Priyank N. Shah*a,
Namjoon Kimc,
Zhuangrong Huangc,
Mahesh Jayamannaa,
Akshay Kokila,
Alex Pineb,
Jarmin Kaltsasb,
Edwin Jahngena,
David K. Ryana,
Seongkyu Yoonc,
Robert F. Kovard and
Yongwoo Lee*a
aDepartment of Chemistry, University of Massachusetts Lowell, One University Avenue, Lowell, Massachusetts 01854, USA. E-mail: Priyank_shah@uml.edu; Yongwoo_Lee@uml.edu; Tel: +1-978-934-3734 Tel: +1-978-934-3792
bMaine Standard Biofuels, 51 Ingersoll Dr., Portland, Maine 04103, USA
cDepartment of Chemical Engineering, University of Massachusetts Lowell, One University Avenue, Lowell, Massachusetts 01854, USA
dR. F. Kovar & Associates, 203 Beach Street, Wrentham, MA 02093-1513, USA
First published on 22nd April 2015
We present here for the first time a novel environmentally benign protocol for the synthesis of vinyl ester resin (VER). Our synthetic strategy utilizes a commercial waste material, glycerin, from biodiesel manufacturing and converts it into a widely utilized resin. The VER was synthesized using bisphenol A (BPA) and glycidyl methacrylate (GMA) as precursors. GMA was synthesized via a multistep synthetic protocol using glycerin obtained from a biodiesel manufacturing waste stream. The structure of the intermediates was confirmed by 1H NMR, HPLC and FT-IR spectroscopy.
VER can be processed at ambient temperature using vacuum-assisted resin transfer molding (VARTM) into massive carbon-fiber-reinforced composites.5 The synthetic protocols used for manufacture of VER has two main disadvantages. First, VER is currently synthesized from petroleum feedstock, which reduces the sustainability. Second, VER is synthesized from epichlorohydrin which is a known environmental hazard that produces acute toxicity in case of inhalation, oral, and dermal exposure.
Hence, for reducing the environmental impact, it is essential to develop VER synthesis routes that are not dependent on petroleum based feedstock. Moreover, investigations of the VER synthesis routes that lead to elimination of the use of hazardous chemicals, such as epichlorohydrin, are necessary. To assure sustainability of the new processing route, starting materials should be derived from readily available renewable resources.
Recently, significant advances have been made for obtaining biodiesel, a renewable biofuel for use in diesel engines and heating applications. Biodiesel can be produced by base catalyzed hydrolysis of rapeseed oil,7 soybean and wastes of cooked oil,8 rice straw,9 vegetable oil mixtures of cottonseed, soybean and castor oils,10 jatropha oil,11 and crude palm oil.12 Biodiesel is environmentally beneficial because it is biodegradable, nontoxic and has low emission.13 During manufacturing of biodiesel, approximately a 10% volume of glycerin is produced as a by-product or waste.14 Therefore, the effective utilization of glycerin enlarges the economy of biodiesel production; moreover, the conversion of glycerin to value added chemicals can expand the scope of green chemistry.15 Although biodiesel uses non-petroleum feedstocks, it is still subject to the price fluctuations of the petroleum liquid fuels market. Subsidization also plays an important role in the overall market price of biodiesel. These two market factors often make it very important for biodiesel manufacturers to sell as many of their byproducts as possible.
Only limited systematic investigations are reported on the use of functional vinyl monomer such as glycidyl methacrylate (GMA),16 which is a versatile bidentate monomer capable of imparting oxirane functionality to VER. It is also worth mentioning that bisphenol A (BPA) is an important chemical used to manufacture polycarbonate plastic, epoxy resin, flame retardants, and other specialty products,17 and is manufactured by acid catalyzed condensation of acetone and phenol.18
In the present work, we focused on the synthesis of the green vinyl ester resins (GVER) from renewable sources using three steps (Fig. 1): (1) synthesis of GMA from waste glycerin; (2) conversion of phenol into BPA using environmentally benign conditions, and (3) synthesis of GVER from BPA and GMA.
:
30 mixture of hexane and ethyl acetate. Samples were prepared in ethyl acetate.
O stretching), 1480, 1399, 1277 (–CH bending).
