Next Article in Journal
Inhibitory Effect of Rosa rugosa Tea Extract on the Formation of Heterocyclic Amines in Meat Patties at Different Temperatures
Next Article in Special Issue
Bio-Based Solvents for Green Extraction of Lipids from Oleaginous Yeast Biomass for Sustainable Aviation Biofuel
Previous Article in Journal
Synthesis and Characterization of Novel Polythiophenes Containing Pyrene Chromophores: Thermal, Optical and Electrochemical Properties
Previous Article in Special Issue
Comparative Study of Essential Oils Extracted from Egyptian Basil Leaves (Ocimum basilicum L.) Using Hydro-Distillation and Solvent-Free Microwave Extraction
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

Synthesis of the Fatty Esters of Solketal and Glycerol-Formal: Biobased Specialty Chemicals

Dipartimento di Scienze Molecolari e Nanosistemi, Centro per le Tecnologie Chimiche Sostenibili, Università Ca’ Foscari Venezia, Via Torino 155, Venezia Mestre 30172, Italy
*
Author to whom correspondence should be addressed.
Molecules 2016, 21(2), 170; https://doi.org/10.3390/molecules21020170
Submission received: 22 December 2015 / Revised: 22 January 2016 / Accepted: 25 January 2016 / Published: 30 January 2016

Abstract

:
The caprylic, lauric, palmitic and stearic esters of solketal and glycerol formal were synthesized with high selectivity and in good yields by a solvent-free acid catalyzed procedure. No acetal hydrolysis was observed, notwithstanding the acidic reaction conditions.

Graphical Abstract

1. Introduction

The impact on the environment of fossil-based fuels and chemicals is a matter of widespread concern. It is therefore desirable—if not unavoidable—to investigate new feedstocks, products and processes with lower environmental impact and that are sustainable in the longer term [1]. For example, in the recent past the growing production and use of carbon-neutral biofuels such as biodiesel has become an option and a valuable addition to conventional fuels [2], as justified by two basic needs of the economic model in the industrialised countries. First, the need to reduce the dependence on imported oil both in terms of price stability as well as in terms of political stability. Second, the need to reduce emissions associated with fossil-based diesel combustion in engines, with special emphasis in CO, CO2, SOX, C and particulate matter, which decrease using biodiesel [3]. Currently, most biodiesel derives from the transesterification reaction between an oil and an alcohol such as methanol. This reaction provides two main products: the methyl esters of the fatty acids, i.e., biodiesel itself, and an important by-product: glycerol. Crude glycerol is nowadays the most abundant renewable chemical feedstock in the world [4] and as such, it is a promising starting material to produce higher value-added chemicals. In countries with high volumes of biodiesel production, this by-product may even represent a disposal problem [5]. Prior to chemical upgrading, crude glycerol normally requires a first purification step [6]. The subsequent steps, e.g., upgrading to biofuels and fuel components, are widely investigated processes [7]. For example, recent publications have described different synthetic pathways to obtain a variety of glycerol derivatives by microbial fermentation [8], ketalization [9], acetylation [10], etherification [11], transesterification [12], catalytic decomposition [13], or combinations thereof [14]. In particular, acid-catalyzed condensation of glycerol with acetone [15,16], acetaldehyde or formaldehyde (or dimethoxymethane) yields the products solketal®, glycerol acetal and glycerol formal (GlyF), which are interesting because they can be used directly as fuel additives [17,18] that reduce soot formation [19,20] or as reagents for further production of biofuel components [21]. GlyF—the acetal of glycerol with formaldehyde—exists as a mixture of two isomers (5- and 6-membered rings in a 2:3 molar ratio, respectively), while solketal—the ketal of glycerol with acetone—is present as a single five-membered ring product [22,23,24,25]. Ketals are considered a subclass of acetals and we will therefore refer to both as acetals. Both these acetals are currently used mainly as solvents for injectable pharmaceutical preparations, paints and waterbased inks, and for the preparation of additives for biodiesel formulations [10,25,26,27,28,29,30,31,32,33]. However, GlyF and solketal are also valuable glycerol synthons due to the presence of a free hydroxyl functionality available for esterification and etherification reactions.
Recently, a combined transesterification-acetalization approach towards the synthesis of a class of potential fuel additives based on crude glycerol and waste oils was described [7]. Specifically, a process was proposed whereby starting from a feed constituted by waste triglycerides, glycerol and dimethoxymethane as acetalization reagent, the glycerol-formal esters of the fatty acids were obtained, either in pure form or as a blend with the methyl esters of the fatty acids (biodiesel) (Scheme 1). The physical properties of the pure glycerol-formal esters of the fatty acids or of the blend containing the methyl esters were analyzed as diesel additives. These compounds have higher lubricity and higher cetane numbers compared to pure biodiesel. Nonetheless, the results indicated that this biofuel or its blends with diesel fuels require additional studies.
Scheme 1. Process for the synthesis of the fatty acid esters of glycerol-formal [7].
Scheme 1. Process for the synthesis of the fatty acid esters of glycerol-formal [7].
Molecules 21 00170 g002
The work described in the present paper originates from the idea of combining glycerol with free fatty acids (FFAs) for the synthesis of new totally biobased chemicals. FFAs are established platform chemicals derived from triglycerides by saponification and as such represent oleochemicals of renewable origin obtainable from biorefinery process streams. In fact, soaps were the predominant products obtained from vegetable oils before the advent of biodiesel. Several FFAs are still valuable oleochemicals used for a variety of applications [34], implying that the technologies for their production are well established and that the renewed large availability of vegetable oils may provide a driver for their use as building blocks for new bio-based chemicals. In particular, we here describe the direct acid-catalyzed synthesis and characterization of fatty acids solketal esters (FASEs) and fatty acid glycerol formal esters (FAGEs).

