首页> 外文期刊>Journal of Catalysis >Methane Partial Oxidation by Unsupported and Silica Supported Iron Phosphate Catalysts: Influence of Reaction Conditions and Co-Feeding of Water on Activity and Selectivity
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Methane Partial Oxidation by Unsupported and Silica Supported Iron Phosphate Catalysts: Influence of Reaction Conditions and Co-Feeding of Water on Activity and Selectivity

机译:无载体和二氧化硅载体的磷酸铁催化剂对甲烷的部分氧化:反应条件和水的共进料对活性和选择性的影响

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The partial oxidation of methane to methanol and formaldehyde by molecular oxygen has been investigated over crystalline and silica supported FePO_4 at a pressure of 1 atm and in the temperature range of 723-973 K. The quartz Phase of FePO_4, as well as silica supported FePO_4 prepared by impregnations (5 wt%), were examined in a continuous flow reactor. Experiments carried out over FePO_4 show high selectivity to formaldehyde at low conversion and suggest that formaldehyde is the primary reaction product, but selectivity decreased rapidly as conversion was increased. The highest space-time yield of formaldehyde observed for this catalyst was 59 g/kg_(cat)-h. Above 5% methane conversion, carbon oxides were the only products. For silica-supported FePO_4, formaldehyde selectivity did not fall off rapidly, exhibiting a formaldehyde selectivity of 12% at about 10% conversion (STY = 285 g/kg_(cat)-h). Quantifiable fields of methanol were observed at very low conversion levels, i.e. below 3% (STY = 11 g/kg_(cat)-h). Addition of steam (up to 0.1 atm partial pressure) into the feed stream increased the selectivity to methanol (approx 25 g/kg cat/h with up to 3% selectivity) and formaldehyde (approx 487 g/kg cat/h with up to 94% selectivity) for the silica-supported FePO_4 catalyst. Steam addition had little effect on catalyst activity. Characterization results indicate the presence of FePO_4, as well as fivefold coordinate Fe~(3+) in silica supported catalyst samples, and this species is proposed to be responsible for methane activation. After catalysis in the presence of steam, the fivefold coordinate iron is present, but a significant freaction of the FePO_4 has been reduced to Fe_2P_2O_7. enhanced selectivity in the presence of steam is attributed in part to the ease of the reversible formation of surface hydroxyl groups (P-OH) from pyrophosphate (P-O-P) groups.
机译:在1atm的压力和723-973 K的温度范围内,研究了在晶体和二氧化硅负载的FePO_4上甲烷由分子氧将甲烷部分氧化为甲醇和甲醛的情况。FePO_4的石英相以及二氧化硅负载的FePO_4在连续流反应器中检查通过浸渍(5重量%)制备的溶液。在FePO_4上进行的实验显示出低转化率时对甲醛的高选择性,并表明甲醛是主要的反应产物,但随着转化率的提高,选择性迅速降低。对于该催化剂观察到的甲醛的最高时空产率为59g / kg_cat-h。甲烷转化率高于5%时,碳氧化物是唯一的产物。对于二氧化硅负载的FePO_4,甲醛的选择性并未迅速下降,在约10%的转化率下(STY = 285 g / kg_cat-h)表现出12%的甲醛选择性。在非常低的转化率下,即低于3%(STY = 11 g / kg_cat-h),观察到了可量化的甲醇场。在进料流中添加蒸汽(分压最​​高为0.1 atm)可提高对甲醇的选择性(约25 g / kg cat / h,选择性高达3%)和甲醛(约487 g / kg cat / h,最高可达90%)。二氧化硅负载的FePO_4催化剂的选择性为94%)。加入蒸汽对催化剂活性影响很小。表征结果表明,FePO_4的存在以及二氧化硅负载的催化剂样品中Fe〜(3+)的五重配位,并且该物种被认为与甲烷活化有关。在蒸汽存在下催化后,存在五重配位铁,但FePO_4的明显碎片已还原为Fe_2P_2O_7。在蒸汽存在下提高的选择性部分归因于易于从焦磷酸盐(P-O-P)基团可逆形成表面羟基(P-OH)。

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