重油催化,RFCC
1)RFCC重油催化
1.Analysis on frequent shutdowns of flue gas turbine of RFCC Unit and countermeasures;重油催化装置烟机频繁停机原因分析及对策
2.Application of Combined Column Plates with Slopping Holes in the Revamp of the Absorption and Stabilization System of RFCCU;复合斜孔塔板在重油催化吸收稳定系统改造中的应用
3.Technical Transformation for Increasing Propylene Output of RFCC Unit;提高重油催化装置丙烯产量的技术改造
英文短句/例句

1.Investigation on the causes for abnormal loss of FCC catalyst in RFCC unit重油催化裂化装置催化剂跑损原因分析
2.Application of CDC FCC Catalyst in Dalian Petrochemical's RFCC UnitCDC催化剂在大连石化重油催化装置的应用
3.Analysis of adsorbed substances on catalysts in RFCCU重油催化裂化催化剂上吸附物的汽提过程分析
4.The Amelioration and Optimization Riser Reactor System in the Process of Catalyse and Cracking Technics;重油催化裂化反应系统的改进与优化
5.Influencing Factors of Coking for Heavy Oil Catalytic Pyrolysis重油催化裂解催化剂结焦影响因素的研究
6.Discussion on Process Optimization to Residuum Hydrogenated Combined with RFCC渣油加氢与重油催化裂化组合工艺优化探讨
7.Technical Measures of Improving Ratio of Diesel Oil and Gasoline in Heavy Oil FCC重油催化裂化提高柴汽比的技术措施
8.Applications of the Maximizing Gas and Diesel Technology(MGD) in the RFCCMGD技术在重油催化裂化装置的应用
9.EFFECT OF ENHANCEMENT OF CATALYST-OIL MIXING HEAT ON RESIDUE CATALYTIC CRACKING高油-剂混合热量对重油催化裂化反应的影响
10.Application of Endurance Catalyst in Heavy Oil Catalytic CrackerEndurance催化剂在长庆石化重油催化裂化装置上的应用
11.Development of a new nickel passivator for FCC process一种新型重油催化裂化抗镍钝化剂的开发研究
12.Simulation and Optimization of the Gas Fractionation Unit in the RFCC重油催化裂化气体分馏装置的工艺模拟与优化
13.Design and Application of Real Time Optimization of Rfccu with Correlation Integration Optimizer重油催化裂化相关积分优化控制设计与应用
14.Study on Chemical Stripping Process of Residue Fluid Catalytic Cracking重油催化裂化化学汽提器工艺条件的研究
15.Hydrocarbon Components of Products from Residue Fluid Catalytic Cracking under Different Reaction Conditions不同条件下重油催化裂化产物的烃组成变化
16.DEVELOPMENT OF INTERCALATED CLAY CATALYST AS HEAVY OIL CATALYTIC CRACKING膨润土作重质油催化裂化催化剂的开发
17.Aqua-Thermolysis of Resins from Heavy Oil Catalyzed by Dispersed Catalysts分散型催化剂催化重油胶质的水热裂解反应
18.INDUSTRIAL APPLICATION OF HEAVY OIL CRACKING CATALYST RMS-8重油裂化催化剂RMS-8的工业应用
相关短句/例句

Heavy oil catalysis重油催化
1.A failure analysis of the sealing head at the bottom of the ammonia refining tower in a heavy oil catalysis unit has been made.分析了重油催化装置的氨精制塔塔底封头开裂原因 ,发现母材 30 4不锈钢由于冷加工 (旋压 )发生马氏体相变 。
2.0 Mt/a heavy oil catalysis construction in one company was reformed,the reform of anticorrosion and energy saving was carried out for the residue heat boiler.0 M t/a重油催化装置技术改造后,为适应前部生产要求,对余热锅炉进行防腐节能改造,改造后锅炉过热蒸汽温度由改造前370℃提高到420℃以上,排烟温度由330℃降低至185℃,装置能耗降低。
3)catalytic reformed gasoline催化重整油
4)catalyst[英]['k?t?l?st][美]['k?tl??st]重油催化轻柴油
1.Hydrofining of Daqing mixed oil on FH-98 catalyst;FH-98型催化剂用于大庆焦化柴油和重油催化轻柴油混合油加氢精制的研究
5)heavy oil FCC重油催化裂化
1.Analysis of feasibility of energy saving in absorption & stabilization system of heavy oil FCC unit重油催化裂化装置吸收稳定系统的节能可行性分析
2.In the revamping of 20 000 b/d heavy oil FCC unit with MIP-CGP process in Qingdao Petro- chemical Co.介绍了青岛石化1 Mt/a重油催化裂化装置MIP-CGP技术改造情况,沉降器汽提段改造应用了中国石化集团洛阳石油化工工程公司开发的高效汽提段和两段汽提技术。
6)heavy oil catalytic cracking重油催化裂化
1.Lanzhou Petrochemical heavy oil catalytic cracking transformation unit,using optimized process parameters,the transformation of flue gas turbine-expander,the four units configuration,stable operation of the device,the improved flue gas turbine-expander efficiency,greatly reduced the unit energy consumption of devices to create a good economic benefits.兰州石化重油催化裂化装置机组改造中,采用优化工艺参数、改造烟气轮机、进行四机组配置,在装置平稳运行的情况下,提高了烟气轮机效率,大大降低了装置的机组能耗,创造了良好的经济效益。
2.For example,an analysis of heavy oil catalytic cracking unit to absorb the stability of the system to reduce hydrocarbon C2 content of the feasibility,actual data on the device analysis and optimization program for the production of devices to create economic benefits.举例分析了重油催化裂化装置吸收稳定系统降低液态烃C2含量的可行性,对装置实际生产数据进行分析并提出优化方案,为装置生产创造经济效益。
延伸阅读

重油分子式:CAS号:性质:(一)heavy oil 在石油工业中,指由天然石油或人造石油提去汽油、煤油和柴油后的液态残余物。暗黄色。黏稠而重。密度约为0.90~0.96g/cm3。热值约为45 171kJ/kg。用作裂化和气化原料、锅炉燃料以及制造润滑油的原料。(二)creosote(oil);dead oil在煤焦油工业中,指高温煤焦油在轻油和中油后的第三个馏分即在230~300℃蒸出的馏分。又称杂酚油(creosote)。黄绿色。黏稠而重。密度约为1.04~1.07g/cm3。久露空气中变褐色。冷却时有萘等固体析出。并可提取苊、芴、甲酚、二甲酚、喹唑、异喹啉等。也可用作木材的防腐剂等。