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作 者:叶青[1] 金钧[1] 王道[1] 武少华[1] 沈忱 周克斌
机构地区:[1]北京工业大学化学与环境工程学系,北京100022
出 处:《北京工业大学学报》1999年第1期50-55,共6页Journal of Beijing University of Technology
摘 要:以CH4、CO2转化反应所筛选出的Ni-5和Ni-5PM为催化剂,在固定床石英反应器上 考察了天然气及天然气主要成分与CO2转化反应的活性,并将考察筛选出的消炭剂加入到原料 气中,考察了Ni-5PM的活性和稳定性。结果表明:对于CH4、CH4(含4.8%C2H6)、C2H4与 CO2反应体系,低空速时Ni-5和Ni-5PM活性相似、合成气接近平衡,高空速时Ni-5PM的活 性大于Ni-5;对于天然气、CO2转化反应体系Ni-5PM仍具有高活性和高抗积碳性能,加入适 当消碳剂后,产物合成气(H2+CO)摩尔百分含量保持在96%左右,接近理论值,表明 Ni-5PM对天然气、CO2反应体系具有高的活性、选择性及良好的稳定性.Reforming natural gas with CO2 into Synthesis gas was studied on the base of Ni-5 and Ni-SPM catalyst which was previously selected in the reforming of methane with CO2. The activity, stability, and ability of inhibiting the carbon deposition of Ni-5 and Wi-5PM catalyst was studied in the reform of natural gas with CO2. The results showed that the activity of Ni-5 was higher than that of Ni-5 catalyst and its resistance to carbon deposition was higher than that of Wii-5 catalyst. However, there was carbon deposition in the reactor, formed by cracking of high hydrocarbon of natural gas in the reforming of natural gas with CO2. Therefore a gas "A" was added to feed gas to remove the carbon deposition. The resuts show that it can effectively inhibit carbon deposition with little effect on synthesis yield, catalyst activity, selectivity and stability, and it didn't pass into the gases at exit as well. Thus, Ni-5PM has high activity, selectivity and stability in the reforming of natural gas with CO2.
分 类 号:TE665.3[石油与天然气工程—油气加工工程]
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