Reduction method of copper zinc catalyst for hydrogen production by methanol steam reforming
A technology for reforming hydrogen production and catalysts, applied in chemical instruments and methods, catalyst activation/preparation, physical/chemical process catalysts, etc., can solve the problems of affecting catalyst activity, large investment, long reduction time, etc. The effect of low equipment investment and high operating cost
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Embodiment 1
[0020] Methanol steam reforming hydrogen production copper zinc catalyst 2 tons, the mass percentage of copper oxide in the catalyst is 65%, in the reactor catalyst bed, pass into the dry air that space velocity is 20h-1, by normal temperature at 20 degree / hour The heating rate was raised to 80°C, and then raised to 170°C at a rate of 5°C / hour until no physical water was discharged, the drying air was stopped, and the entire system was replaced with nitrogen.
[0021] Be warming up to 180 degrees, and pass into deionized water, the air space velocity of deionized water is 300h-1, pass into hydrogen, the space velocity of hydrogen is 8h-1, hydrogen accounts for the volume percentage of both is about 2.6%, with Raise the temperature to 200°C at a heating rate of 5°C / h, and then stop the heating at a rate of 2°C / h to 240°C, and maintain the system pressure at 0.2MPa.
[0022] To maintain the temperature of the catalyst bed, a 10% aqueous methanol solution was introduced, the liqu...
Embodiment 2
[0025] 4 tons of copper-zinc catalyst for hydrogen production by steam reforming of methanol, the mass percentage of copper oxide in the catalyst is 65%, and the dry air with a space velocity of 20h-1 is passed into the catalyst bed, and the temperature rise rate is 20 degrees / hour from normal temperature Raise to 80°C, and then raise the temperature to 170°C at a rate of 5°C / hour until no physical water is discharged, stop drying the air, and replace the entire system with nitrogen.
[0026] Be warming up to 180 degrees, and pass into deionized water, the gas space velocity of deionized water is 350h The temperature was raised to 200°C at a heating rate of 5°C / h, and then stopped at a rate of 4°C / h to 240°C, and the system pressure was maintained at 0.2MPa.
[0027] To maintain the temperature of the catalyst bed, a 15% aqueous methanol solution was introduced, and the liquid space velocity was 0.2h-1. The system pressure is controlled at 0.4MPa.
[0028] Detect the compone...
Embodiment 3
[0030] 8 tons of methanol steam reforming hydrogen production catalysts, the mass percentage of copper oxide in the catalyst is 60%, the dry air that passes into the catalyst bed with a space velocity of 30h-1 is raised from normal temperature to 80°C, and then raised to 170°C at a rate of 5°C / hour, until no physical water was discharged, the air was stopped, and the entire system was replaced with nitrogen.
[0031] Be warming up to 180 degree, and pass into deionized water, the gas space velocity of deionized water is 400h The temperature was raised to 200°C at a heating rate of 8°C / h, and then stopped at a rate of 2°C / h to 240°C, and the system pressure was maintained at 0.2MPa.
[0032] To maintain the temperature of the catalyst bed, 20% aqueous methanol solution was introduced, and the liquid space velocity was 0.2h-1. The system pressure is controlled at 0.3MPa.
[0033] Detect the components of the cracked gas, wherein the hydrogen content is about 74.2%, and the car...
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