1)  hic susceptibility
氢裂纹瞧
2)  susceptibility to hydrogen cracking
氢裂纹瞧
3)  hydrogen craking
氢裂
4)  hydrogen cracking
氢裂
5)  hydrocracking
加氢裂化
1.
Energy utilization analysis and energy-saving measures of hydrocracking units;
加氢裂化装置用能分析及节能途径探讨
2.
Selection of Medium Pressure and High Pressure Hydrocracking Technology;
中压和高压加氢裂化工艺技术的选用
3.
Research of Hydrocracking Catalyst FC-40 for High Middle Distillates Production;
FC-40高中油型加氢裂化催化剂的反应性能研究
6)  hydrocracking unit
加氢裂化
1.
This paper introduces clean production management system,environmental targets and management measures in the hydrocracking unit in SINOPEC Yangzi petrochemical company Ltd.
介绍了中国石化扬子石化有限公司芳烃厂加氢裂化车间清洁生产管理体制、环境管理目标及环境管理措施。
2.
According to the practical situation of the HP hydrocracking unit in Yangzi Petrochemical Company and by the testing of the unit′s energy balance,the character of energy comsuption in hydrocracking unit has been analyzed.
结合扬子石化高压加氢裂化装置的实际情况,通过装置的能量平衡测试,对加氢裂化装置的用能特点进行分析,并以用能分析为依据,提高技术水平,优化能源管理,降低装置能耗。
3.
The computer simulation training system of the 2,200,000t/y hydrocracking unit in Zhenhai Refining & Chemical Company Ltd.
镇海炼油化工股份有限公司220万吨/年加氢裂化装置计算机仿真培训系统是1998年由北京东方仿真控制技术有限公司开发的,在该生产装置开工培训中取得了良好的培训效果。
7)  hydrocrack
加氢裂化
1.
Effect and countermeasures to hydrocracker of processing row oil with high sulfur;
加工高含硫原料油对加氢裂化装置的影响及对策
2.
Building of static model for residual hydrocracking processes;
重油加氢裂化过程稳态模型的建立
8)  catalyst
加氢裂化
1.
Heavy distillate hydrocracking technologies and catalysts;
重馏分油加氢裂化工艺和催化剂的新进展
2.
Development of residue slurry-bed hydrocracking catalysts;
渣油悬浮床加氢裂化催化剂研究
3.
Study on deactivated commercial hydrocracking catalysts;
失活加氢裂化催化剂的研究
9)  Hydrocracking
加氢裂解
10)  dehydrogenation and cracking
脱氢裂解
1.
From comparative research of synchronous and asynchronous reaction of dehydrogenation and cracking of dipentene,it is shown that farraginous extent of by-products from synchronous reaction is relatively high.
双戊烯脱氢裂解的同步反应和异步反应对比研究显示,双戊烯脱氢裂解的同步反应产物比较混杂,反应产物中甲苯的相对含量仅为24。
补充资料：缓和加氢裂化
分子式：
CAS号：

性质： 是在中等压力(6.5～10MPa)下对重质馏分油进行加氢裂化增产轻质油品(汽油、煤油、柴油)和裂解原料的炼油技术。流程与高压加氢裂化相似，但它们为一次通过，尾油不循环，且原料为直馏减压馏分油(减压瓦斯油)。其装置投资和操作费均低于高压加氢裂化，约为后者的60％。但所能处理原料的范围和产品灵活性都较小。

说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条