重油催化裂化是炼油厂重要的二次加工装置，是原油深度加工的重要手段之一。
Residue oil catalytic cracking is an important and major means in deep process in crude treatment.
用催化剂RN-10研究了催化裂化柴油加氢深度脱芳烃工艺参数对芳烃加氢饱和反应的影响。
The impact of process parameters on aromatics saturation reaction of FCC light cycle oil over RN-10 hydrotreating catalyst was studied.
加氢裂化是重油深度加工工艺之一，已在现代炼油和石油化学工业得到广泛应用。
Hydrocracking is one of the most important heavy oil deep conversion processes and has been widely used in modern refining and petrochemical industry.
各种组合工艺的运用为重油催化裂化提供了优质原料，提高了渣油加工深度，增强了企业的应变能力和经济效益。
The use of integrated process provides more qualified feedstock for RFCC, increases the yield of light oil, and enhances the economic benefit of refineries and adaptability of crude oil.
新技术适合稠油减渣的减粘裂化， 裂解深度大，反应灵敏，并经过了长周期的实践，可供同类装置技术改进时参考。
The new technology is suitable for vacuum residue of dense crude oil. The breaking depth can be increased. As the unit has passed a long term practice, it can be a reference for similar units.
渣油沸腾床加氢裂化是实现劣质渣油深度加工的工艺技术，有利于提高炼油厂的轻质油收率。
Ebullating bed hydrocracking technology could be used to upgrade heavy residue for improving the light products yield of a refinery.
渣油沸腾床加氢裂化是实现劣质渣油深度加工的工艺技术，有利于提高炼油厂的轻质油收率。
Ebullating bed hydrocracking technology could be used to upgrade heavy residue for improving the light products yield of a refinery.
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