Method for producing hydrogen by biogas liquid aqueous-phase reforming
A water-phase reforming and hydrogen technology, applied in hydrogen/synthesis gas production, chemical instruments and methods, hydrogen, etc., can solve the problems of high production cost, high process conditions, complex operation, etc., and achieve value enhancement and convenient operation , the effect of simple equipment
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Embodiment 1
[0055] (1) Prepare Ni / Al with Ni loading of 15wt% by equal volume impregnation method 2 o 3 Catalyst, reduced under hydrogen atmosphere to obtain black powdery catalyst;
[0056] (2) Put 0.2g catalyst and 100mL biogas slurry in the reactor, seal the reactor, ventilate nitrogen to discharge the air, adjust the pressure to 2.5MPa, raise the temperature to 250°C, stir at 250r / min, and react for 3h;
[0057] (3) Heating and stirring were stopped, and the reactor was placed in an ice bath to cool to room temperature. The noncondensable gas obtained from the gas outlet was a gas phase product containing hydrogen. The components and contents of the detected gas products were shown in Table 1.
Embodiment 2
[0059] (1) Prepare Ni / CeO with a Ni loading of 15wt% by equal volume impregnation method 2 Catalyst, reduced under hydrogen atmosphere to obtain black powdery catalyst;
[0060] (2) Put 0.2g catalyst and 100mL biogas slurry in the reactor, seal the reactor, ventilate nitrogen to discharge the air, adjust the pressure to 2.5MPa, raise the temperature to 250°C, stir at 250r / min, and react for 3h;
[0061] (3) Heating and stirring were stopped, and the reactor was placed in an ice bath to cool to room temperature. The noncondensable gas obtained from the gas outlet was a gas phase product containing hydrogen. The components and contents of the detected gas products were shown in Table 1.
Embodiment 3
[0063] (1) Prepare Ni / Al with Ni loading of 15wt% by equal volume impregnation method 2 o 3 Catalyst, reduced under hydrogen atmosphere to obtain black powdery catalyst;
[0064] (2) Put 0.5g of catalyst and 100mL of biogas slurry in the reactor, seal the reactor, ventilate nitrogen to discharge the air, adjust the pressure to 2.5MPa, raise the temperature to 200°C, stir at 250r / min, and react for 3h;
[0065] (3) Heating and stirring were stopped, and the reactor was placed in an ice bath to cool to room temperature. The noncondensable gas obtained from the gas outlet was a gas phase product containing hydrogen. The components and contents of the detected gas products were shown in Table 1.
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