Abstract:Untreated waste cooking oil (WCO) with significant levels of water and fatty acids (FFAs) was deoxygenated over Co3O4–La2O3/ACnano catalysts under an inert flow of N2 in a micro-batch closed system for the production of green diesel.
“…From XRD analysis (spectra not shown), Co 3 O 4 and Fe 2 O 3 were detected as the active phases on activated carbon. Similar observation was also reported in [12].…”
Section: Results and Discussion 31 Characterization Of Catalystsupporting
confidence: 91%
“…6 shows the carbon number selectivity for C 5 -C 20 hydrocarbons content in liquid product obtained by using the Fe/AC catalysts with different Fe loading. Liquid product exhibited more selectivity for n-(C 15 + C 17 ) hydrocarbons and it could be deduced as the consequence of deoxygenation of palmitic acid (C 16 ) and oleic acid (C 18 ) in WCO via decarboxylation and/or decarbonylation [12]. The highest n-(C 15 + C 17 ) hydrocarbons selectivity (52 %) was detected for 7.5-Fe/AC which was also in line with the highest liquid yield obtained.…”
Section: Effect Of Metal Loading On Ac 321 Fe Loadingsupporting
confidence: 66%
“…In catalysis, metal oxides provide acid and/or basic sites for the reactions and the active metal phase is anchored to highly porous support with large surface area [11]. Cobalt oxide promotes decarboxylation and decarbonylation to produce paraffinic and olefinic hydrocarbons, respectively [12]. Cobalt supported on activated carbon produced 91 % of C 8 -C 20 hydrocarbons with 72 % of n-(C 15 + C 17 ) selectivity in deoxygenation of palm fatty acid distillate via high decarboxylation and/or decarbonylation [13] [12].…”
This work studied the catalyst activity of activated carbon (AC) supported Co, Fe and Co-Fe oxides in catalytic cracking of waste cooking oil. Reactions were carried out in a fixed bed reactor at 450 °C with WHSV 9 hr–1. Single metal Co/AC and Fe/AC catalysts with different metal loading (2.5–15 wt.%) and bimetal xCo-yFe/AC (x, y = 2.5 to 12.5 wt.%; x + y =15 wt.%) catalysts were investigated. Co/AC and Fe/AC catalysts both contributed to significant liquid yield with high selectivity towards C15 and C17 hydrocarbons. Fe/AC catalysts gave high C5 – C20 hydrocarbon yield whereas Co/AC attained more palmitic (C16) and oleic (C18) acid conversion. Synergistic effect in two metals Co-Fe/AC catalysts had further improved the liquid hydrocarbon yield (up to ~93 %) and fatty acid conversion (up to 94 %). The best catalyst, 10Co-5Fe/AC had been further tested under the effect of reaction temperature, feed flow rate (WHSV) and deactivation for its catalytic performance.
“…From XRD analysis (spectra not shown), Co 3 O 4 and Fe 2 O 3 were detected as the active phases on activated carbon. Similar observation was also reported in [12].…”
Section: Results and Discussion 31 Characterization Of Catalystsupporting
confidence: 91%
“…6 shows the carbon number selectivity for C 5 -C 20 hydrocarbons content in liquid product obtained by using the Fe/AC catalysts with different Fe loading. Liquid product exhibited more selectivity for n-(C 15 + C 17 ) hydrocarbons and it could be deduced as the consequence of deoxygenation of palmitic acid (C 16 ) and oleic acid (C 18 ) in WCO via decarboxylation and/or decarbonylation [12]. The highest n-(C 15 + C 17 ) hydrocarbons selectivity (52 %) was detected for 7.5-Fe/AC which was also in line with the highest liquid yield obtained.…”
Section: Effect Of Metal Loading On Ac 321 Fe Loadingsupporting
confidence: 66%
“…In catalysis, metal oxides provide acid and/or basic sites for the reactions and the active metal phase is anchored to highly porous support with large surface area [11]. Cobalt oxide promotes decarboxylation and decarbonylation to produce paraffinic and olefinic hydrocarbons, respectively [12]. Cobalt supported on activated carbon produced 91 % of C 8 -C 20 hydrocarbons with 72 % of n-(C 15 + C 17 ) selectivity in deoxygenation of palm fatty acid distillate via high decarboxylation and/or decarbonylation [13] [12].…”
This work studied the catalyst activity of activated carbon (AC) supported Co, Fe and Co-Fe oxides in catalytic cracking of waste cooking oil. Reactions were carried out in a fixed bed reactor at 450 °C with WHSV 9 hr–1. Single metal Co/AC and Fe/AC catalysts with different metal loading (2.5–15 wt.%) and bimetal xCo-yFe/AC (x, y = 2.5 to 12.5 wt.%; x + y =15 wt.%) catalysts were investigated. Co/AC and Fe/AC catalysts both contributed to significant liquid yield with high selectivity towards C15 and C17 hydrocarbons. Fe/AC catalysts gave high C5 – C20 hydrocarbon yield whereas Co/AC attained more palmitic (C16) and oleic (C18) acid conversion. Synergistic effect in two metals Co-Fe/AC catalysts had further improved the liquid hydrocarbon yield (up to ~93 %) and fatty acid conversion (up to 94 %). The best catalyst, 10Co-5Fe/AC had been further tested under the effect of reaction temperature, feed flow rate (WHSV) and deactivation for its catalytic performance.
“…It was found that the primary absorption bands of WCO were at 1120 cm À1 , 1740 cm À1 , and 2922 cm À1 , and these were attributed to the carbonyl group (C-O-C), the ester group (C]O), and the stretching absorption of the C-H bond, respectively. 67 It also showed that the deoxygenated liquid products rendered a carboxylic acid (-COOH) group peak at 1711 cm À1 , indicating that the deoxygenation of WCO was initiated by breaking the ester bond of triglycerides. The successful progression of deoxygenation activity was also in accordance with the disappearance of the carbonyl group (C-O-C) absorption band at 1120 cm À1 .…”
In this work, the catalytic deoxygenation of waste cooking oil (WCO) over acid–base bifunctional catalysts (NiLa, NiCe, NiFe, NiMn, NiZn, and NiW) supported on activated carbon (AC) was investigated.
“…The authors investigated the catalytic conversion reaction pathways that were used in the production of biodiesel fuels through two specific approaches containing experimental approach and theoretical approach. Finally, the authors described the potential of various thermocatalytic pathways that could be effectively used in the production process of producing biodiesel fuels through computational modeling techniques that were directed to elucidate the major information associated with the optimization of the conversion process [42,43]. The authors described the pathways that were used for the production of biodiesel fuels through the utilization of microalgae in association with carbohydrates, lipids and proteins as shown in Fig.…”
Section: Recent Progress Of Do Of Realistic Green Oil Worldmentioning
The critical problem arises from the fossil fuels which has stimulated recent interests in alternative sources for petroleum-based fuel. An alternative fuel should be technically feasible, readily available, environment acceptable and techno-economically competitive. The new generation of renewable fuel is known as green diesel. Green diesel is composed of long chain hydrocarbons that can be prepared from DO (deoxygenation) of palm oil. The feedstock used for the production of green diesel mainly comes from edible vegetable oil which is highly available in most of the countries around the world. However, the compotation between food and fuel economies towards the same oil resources may bring global imbalance to the food supply and demand market. The focus on this research is to produce green diesel using edible feedstock via heterogeneous catalysed DO reaction.
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