Abstract:A glut of glycerol has formed from the increased production of biodiesel, with the potential to integrate the supply chain by using glycerol additives to improve biodiesel properties. Acetylated acetals show interesting cold flow and viscosity effects. Herein, a solventless heterogeneously catalyzed process for the acetylation of both solketal and glycerol formal to new products is demonstrated. The process is optimized by studying the effect of acetylating reagent (acetic acid and acetic anhydride), reagent m… Show more
“…They are shown to have good solubility and stability towards oxidation but hydrolyze in the presence of acid [4] . This class of compound and its derivatives also have shown potential in different applications including as surfactant, [5] fuel additives [6–8] and anti‐freezing agent [9,10] . Dodson et al.…”
Section: Introductionmentioning
confidence: 99%
“…[3] They are shown to have good solubility and stability towards oxidation but hydrolyze in the presence of acid. [4] This class of compound and its derivatives also have shown potential in different applications including as surfactant, [5] fuel additives [6][7][8] and anti-freezing agent. [9,10] Dodson et al (2014b) showed the anti-oxidant activity exhibited by aromatic glycerol acetal indicated wide range of potential of this class of compound in industrial application including biodiesel industry.…”
Acetalization of glycerol with acetone (1 : 5) at 60 °C catalyzed by A‐46 (10 wt %) under nitrogen (N2) afforded 63 % solketal 1 a in just 15 min. Subsequently, acetalization of glycerol and bio‐based aldehydes i. e. acetaldehyde, isobutyraldehyde, n‐heptaldehyde, p‐anisaldehyde and benzaldehyde were investigated under optimized reaction conditions. The conversion and selectivity of this reaction was found to be affected by structure of aldehydes employed. Excellent conversion of 97 and 99 % were obtained using acetaldehyde and isobutyraldehyde, respectively while longer chain or aromatic aldehyde gave poor conversion between 17 and 36 %. Aldehyde with branching or aromatic ring gave better selectivity towards 6‐membered ring acetal b at the expense of conversion: p‐anisaldehyde > benzaldehyde>isobutyraldehyde>acetaldehyde>n‐heptaldehyde. Conversely, organic solvent gave adverse effects to both conversion and selectivity towards b. Optimized acetalization of glycerol/benzaldehyde was also studied. A‐46 has shown excellent stability and reactivity with no significant loss of catalytic activity in 10 subsequent runs.
“…They are shown to have good solubility and stability towards oxidation but hydrolyze in the presence of acid [4] . This class of compound and its derivatives also have shown potential in different applications including as surfactant, [5] fuel additives [6–8] and anti‐freezing agent [9,10] . Dodson et al.…”
Section: Introductionmentioning
confidence: 99%
“…[3] They are shown to have good solubility and stability towards oxidation but hydrolyze in the presence of acid. [4] This class of compound and its derivatives also have shown potential in different applications including as surfactant, [5] fuel additives [6][7][8] and anti-freezing agent. [9,10] Dodson et al (2014b) showed the anti-oxidant activity exhibited by aromatic glycerol acetal indicated wide range of potential of this class of compound in industrial application including biodiesel industry.…”
Acetalization of glycerol with acetone (1 : 5) at 60 °C catalyzed by A‐46 (10 wt %) under nitrogen (N2) afforded 63 % solketal 1 a in just 15 min. Subsequently, acetalization of glycerol and bio‐based aldehydes i. e. acetaldehyde, isobutyraldehyde, n‐heptaldehyde, p‐anisaldehyde and benzaldehyde were investigated under optimized reaction conditions. The conversion and selectivity of this reaction was found to be affected by structure of aldehydes employed. Excellent conversion of 97 and 99 % were obtained using acetaldehyde and isobutyraldehyde, respectively while longer chain or aromatic aldehyde gave poor conversion between 17 and 36 %. Aldehyde with branching or aromatic ring gave better selectivity towards 6‐membered ring acetal b at the expense of conversion: p‐anisaldehyde > benzaldehyde>isobutyraldehyde>acetaldehyde>n‐heptaldehyde. Conversely, organic solvent gave adverse effects to both conversion and selectivity towards b. Optimized acetalization of glycerol/benzaldehyde was also studied. A‐46 has shown excellent stability and reactivity with no significant loss of catalytic activity in 10 subsequent runs.
“…Various studies have been carried out on transformation of glycerol into valuable products, such as glycerol carbonate [16][17][18] and solketal [19][20][21][22]. Glycerol carbonate has applications as a curing agent in cement and concrete building, solvent for active medical ingredients in various pharmaceutical formulations, an electrolyte in lithium and lithium-ion batteries, and in production of various polymers and plastics [23,24].…”
Methyl esters of fatty acids are widely used as biodiesel, a sustainable replacement for petro-diesel.The conventional biodiesel process produces crude glycerol, which constitutes about 10wt% of the total products. This has led to a surplus of crude glycerol due to global increase in biodiesel use, necessitating increased research into sustainable processes that could convert the crude glycerol into higher value-added products. This study investigates biodiesel processes for continuous transesterification of triglycerides to methyl esters, coupled to conversion of the glycerol by-product into solketal, a value-added product, via reaction with acetone in situ. The study was carried out using one-stage and two-stage catalytic transesterification of triacetin and methanol in mesoscale oscillatory baffled reactors (meso-OBRs). The two-stage process involved two meso-OBRs in series packed with Amberlyst TM resin catalysts: a basic Amberlyst TM A26-OH in the first stage to catalyse transesterfication of triacetin with methanol, and an acidic Amberlyst TM 70-SO3H in the second stage to catalyse the coupling of glycerol and acetone to form solketal. One-stage triacetin transesterification and glycerol coupling with acetone was carried out in a meso-OBR packed with the acidic Amberlyst TM 70-SO3H resin. In the two-stage process, the triacetin was converted to 99.1±2.0% methyl acetate and 98.0±1.3% glycerol after 25min residence time in the first reactor and the glycerol was reacted with acetone in the second reactor to achieve 76.5±2.8% solketal conversions after 35min.The single-stage process achieved 48.5±2.7% solketal conversion after 30min. The meso-OBR was operated continuously to achieve high quality steady states and consistent triacetin conversions. The triglyceride transesterification with reactive coupling of glycerol with acetone produces less crude glycerol by-product. This process strategy could be optimised for future biodiesel production.
“…[20][21][22][23][24][25] Glycerol esters, ketals and ethers are commonly used as solvents and additives in cleaning, cosmetic, food and pharmaceutical industry. [26][27][28][29][30] Glycerol ethers stand out among other glycerol derivatives by their relative chemical inertness, which make them very suitable as solvents. Apart from the synthesis of glycerol tertbutyl ethers from glycerol and isobutene, deeply studied due to their use as biofuel additives, 31 the synthesis of alkyl glyceryl ethers from glycerol has been investigated in order to obtain a large class of compounds with tunable properties depending on the number and nature of the alkyl chains.…”
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