2. Results and Discussion

The target molecules were synthesized as shown in Equations (1) and (2), by acid catalyzed esterification of four different FFAs: caprylic (CH3(CH2)6COOH, C8:0), lauric (CH3(CH2)10COOH, C12:0), palmitic (CH3(CH2)14COOH, C16:0) and stearic (CH3(CH2)16COOH, C18:0) with the glycerol acetals solketal and GlyF. Glycerol was incorporated in the products in the form of its acetals—solketal and glycerol formal (GlyF)—two compounds that are already used as constituents of additives for biodiesel formulations [26,27,28,29,30,31]. Both possess one free hydroxyl group available for functionalization. Generally, one of the main issues associated with using these acetals is their reported lack of stability under acidic conditions [35]. Here we demonstrate that it is possible to carry out the esterification of solketal and GlyF with free fatty acids under acid catalysis with no concurrent acetal ring-opening, under mild operative conditions and in the presence of low concentrations of p-toleuensulfonic acid (PTSA).
A preliminary screening of catalyst type (H2SO4 vs. PTSA) and its concentration (5, 10%), of the effect of added solvents (acetone), of reaction temperature (20, 30, 40, 60 °C), of the molar amount of solketal with respect to dodecanoic acid (1.2, 1.5, 2.0 molar equivalents) and of time was carried out. This investigation of the model reaction between solketal and dodecanoic acid allowed to determine the best operative conditions. We initially established that good yields in reasonable times could be achieved with 5% PTSA, without added solvents at 60 °C. Next, we investigated the reaction progress as a function of time and of the molar amount of solketal respect to the FFA (Figure 1). Based on the trends of the figure, we chose for all further reactions a molar ratio solketal:FFA = 1.5 as this allowed to reach > 90% yield of the desired product in 4 h. From Figure 1 it is evident that a molar ratio = 1.2 is insufficient, while 2.0 causes only a 2% increase in yield over the same time, that we deemed inconsequential. In summary for the remainder of the study we used the following reaction conditions: T = 60 °C, time = 4 h, 2.0 g FFA, 1.5 molar equivalents of solketal or GlyF and 5% w/w of PTSA with respect to the FFA.
Figure 1. Time-dependent formation of (2,2-dimethyl-1,3-dioxolan-4-yl)methyl dodecanoate (2) at T = 60 °C in the presence of 5% PTSA with different solketal-dodecanoic acid molar ratios.
Figure 1. Time-dependent formation of (2,2-dimethyl-1,3-dioxolan-4-yl)methyl dodecanoate (2) at T = 60 °C in the presence of 5% PTSA with different solketal-dodecanoic acid molar ratios.
Molecules 21 00170 g001

2.1 Synthesis of the Fatty Acid Solketal Esters (FASEs)

Four different free fatty acids (RCH2CO2H, R = C6H13, C8:0; C10H21, C12:0; C14H29, C16:0; C16H33, C18:0) were reacted with 1.5 molar equivalents of solketal in the presence of 5 wt % of PTSA at 60 °C and without added solvents (Equation (1)).
Molecules 21 00170 i001
After 4 h, complete conversion of the FFA was observed by GC analysis. The results are summarized in Table 1: the reactions were 100% selective towards the formation of the fatty acid solketal esters (FASEs) 14 that were purified by FCC and obtained with high yields (80%–99%) and high purity. The products were characterized by IR, GC/MS and 1H-, 13C-NMR spectroscopy and by thermal analysis (DSC).
It is significant that the reaction could be conducted in the absence of added solvents, i.e. using just 1.5 molar equivalents of solketal itself as the reaction medium. This feature is desirable in view of developing more efficient and less waste-generating processes. No other products such as mono-glycerides deriving from ring opening were detected by GC-MS analysis of the crude reaction mixture and in the NMR spectrum of the isolated product, thus ensuring that no acetal ring-opening occurred, notwithstanding the acidic conditions determined by the PTSA catalyst as well as by the FFA itself.
Table 1. Reactions between solketal and FFAs a.
Table 1. Reactions between solketal and FFAs a.
FFAmol × 10−3Solketal b (mol × 10−3)PTSA c (g)ProductIsolated Yield (%)Purity (% GC)Melting Point (°C)
C8:013.8020.70.1192> 99liquid
C12:09.9815.00.12809740–48
C16:07.7911.70.13> 999255
C18:07.0310.50.1487>9954
a Conditions: T = 60 °C, time = 4 h, 2.0 g FFA; b solketal 1.5 mol eq with respect to FFA; c p-toluensulfonic acid: 5% w/w of FFA.
DSC scans of compounds 24i.e., the solid solketal esters of the fatty acids—were acquired in order to determine their melting points (see the supplementary materials). Two consecutive cooling and heating cycles were completed for each compound in order to exclude decomposition and to ensure reproducibility. Interestingly, the C16- and C18-solketal analogs 3 and 4 each showed two thermal transitions upon heating. Namely, (2,2-dimethyl-1,3-dioxolan-4-yl)methyl palmitate (3) showed a first endothermic peak at 30 °C followed by melting at 55 °C (Figure S12); while (2,2-dimethyl-1,3-dioxolan-4-yl)methyl stearate (4) showed a first endothermic peak at 39 °C followed by melting at 54 °C (Figure S16). This behavior indicated that compounds 3 and 4 were thermotropic and likely possessed a liquid-crystal-like mesophase in the interval between the two endothermic transitions. Given the amphiphilic structure of these molecules our hypothesis of liquid-crystalline behavior is supported by analogous thermotropic liquid crystalline behavior of a similar dodecyloxy-substituted polyol [36]. Specifically, 1-O-dodecylpropanetriol was shown to have a smectic phase in the temperature interval 32–48 °C, very similar to the intervals observed in our case for 3 and 4. Additional support for the liquid crystal behavior came also by the evidence that analogous glycol-glycerol-lipid compounds also showed comparable mesogenic properties [37]. Unlike 3 and 4, upon heating, the C12 fatty acid derivative (2,2-dimethyl-1,3-dioxolan-4-yl)methyl dodecanoate (2) showed only one broad transition around its melting point between 40 and 48 °C (Figure S8). The apparent reason why compound 2 did not show two endothermic transitions as did 3 and 4 may possibly be due to its narrow liquid crystalline interval and to the limited resolution of the DSC trace of Figure S8.

