the introduction of H 2 The flow rate is 100ml / min, the reduction treatment is carried out at 500°C for 200min, and the hydrogen is cut off. The particle size and dispersion of metal cobalt particles are shown in Table 1.
[0031] 2. Hydrogen production by steam reforming of ethanol: Introduce nitrogen, the flow rate of nitrogen gas is controlled at 80ml / min, and the aqueous ethanol solution with a molar ratio of water to ethanol of 9:1 is pumped into the reactor at a flow rate of 0.2ml / min at 500°C Under the conditions of the reaction to produce hydrogen. The reaction results are shown in Table 2.
Embodiment 3
[0033] 1. CO reduction treatment: Weigh 500 mg of the ground catalyst precursor, put it into the reactor, control the flow rate of CO to 20ml / min, and perform reduction treatment at 500°C for 200 minutes to cut off carbon monoxide. The particle size and dispersion of metal cobalt particles are shown in Table 1.
[0034] 2. Hydrogen production by steam reforming of ethanol: Introduce nitrogen, the flow rate of nitrogen gas is controlled at 80ml / min, and the aqueous ethanol solution with a molar ratio of water to ethanol of 9:1 is pumped into the reactor at a flow rate of 0.2ml / min at 500°C Under the conditions of the reaction to produce hydrogen. The reaction results are shown in Table 2.
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