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含烯烃原料的选择性加氢脱硫
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作者 肖锦堂 《石油与天然气化工》 CAS 1984年第4期35-39,共5页
与一般饱和烃类的加氢脱硫过程相比,含烯烃原料的加氢脱硫过程具有明显的特殊性。通用的铝酸钴加氧化锌联合处理的加氢脱硫工艺,在用于含烯烃原料脱硫时,由于在加氢脱硫同时,作为原料的烯烃亦极易在钼酸钴催化剂上发生加氢饱和的强烈放... 与一般饱和烃类的加氢脱硫过程相比,含烯烃原料的加氢脱硫过程具有明显的特殊性。通用的铝酸钴加氧化锌联合处理的加氢脱硫工艺,在用于含烯烃原料脱硫时,由于在加氢脱硫同时,作为原料的烯烃亦极易在钼酸钴催化剂上发生加氢饱和的强烈放热反应,不仅使原料的性质发生了根本的变化。 展开更多
关键词 含烯烃 原料 选择性加氢 脱硫 炼油
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催化裂化汽油选择性加氢脱硫中轻重馏分切割温度的研究 被引量:10
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作者 梁咏梅 史权 +1 位作者 刘旭霞 何俊辉 《石油炼制与化工》 CAS CSCD 北大核心 2011年第5期40-44,共5页
利用实验室自制的精馏装置将4种催化裂化汽油分别切割为11个窄馏分,进行总硫、单体烃、族组成和单体硫化物分析,研究烯烃和硫化物在催化裂化汽油中的分布规律,并据此确定催化裂化汽油选择性加氢脱硫中轻、重馏分的最佳切割温度。结果表... 利用实验室自制的精馏装置将4种催化裂化汽油分别切割为11个窄馏分,进行总硫、单体烃、族组成和单体硫化物分析,研究烯烃和硫化物在催化裂化汽油中的分布规律,并据此确定催化裂化汽油选择性加氢脱硫中轻、重馏分的最佳切割温度。结果表明:不同来源催化裂化汽油的烃类化合物组成十分接近,主要由C_4~C_(10)的烷烃、环烷烃、芳烃和烯烃组成;含硫化合物在不同汽油中的浓度差异很大,但其化合物类型十分相似,以C_0~C_4烷基取代的噻吩类化合物为主,四氢噻吩类是另一类重要的含硫化合物;催化裂化汽油中存在一部分小分子硫醇,但其占硫化合物的相对含量随汽油不同而存在较大的差异;催化裂化汽油选择性加氢脱硫中轻、重馏分的最佳切割温度范围为72~80℃。 展开更多
关键词 催化裂化汽油 硫化合物 加氢脱硫 切割点
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Effect of Operating Conditions on Olefin Distribution in FCC Gasoline as Part of an Olefin Reduction Process 被引量:1
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作者 Ouyang Fusheng Pei Xu +2 位作者 Zhao Xuhong Liu Xuan Weng Huixin (Research Institute of Petroleum Processing,East China University of Science and Technology,Shanghai 200237) 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2010年第4期34-42,共9页
The effects of operating conditions on the distribution of olefins in the FCC gasoline, obtained during catalytic cracking reaction in the presence of the GOR-Q catalyst and conventional MLC-500 catalyst, have been st... The effects of operating conditions on the distribution of olefins in the FCC gasoline, obtained during catalytic cracking reaction in the presence of the GOR-Q catalyst and conventional MLC-500 catalyst, have been studied in detail. The test results showed that the GOR-Q catalyst could obviously reduce the content of several kinds of olefins in FCC gasoline. Olefins in the FCC gasoline consist mainly of C5- C7 compounds, that are composed of C=C bond with normal or mono- branched chains. The reduction of gasoline olefin content could be achieved by decreasing the content of above-mentioned olefins. Lower reaction temperature, lower weight hourly space velocity (WHSV) and higher catalyst to oil ratio would help to reduce the content of olefins with a C = C double bond, normal olefins, mono-branched-chain olefins and diolefins. To decrease the loss of gasoline octane number, the operation for olefin reduction should be firstly focused on increasing the catalyst to oil ratio. 展开更多
关键词 operating conditions FCC gasoline olefin CATALYST
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Catalyst Innovation for Reducing Olefin Content in MGG Gasoline
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作者 Yu Daping Qiu Zhonghong 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2010年第2期19-21,共3页
In order to reduce the olefin content in gasoline manufactured by the MGG (Maximizing Liquefied Gas and Gasoline) process while retaining the LPG yield, RIPP has developed a novel catalyst consisting of a more pore-... In order to reduce the olefin content in gasoline manufactured by the MGG (Maximizing Liquefied Gas and Gasoline) process while retaining the LPG yield, RIPP has developed a novel catalyst consisting of a more pore-opened matrix and the modified Y-zeolite and the ZRP zeolite modified with metal oxides. Test results have revealed that compared with the commercial catalyst RAG under comparable reaction conditions the reaction conversion rate and product distribution provided by the novel catalyst were similar, but the olefin content in gasoline obtained thereof was decreased with the octane rating unchanged along with a slight reduction of olefin content in the LPG fraction. The hydrothermal stability of the novel catalyst was better than the commercial catalyst RAG. 展开更多
关键词 CATALYST GASOLINE OCTANE hydrogen transfer reaction olefin selectivity
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Superparamagnetic Supported Catalyst H_3PW_(12)O_40/γ-Fe_2O_3 for Alkylation of Thiophene with Olefine 被引量:1
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作者 许翠霞 杨克迪 +5 位作者 刘自力 秦祖赠 何维 代倩雯 张健杰 张帆 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2014年第3期305-311,共7页
The alkylation of sulfur compounds with olefine is considered to be an attractive way to attain high level of sulfur removal by raising the boiling point of sulfur-containing compounds to ease their separation from li... The alkylation of sulfur compounds with olefine is considered to be an attractive way to attain high level of sulfur removal by raising the boiling point of sulfur-containing compounds to ease their separation from lighl fractions by distillation. A series of superparamagnetic supported catalysts, used for alkylation of thiophene with 1-octene, were prepared by loading H3PW12040 (HPW) onto commercially available nanoparticles γ-Fe2O3 through incipient wet impregnation method. The catalysts were characterized by X-ray diffraction (XRD), Fourier transform infra-red (FT-IR), thermo gravimetric analysis (TG), N2-adsorption and vibrating sample magnetometer (VSM). The physicochemical characterization reveals that 7-Fe203 could be accommodated to immobilize and disperse HPW. Moreover, possessing high magnetization of 26.1 A.mZ.kg-1 and with mesoporous structure with specific surface area of 35.9 m2·g^-1, the 40% (by mass) HPW loading catalyst is considered the proper catalyst for olefinic alkylation of thiophenic sulfur (OATS) and can be separated in an external magnetic field. The catalytic activity was investigated in the alkylation reaction of thiophene with 1-octene, and the conversion of thiophene is up to 46% at 160 ℃ in 3 h. The 40% (by mass) H3PW12O40/γ-Fe2O3 catalyst can be reused 6 times without too much loss of activit and keeps its property of superparamagnetism. 展开更多
关键词 ALKYLATION HETEROPOLYACID THIOPHENE superparamagetism
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