2.2 Synthesis of the Fatty Acid Glycerol Formal Esters (FAGEs)

The same four different free fatty acids as above were reacted with 1.5 molar equivalents of GlyF under the same operative conditions (Equation (2)).
Molecules 21 00170 i002
The results are summarized in Table 2: after 4 h, complete conversion of the FFA was observed by GC analysis and the reactions were 100% selective towards the formation of the fatty acid GlyF esters (FAGEs) 58 that were purified by FCC and obtained with high yields (72%–97%) and high purity. Not even traces of the ring-opening products derived from deacetalization were observed. The products were characterized by IR, GC/MS and 1H-, 13C-NMR spectroscopy and by thermal analysis (DSC).
The DSC traces of compounds 68, i.e., the solid GlyF esters of the fatty acids, all showed one single endothermal peak in correspondence with their liquid to solid transition. Unlike the corresponding solketal derivatives 3 and 4 that showed mesogenic behavior, the single liquid-solid transition of the GlyF derivatives 68 was ascribed to impaired packing of these compounds due to their existence as a mixture of the five- and six-membered acetals rings.
Table 2. Reaction between glycerol formal and the FFAs a.
Table 2. Reaction between glycerol formal and the FFAs a.
FFAmol × 10−3GlyF b (mol × 10−3)PTSAc (g)ProductIsolated Yield (%)Purity (% GC)Melting Point (°C)
C8:013.8020.70.157286liquid
C12:09.9815.00.16917635–38
C16:07.7911.70.17979751–54
C18:07.0310.50.1897> 9966–70
a Conditions: T = 60 °C, time = 4 h, 2.0 g FFA; b GlyF 1.5 mol eq with respect to FFA; c p-toluensulfonic. acid: 5% w/w of FFA.

3. Experimental Section

3.1 Materials and Methods

All reagents and analytical grade solvents are commercially available and were used as received. Solketal ((±)-2,2-dimethyl-1,3-dioxolane-4-methanol, (±)-2,2-dimethyl-4-hydroxymethyl-1,3-dioxolane, 1,2-isopropylidene-rac-glycerol); glycerol formal (4-hydroxymethyl-1,3-dioxolane); p-toluenesulfonic acid monohydrate (ACS reagent, ≥98.5); caprylic acid (octanoic acid, C8:0); lauric acid (dodecanoic acid C12:0); palmitic acid (hexadecanoic acid C16:0); stearic acid (octadecanoic acid C18:0) were purchased from Sigma-Aldrich (Italy). Here we describe the general synthetic procedure used for the synthesis of 2,2-dimethyl-1,3-dioxolan-4-yl)methyl dodecanoate as an example of fatty acid solketal esters (FASE) and of 1,3-dioxolan-4-yl)methyl dodecanoate as an example of fatty acid glycerol formal esters (FAGE). All experimental and characterization details of the other products can be found in the Supplementary Materials.

3.2 Characterization

All the 1H- and 13C-NMR spectra were collected at 25 °C on a Unity spectrometer operating at the frequency of 400 MHz for 1H and at 100 MHz for 13C (Varian, Palo Alto, CA, USA). Chemical shifts (δ) are reported in ppm relative to residual solvent signals for 1H- and 13C-NMR (1H-NMR: 7.26 ppm for CDCl3; 13C-NMR: 77.0 ppm for CDCl3). MS spectra were acquired with an Agilent GC 6890 gas chromatograph coupled with a MS 5975 mass spectrometer (Agilent, Cernusco sul Naviglio, Italy). IR spectra were measured using a Spectrum One FT-IR Spectrometer from Perkin Elmer (Milano, Italy); FR-DTGS Detector 7800–350 cm−1 with beamsplitter. Calorimetric measurements were performed on a DSC 92 apparatus (Setaram Abbiategrasso, Italy): approximately 100 mg of product was placed in an aluminium crucible. An empty crucible was placed in the reference cell. The temperature scanning rate was 2 °C/min.

