用噻吩加氢脱硫反应评定了催化剂的性能。
The thiophene hydrodesulfurization was adopted to evaluate the activity of the nitride catalysts.
综述了国内外催化裂化汽油降烯烃及加氢脱硫技术进展。
This paper reviewed the advances of olefins degradation and hydrodesulphurization technologies for FCC gasoline at home and abroad.
研究了新型固体硫化剂硫代硫酸铵对加氢脱硫催化剂的预硫化。
Ammonium thiosulfate as a novel sulfiding agent was used for desulfidation of hydrodesulfurization ( HDS) catalysts.
介绍了当前轻质油品脱硫的一些方法，包括传统的加氢脱硫和吸附脱硫等。
Some methods of desulfurization for the light oil were described, including hydrodesulfurization and adsorptiondesulfurization.
近几年，出现了许多新的脱硫技术，其中柴油非加氢脱硫技术的研究进展较快。
Many new desulphurization technologies have been developed in recent years, among which non-hydrogenation desulfurization technology develops faster.
介绍了RI DOS系列催化汽油加氢脱硫降烯烃催化剂的工业试生产及首次工业应用。
Manufacture and first commercial application of RIDOS catalysts for FCC gasoline hydrodesulfurization (HDS) and olefin reduction were described.
介绍了齐鲁石化公司引进的减压渣油加氢脱硫装置生产及催化裂化装置掺炼其产品蜡油和渣油的情况。
The operation of vacuum residue hydrodesulfurization unit imported by Qilu Petrochemical Company and FCCU which processes the obtained VGO and residue as mixed feedstock was discussed.
原位还原法制备的负载型磷化钼催化剂的加氢脱硫活性高于传统的还原-钝化-还原法制备的催化剂。
It is shown that the in situ reduction conditions have great influence on the HDS performance of the prepared catalysts.
研究表明磷化镍在加氢脱硫反应过程中显示出优异的深度脱硫性能，被认为是新一代加氢脱硫催化剂。
Nickel phosphides(Ni2P) as the active component in the hydrodesulfurization process which have showed excellent desulfurization performance is considered as new generation of HDS catalysts.
该催化剂可用于含有机硫化物的轻油馏分或气体的加氢脱硫，特别适用于石脑油和焦化干气的加氢脱硫。
Said catalyst can be used for hydrodesulphurization of light oil fraction or gas containing organic sulphide, in particular, it is applicable to hydrodesulphurization of naphtha and coking dry gas.
主要从单组分载体、复合氧化物载体和新型介孔分子筛三个方面详细论述了加氢脱硫催化剂载体研究进展。
The paper was a review on the development of hydrodesulfurization catalysts in three aspects: single-component support, mixed oxide support and mesoporous molecular sieve.
目前，在研究较多的非加氢脱硫技术中，吸附脱硫技术因其工艺设备简单、操作费用低廉而得到广泛关注。
At present, the adsorption desulfurization technology has attracted a widespread attention as a non-hydrodesulfurization process because of its simple equipment and low operating costs.
本文研究以DX - 30活性炭为载体的镍-铝催化剂制备因素对煤液化油的加氢脱硫脱氮反应的影响。
The effects of preparation factors of Ni-Mo catalyst with DX-30 active carbon as carrier on hydro-desulfurization and hydro-denitrification of coal liquefaction oil were studied.
该催化剂可以广泛的用于石油馏分的加氢处理过程，特别适合于中间馏分油的加氢脱硫、加氢脱氮和加氢脱芳过程。
The said catalyst can be used for hydrotreating process of fraction of petroleum, especially for hydrodesulphurization and hydrodenitrification process of middle distillate oil .
本发明通过掺杂和负载的方法制备了含钴m CM - 41催化剂，在加氢脱硫条件下表现出良好的烯烃骨架异构活性。
In the invention, a catalyst containing cobalt MCM-41 is prepared by the method of doping and loading, and has good olefin skeletal isomerization activity in the hydrodesulfurization condition.
