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1)  reformate raffinate
重整抽余油
1.
Based on molecular management and composition of reformate raffinate, separation of nor- mal paraffins from reformate raffinate through adsorption process was studied in the 5A molecular sieve fixed bed.
根据重整抽余油的组成特点,依据5A分子筛择形吸附特性将重整抽余油中的正构烷烃进行吸附分离。
2.
In order to prolong the running cycle of producing high purity n-hexane from reformate raffinate through adsorption-distillation technology,coking of olefins in the channels of 5A molecular sieve and regeneration of coked 5A molecular sieve were studied by microstructure analysis.
为实现吸附-精馏耦合由重整抽余油生产高纯度正己烷工艺的长周期运行,采用微结构分析方法研究了烯烃在5A分子筛孔道中的结焦行为及失活分子筛的再生工艺。
2)  platformate raffinate
铂重整抽余油
3)  remaining fraction
抽余油
1.
Daqing crude oil was separated into tree components of asphaltene, polar fraction and remaining fraction with precipitation method and silica gel column.
用沉淀法和色谱分离法将大庆原油分离成沥青质、极性物和抽余油 3部分。
2.
Kelamayi crude oil was separated into asphaltene, polar fraction and remaining fraction by precipitation method and separation through silica gel column.
用沉淀法和色谱分离法将克拉玛依原油分离成沥青质、极性物和抽余油三组分。
4)  raffinate [英]['ræfineit]  [美]['ræfə,net]
抽余油
1.
Reaction of hydrogenated pyrolysis gasoline raffinate partly incorporated with isomerization feed stocks,was studied in an experimental unit,using commercial xylene isomerization catalyst and technology.
利用小型临氢装置对裂解加氢汽油抽余油掺兑二甲苯异构化原料的反应进行了研究,考察了正常异构化原料、配制模拟油和抽余油在二甲苯异构化催化剂上的反应性能,进行了工艺条件和稳定性实验,并对简化工艺进行模拟核算。
2.
Under the conditions of an extraction temperature of 70 ℃ and a VGO/NMP phase ratio of 2, the raffinate yield and de aromatics rate were all higher than 70%, and the BMCI value of the raffinate was lower than 16.
结果表明 ,N 甲基吡咯烷酮 (NMP)具有优异的脱芳烃和脱胶质性能 ,在 2 0 0t/a中试抽提装置上 ,温度 75℃、相比 (原料油与溶剂体积比 )为 2的条件下 ,试验所得抽余油的收率和脱芳烃率均大于 70 % ,BMCI值小于 16 ,经 785℃模拟蒸汽裂解试验 ,抽提改质油的乙烯收率和乙烯、丙烯及丁二烯总收率分别大于 2 7%和 5 0 % ,表明NMP溶剂抽提改质减压瓦斯油的工艺是一条生产蒸汽裂解原料的可行途
3.
The combined trapezoid spray trays(CTST)developed by Hebei University of Technology have been successfully used in the technical transform of the reformer raffinate fractionating column in Shijiazhuang Refinery.
采用河北工业大学开发的新型大通量高效塔板———立体传质塔板 (CTST) ,在石家庄炼油厂催化重整装置的芳烃抽余油分馏塔扩产技术改造中成功应用。
5)  raffinate oil
抽余油
6)  Aromatic raffinate
芳烃抽余油
补充资料:抽余油
      泛指工业上采用溶剂萃取方法得到的剩余物料。在石油炼制过程中,抽余油一般指富含芳烃的催化重整产物(重整汽油)经萃取(抽提)芳烃(见芳烃抽提)后剩余的馏分油,其主要成分为C6~C8的烷烃及一定量的环烷烃,是良好的石油化工原料,可用于烃类裂解制乙烯。
  

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