3.3 General Procedure for Synthesis of Fatty Acid Solketal Esters (FASEs)

The free fatty acid (2.0 g), solketal (1.5 molar equivalent respect to the free fatty acid) and p-toluenesulfonic acid (5% w/w respect of the weight of the free fatty acid) were charged into a conventional round bottom flask with a magnetic stirrer. The mixture was heated at 60 °C and stirred vigorously for 4 h. The reaction was quenched by neutralizing the acid catalyst with a saturated solution of sodium carbonate then filtered. The liquid phase was collected in a separatory funnel and partitioned between chloroform and water (3 × 20 mL). The organic layer was dried over sodium sulfate, filtered and the solvent eliminated using a rotary evaporator. The sample was stored in a glass vial. Equation (1) and Table 1 summarize experimental conditions and results of reactions between solketal and the FFAs.
(2,2-Dimethyl-1,3-dioxolan-4-yl)methyl octanoate (1) Liquid at RT, m.p. ≈ −25 °C; 1H-NMR (400 MHz) 4.36–3.44 (m, 4H), 2.35 (td, J = 7.5, 2.2 Hz, 2H), 1.63 (tq, J = 10.6, 6.8, 5.2 Hz, 2H), 1.44 (t, 2H), 1.37 (t, 2H), 1.29 (dtq, J = 13.8, 9.0, 5.0, 4.6 Hz, 9H), 0.88 (t, J = 6.4 Hz, 3H); 13C-NMR (CDCl3, 100 MHz) (ppm): 173.39, 109.51, 77.38, 69.93, 65.52, 33.79, 31.31, 28.73, 28.57, 26.33, 25.05, 24.56, 22.25, 13.71; GC-MS (relative intensity, 70 eV) m/z: 83 (10), 55 (10), 69 (11), 41 (11), 116 (12), 41 (14), 116 (15), 244 (15), 43 (18), 130 (19), 117 (20), 284 (20), 131 (21), 55 (23), 129 (25), 127 (30), 57 (31), 101 (32), 43 (35), 101 (37), 243 (100), 258 ([M]+, <1%); IR (wavenumber cm−1; Transmittance %): 3458; 70, 2930; 52, 1741; 51, 1384; 61, 1164; 63, 1050; 73, 700; 80.
(2,2-Dimethyl-1,3-dioxolan-4-yl)methyl dodecanoate (2) m.p. = 40–48 °C; 1H-NMR (400 MHz) 4.38–3.42 (m, 4H), 2.34 (td, J = 7.6, 3.1 Hz, 2H), 1.63 (td, J = 7.3, 4.2 Hz, 3H), 1.44 (d, J = 4.8 Hz, 2H), 1.38 (d, J = 2.9 Hz, 2H), 1.26 (s, 18H), 0.88 (t, J = 6.6 Hz, 3H); 13C-NMR (100 MHz): 173.36, 109.53, 76.10, 69.98, 64.88, 33.85, 33.28, 31.61, 29.30, 29.15, 29.03, 28.95, 28.83, 26.40, 25.11, 24.61, 22.39, 13.82; GC-MS (relative intensity, 70 eV) m/z: 83 (3), 85 (3), 185 (3), 213 (3), 41 (5), 71 (5), 171 (5), 55 (6), 183 (7), 57 (8), 129 (9), 116 (12), 43 (15), 300 (18), 101 (21), 299 (100), 314 ([M]+, <1%); IR (wavenumber cm−1; Transmittance %) 3292; 20, 2920; 0, 1739; 1, 1469; 7, 1418; 20, 1380; 14, 1208; 11, 1183; 10, 1104; 15, 1048; 12, 992; 31, 943; 37, 849; 41, 757; 13, 720; 25.
(2,2-Dimethyl-1,3-dioxolan-4-yl)methyl palmitate (3) m.p. = 55 °C; 1H-NMR (400 MHz) 4.11 (dt, J = 11.5, 6.1 Hz, 2H), 2.36 (t, J = 7.5 Hz, 2H), 1.64 (s, 3H), 1.45 (t, 3H), 1.38 (t, 3H), 1.28 (d, J = 6.8 Hz, 34H), 0.89 (t, J = 6.2 Hz, 3H); 13C-NMR (100 MHz): 173.63, 109.52, 73.37, 66.07, 64.87, 33.84, 31.63, 29.38, 29.15, 29.06, 29.06, 29.06, 29.06, 28.95 28.95, 28.83, 26.40, 26.22, 25.10, 24.62, 22.41, 13.83; GC-MS (relative intensity, 70 eV) m/z: 171 (7), 55 (8), 57 (10), 116 (12), 129 (12), 43 (17), 101 (21), 356 (24), 355 (100), 370 ([M]+, <1%); IR (wavenumber cm−1; Transmittance %) 3234; 30, 2917; 6, 1730; 9, 1469; 13, 1382; 14, 1220; 13, 1048; 15, 849; 27, 757; 12, 667; 35, 516; 48.
(2,2-Dimethyl-1,3-dioxolan-4-yl)methyl stearate (4) m.p. = 54 °C;1H-NMR (400 MHz) δ 4.38–3.53 (m, 5H), 2.42–2.29 (m, 2H), 1.45 (dt, J = 2.5, 0.7 Hz, 2H), 1.39 (h, J = 0.7 Hz, 2H), 1.27 (s, 32H), 0.97–0.82 (m, 3H); 13C-NMR (100 MHz) 173.36, 109.53, 77.36, 76.88, 76.72, 76.23, 76.09, 73.39, 69.99, 66.07, 64.23, 63.04, 33.86, 31.64, 29.41, 29.17, 29.07, 28.97, 28.84, 26.40, 25.12, 24.63, 22.41, 13.83; GC-MS (relative intensity, 70 eV) m/z: 69 (3), 83 (3), 85 (3), 267 (3), 297 (4), 341 (4), 385 (4), 41 (5), 71 (5), 185 (5), 55 (6), 171 (7), 340 (7), 57 (8), 116 (9), 129 (11), 43 (14), 101 (17), 384 (25), 383 (100), 398 ([M]+, <1%); IR (wavenumber cm−1; Transmittance %) 3234; 26, 2916; 0, 2890; 0, 1730; 2, 1472; 1, 1418; 23, 1381; 10, 1292; 25, 1216, 3; 1180; 5, 1048; 6, 991; 36, 944; 42, 848; 33, 758; 3, 719; 17, 667; 52, 515; 60.