CH2), 4.48, 3.92 (2H, –CH2–CH–), 3.25 (1H, –CH2–CH–), 2.82, 2.67 (2H, –O–CH2), 1.90 (3H, –C–CH3). 13C NMR (CDCl3, 125 MHz) δ (ppm): 166.35 (
C–CO–O–), 135.70 (–CH2
C–CO–O), 125.51 (–CH2
C–CO–O), 64.92 (–O–CH2–epoxy ring), 48.93 (–O–CH2–CH (epoxy ring)), 43.96 (–O–CH2 (epoxy ring)), 17.78 (–CH2
C–CH3). IR (cm−1): 2995, 2951 (–CH stretching aliphatic), 1726 (–C
O stretching), 1452, 1397, 1326, 1269 (–CH bending).
:
7 ethyl acetate
:
hexane ratio. The 1H NMR showed that the conversion of BPA from phenol was ∼27.0%, but after column purification, we could successfully isolated BPA with 9.0% yield. Bisphenol A: 1H NMR (DMSO, 500 MHz), δ (ppm), 9.12 (2H, –OH), 6.98, 6.62 (8H, –ArH), 1.54 (6H, –C–CH3). 13C NMR (DMSO, 125 MHz) δ (ppm): 155.39 (OH–C(ArC)), 141.57 (–CH3–C–C(ArC)), 127.7 (–CH3–C–C(ArC)–C(ArC)), 155.08 (OH–C(ArC)–C(ArC)), 41.38 (–CH3–C–C(ArC)), 31.40 (–CH3–C–C(ArC)). IR (cm−1): 3320 (–OH stretching), 2963 (–CH stretching Ar), 1508, 1434, 1383 (–CH bending).
CH2), 4.48, 3.92 (2H, –CH2–CH–), 3.25 (1H, –CH2–CH–), 2.82, 2.67 (2H, –O–CH2), 1.90 (3H, –C–CH3). 13C NMR (DMSO, 125 MHz) δ (ppm): 167.09 (
C–CO–O–), 156.58 (–CH2–O–C(ArC)), 143.25 (–CH3–C–C(ArC)), 136.13 (–CH2
C–CO–O), 127.78 (–CH2
C–CO–O), 126.45 (–CH2–O–C(ArC)–C(ArC)), 114.10 (–CH3–C–C(ArC)–C(ArC)), 69.27 (CO–O–CH2–CH– CH2), 67.35 (CO–O–CH2–CH–CH2), 66.01 (CO–O–CH2–CH–CH2), 39.48 (–CH3–C–C(ArC)), 30.78 (–CH3–C–C(ArC)), 18.35 (–CH2
C–CH3). IR (cm−1): 3424 (–OH stretching), 2963, 2926 (–CH stretching aliphatic), 1724 (–C
O stretching), 1634, 1607, 1597, 1403, 1362 (–CH bending).
![]() | ||
| Fig. 2 Small scale biodiesel reaction at Maine Standard Biofuels (MSB). Biodiesel/methyl esters (top), soaps (middle), crude glycerin (bottom). | ||
Glycerol carbonate (GC), a first intermediate in the synthetic route to GMA from the distilled glycerin, is an attractive intermediate having a large number of applications in various fields. Various approaches had been adopted by different groups for the synthesis of the GC; such as, using (a) Novozyme 435 catalyst and dimethyl carbonate as a precursor,17 and (b) metal oxide as a catalyst and urea as a precursor.18 In a new approach, GC was synthesized by reaction between glycerin and dimethyl carbonate at 73 °C for 3 h in the presence of potassium carbonate.19 The method is promising, with several challenges for example the separation of potassium carbonate from the reaction mixture. Firstly, the reaction was performed at 73 °C and the GC was synthesized successfully. The product formation was confirmed by 1H NMR as shown in Fig. 4. The peak integration value suggested ∼98.5% conversion of glycerin to GC at 73 °C. In order to complete the reaction to 100.0%, the reaction temperature was increased to 100 °C; however, as the temperature increased to 100 °C, formation of some side product was observed and unreacted glycerin was also found in the final mixture. The FT-IR spectra of glycerol carbonate synthesized at 73 °C clearly showed peaks of –C
O at 1772.51 cm−1 and –OH at 3456.9 cm−1 as shown in Fig. S2 in ESI.†
Glycidol is the second intermediate during the synthesis of GMA from glycerin. Glycidol was obtained by decarboxylation of GC as shown in Fig. 1. In a typical setup for the synthesis of glycidol, a vacuum distillation apparatus was utilized. Glycidol was synthesized by heating the glycerol carbonate in the presence of sodium sulfate at 180 °C for 3 h.20 The formation of glycidol was confirmed by 1H NMR by matching the integration value of each proton as shown in Fig. 4. Strong evidence is provided by the FT-IR exhibiting a clear disappearance of the –C
O peak at 1761 cm−1 as shown in Fig. S2 in ESI.† Glycidol was isolated with 33.0% yield.
