重整原料预加氢催化剂的性能评价  被引量:2

Performance evaluation of pre-hydrotreating catalyst for reforming feedstock

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作  者:王宗宝[1] 胡晓丽[1] 钱颖[1] 王斌[1] 潘曦竹[1] 孙利民[1] 郑云弟[1] 马好文[1] 

机构地区:[1]中国石油天然气股份有限公司兰州化工研究中心,甘肃兰州730060

出  处:《工业催化》2014年第4期306-309,共4页Industrial Catalysis

摘  要:为了考察086-11-46催化剂(W-Ni/SiO2-Al2O3)加氢脱硫、加氢脱氮性能以及处理劣质原料油的能力,分别以直馏石脑油、加入吡啶的直馏石脑油和加入催化汽油的直馏石脑油为原料油,进行了086-11-46催化剂与国内某重整原料预加氢催化剂(Mo-Co/γ-Al2O3)的对比评价,并以直馏石脑油为原料,考察其稳定性。结果表明,086-11-46催化剂的加氢脱硫和加氢脱氮性能均优于对比剂,更加适合处理氮含量及烯烃含量较高的劣质原料油。086-11-46催化剂在入口温度低于对比剂15℃的条件下,产品与对比剂相当,稳定性优于对比剂。In order to study the hydrodesulfurization and hydrodenitrification performance of the catalyst and its treatment ability of inferior raw oils, the evaluation test with 086-11-46 catalyst (W-Ni/SiO2- Al2O3) and the contrast catalyst Mo-Co/γ-Al2O3 was carried out by using straight run naphtha and straight run naphtha with pyridine and catalytic gasoline as the feedstocks,respectively. The long term sta- bility test was investigated using straight run naphtha as the raw material. The results showed that the hydrodesulfurization and hydrodenitrogenation performance of 086-11-46 catalyst was better than that of the contrast catalyst, and 086-11-46 catalyst was suitable for processing inferior raw oils with high contents of nitrogen and olefins. When the inlet temperature of the catalyst was 15 ℃ lower than that of the contrast catalyst, the ability of inferior raw oils treatment and long term running of 086-11-46 catalyst was better than those of the contrast catalyst.

关 键 词:石油化学工程 重整预加氢 直馏石脑油 催化汽油 加氢脱硫 加氢脱氮 

分 类 号:TE624.92[石油与天然气工程—油气加工工程] TQ426.95[化学工程]

 

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