考察了循环氢中硫化氢含量对催化裂化汽油重馏分（HCN）加氢脱硫性能的影响和HCN加氢产物的无碱脱臭处理效果。
The influence of hydrogen sulfide content in recycle hydrogen on the hydrodesulfurization(HDS)of heavy cracked naphtha(HCN)and the performance of sweetening process were studied.
对国内外各种加氢脱硫反应的动力学模型进行了综述，并指出了这些模型存在的不足，以及加氢脱硫动力学的研究方向和面临的挑战。
The kinetics models of HDS at home and abroad are summarized and the shortage of the models is pointed out. The research direction and challenges of kinetics for HDS are put forward.
与以前的沸腾床催化剂相比，该公司最近开发的沸腾床催化剂KF 1302t和KF 1311能够降低沉积物的生成，提供更高的加氢脱硫性能。
The new fluidized bed catalysts KF1302T and KF1311 developed recently provide lower sediment formation and higher HDS activity comparing with the previous catalysts.
轻组分向上流至催化剂段，在那里丁二烯选择性加氢、脱硫和一些烯烃的饱和同时进行。
The light constituents flow upward to the catalyst zone, where the selective hydrogenation of butadiene is carried out together with desulfurization and some olefin saturation.
为加氢裂化装置所使用的精制催化剂和反应催化剂的性能、脱硫效果以及催化剂使用寿命的判断提供了依据。
This provides a good basis for assessing the performance and desulfurization result of the refining catalyst and cracking catalyst of the hydrocracker as well as the service life of the catalysts.
裂解汽油的二段加氢反应主要是脱硫、烯烃饱和等反应。
The second-stage hydrogenation reaction is mainly hydrodesulfurization and alkene saturation hydrogenation of pyrolysis gasoline.
由于微生物脱硫工艺操作压力、温度低，尤其是与加氢技术偶联的生物脱硫工艺成本较小而具有广阔的市场前景。
The biological desulfurization process has broad prospects due to low operating pressure and temperature as well as low production cost coupled with hydrogenation.
采用常压渣油脱硫及渣油预处理-加氢处理两种方案对伊朗常压渣油加工工艺进行了对比。
Two processing schemes, Atmospheric Residue Desulfurization and Residual Oil Pretreating succeeded by hydrotreating, for upgrading Iranian atmospheric residue were compared.
试验结果证明，气液逆流加氢具有更高的脱硫、脱芳烃深度，是一种经济有效的先进加氢精制工艺。
The tests reveal that the gas-liquid countercurrent process offers higher desulfurization and dearomatization efficiency and is a cost-effective hydrotreating process.
新开发的加氢脱氮、脱硫、脱芳烃等催化剂具有活性更高和适用范围宽的特点。
Newly developed catalysts for HDN, HDS, aromatic saturation with still higher activity will find uses in much wider applications.
采用加氢精制催化剂-脱氯剂- 脱硫剂串联方法，从而使所加工的石脑油达到既脱氯又脱硫的目的。该工艺实施以来，运行稳定，脱氯效果良好。
The hydrotreating catalyst, dechlorinating catalyst and desulfurization catalyst are packed in series in one reactor, thus to achieve both dechlorination and desulfurization in one step.
加氢精制反应对催化剂的脱硫、氮、氧，加氢饱和的活性要求更高。
The higher active catalyst of HDS, HDN and saturation hydrogenation is required.
本发明的后加氢制备高质量汽油的系统和方法不仅能脱烯烃，还能脱硫醇和双烯。
The system and the method for preparing high-quality petrol by hydrogenation after recombining component oil refining hydrocarbon cannot only remove olefin, but also can remove thioalcohol and diene.
本发明的后加氢制备高质量汽油的系统和方法不仅能脱烯烃，还能脱硫醇和双烯。
The system and the method for preparing high-quality petrol by hydrogenation after recombining component oil refining hydrocarbon cannot only remove olefin, but also can remove thioalcohol and diene.
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