3.4 General Procedure for Synthesis of Fatty Acid Glycerol Formal esters (FAGE)

The FFA (2.0 g), glycerol formal (GlyF: 1.5 molar equivalent respect to the FFA) and p-toluene-sulfonic acid (5% w/w respect of the weight of the FFA) were charged in a conventional round bottom flask with a magnetic stirrer. The mixture was heated at 60 °C and stirred vigorously for 4 h. The reaction was quenched by neutralizing the acid catalyst with saturated solution of sodium carbonate then filtered. The liquid phase was collected in a separatory funnel and partitioned between chloroform and water (3 × 20 mL). The organic layer was dried over sodium sulfate, filtered and the solvent eliminated using a rotary evaporator. The sample was stored in a glass vial Table 2 summarizes the experimental conditions and the results of reactions between GlyF and the FFAs.
(1,3-Dioxolan-4-yl)methyl octanoate (5) Liquid at RT; 1H-NMR (400 MHz, CDCl3) δ 4.35–3.41 (m, 4H), 2.35 (ddd, J = 9.8, 6.6, 2.2 Hz, 2H), 1.63 (depth, J = 11.1, 3.5 Hz, 2H), 1.44 (s, 2H), 1.29 (d, J = 6.0 Hz, 9H), 0.92–0.85 (m, 3H); 13C-NMR (100 MHz) δ 178.88, 95.12, 77.38, 68.26, 63.03, 33.95, 33.84, 31.32, 28.75, 28.72, 28.58, 24.57, 24.39, 22.27, 13.73; GC-MS (relative intensity, 70 eV) m/z: 69 (5), 83 (5), 116 (5), 84 (6), 109 (7), 42 (8), 58 (8), 73 (8), 126 (8), 128 (8), 98 (9), 103 (10), 45 (11), 87 (11), 145 (12), 146 (15), 41 (21), 43 (21), 55 (26), 86 (68), 57 (77), 127 (100), 230 ([M]+, <1%); IR (wavenumber cm−1; Transmittance %) 3558; 77, 2930; 32, 2858; 44, 1739; 32, 1492; 68, 1384; 61, 1166; 44, 1045; 55, 942; 64,757; 56.
(1,3-Dioxolan-4-yl)methyl dodecanoate (6) m.p. = 35–38 °C; 1H-NMR (400 MHz) δ 5.14–3.82 (m, 6H), 3.71 (dq, J = 14.0, 5.0, 4.1 Hz, 2H), 2.37 (t, J = 7.6 Hz, 3H), 1.65 (t, J = 7.3 Hz, 3H), 1.42–1.22 (m, 9H), 0.95–0.82 (m, 3H); 13C-NMR (100 MHz, ) δ 178.71, 93.37, 77.35, 68.29, 63.59, 33.97, 29.30, 29.03, 28.94, 28.82, 28.77, 26.39, 24.60, 24.40, 22.38, 13.81; GC-MS (relative intensity, 70 eV) m/z: 56 (10), 184 (10), 58 (12), 112 (12), 97 (13), 95 (14), 201 (14), 69 (15), 83 (17), 85 (17), 45 (19), 71 (19), 84 (21), 87 (23), 73 (24), 146 (24), 103 (25), 41 (33), 98 (37), 55 (39), 43 (40), 57 (56), 183 (69), 86 (100), 286 ([M]+, <1%); IR (wavenumber cm−1; Transmittance %) 3451; 62, 2926; 25, 2855; 37, 1740; 4 4, 1467; 66, 1384; 61, 1156; 57, 1117; 60, 956; 74, 556; 76.
(1,3-Dioxolan-4-yl)methyl palmitate (7) m.p. = 51–54 °C; 1H-NMR (400 MHz) δ 5.06–3.52 (m, 6H), 2.35 (t, J = 7.5 Hz, 2H), 1.64 (t, J = 7.3 Hz, 3H), 1.26 (s, 27H), 0.89 (t, J = 6.3 Hz, 3H); 13C-NMR (100 MHz) δ 178.71, 95.15, 77.36, 68.29, 66.43, 65.17, 33.97, 33.82, 33.59, 31.63, 29.39, 29.36, 29.30, 29.06, 28.95, 28.83, 28.77, 24.60, 24.40, 22.40, 13.82; GC-MS (relative intensity, 70 eV) m/z: 67 (10), 341 (10), 56 (11), 81 (11), 129 (11), 257 (11), 95 (13), 111 (13), 58 (18), 85 (18), 45 (19), 146 (19), 112 (21), 69 (22), 83 (22), 71 (23), 97 (24), 84 (32), 41 (33), 87 (37), 55 (38), 103 (38), 73 (43), 43 (44), 239 (52), 57 (63), 98 (64), 86 (100), 342 ([M]+, <1%); IR (wavenumber cm−1; Transmittance %) 2916; 1, 2850; 2, 1738; 7, 1704; 11, 1463; 19, 1383; 43, 1297; 29, 1175; 17, 1097; 25, 1015; 27, 943; 23, 758; 11, 720; 40, 667; 63.
(1,3-Dioxolan-4-yl)methyl stearate (8) m.p. = 66–70 °C; 1H-NMR (400 MHz) δ 5.16–3.53 (m, 4H), 2.37 (s, 1H), 1.64 (s, 1H), 1.28 (d, J = 7.1 Hz, 25H), 0.97–0.82 (m, 3H); 13C-NMR (100 MHz) δ 175.83, 93.76, 74.68, 71.63, 66.89, 65.04, 63.77, 62.18, 32.58, 32.42, 32.01, 28.01, 27.97, 27.91, 27.76, 27.56, 27.44, 27.39, 23.21, 23.05, 13.57, 12.42; GC-MS (relative intensity, 70 eV) m/z: 129 (8), 268 (8), 369 (8), 96 (9), 99 (9), 109 (9), 67 (10), 81 (11), 159 (11), 285 (11), 56 (12), 111 (12), 95 (13), 58 (17), 45 (19), 112 (19), 97 (20), 85 (22), 71 (23), 69 (24), 83 (24), 146 (25), 103 (27), 84 (28), 41 (30), 73 (33), 87 (36), 267 (40), 55 (41), 43 (55), 98 (56), 57 (59), 86 (100), 370 ([M]+, <1%); IR (wavenumber cm−1; Transmittance %) 2977; 32, 2927; 32, 2855; 28, 1737; 66. 1472; 66, 1383; 49, 1350; 65, 1122; 21, 953; 80, 830; 79, 680; 77.

