馏分油

ICP/AES法测定焦化馏分油中的硅含量

The determination of silicon in the coking distillate by ICP / AES

C5馏分油作民用燃料的研究

Study on C_5 Distillate Oil Used as Domestic Fuel

C9馏分油加氢精制工艺研究

Process Study of C_9 Distillate Oil Hydrofining

以单质硫和FCC馏分油为原料合成有机硫化剂。

Polysulfides was synthesized using FCC gasoline and sulfur .

GC-MS在重质馏分油组成分析中的应用

The Application of GC - MS on Heavy Fraction Oil

氟离子CIMS法测定北海高酸馏分油中的羧酸

Determination of naphthenic acids in distillates of North Sea crude oil by fluoride ion CIMS

馏分油浆态床加氢处理研究：ⅡFCC柴油加氢工艺条件及动力学研究

A study on process for slurry-bed hydrotreating of distillate oil : ⅱ Processing conditions and kinetics analysis of FCC diesel oil

润滑油馏分油加助剂NMP溶剂精制

NMP Additive Assistant Refining Lubricated Fraction Oil

可同时生产高芳烃潜含量的重整原料和低硫中间馏分油，以及作乙烯原料的优质尾油；RMC中压加氢裂化技术的整体水平与国外同类工业化技术的水平相当。

The said technology can produce high aromatics potential reforming feedstock and low sulfur middle distillates simultaneously .

高含蜡减压馏分油（VGO）直接溶剂脱油

Direct solvent deoiling of highly waxy VGO

因此，馏分油的深度加氢脱硫（HDS）成为一个非常具有经济和现实意义的课题。

Therefore , the deep hydrodesulfurization ( HDS ) of petroleum fractions has become an issue of high economic value and realization values problem .

研究了以大庆馏分油为原料，以发烟硫酸为磺化剂制备天然石油磺酸盐（NPS）的工艺。

The preparation process of natural petroleum sulfonates ( NPS ) was studied making of Daqing distillate oil as feed stock and oleum as sulfonated agent .

新一代馏分油加氢精制催化剂RN-10的研制与开发

A new generation catalyst RN 10 for distillate hydrotreating

利用芳烃抽提、分子筛脱蜡等方法改进裂解原料，并对F-T合成馏分油的裂解性能进行了初步研究。

Steam cracking performance of aromatic extracted naphtha , 5A molecular sieve dewaxing treated naphtha and F-T synthesis oil had been studied .

馏分油的酸值（KOH）由0.57mg/g降至0.0481mg/g，馏分油回收率为99.3%。

The acid value ( KOH ) of oil were reduced from 0.57 mg / g to 0.0481 mg / g and the recovery of oil reach 99.3 % .

该法总Cl量的测量范围为0.50μg/g～0.05g/g，对于300℃以下馏分油中总Cl量的测定准确度高，重复性好，用时省。

The measuring range of total Cl ~ - is 0.50 ppm ~ 0.05 g / g. For the oil fractions lower than 300 ℃, the measurement is high in accuracy and good in repeatability .

推荐使用修正的对比态Antoine方程进行低压体系馏分油的汽液平衡计算。

For petroleum fractions , VLE system at low pressure and the modified reduced Antoine equation are recommended for the calculation of phase equilibrium .

减三线馏分油粘度指数很低，加氢处理后其粘度指数达40～50，可用于调制CA级柴油机油。

The viscosity index of distillate oil from the 3rd side line of vacuum tower is very low . After being treated by hydrogenation , the viscosity index reaches 40 ~ 50 , and can be used for modulating diesel oil of grade CA.

多产中间馏分油的渣油裂化催化剂MLC-500的开发

Development of a residual oil cracking catalyst for LCO

FC-16多产中间馏分油的灵活型加氢裂化催化剂的工业应用

Commercial Application of the FC-16 Flexible Hydrocracking Catalyst for Increasing Middle Distillates Output

研究表明，NMP溶剂精制馏分油无论剂油比还是抽提温度均远远低于糠醛，说明NMP用于润滑油精制具有良好的溶解能力和选择性。

5 , the ratio of either solvent to oil or extraction temperature , are lower than furfural 's , indicating that the NMP has good dissolving ability and selectivity in refining lube stock .

在选定的反应条件下，2g大庆减压馏分油，加入15mL异丙醇，3g尿素，正构烷烃的平均收率为42.51%。

Under the selected reaction conditions , 15 mL of isopropanol and 3 g of urea were added to 2 g of Daqing VGO , an average normal paraffin yield of 42 . 51 % was obtained .

将胜利减压渣油中的胶质与饱和分、芳香分以及减压馏分油加氢裂化（SSOT）尾油中的石蜡进行调合。

The resins of Shengli vacuum residue were blent with saturates , aromatics from Shengli vacuum residue and paraffin from SSOT hydrogenation residue .

结果表明，FC-14催化剂初期活性、中间馏分油选择性高，装置产品质量优良。

The results showed that FC - 14 catalyst had good activity and high selectivity of jet fuel and diesel oil . High quality of products were gained .

FDS4催化剂是抚顺石油化工研究院（FRIPP）针对炼油企业加工进口高硫原油馏分油而研制成功的专用加氢脱硫催化剂。

Hydrodesulfurization Catalyst FDS-4 , developed by Fushun Research Institute of Petroleum and Petrochemicals ( FRIPP ), is especially designed to processing the distillates of imported high sulfur-content crude oil .

讨论了利用SRK状态方程计算相平衡的连续热力学步骤，并对原油和馏分油进行了闪蒸及泡点计算。

The way for calculation phase equilibrium using SRK equation of state based on continuous thermodynamics is also discussed . Flash distillation of a real crude system and the bubble point for a dewaxing oil fraction are illustrated in the calculation .

以C9馏分油为原料，开发研制出的两段串联加氢精制工艺，可用于生产油漆工业用溶剂油，使C9资源得以更合理的利用。

Two sections in series of hydrofining process was researched and developed with C 9 distillate oil as raw material , which can be used to produce solvent oil utilized for painting industry , and make C 9 resource utilization more rational .

FC-28和FC-14是采用浸渍法制备的分子筛型催化剂，FC-14是最大量生产柴油的催化剂，FC-28是FRIPP最新开发的高活性及高中间馏分油选择性催化剂。

FC-28 and FC-14 are molecular sieve catalysts prepared by impregnation . FC-14 is used for maximizing diesel production and FC-28 is a newly developed catalyst with high activity and middle distillate selectivity .

以水溶性双金属钼-镍催化剂处理常压渣油，500h连续运转得到的馏分油（低于538℃）收率超过70%，进行尾油循环后馏分油（低于538℃）收率超过80%。

Using water-soluble Mo-Ni bimetallic catalyst to treat atmospheric residuum , the total yield of the distillates ( below 538 ℃) was over 70 % in the 500 h continuous running and the yield of the distillates after tail oil circulation was over 80 % .

用落球式粘度计首次系统测定新疆九区稠油7个馏分油在温度303.15～393.15K和压力0.1～12MPa范围内的动力粘度，共231个数据点。

The dynamic viscosities of 231 data points for 7 petroleum distillates of Xinjiang crude were measured under the pressure from 0.1 to 12.3 MPa in a temperature range of 303.15 to 393.15 K using a falling ball viscometer .