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作者:Rupesh Verma , Pyarimohan Dehury , Anand Bharti ...
来源:[J].Journal of Molecular Liquids(IF 1.684), 2018, Vol.265, pp.824-839
摘要:...864 g/cm 3 ) and oleyl alcohol (ρ = 0.849 g/cm 3 ). The ternary Liquid-Liquid Equilibrium (LLE) studies for mesitylene (1) + 1-butanol (2) + water (3) and oleyl alcohol (1) + 1-butanol (2) + water (3) were conducted to explain the effectiveness of the two solvents. A type-...
作者:Y. Pouilloux , A. Piccirilli , J. Barrault
来源:[J].Journal of Molecular Catalysis. A, Chemical(IF 3.187), 1996, Vol.108 (3), pp.161-166
摘要:Abstract(#br)The hydrogenation of methyl-9-octadecenoate (methyl oleate) into 9-octadecen-1-ol (oleyl alcohol) was carried out in the presence of RuSnB Al 2 O 3 catalysts at 8.0 MPa and 270°C. The selectivity to unsaturated alcohol (oleyl alcohol) was enhanced significan...
作者:Shaozhi Zhang , Xiaoyan Huang , Chunyun Qu ...
来源:[J].Biochemical Engineering Journal(IF 2.579), 2017, Vol.117, pp.112-120
摘要:Abstract(#br)Liquid–liquid extractions using the mixtures of aliphatic acids and oleyl alcohol as extractants are investigated to improve isopropanol and butanol (IB) production in fed-batch fermentation. Extractive fermentation with a mixture of tetradecanoic acid (30%) and oleyl alcohol...
作者:Mehmet Bilgin , Çiğdem Arısoy
来源:[J].Fluid Phase Equilibria(IF 2.379), 2006, Vol.250 (1), pp.59-63
摘要:Abstract(#br)(Liquid–liquid) equilibrium (LLE) data are investigated for mixtures of (water + propionic acid + oleyl alcohol) at 298.15, 308.15 and 318.15 K and atmospheric pressure. The solubility curves and the tie-line end compositions of liquid phases at equilibrium wer...
作者:Mehmet Bilgin
来源:[J].The Journal of Chemical Thermodynamics(IF 2.297), 2006, Vol.38 (12), pp.1634-1639
摘要:Abstract(#br)(Liquid + liquid) equilibrium (LLE) data for the ternary system of (water + butyric acid + oleyl alcohol) at T = (298.15, 308.15, and 318.15) K are reported. Complete phase diagrams were obtained by determining solubility and the tie-line data. The reliability of...
作者:María A. Sánchez , Vanina A. Mazzieri , Marcelo Oportus ...
来源:[J].Catalysis Today(IF 2.98), 2013, Vol.213, pp.81-86
摘要:Abstract(#br)The influence of Ge content on the activity and selectivity of Ru–Ge–B/Al 2 O 3 catalysts for the hydrogenation of methyl oleate to oleyl alcohol was studied. The results of catalyst characterization by TPR and XPS show that Ge is deposited on both the metal f...
作者:XiaoZhong Liu , Fanzhi Kong , Xiaolai Zheng ...
来源:[J].Catalysis Communications(IF 2.915), 2003, Vol.4 (3), pp.129-133
摘要:Abstract(#br)Water-soluble triaryl phosphine oxides bearing polyether moiety proved to be efficient ligand for rhodium catalyzed aqueous/organic two-phase hydroformylation of water-immiscible oleyl alcohol. Under the selected conditions, yield of aldehydes reached 83.3% with...
作者:Gholam Khayati , Hassan Pahlavanzadeh , Ebrahim Vasheghani-Farahani ...
来源:[J].The Journal of Chemical Thermodynamics(IF 2.297), 2008, Vol.41 (2), pp.150-154
摘要:Abstract(#br)(Liquid + liquid equilibrium) (LLE) data for ternary system: (water + 2,3-butanediol + oleyl alcohol) has been measured at T = (300.2, 307.2, and 314.2) K. Complete phase diagrams were obtained by determining solubility and tie-line data. Tie-line compositions wer...
作者:Marek Blahušiak , Ján Marták , Fernando Miranda ...
来源:[J].Chemical Papers, 2013, Vol.67 (12), pp.1560-1568
摘要:... Oleyl alcohol (OA) is frequently used as the solvent or diluent in the extraction of carboxylic acids. A disadvantage of OA is its relatively high viscosity of 28.32 mPa s at 25°C. This can be decreased by the application of a less viscous OA diluent, e.g. dodecane. The re...
作者:Y Pouilloux , F Autin , A Piccirilli ...
来源:[J].Applied Catalysis A, General(IF 3.41), 1998, Vol.169 (1), pp.65-75
摘要:Abstract(#br)The hydrogenation of methyl oleate into oleyl alcohol was studied in the presence of a CoSn catalyst at 270°C and 8.0 MPa. The selectivity of the CoSn catalyst to oleyl alcohol is comparable to that of the RuSn catalyst but the CoSn catalyst is less active. The...

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