甲烷
合成气
化学
二氧化碳重整
碳纤维
催化作用
化学计量学
动力学
化学动力学
化学工程
分析化学(期刊)
无机化学
物理化学
材料科学
环境化学
有机化学
物理
工程类
复合材料
复合数
量子力学
作者
Jiazheng Ren,Alex Chinghuan Lee,Kai Cheng,Ming Li,Yongsheng Chen
出处
期刊:ChemPhysChem
[Wiley]
日期:2018-04-17
卷期号:19 (15): 1814-1819
被引量:5
标识
DOI:10.1002/cphc.201800137
摘要
Abstract Dry reforming of methane converts two greenhouse gases to syngas, and Ni catalysts are commonly used for this reaction. A major catalyst deactivation mechanism is carbon deposition. Although numerous kinetic modelling works have been performed on carbon formation, there have been only scarce attempts to measure carbon deposition kinetics under relevant (but not real) conditions, owing to technical difficulties. Here, we report the first successful measurements of the kinetics under real reaction conditions. This was made possible by using a novel algorithm that we have developed. We use IR to measure the molar fractions of unreacted CH 4 and CO 2 , and reaction products, CO and H 2 O, in the effluent from the reactor. By applying the general mass balance principle and the relevant reaction stoichiometries, the carbon deposition rate as well as the flow rates of all these gases in the effluent, including H 2 , are calculated. Compared to the dominant GC‐based approach for catalyst performance evaluation, this method has much higher time resolution and much smaller measurement errors.
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