Method of using methanol, carbon dioxide and water to prepare high-quality synthetic gas
A carbon dioxide, high-quality technology, applied in chemical instruments and methods, hydrogen/syngas production, inorganic chemistry, etc., can solve problems such as the safety obstruction of hydrogen storage and transportation, the non-direct storage of electrical energy, and the unsatisfactory molar ratio. , to achieve the effect of renewable resources, high energy efficiency and high concentration
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Embodiment 1
[0022] γ-Al with a diameter of 2mm 2 o 3 The ball is used as the carrier, and the supported Co / γ-Al containing 10wt% Co is prepared by the impregnation method 2 o 3 The catalyst is packed in the plasma catalytic reforming reactor. The plasma is generated by sliding arc discharge, the upper end of the catalyst is 4cm away from the end of the plasma, and the outside of the catalytic bed is heated by an electric furnace.
[0023] The flow rate of water flowing into the electrolytic cell is 4.9 mol / h, and the anode and cathode sides of the electrolytic cell generate 2.5 mol / h of O 2 and 4.9mol / h of H 2 . 2.3mol / h O produced on the anode side of the electrolytic cell 2 (the rest is evacuated), with 7.0mol / h CH 4 and 2.3mol / h CO 2 , as reformed feed gas (CH 4 / CO 2 / O 2 The molar ratio is 3 / 1 / 1), and flows into the plasma catalytic reforming reactor. The reaction conditions of the plasma catalytic reforming reactor are: plasma energy density 27kJ / mol, catalyst space velo...
Embodiment 2
[0026] γ-Al with a diameter of 2mm 2 o 3 The pellets were used as the carrier, and the supported Ni / CeO with the weight percentage of Ni and Ce respectively 11wt% and 8wt% was prepared by the step-by-step impregnation method 2 / γ-Al 2 o 3 The catalyst is packed in the plasma catalytic reforming reactor. The plasma catalytic reforming reactor is the same as in Example 1.
[0027] The flow rate of water flowing into the electrolytic cell is 5.7mol / h, and the anode and cathode sides of the electrolytic cell respectively produce 2.9mol / h of O 2 and 5.7mol / h of H 2 . 2.3mol / h O produced on the anode side of the electrolytic cell 2 (the rest is evacuated), with 5.7mol / h CH 4 and 2.3mol / h CO 2 , as reformed feed gas (CH 4 / CO 2 / O 2 The molar ratio is 2.5 / 1 / 1), and flows into the plasma catalytic reforming reactor. The reaction conditions of the plasma catalytic reforming reactor are: plasma energy density 27kJ / mol, catalyst space velocity 254mmol g -1 h -1 (5700ml·g ...
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