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作 者:张齐[1] 鲁树亮[1] 陈勇 Zhang Qi;Lu Shuliang;Chen Yong(Beijing Research Institute of Chemical Industry,SINOPEC,Beijing 100013,China)
机构地区:[1]中石化(北京)化工研究院有限公司,北京100013
出 处:《精细石油化工》2023年第4期27-31,共5页Speciality Petrochemicals
摘 要:研究了Ni/Al_(2)O_(3)催化剂上CO和H_(2)的暂态反应和稳态反应过程吸附态的变化。结果表明:在250℃下,Ni/Al_(2)O_(3)催化剂在吸附CO形成了线式吸附态(2065 cm^(-1))和桥式吸附态(1913 cm^(-1))。在250℃下CO和H_(2)共吸附时,CO发生了氢助解离而不是直接解离,线式吸附态(2073 cm^(-1))和桥式吸附态(1909 cm^(-1))会和催化剂表面解离吸附的氢发生反应生成羰基氢化物(2060和1895 cm^(-1)),在氢气过量的情况下又进一步生成多氢羰基氢化物(1854 cm^(-1)),而多氢羰基化合物是生成甲烷的中间产物。The transient and steady-state reactions of CO and H_(2) over Ni/Al_(2)O_(3)catalysts were studied by in-situ DRIFTS.The results showed that the Ni/Al_(2)O_(3)catalyst formed a linear adsorption state(2065 cm^(-1))and a bridge adsorption state(1913 cm^(-1))for CO adsorption at 250℃.When CO and H_(2) were adsorbed at 250℃,CO undergoes hydrogen assisted dissociation rather than direct dissociation.The linear adsorption state(2073 cm^(-1))and bridge adsorption state(1909 cm^(-1))react with the dissociated adsorbed hydrogen on the catalyst surface to generate carbonyl hydrides(2060 and 1895 cm^(-1)).In the case of excessive hydrogen,it will further generate multi carbonyl hydrogen hydride(1854 cm^(-1)),which is an intermediate product of methane generation.
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