1) SBS hydrogenation
SBS加氢反应
2) hydrogenation
[,haidrədʒə'neiʃən]
加氢反应
1.
Effect of hydrogen partial pressure on terephthalic acid hydrogenation;
氢气分压对对苯二甲酸加氢反应的影响
2.
Hydrogenation and application of Pd-based catalysts;
钯系催化剂加氢反应及应用开发
3.
Characterization of hydrogenation of SBS under normal pressure by IR spectrum;
SBS常压加氢反应的红外光谱表征
3) hydrogenation reaction
加氢反应
1.
According to the production running status of PTA plant ,the factors that had effect on the 4-CBA content in PTA product were analysed from the aspects of oxidation reaction deepth and hydrogenation reaction effects.
根据PTA装置生产运行状况,从氧化反应深度和加氢反应效果2个方面分析了影响PTA中4-CBA含量的因素,并探讨降低4-CBA含量的方法。
2.
Bio-catalysis in supercritical fluids,supercritical water oxidation,organometallic reaction and supercritical-CO2 and supercritical-CO hydrogenation reaction were introduced in detail.
介绍了超临界流体中化学反应的特点及基础理论研究,简要评述了超临界流体作为反应介质的酶催化反应、超临界水氧化反应、金属有机反应和超临界流体作为反应原料的超临界CO2、超临界CO加氢反应。
3.
The test results showed that the aromatics hydrogenation reactions conducted in the presence of different contents of H2S and NH3 in gas phase could be written in the form of a pseudo-first-order reaction and the rate constant was obtained.
在30 mL连续流动固定床加氢试验装置上考察了气相H2S、NH3对柴油馏分芳烃加氢反应的影响。
4) Hydrogenation reactor
加氢反应器
1.
Numeric simulation of transient temperature field on hydrogenation reactor;
加氢反应器瞬态温度场数值模拟
2.
Application of narrow gap welding technique in thick-wall hydrogenation reactor;
窄间隙埋弧焊在厚壁加氢反应器中的应用
5) pre-hydrotreating reaction
预加氢反应
6) hydroprocessing reactor
加氢反应器
1.
Technology of Chinese hot wall hydroprocessing reactor and suggestions on its development in 21st century;
我国热壁加氢反应器技术实力与下世纪发展建议
2.
Study on gas-liquid mixing and distributing system for hydroprocessing reactors
加氢反应器气液混合分配系统浅析
3.
The causes of weld overlay cracking on hydroprocessing reactors and the effect on serviceability were analyzed in this paper.
分析了加氢反应器堆焊层裂纹的成因与对使用的影响。
补充资料：加氢反应器
分子式：
分子量：
CAS号：
性质：加氢装置中进行加氢反应的设备。在工艺上应满足：（1）反应物在反应器中分布均匀，与催化剂接触良好；（2）及时排出反应热，避免超温；（3）合适的反应器长径比，防止催化剂粉碎，避免催化床层压降过大。根据工艺特点分为固定床和沸腾床两种。
分子量：
CAS号：
性质：加氢装置中进行加氢反应的设备。在工艺上应满足：（1）反应物在反应器中分布均匀，与催化剂接触良好；（2）及时排出反应热，避免超温；（3）合适的反应器长径比，防止催化剂粉碎，避免催化床层压降过大。根据工艺特点分为固定床和沸腾床两种。
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