Abstract:Ni‐Agx/SBA‐15 catalysts with different contents of the silver (Ag) promoter were prepared by the co‐impregnation method using the support of the mesoporous material SBA‐15. The Ni‐Agx/SBA‐15 catalysts were characterized by ICP‐OES, X‐ray diffraction (XRD), transmission electron microscope (TEM), and N2 adsorption–desorption isotherms. The activity of the catalysts on hydrogenation of soybean oil was evaluated. The results indicated that all the catalysts retained the hexagonally ordered structure of SBA‐15, th… Show more
“…It was necessary to control the formation of trans fatty acids and stearic acid as much as possible to increase the oleic acid content. Although the fatty acid composition of soybean oil and low-erucic rapeseed oil are different, the decrease in the reaction temperature led to a decrease in the trans fatty acid content 16 .…”
Section: Trans Fatty Acids and Oleic Acid Content Of Hydrogenated Oilsmentioning
confidence: 97%
“…In the application of silver-nickel catalysts, because the active metal nickel tends to cluster on the support during the preparation of the supported catalyst, silver is beneficial for the prevention of the metallic nickel cluster 15 . It was pointed out that in nickel-silver/SBA15 catalysts, an appropriate amount of silver increase the dispersion of metallic nickel 16 .The addition of an appropriate amount of silver in the nickel catalyst can also effectively inhibit the formation of trans fatty acids 17 . Ni-Ag catalyst was shown to exhibit a better selectivity for linoleic acid and lower isomer formation 18 .…”
Section: Introductionmentioning
confidence: 99%
“…acid: 52 , erucic acid: ≤ 5 ; ammonium formate solution prepared in the laboratory .2.2 Experimental methods2.2.1 Catalyst preparationNi-Ag 0.15 /SBA15 was prepared by the coimpregnation method with the mass fraction of 12 Ni metal and silver nitrate as the main catalyst16 . 2.2.2 Method for the preparation of CTH low-erucic-acid rapeseed oil The overall mechanism of catalytic transfer hydrogenation CTH using ammonium formate as the hydrogen donor can be expressed as22 :…”
The kinetics of CTH of low-erucic-acid rapeseed oil using ammonium formate as a hydrogen donor over a Ni-Ag0.15/SBA15 catalyst were studied. Then, a kinetic model for the hydrogenation of lowerucic-acid rapeseed oil was established, and it was found that the reaction rate constants of hydrogenations of 9c-18:1 and 12c-18:1 oleic acid were 0.1262 and 0.0148, and the catalytic selectivity of linoleic acid was 2.04. For the catalyst loading of 0.23%, the hydrogenation temperature was 80℃, the ammonium formate concentration was 0.32 mol/50 mL, and the low-erucic-acid rapeseed oil was hydrogenated in 90 min; it was also found that the iodine value of low-erucic-acid rapeseed oil was 80 g I 2 /100 g, the oleic acid content was 65%, and the trans fatty acids (TFAs) content was only 6.7%. Therefore, catalytic transfer hydrogenation (CTH) may be widely used in the modification of oils and fats.
“…It was necessary to control the formation of trans fatty acids and stearic acid as much as possible to increase the oleic acid content. Although the fatty acid composition of soybean oil and low-erucic rapeseed oil are different, the decrease in the reaction temperature led to a decrease in the trans fatty acid content 16 .…”
Section: Trans Fatty Acids and Oleic Acid Content Of Hydrogenated Oilsmentioning
confidence: 97%
“…In the application of silver-nickel catalysts, because the active metal nickel tends to cluster on the support during the preparation of the supported catalyst, silver is beneficial for the prevention of the metallic nickel cluster 15 . It was pointed out that in nickel-silver/SBA15 catalysts, an appropriate amount of silver increase the dispersion of metallic nickel 16 .The addition of an appropriate amount of silver in the nickel catalyst can also effectively inhibit the formation of trans fatty acids 17 . Ni-Ag catalyst was shown to exhibit a better selectivity for linoleic acid and lower isomer formation 18 .…”
Section: Introductionmentioning
confidence: 99%
“…acid: 52 , erucic acid: ≤ 5 ; ammonium formate solution prepared in the laboratory .2.2 Experimental methods2.2.1 Catalyst preparationNi-Ag 0.15 /SBA15 was prepared by the coimpregnation method with the mass fraction of 12 Ni metal and silver nitrate as the main catalyst16 . 2.2.2 Method for the preparation of CTH low-erucic-acid rapeseed oil The overall mechanism of catalytic transfer hydrogenation CTH using ammonium formate as the hydrogen donor can be expressed as22 :…”
The kinetics of CTH of low-erucic-acid rapeseed oil using ammonium formate as a hydrogen donor over a Ni-Ag0.15/SBA15 catalyst were studied. Then, a kinetic model for the hydrogenation of lowerucic-acid rapeseed oil was established, and it was found that the reaction rate constants of hydrogenations of 9c-18:1 and 12c-18:1 oleic acid were 0.1262 and 0.0148, and the catalytic selectivity of linoleic acid was 2.04. For the catalyst loading of 0.23%, the hydrogenation temperature was 80℃, the ammonium formate concentration was 0.32 mol/50 mL, and the low-erucic-acid rapeseed oil was hydrogenated in 90 min; it was also found that the iodine value of low-erucic-acid rapeseed oil was 80 g I 2 /100 g, the oleic acid content was 65%, and the trans fatty acids (TFAs) content was only 6.7%. Therefore, catalytic transfer hydrogenation (CTH) may be widely used in the modification of oils and fats.
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