4. Conclusions

We have presented the acid-catalyzed synthesis and characterization of the fatty acid esters of solketal and glycerol formal. The novelty lies in the fact that acid catalysis does not promote undesired acetal hydrolysis and that the procedure can be conducted in the absence of added solvents. In fact, it is likely that the absence of added solvents, normally containing traces of water, is one of the reasons for the observed lack of hydrolysis of the acetals. High yields of isolated products can be obtained and all synthesized compounds are stable. In addition, the derivatives of solketal 3 and 4 possess mesogenic behavior and show a liquid crystalline phase. These new products contain different carbon-oxygen moieties that can in principle provide interesting properties as fuel additives such as better ignition and/or lubricity.

Supplementary Materials

Supplementary materials can be accessed at: https://www.mdpi.com/1420-3049/21/2/170/s1.

Acknowledgments

Funding from Università Ca’ Foscari—in the form of a Research Prize—is gratefully acknowledged. No funds for covering the costs to publish in open access were received. Sabrina Fabris is gratefully acknowledged for her help with DSC mesaurements.

Author Contributions

Alvise Perosa conceived and designed the experiments and wrote the paper; Andrea Moraschini and Marco Noè performed the experiments and analyzed the data; Maurizio Selva contributed to planning of research and interpretation of the data.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Demirbas, A. Progress and recent trends in biodiesel fuels. Energy Convers. Manag. 2009, 50, 14–34. [Google Scholar] [CrossRef]
  2. Lin, L.; Cunshan, Z.; Vittayapadung, S.; Xiangqian, S.; Mingdong, D. Opportunities and challenges for biodiesel fuel. Appl. Energy 2011, 88, 1020–1031. [Google Scholar] [CrossRef]
  3. Liaquat, A.M.; Kalam, M.A.; Masjuki, H.H.; Jayed, M.H. Potential emissions reduction in road transport sector using biofuel in developing countries. Atmos. Environ. 2010, 44, 3869–3877. [Google Scholar] [CrossRef]
  4. Quispea, C.A.G.; Coronadoc, C.J.R.; Carvalho, J.A., Jr. Glycerol: Production, consumption, prices, characterization and new trends in combustion. Renew. Sustain. Energ. Rev. 2013, 27, 475–493. [Google Scholar]
  5. Ciriminna, R.; Della Pina, C.; Rossi, M.; Pagliaro, M. Understanding the glycerol market. Eur. J Lipid Sci. Technol. 2014, 116, 1432–1439. [Google Scholar] [CrossRef]
  6. Zhou, Y.; Nie, K.; Zhang, X.; Liu, S.; Wang, M.; Deng, L.; Wang, F.; Tan, T. Production of fumaric acid from biodiesel derived crude glycerol by Rhizopus arrhizus. Bioresour. Technol. 2014, 163, 48–53. [Google Scholar] [CrossRef] [PubMed]
  7. Lapuerta, M.; Rodríguez-Fernandez, J.; Estevez, C.; Bayarri, N. Properties of fatty acid glycerol formal ester (FAGE) for use as a component in blends for diesel engines. Biomass Bioenerg. 2015, 76, 130–140. [Google Scholar] [CrossRef]
  8. Yang, L.; Zhu, Z.; Wang, W.; Lu, X. Microbial recycling of glycerol to biodiesel. Bioresour. Technol. 2013, 150. [Google Scholar] [CrossRef]
  9. Nanda, M.R.; Yuan, Z.; Qin, W.; Ghaziaskar, H.S.; Poirier, M.-A.; Xu, C.C. Thermodynamic and kinetic studies of a catalytic process to convert glycerol into solketal as an oxygenated fuel additive. Fuel 2014, 117, 470–477. [Google Scholar] [CrossRef]
