Carbon dioxide and water processing methane catalyst and preparation method and application thereof
A carbon dioxide and catalyst technology, which is applied in the new catalytic process and preparation field of thermocatalytic carbon dioxide and water to methane, can solve the problems of complex catalyst preparation process, low photocatalytic quantum yield, and limited industrial scale-up application, and is easy to promote , Extensive sources of raw materials and low cost
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Embodiment 1
[0023] Weigh 2.0 g Ni(NO 3 ) 2 ·6H 2 O was dissolved in distilled water, followed by the addition of 18g Al 2 o 3 , impregnated for 12 hours under magnetic stirring. Then put it in a blast drying oven at 120 o C dried for 10 h, then placed in a muffle furnace at 500 o C roasting for 4 h, then in H 2 Atmosphere 450 o 2.5 wt. % Ni / Al was obtained after C reduction treatment for 5 h 2 o 3 catalyst. Physically mix the catalyst with metal Fe powder at a mass ratio of 1:2, press into tablets, crush, and sieve to obtain 40-60 mesh catalyst particles.
[0024] The catalyst particles were placed in a fixed-bed reactor at a space velocity of 300 h -1 , water volume 0.03 mL / min, 300°C, 2 MPa reaction conditions for activity evaluation, the result: CO 2 The conversion rate (C-mol %) is 3.5; CH 4 The selectivity (C-mol%) was 94.6.
Embodiment 2
[0026] Weigh 4.0 g Ni(NO 3 ) 2 ·6H 2 O was dissolved in distilled water, and 9 g of TiO was added 2 , impregnated for 12 hours under magnetic stirring. Then put it in a blast drying oven at 120 o C dried for 10 h, then placed in a muffle furnace at 500 o C roasting for 4 h, then in H 2 Atmosphere 450 o 10 wt. % Ni / TiO was obtained after C reduction treatment for 5 h 2 catalyst. Physically mix the catalyst and metal Mn powder at a mass ratio of 1:3, press into tablets, crush, and sieve to obtain catalyst particles of 40-60 mesh.
[0027] The catalyst particles were placed in a fixed-bed reactor at a space velocity of 600 h -1 , water volume 0.05 mL / min, 400°C, 3 MPa reaction conditions for activity evaluation, the result: CO 2 The conversion rate (C-mol %) is 7.8; CH 4 The selectivity (C-mol%) was 86.4.
Embodiment 3
[0029] Weigh 4.0 g Ni(NO 3 ) 2 ·6H 2 O was dissolved in distilled water, and 9 g of ZrO 2 , impregnated for 12 hours under magnetic stirring. Then put it in a blast drying oven at 120 o C dried for 10 h, then placed in a muffle furnace at 500 o C roasting for 4 h, then in H 2 Atmosphere 450 o 10 wt. % Ni / ZrO was obtained after C reduction treatment for 5 h 2 catalyst. The catalyst is physically mixed with the metal Al powder at a mass ratio of 1:1, pressed into tablets, crushed, and sieved to obtain 40-60 mesh catalyst particles.
[0030] The catalyst particles were placed in a fixed-bed reactor at a space velocity of 1200 h -1 , water volume 0.07 mL / min, 500°C, 4 MPa reaction conditions for activity evaluation, the result: CO 2 The conversion rate (C-mol %) is 9.3; CH 4 The selectivity (C-mol%) was 80.5.
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