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The oxidative dehydrogenation of ethane: Gas phase and catalytic.

机译:乙烷的氧化脱氢:气相和催化。

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The gas-phase and the catalytic oxidative dehydrogenation of ethane were studied. Lithium-promoted magnesium oxide was investigated as the catalyst. In the gas-phase oxidation study a perfectly mixed tubular reactor was used. The most dramatic effect in this study was an increase in the rate of ethane conversion when the concentration of water vapor was increased. The conversion for ethane and selectivity for ethylene with a C{dollar}sb{lcub}rm 2{rcub}{dollar}H{dollar}sb{lcub}rm 6{rcub}{dollar}:O{dollar}sb{lcub}rm 2{rcub}{dollar} ratio of 2 at 560 {dollar}sp{lcub}rm circ{rcub}{dollar}C was 2.1 and 81%, respectively, while the addition of ca. 300 torr of water vapor increased the conversion and selectivity to 31 and 81%, respectively. This unusual and dramatic effect was attributed to water acting as a third body in the hydrogen peroxide decomposition to hydroxyl radicals.; Lithium-promoted magnesium oxide has been found to be an effective catalyst in the conversion of ethane to ethylene. In this study a fixed-bed, plug flow reactor, operating at atmospheric pressure and in the range of 500-700{dollar}spcirc{dollar}C, was used. The activation of ethane in the gas-phase was inhibited by filling the empty space in the reactor with quartz chips. A selectivity of 75% was obtained at a 40% ethane conversion over 6.5 g of 3 wt % Li/MgO catalyst and a C{dollar}sb{lcub}rm 2{rcub}{dollar}H{dollar}sb{lcub}rm 6{rcub}{dollar}:O{dollar}sb{lcub}rm 2{rcub}{dollar} ratio of 2 at 600 {dollar}sp{lcub}rm circ{rcub}{dollar}C. An apparent activation energy of 37.3 kcal mol{dollar}sp{lcub}rm -1{rcub}{dollar} was obtained for this process. The kinetic and spectroscopic data suggest that (Li{dollar}sp{lcub}rm +{rcub}{dollar}O{dollar}sp{lcub}rm -{rcub}{dollar}) centers are responsible for the initial activation of ethane via hydrogen atom abstraction to produced C{dollar}sb{lcub}rm 2{rcub}{dollar}H{dollar}sb{lcub}rm 5{rcub}bullet{dollar} radicals. These surface-generated radicals can be desorbed into the gas-phase to subsequently dehydrogenate to ethylene or they can be adsorbed on the surface and eventually decompose to carbon oxides. This mechanism is similar to the activation of methane over the same material, which may indicate that the activation of alkanes by (Li{dollar}sp{lcub}rm +{rcub}{dollar}O{dollar}sp{lcub}rm -{rcub}{dollar}) centers on the Li/MgO catalyst is a general phenomenon.
机译:对乙烷的气相和催化氧化脱氢进行了研究。研究了锂促进的氧化镁作为催化剂。在气相氧化研究中,使用了完全混合的管式反应器。在这项研究中,最显着的效果是当水蒸气浓度增加时,乙烷转化率增加。 C {dollar} sb {lcub} rm 2 {rcub} {dollar} H {dollar} sb {lcub} rm 6 {rcub} {dollar}:O {dollar} sb {lcub的乙烷转化率和乙烯选择性} rm 2 {rcub} {dollar}在560 {dollar} sp {lcub} rm circ {rcub} {dollar} C处的比率2分别为2.1和81%,而添加ca时。 300托水蒸气将转化率和选择性分别提高到31%和81%。这种异常而引人注目的效果归因于水在过氧化氢分解为羟基自由基时作为第三体。已发现锂促进的氧化镁是乙烷转化为乙烯的有效催化剂。在这项研究中,使用了固定床,活塞流反应器,该反应器在大气压下且在500-700℃的温度范围内运行。通过用石英片填充反应器中的空白空间来抑制气相中的乙烷活化。在6.5 g的3 wt%Li / MgO催化剂和C {dollar} sb {lcub} rm 2 {rcub} {dollar} H {dollar} sb {lcub}上,乙烷转化率为40%时,选择性达到75% rm 6 {rcub} {dollar}:O {dollar} sb {lcub} rm 2 {rcub} {dollar}在600 {dollar} sp {lcub} rm circ {rcub} {dollar} C处的比率为2。对于该过程,获得了37.3kcal mol {dollar} sp {lcub} rm -1 {rcub} {dollar}的表观活化能。动力学和光谱数据表明(Li {dollar} sp {lcub} rm + {rcub} {dollar} O {dollar} sp {lcub} rm-{rcub} {dollar}个中心负责乙烷的初始活化通过氢原子提取产生C {dollar} sb {lcub} rm 2 {rcub} {dollar} H {dollar} sb {lcub} rm 5 {rcub} bullet {dollar}自由基。这些表面产生的自由基可被解吸到气相中,随后脱氢成乙烯,或者它们可被吸附在表面上并最终分解成碳氧化物。该机制类似于在同一材料上甲烷的活化,这可能表明烷烃通过(Li {dollar} sp {lcub} rm + {rcub} {dollar} O {dollar} sp {lcub} rm- {rcub} {dollar})以Li / MgO催化剂为中心是普遍现象。

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