  10. Garcia, E.; Laca, M.; Perez, E.; Garrido, A.; Peinado, J. New class of acetal derived from glycerin as biodiesel fuel component. Energy Fuels 2008, 22, 4274–4280. [Google Scholar] [CrossRef]
  11. Selva, M.; Benedet, V.; Fabris, M. Selective Catalytic Etherification of Glycerol Formal and Solketal with Dialkyl Carbonates and K2CO3. Green Chem. 2012, 14, 188–200. [Google Scholar] [CrossRef]
  12. Selva, M.; Guidi, S.; Noè, M. Upgrading of glycerol acetals by thermal catalystfree transesterification of dialkyl carbonates under continuous-flow conditions. Green Chem. 2015, 17, 1008–1023. [Google Scholar] [CrossRef]
  13. Haider, M.H.; Dummer, N.F.; Knight, D.W.; Jenkins, R.L.; Howard, M.; Moulijn, J.; Taylor, S.H.; Hutchings, G.J. Efficient green methanol synthesis from glycerol. Nat. Chem. 2015, 7, 1028–1032. [Google Scholar] [CrossRef] [PubMed]
  14. Beatrice, C.; di Blasio, G.; Lazzaro, M.; Cannilla, C.; Bonura, G.; Frusteri, F.; Asdrubali, F.; Baldinelli, G.; Presciutti, A.; Fantozzi, F.; et al. Technologies for energetic exploitation of biodiesel chain derived glycerol: Oxy-fuels production by catalytic conversion. Appl. Energ. 2013, 102, 63–71. [Google Scholar] [CrossRef]
  15. Gras, J.L.; Nouguier, R.; Mchich, M. Transacetalisation de triols a partir du dimethoxymethane. Selectivite et applications synthetiques. Tetrahedron Lett. 1987, 28, 6601–6604. [Google Scholar] [CrossRef]
  16. Da Silva, C.X.A.; Gonçalves, V.L.C.; Mota, C.J.A. Water-tolerant zeolite catalyst for the acetalisation of glycerol. Green Chem. 2009, 11, 38–41. [Google Scholar] [CrossRef]
  17. De Torres, M.; Jiménez-osés, G.; Mayoral, J.A.; Pires, E.; de los Santos, M. Glycerol ketals: Synthesis and profits in biodiesel blends. Fuel 2012, 94, 614–616. [Google Scholar] [CrossRef]
  18. Oprescu, E.-E.; Stepan, E.; Dragomir, R.E.; Radu, A.; Rosca, P. Synthesis and testing of glycerol ketals as components for diesel fuel. Fuel Process. Technol. 2013, 110, 214–217. [Google Scholar] [CrossRef]
  19. Song, J.; Zello, V.; Boehman, J. Energy Fuels. Performance and Emissions of a Compression Ignition Engine Fueled with Diesel/Oxygenate Blends for Various Fuel Delivery Advance Angles. Energy Fuels 2005, 19, 403–410. [Google Scholar]
  20. Boot, M.; Frijters, P.; Liijten, C.; Somers, B.; Baert, R.; Donkerbroek, A.; Klein-Douwel, R.J.H.; Dam, N. Cyclic Oxygenates: A New Class of Second-Generation Biofuels for Diesel Engines? Energy Fuels 2009, 23, 1808–1817. [Google Scholar]
  21. Soares, V.L.P.; Lachter, E.R.; Rodrigues, A., Jr.; Batista, L.N.; Nascimento, R.S.V. New Applications for Soybean Biodiesel Glycerol in Soybean—Applications and Technology, 1st ed.; Ng, T.-B., Ed.; InTech: Rijeka, Croatia, 2011; Volume 4, pp. 151–172, and references therein. [Google Scholar]
  22. Cablewsky, T.; Faux, A.F.; Strauss, C.R.J. Development and Application of a Continuous Microwave Reactor for Organic Synthesis. J. Org. Chem. 1994, 59, 3408–3412. [Google Scholar] [CrossRef]
  23. Sahai, P.; Vishwakarma, R.A.J. Phospholipase-A2-mediated stereoselective synthesis of (R)-1-O-alkylglycero-3-phosphate and alkyl-acyl analogues: Application for synthesis of radiolabelled biosynthetic precursors of cell surface glycoconjugates of Leishmania donovani. J. Chem. Soc. Perkin Trans. 1 1997, 12, 1845–1850. [Google Scholar] [CrossRef]
