Low temperature conversion catalyst for partial oxidation of methane to syngas
A synthesis gas and methane technology, applied in molecular sieve catalysts, physical/chemical process catalysts, inorganic chemistry, etc., can solve the problems of poor reaction performance and large metal loading, and achieve improved methane conversion rate, simple preparation process, and improved utilization rate effect
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Embodiment 1
[0014] Weigh 5.1 grams of molecular sieve H-ZSM-5 (SiO 2 / Al 2 o 3 =20), add 7.6 milliliters of nickel nitrate solution (concentration is 6.7×10 -3 g (Ni) / ml), let stand at room temperature, dry at 80°C, and then roast at 600°C to obtain a Ni / H-ZSM-5 catalyst with a mass percentage of 1%.
[0015] Take 0.2 grams of catalyst (20-40 mesh) mm stainless steel reactor, under atmospheric pressure H 2 The temperature was continuously raised to 600°C, and after reduction for 0.5 hours, the same temperature was switched to CH with a molar ratio of 2:1. 4 and O 2 Reaction raw material gas (flow rate is 100 ml / min) after continuous reaction, the volume space velocity is 20000 hours -1 .
[0016] Under the above reaction conditions, the conversion rate of methane on the catalyst is 17.9%, the selectivity of carbon monoxide is 39.7%, and the selectivity of hydrogen is 8.7%.
Embodiment 2
[0018] Weigh 15.7 grams of molecular sieve H-ZSM-5 (SiO 2 / Al 2 o 3 =38), add 23.5 milliliters of nickel nitrate solution (concentration is 6.7×10 -3 g (Ni) / ml), let stand at room temperature, dry at 80°C, and then roast at 600°C to obtain a Ni / H-ZSM-5 catalyst with a mass percentage of 1%.
[0019] Get 0.2 gram catalyst (20~40 orders), adopt the reaction device of embodiment 1 and reaction condition, the conversion rate of methane as a result is 38.9%, carbon monoxide selectivity is 50.0%, and the selectivity of hydrogen is 51.7%.
Embodiment 3
[0021] Weigh 20.9 grams of molecular sieve H-ZSM-5 (SiO 2 / Al 2 o 3 =120), add 31.5 milliliters of nickel nitrate solution (concentration is 6.7×10 -3 g (Ni) / ml), let stand at room temperature, dry at 80°C, and then roast at 600°C to obtain a Ni / H-ZSM-5 catalyst with a mass percentage of 1%.
[0022] Get 0.2 gram catalyst (20~40 orders), adopt the reaction apparatus of embodiment 1 and reaction condition, the conversion rate of methane as a result is 44.4%, carbon monoxide selectivity is 51.2%, and the selectivity of hydrogen is 67.4%.
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