Gasification of deposit formed in steam reforming or cracking of n-butane on the promoted nickel catalysts

被引：0
|
作者：
Stasinska, B [1 ]
Golebiowski, A
Borowiecki, T
机构：
[1] Marie Curie Sklodowska Univ, Fac Chem, PL-20031 Lublin, Poland
[2] Inst Fertilizers, PL-24100 Pulawy, Poland
来源：
CATALYST DEACTIVATION 1999 | 1999年 / 126卷
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D O I：
暂无
中图分类号：
O69 [应用化学];
学科分类号：
081704 ;
摘要：
Small additions of molybdenum compounds (less than or equal to 0.5 wt. %) cause a significant increase in resistance to coking of nickel catalysts in the steam reforming of hydrocarbons. The influence of promoter on the gasification rate of carbon deposits in different gaseous mixtures was studied. It was found out that the rate of carbon gasification on Ni-Mo catalysts is smaller than on Ni catalysts.
引用
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页码：431 / 434
页数：4
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