加氢催化剂

多孔陶瓷为载体的C3馏分选择加氢催化剂的研究

Study on C_ 3 cut selective hydrogenation catalyst supported on porous ceramics

用X射线光电子能谱研究Cu/SiO2加氢催化剂

X ray photoelectron spectroscopic study on cu / sio2 hydrogenation catalyst

C3液相选择加氢催化剂宏观动力学研究

Kinetic study of C_3 cut liquid-phase selective hydrogenation over supported metal catalyst

氰乙基化纤维素Pd络合物加氢催化剂的X射线光电子能谱研究

Studies on x ray photoelectron spectroscopy of cyanoethyl Pd complex catalyst

化学镀法制备Pd负载型碳二馏分选择加氢催化剂及其催化性能

Supported Pd Catalyst Prepared by Electroless Plating for Selective Hydrogenation of C_2 Fraction

失活NiMo/γ-Al2O3工业加氢催化剂的再生

Regeneration of Spent Industrial NiMo / Al2O3 Catalysts for HDS

纳米CeNi/γ-Al2O3加氢催化剂的活性与稳定性

The Studies on Activity and Stability of Nano-CeNi / γ - Al_2O_3 Hydrogenation Catalyst

Sn对肉桂醛加氢催化剂Pt/Al2O3的修饰作用

The modification effect of Sn on pt / al_2o_3 catalyst for selective hydrogenation of Cinnamaldehyde

建立了采用电感耦合等离子体发射光谱（ICP-AES）测定加氢催化剂中钯含量的方法。

Determination method of Pd content in hydrotreating catalyst by ICP-AES was established .

三组分（NiO、La2O3、SiO2）负载型加氢催化剂中La2O3的作用

Promoter action of la_2o_3 in three components ( nio , la_2o_3 , sio_2 ) supported hydrogenation catalysts

Al2O3-TiO2为载体的前加氢催化剂研究

Studies on Aluminium-Titanium Oxide as Support for Front-End Hydrogenation Catalyst

Ni-W/γ-Al2O3加氢催化剂的制备方式对活性组分分布及化学状态的影响

The effect of preparation method on the distribution and chemical states of active components of ni-w / γ - al_2o_3 catalyst

SiO2负载壳聚糖-Pd多相手性加氢催化剂

Pd-chitosan Heterogeneous Catalyst for Chiral Hydrogenation

钾对苯甲酸甲酯加氢催化剂MnOx/γ-Al2O3的修饰作用

Effect of Potassium on the MnO_x / γ - Al_2O_3 Catalysts for Hydrogenation of Methyl Benzoate

以喹啉为代表，考察了氮化合物在Ni-Mo/Al2O3加氢催化剂上的吸附特性。

Adsorption mechanism of nitrogen containing compounds , using quinoline as a representive , on hydrogenation catalyst Ni-Mo / Al_2O_3 was studied .

超细SiO2负载非晶态Ni-B合金植物油加氢催化剂的研究

Study on amorphous alloy ni-b / sio_2 catalyst for catalytic hydrogenation of vegetable oils

ICP-OES方法测定RN型加氢催化剂中金属杂质含量

Determination of Metal Impurities in RN Hydrotreating Catalyst by ICP-OES

采用PASCA技术研究正电子素o-Ps在MoNi/Al2O3加氢催化剂上的反应动力学

Kinetics study of positronium o-Ps on moni / al_2o_3 hydrotreating catalyst by PASCA

以γ-Al2O3为载体，制备了Ni-La/Al2O3双金属选择性加氢催化剂，并用于催化裂化轻汽油的选择性加氢反应。

The bimetallic selective hydrogenation catalysts Ni - based supported on y - Al2O3 were prepared , which were used in the selective hydrogenation of the FCC light gasoline .

RHT系列渣油加氢催化剂在胜利炼油厂VRDS装置上的工业应用

Commercial Application of RHT Series Residual Oil Hydrogenation Catalyst in Qilu VRDS Plant

新开发的HDO18型催化重整生成油选择性加氢催化剂，以γAl2O3为担体，钯为活性金属组分并加有助剂。

The newly developed catalyst HDO-18 for reformate selective hydrogenation takes γ - Al 2O 3 as carrier , and palladium as active metal with co-catalyst is added .

国产丁二烯加氢催化剂DD-1的工业化应用

Industrial application of domestic butadiene hydrogenation catalyst DD-1

采用Mo-Ni-P/-γAl2O3加氢催化剂，对中粘度的聚α-烯烃合成基础油进行加氢精制，精制前对加氢催化剂进行合理的预硫化。

Hydrofining of medium viscosity poly - α - olefin lubricating base oil over Mo-Ni-P / γ - Al_2O_3 was studied . The Mo-N-P / γ - Al_2O_3 catalyst was sulfided before use .

为了不使用任何还原剂而获得聚合物固载高分散零价双金属加氢催化剂，利用金属蒸气法制备了3种不同Pd／Cu质量比的聚合物固载双金属原子簇。

In order to obtain polymer immobilized highly dispersed zero-valent bimetallic catalyst for hydrogenation without using any reductant , the metal vapor method was employed to prepare polymer immobilized Pd Cu bimetallic clusters with three different Pd / Cu mass ratios .

介绍了新型碳二前加氢催化剂E-seriesFEE-DC3在国外A石化公司乙烯装置的工业应用情况，分析了该催化剂反应机理和主要影响因素。

The industry application of the C_2 hydrogenation catalyst E-series FE E-DC3 in the ethylene plant of A petrochemical company was introduced .

实验证明：酸性气作硫化介质对加氢催化剂进行干法硫化是可行的，当CO2浓度达到H2S浓度的1.5倍时，溴价仍满足工业溴价小于0.5gBr2/100g的要求。

The results showed that It was feasible to sulfurize hydrotreating catalyst by acidity gas . The bromine number was still less than 0.5gBr_2/100g when the concentration of CO_2 was up to 1.5 times concentration of H2S .

传统MoS2加氢催化剂粒径大、油溶性差而催化效率相对较低。

Conventional molybdenum disulfide hydrogenation catalysts are inferior in catalytic efficiency due to their relatively larger particle size and lower oil-solubility .

所用RA－1芳烃深度饱和加氢催化剂活性好、强度高，所采用的工艺过程操作简单、运转稳定、生产灵活性大、对原料油的适应性好。

The high aromatic saturation catalyst , RA 1 , possesses high activity and high strength . The two stage hydrogenation process has the advantages of simple and flexible operation , steadily running , and suitable for processing various feeds .

VAH型气相醛加氢催化剂的工艺研究

Study on process of VAH-type aldehyde hydrogenation catalyst by gas-phase method

NCG-6型苯加氢催化剂性能的研究

Research on properties of NCG-6 benzene hydrogenation catalyst