裂解汽油

裂解汽油加氢装置的物料含有大量易自聚的不饱和烃，自聚造成装置中的分馏器堵塞，会严重影响石油化工厂的连续生产。

The materials to be treated in the distillation towers fo pygas hydrogenation unit contain a lot of unsaturated hydrocarbons which have strong tendency of self-polymerization .

气相色谱法测定热裂解汽油C6～C8馏分中硫化物

Quantitative analysis of sulfides in C_6 ~ C_8 fractions of pyrolysis gasoline by gas chromatography

裂解汽油中C4和C5异构烯烃的分析

The Analysis of C 4 and C 5 Olefins in Cracking Gasoline

色谱与色谱/质谱法相结合分析热裂解汽油C9馏分

Analysis of C_9 Fraction of Pyrolysis Gasoline by Gas Chromato-graphy and Gas Chromatography / Mass Spectrometry

裂解汽油在Co-Mo/Al2O3催化剂上的加氢&脱硫工艺条件

Technological Conditions of Hydrogenation and Hydrodesulfurization of Pyrolysis Gasoline over Co-Mo / Al_2O_3Catalyst

裂解汽油中噻吩硫在Co-Mo/Al2O3上的催化加氢宏观动力学

Macrokinetics for catalytic hydrogenation of thiophenic sulfides in pyrolysis gasoline over Co-Mo / Al_2O_3 catalyst

Ni/TiO2-Al2O3裂解汽油一段选择加氢催化剂的研究

Ni / TiO_2-Al_2O_3 Catalyst for First-Stage Selective Hydrogenation of Pyrolysis Gasoline

负载型Ni-B非晶态合金在裂解汽油加氢反应中的应用研究

Study on pyrolysis gasoline selective hydrogenation catalyzed by supported amorphous alloy

笔者还简要介绍从裂解汽油中分离C5／C9+馏分的几种主要流程，及其优缺点。

The advantages and disadvantages of several main processes for separating C5 / C9 + from pygas are also discussed .

采用高效规整填料提高裂解汽油加氢装置脱碳九塔分离效果和C8芳烃收率。

Increase the separating effect and the C8 aromatics yield by using high efficient regular packing .

本文使用特殊的浸渍方法，成功地研究和开发出了裂解汽油二段HDS催化剂LY-8602B。

The second-stage HDS catalyst LY-8602B for pyrolysis gasoline has successfully developed by using specific impregnation method .

综述了裂解汽油重质馏分增产BTX芳烃的技术进展以及与此相关的加氢脱烷基和非芳烃加氢裂解技术。

Technology Progress of producing BTX aromatics from heavy fraction of pyrolysis gasoline and correlative hydrodealkylation and non-aromatics hydrocracking techniques were reviewed in this paper .

用16m工业电热隧道窑，对裂解汽油一段加氢LY-8601催化剂用载体进行了焙烧实验。

The roasting test of carrier for LY-8601 catalyst in pyrolysis gasoline hydrogenation was studied in a 16 m tunnel kiln .

镍基裂解汽油加氢催化剂LY-2008的工业应用

Industrial application of Nickel based catalyst LY-2008 in pyrolysis gasoline hydrogenation

裂解汽油第二段加氢脱硫催化剂8602B的性能及其工业应用

Performance and commercial application of second-stage hydrodesulfurization catalyst 8602B for pyrolysis gasoline

75～150℃催化裂解汽油的BTX体积含量达到57.6%，其中甲苯和二甲苯分别为21.9%和30.3%。

The total BTX in the 75 ~ 150 ℃ naphtha fraction was 57.6 v % , in which toluene and xylenes were 21.9 v % and 30.3 v % respectively .

以Complex优化法和Merson迭代法对动力学实验数据进行非线性参数估值，建立了能良好吻合实验数据的、裂解汽油中环戊烯和苯乙烯催化加氢的幂函数型本征动力学模型。

By means of the complex optimal method and Merson integral method , power-law type intrinsic kinetic models of catalytic hydrogenation of cyclopentene and styrene were developed , and a good agreement between the experimental and calculated data by the kinetic models estimated here was obtained .

用过氧化氢异丙苯（CHP）作为裂解汽油脱砷的氧化剂，其特点是加量少，无副作用，氧化完全，反应速度快，脱砷效果好。

Using cumine hydroperoxide ( CHP ) as the oxidation accelerator of the removing arsenide from cracked gasoline . This method is noted for its less addition , no by-effect , totally oxidation , high reaction rate and the good result of removing arsenide .

裂解汽油二段加氢脱硫（简称HDS）催化剂的性能受制备方法、载体性质、活性组分在载体上的分布和结合形式、以及载体与活性组分之间相互作用等的影响很大。

The second-stage hydrodesulfurization ( HDS ) catalyst for pyrolysis gasoline is strongly influenced by the method of preparation , the property of support , the dispersion and binding patterns of active components in the support , as well as the interaction between support and active components .

采用氢氧化铝干胶、硝酸钴和钼酸铵为主要原料，通过载体改性和催化剂的制备工艺研究，开发了LH-02裂解汽油的二段加氢脱硫催化剂。

Preparation process of modified carrier and catalyst was studied . The LH-02 second-stage hydrodesulfurization catalyst was developed from aluminum hydrate xerogel , cobaltous nitrate and ammonium molybdate which all served as main materials .

催化裂解汽油精制的最佳工艺条件是：反应温度为70℃，反应压力为0.3MPa，体积空速为1.5h-1。

The ideal process parameters for purification of catalytic pyrolysis gasoline are that : the temperature is 70 ℃, the pressure is 0.3 MPa , the liquid-time space velocity is 1.5 h - 1 .

采用毛细管气相色谱-氢火焰离子化检测器（CGC-FID）和气相色谱-质谱法（GC/MS）分析了热裂解汽油C9馏分的组成。

The constituents of C_9 fraction of pyrolysis gasoline were analyzed by gas chromatography ( GC ) with flame ionization detector ( FID ) and gas chromatography / mass spectrometry ( GC / MS ) . A 100 m × 0.25 mm i.d.

裂解汽油加氢钯系催化剂失活原因浅析

Analysis on inactivation reasons of palladium catalyst in pyrolysis gasoline hydrogenation

红外光谱透射法测定裂解汽油二烯值

Determination of Diene Value in Cracking Gasoline by Infrared Transmission Spectrophotometry

裂解汽油二段加氢催化剂热氢循环再生法的工业应用

Application of hot circulation regeneration of pyrolysis gasoline secondary , hydrogenation catalyst

裂解汽油中环戊烯和苯乙烯催化加氢本征动力学研究

Intrinsic kinetics of catalytic hydrogenation of cyclopentene and styrene in pyrolysis gasoline

裂解汽油加氢装置设备选材浅析

Material Selection for Equipment Used in Hydrogenation Device for Splitting Decomposition Gasoline

催化裂解汽油改质的中试研究

Study on Improving Quality of Catalytic Gasoline in Middle-Scale Test

裂解汽油加氢装置反应系统工艺设计的改进

Improvement of process design for reaction system of pyrolysis gasoline hydrogenation unit

裂解汽油加氢装置脱重塔技术改造

Revamping De - Heavy Fractionator of Crack Gasoline Hydrogenation Plant