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LH-26加氢处理催化剂的重生及其活性评价 被引量:1
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作者 黄新平 魏军 +1 位作者 王华 伍三军 《石化技术与应用》 CAS 2021年第5期305-309,共5页
采用氧化再生和有机溶剂浸渍重生工艺对失活LH-26加氢处理催化剂进行重生,制备出重生催化剂,利用物理吸附仪、X射线衍射仪、碳硫分析仪等仪器分析了其物性,并以脱沥青油为原料,按照工业装置运行工艺条件,对新鲜催化剂和重生催化剂进行... 采用氧化再生和有机溶剂浸渍重生工艺对失活LH-26加氢处理催化剂进行重生,制备出重生催化剂,利用物理吸附仪、X射线衍射仪、碳硫分析仪等仪器分析了其物性,并以脱沥青油为原料,按照工业装置运行工艺条件,对新鲜催化剂和重生催化剂进行加氢活性评价。结果表明:与再生催化剂相比,使用有机溶剂(质量分数8%)浸渍过的重生催化剂比表面积和孔体积均得到有效恢复,有机溶剂起到再分散金属的作用,团聚金属晶型峰强度明显变小;与新鲜催化剂相比,重生催化剂的活性反应温度约高5℃,当反应温度为375~390℃时,重生催化剂生成油中含硫(氮)质量浓度均小于10 mg/L,重质润滑油收率为51.20%~64.30%,其黏度指数为92~105,满足催化剂工业应用要求。 展开更多
关键词 加氢处理催化剂 催化剂重生 脱沥青油 质润滑油 黏度指数 活性评价
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Advances in DCC Process and Catalyst for Propylene Production from Heavy Oils 被引量:5
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作者 Liu Yujian Long Jun +2 位作者 Tian Huiping Xu Yun Zhao Liuzhou (Research Institute of Petroleum Processing,SINOPEC,Beijing 100083) 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2011年第1期1-5,共5页
In the past several decades,SINOPEC has devoted continuously great efforts to the development of DCC technology,the only commercial process using heavy feeds aiming at propylene production.Recently,a series of researc... In the past several decades,SINOPEC has devoted continuously great efforts to the development of DCC technology,the only commercial process using heavy feeds aiming at propylene production.Recently,a series of research breakthroughs have been achieved in molecular refining.Based on the detailed analysis on the complex DCC reaction network,an innovative catalyst technology has been developed to Optimize Catalysis Kinetics (OCK in brief).The deep-cracking process can be improved with optimizing the availability of the active sites.The updated MFI and beta zeolites are used to boost the propylene selectivity.The latest generation catalyst DMMC-1 has been applied commercially.Compared with the best historical records in the past,the propylene yield upon application of the catalyst DMMC-1 increases by 2.4 m% coupled with an improved distribution of products.The DCC technology continues to assume a leading position for manufacturing propylene from heavy feedstocks. 展开更多
关键词 petrochemical engineering PROPYLENE catalytic cracking CATALYST catalysis kinetics
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Major Technical Measures for Revamp of FCC Units in China
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作者 LiWenjie 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2003年第4期11-14,共4页
FCC units are playing an important role at refineries, in particular at Chinese refineries. To cope with the current demand for better economic benefits, environmental protection and product slate adjustment, a host o... FCC units are playing an important role at refineries, in particular at Chinese refineries. To cope with the current demand for better economic benefits, environmental protection and product slate adjustment, a host of FCC units need to be technically revamped. This article describes the practical processes, technologies and equipment to serve different revamp targets with analysis of two examples on revamp of commercial units. 展开更多
关键词 catalytic cracking technical revamp commercial scale
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Maximum Hydrogen Production by Autothermal Steam Reforming of Bio-oil With NiCuZnAI Catalyst 被引量:1
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作者 Shi-zhi Yan Qi Zhai Quan-xin Li 《Chinese Journal of Chemical Physics》 SCIE CAS CSCD 2012年第3期365-372,374,共9页
Autothermal steam reforming (ATR) of bio-oil, which couples the endothermic steam reform- ing reaction with the exothermic partial oxidation, offers many advantages from a technical and economic point of view. Effec... Autothermal steam reforming (ATR) of bio-oil, which couples the endothermic steam reform- ing reaction with the exothermic partial oxidation, offers many advantages from a technical and economic point of view. Effective production of hydrogen through ATR of bio-oil was performed at lower temperature with NiCuZnAl catalyst. The highest hydrogen yield from bio-oil reached 64.3% with a nearly complete bio-oil conversion at 600℃, the ratio of steam to carbon fed (S/C) of 3 and the oxygen to carbon ratio (O/C) of 0.34. The reaction conditions in ATR including temperature, O/C, S/C and weight hourly space velocity can be used to control both hydrogen yield and products distribution. The comparison between the ATR and common steam reforming of bio-oil was studied. The mechanism of the ATR of bio-oil was also discussed. 展开更多
关键词 HYDROGEN BIO-OIL Autothermal steam reforming NiCuZnA1 catalyst
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Influence of ultrasonic on the coking amount of catalyst (Ni/γ-Al2O3) for the dry reforming of benzene
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作者 杨国来 陈汉平 +1 位作者 米铁 冯波 《Journal of Coal Science & Engineering(China)》 2007年第1期79-84,共6页
The Influence of ultrasonic treatment on the coking amount of a nickel-based catalyst (Ni/γ-Al2O3) for the reaction of reforming with carbon dioxide of Benzene was investigated. The results show that ultrasonic tre... The Influence of ultrasonic treatment on the coking amount of a nickel-based catalyst (Ni/γ-Al2O3) for the reaction of reforming with carbon dioxide of Benzene was investigated. The results show that ultrasonic treatment modify the pore size distribution of the catalysts significantly and also reduce the amount of coke formed on the catalyst. The reduction in the coking amount is not sensitive to the power output of the ultrasonic treatment device in the power range tested (120 W and 500 W). 展开更多
关键词 Ni/γ-Al2O3 ultrasonic treatment COKING benzene reforming
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