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NO_x催化的甲烷气相氧化反应 被引量:2

Gas-Phase Oxidation of Methane Catalyzed by NO_x
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摘要 考察了没有固体催化剂时NOx 对甲烷气相氧化的催化作用 ,并用原位红外光谱研究了CH4 O2 NOx 体系随温度的变化 .实验结果表明 ,NOx 对甲烷气相氧化有很高的催化活性 .在 2 0 %CH4 10 %O2 体系中加入 0 0 5 %~ 0 2 %的NO后 ,反应温度可降低 2 0 0~ 3 0 0℃ ,在 65 0~ 70 0℃下反应时 ,CH4 转化率和CO选择性可分别达到 3 8%和 90 % ,产物中的n(H2 ) /n(CO)比为 0 4~ 0 7.反应产物中可观察到有甲醛、甲醇和乙烯等 。 Catalytic conversion and catalytic combustion of CH_4 have received extensive attention because of their potential to synthesize useful chemicals and to reduce pollutant emissions. Both the processes require activation of CH_4, which has been mostly achieved over solid catalysts to date. In the catalytic conversion of CH_4, the promotional effects of NO_x on CH_4 oxidation were reported by some researchers, but the role that NO_x may play in CH_4 activation and the importance of this gas-phase reaction have not received more attention. This work investigated the catalytic effect of NO_x on partial oxidation of CH_4 in the absence of solid catalyst. The product distribution was studied by in-situ FT-IR under different reaction conditions. The results showed that the addition of a small amount of NO into 20%CH_4-10%O_2 system decreased the reaction temperature by 200~300 ℃. At 650~700 ℃, the CH_4 conversion and CO selectivity were 38% and 90%, respectively, and n(H_2)/ n(CO)=0.4~0.7. The optimum conditions for CO formation were n(CH_4)/ n(O_2)=2 and low flow rate. Some reducible substances, such as HCHO, CH_3OH and C_2H_4, were also observed in the products. The HCHO was formed at 460 ℃, then CO (480 ℃), CH_3OH (500 ℃), and C_2H_4 (540 ℃) were formed. Low temperature favours the formation of HCHO and CH_3OH, while high temperature favours C_2H_4. Under strong oxidizing conditions ( n(O_2)/ n(CH_4)=5), NO_x also exhibits considerable catalytic activity and selectivity for CH_4 conversion to CO. For 0.4%CH_4-2%O_2 system, the temperature for CH_4 activation is higher than 800 ℃ in the absence of NO_x. In the presence of NO_x, however, the activation temperature is reduced to below 570 ℃. The addition of 0.06%NO results in the increase of CO yield from 25% to 68%. It was shown that no reaction was observed for CH_4-NO_x system (without O_2) under the reaction conditions, indicating that the NO_2 formation is a prerequisite for CH_4 activation. Also, no decrease of NO/NO_2 concentration was observed up to 950 ℃, indicating that NO_x cannot be reduced by CH_4 in the absence of solid catalyst. Both CH_4 conversion and CO yield reached a maximum when φ(NO)=0.04%~0.06%, while the highest TOF (turnover frequency) of 40 s -1 was obtained when φ(NO)=0.01%.
出处 《催化学报》 SCIE CAS CSCD 北大核心 2003年第1期37-41,共5页
关键词 气相氧化反应 甲烷 氮氧化物 均相催化 催化燃烧 催化氧 天然气 催化转化 methane, oxidation, nitrogen oxide, homogeneous catalysis, catalytic combustion
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同被引文献32

  • 1汪晓星,林宝敏,杨薇,郭倩,张庆红,王野.SBA-15负载钒氧化物催化剂上甲烷选择氧化反应[J].化学学报,2004,62(18):1738-1744. 被引量:12
  • 2陈立宇,杨伯伦,张秀成,董武,曹凯.V_2O_5催化的甲烷液相部分氧化反应[J].催化学报,2005,26(11):1027-1030. 被引量:13
  • 3刘红梅,徐奕德.甲烷无氧芳构化反应催化剂Mo/HZSM-5的H_2-TPR研究[J].催化学报,2006,27(4):319-323. 被引量:15
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