He Rong, Davda Rupali R, Dumesic James A
Department of Chemical and Biological Engineering, University of Wisconsin-Madison, Madison, Wisconsin 53706.
J Phys Chem B. 2005 Feb 24;109(7):2810-20. doi: 10.1021/jp045470k.
Reaction kinetics measurements of the water-gas shift reaction were carried out at 373 K on Pt/Al2O3 in vapor phase to investigate the effects of CO, H2, and H2O partial pressures. Results of in situ ATR-IR studies conducted in vapor phase under similar conditions suggest that the Pt surface coverage by adsorbed CO is high (approximately 90% of the saturation coverage), leading to a negligible effect of the CO pressures on the rate of reaction. The negative reaction order with respect to the H2 pressure is caused by the increased coverage of adsorbed H atoms, and the fractional positive order with respect to the water pressure is consistent with non-equilibrated H2O dissociation on Pt. Results of in situ ATR-IR studies carried out at 373 K show that the presence of liquid water leads to a slight decrease in the Pt surface coverage by adsorbed CO (approximately 80% of the saturation coverage) when the CO partial pressure is the same as in the vapor-phase studies. The rate of the WGS reaction in the presence of liquid water is comparable to the rate under complete vaporization conditions when other factors (such as CO partial pressure) are held constant. Reaction kinetics measurements of methanol reforming were carried out at 423 K over a total pressure range of 1.36-5.84 bar. In situ ATR-IR studies were conducted at 423 K to determine the Pt surface coverage by adsorbed CO in completely vaporized methanol feeds and in aqueous methanol solutions. The decomposition of methanol is found to be slower during the reforming of methanol in liquid phase than in vapor phase, which leads to a lower rate of hydrogen production in liquid phase (0.08 min(-1) at 4.88 bar) than in vapor phase (0.23 min(-1) at 4.46 bar). The lower reaction order with respect to methanol concentration observed for vapor-phase versus liquid-phase methanol reforming (0.2 versus 0.8, respectively) is due to the higher extent of CO poisoning on Pt for reforming in vapor phase than in liquid phase, based on the higher coverage by adsorbed CO observed in completely vaporized methanol feeds (55-60% of the saturation coverage) than in aqueous methanol feed solutions (29-40% of the saturation coverage).
在373K下于气相中对Pt/Al₂O₃上的水煤气变换反应进行反应动力学测量,以研究CO、H₂和H₂O分压的影响。在相似条件下于气相中进行的原位ATR-IR研究结果表明,吸附的CO对Pt表面的覆盖率很高(约为饱和覆盖率的90%),导致CO分压对反应速率的影响可忽略不计。对H₂压力的负反应级数是由吸附的H原子覆盖率增加引起的,而对水压力的分数正反应级数与Pt上未达到平衡的H₂O解离一致。在373K下进行的原位ATR-IR研究结果表明,当CO分压与气相研究中的相同时,液态水的存在会导致吸附的CO对Pt表面的覆盖率略有降低(约为饱和覆盖率的80%)。当其他因素(如CO分压)保持恒定时,存在液态水时水煤气变换反应的速率与完全汽化条件下的速率相当。在423K下于1.36 - 5.84 bar的总压力范围内对甲醇重整进行反应动力学测量。在423K下进行原位ATR-IR研究,以确定在完全汽化的甲醇进料和甲醇水溶液中吸附的CO对Pt表面的覆盖率。发现甲醇在液相中重整时的分解比在气相中慢,这导致液相中氢气生成速率(4.88 bar下为0.08 min⁻¹)低于气相中(4.46 bar下为0.23 min⁻¹)。对于气相与液相甲醇重整观察到的相对于甲醇浓度的较低反应级数(分别为0.2和0.8),是由于基于在完全汽化的甲醇进料中观察到的吸附CO的覆盖率(饱和覆盖率的55 - 60%)高于甲醇水溶液进料溶液中(饱和覆盖率的29 - 40%),气相中重整时Pt上的CO中毒程度高于液相。