  24. Clarkson, J.S.; Walker, A.J.; Wood, M.A. Continuous Reactor Technology for Ketal Formation: An Improved Synthesis of Solketal. Org. Process Res. Dev. 2001, 5, 630–635. [Google Scholar] [CrossRef]
  25. Delfort, B.; Durand, I.; Jaecker, A.; Lacome, T.; Montagne, X.; Paille, F. Diesel Fuel Compounds Containing Glycerol Acetals. U.S. Patent 2003163949, 4 September 2003. [Google Scholar]
  26. Corma, A.; Iborra, S.; Velty, A. Chemical Routes for the Transformation of Biomass into Chemicals. Chem. Rev. 2007, 107, 2411–2502. [Google Scholar] [CrossRef] [PubMed]
  27. Schwarz, J.; Weisspapir, M. Topical Composition for Acne Treatment. U.S. Patent 2005255133, 17 November 2005. [Google Scholar]
  28. Moeller, H. A process for the Preparation of Salts of 1,3-Dioxolane-4-carboxylic Acids and Their Use. Patent DE3447783, 10 July 1986. [Google Scholar]
  29. Walsh Reed, H. Dioxolanes and Thio Analogs, Derivating Thereof and Lubricants and Fuels Containing Same. Patent WO8805071, 14 July 1988. [Google Scholar]
  30. Lee Dosuk, D. Delayed-Setting Calcium Phosphate Pastes. Patent WO2005117919, 15 December 2005. [Google Scholar]
  31. Fraatz, K.; Mertin, D.; Heep, I. Controlled Release System. U.S. Patent 2006034926, 16 February 2006. [Google Scholar]
  32. Vicente, G.; Melero, J.A.; Morale, G.; Paniagua, M.; Martin, E. Acetalisation of bio-glycerol with acetone to produce solketal over sulfonic mesostructured silicas. Green Chem. 2010, 12, 899–907. [Google Scholar] [CrossRef]
  33. Jaecker-Voirol, A.; Durand, I.; Hillion, G.; Delfort, B.; Montagne, X. Glycerin for New Biodiesel Formulation. Oil Gas Sci. Technol. 2008, 63, 395–404. [Google Scholar] [CrossRef]
  34. Farmer, T.J.; Mascal, M. Platform Molecules in Introduction to Chemicals from Biomass, 2nd Ed.; Clark, J., Deswarte, F., Eds.; John Wiley & Sons: Chichester, UK, 2015. [Google Scholar]
  35. Ozorio, L.P.; Pianzolli, R.; Mota, M.B.S.; Mota, C.J.A. Reactivity of Glycerol/Acetone Ketal (Solketal) and Glycerol/Formaldehyde Acetals toward Acid-Catalyzed Hydrolysis. J. Braz. Chem. Soc. 2012, 23, 931–937. [Google Scholar] [CrossRef]
  36. Goodby, J.W.; Watson, M.J.; Macenzie, G.; Kelly, S.M.; Bachir, S.; Bault, P.; Gode, P.; Goethals, G.; Martin, P.; Ronco, G.; Villa, P. The dependence of mesomorphic behaviour on the extent of hydrogen-bonding in sugar derived polyols. Liquid Cryst. 1998, 25, 139–147. [Google Scholar] [CrossRef]
  37. Milkereit, G.; Garamus, V.M.; Veermans, K.; Willumeit, R.; Vill, V. Synthesis and mesogenic properties of a Y-shaped glyco-glycero-lipid. Chem. Phys. Lipids 2004, 131, 51–61. [Google Scholar] [CrossRef] [PubMed]
  • Sample Availability: Samples of all compounds are available from the authors.

Share and Cite

MDPI and ACS Style

Perosa, A.; Moraschini, A.; Selva, M.; Noè, M. Synthesis of the Fatty Esters of Solketal and Glycerol-Formal: Biobased Specialty Chemicals. Molecules 2016, 21, 170. https://doi.org/10.3390/molecules21020170

AMA Style

Perosa A, Moraschini A, Selva M, Noè M. Synthesis of the Fatty Esters of Solketal and Glycerol-Formal: Biobased Specialty Chemicals. Molecules. 2016; 21(2):170. https://doi.org/10.3390/molecules21020170

Chicago/Turabian Style

Perosa, Alvise, Andrea Moraschini, Maurizio Selva, and Marco Noè. 2016. "Synthesis of the Fatty Esters of Solketal and Glycerol-Formal: Biobased Specialty Chemicals" Molecules 21, no. 2: 170. https://doi.org/10.3390/molecules21020170

Article Metrics

Back to TopTop