Glycidyl methacrylate (GMA) is one of the precursors for the synthesis of vinyl ester resin monomer along with bisphenol A. GMA was synthesized by transesterfication between methyl methacrylate and the oxirane moiety in the presence of potassium cyanide as a catalyst and 2,4-dimethyl-6-tertbutylphenol.21 First, the pressure was reduced in the reaction flask, and the temperature was raised to 70 °C. The temperature of 70 °C was maintained for 2 h, and after that unreacted methyl methacrylate and methanol were distilled off. In a second fraction unreacted glycidol was collected and in last fraction GMA was obtained. The structure of GMA was confirmed by 1H NMR as shown in Fig. 5. The GMA was isolated with 25.3% yield.
:
ethyl acetate in a 7
:
3 ratio as a solvent mixture. The BPA was isolated with 9.0% yield and product was confirmed by 1H NMR as shown in Fig. 6.
The VER monomer was synthesized by a reaction between BPA and GMA in the presence of amine catalyst. The reaction was performed at 70 °C under argon.22 The 1H NMR did not exhibit the –OH peak of the BPA, so it was presumed that the reaction was 100% complete but, the integration value did not matching precisely. Thin layer chromatography (TLC) displayed three spots. The integration values in the 1H NMR and the higher number of spots in TLC confirmed the presence of product in the reaction mixture as shown in Fig. 7.
After confirming the presence of three different products in the reaction mixture; all fraction were separated by column chromatography using a 3
:
7 ethyl acetate
:
hexane ratio and analysed using 1H NMR as shown in Fig. 8. The 1H NMR clearly indicated the presence of non-functional BPA (NF) in the first fraction; mono-functional BPA (MF), GMA-BPA, in the second fraction; and di-functional BPA (DF), GMA-BPA-GMA, in the third fraction. The data clearly suggested that a 2 h reaction time was insufficient to obtain the maximum amount of DF. In order to increase the yield the reaction time was increased up to 6 h and sample was taken out at periodic interval of time, and the molar ratio of the GMA
:
BPA was increased to 4
:
1. A very strong evidence of the formation of the vinyl ester resin can be observed in the shifting of the aromatic peaks in 1H NMR of the vinyl ester resin as shown in Fig. S9 in the ESI.† The peaks for the BPA aromatic protons can be observed at 7.10 (OH–C–CH(ArH)) and 6.83 (CH–C–C–CH3), which shift to 6.98 (–O–C–CH) and 6.63 (CH–C–C–CH3), respectively. The peak for all four aromatic protons can be observed at 7.10 (OH–C–CH(ArH)), 6.98 (–O–C–CH), 6.83 (CH–C–C–CH3), and 6.63 (CH–C–C–CH3) as shown in Fig. S9 in the ESI.†
In order to determine the kinetics of the reaction, the quantification of NF, MF and DF in the reaction mixture is very essential. Such quantification can be obtained by high performance liquid chromatographic (HPLC) separation of the mixture. Therefore, preliminary work was conducted to develop a HPLC method for the separation and determination of BPA and reaction products in the synthesis of a VER. The ultimate goal was to separate each fraction without overlapping retention time.
Chromatograms shown in Fig. S4–S6 in ESI† clearly demonstrate that the 3 compounds have very different retention times on the diol column with 7
:
3 hexane
:
ethyl acetate and should be easily separated and determined in a reaction mixture. The first fraction (NF), second fraction (MF) and third fraction (DF) exhibited retention time of 5.218, 7.946, and 13.686 min respectively.
We quantified the NF, MF, and DF BPA by calculating and comparing the area under the peak of the chromatogram obtained at different time intervals as shown in Table 1. The results suggested that reaction proceeds well as time progresses. However, it did not attain completion at 6 h, 69.26% of the DF VER monomer was obtained. Experiments are in progress and the results will be published in near future with additional work to further improve the yield of this synthesis.
| Reaction time (h) | Different functional BPA | ||
|---|---|---|---|
| Non | Mono | Di | |
| 2 h | 32.00 | 49.24 | 18.76 |
| 3 h | 20.79 | 46.28 | 32.93 |
| 4 h | 14.13 | 40.63 | 45.23 |
| 5 h | 13.38 | 28.27 | 58.34 |
| 6 h | 12.70 | 18.05 | 69.26 |
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: 10.1039/c5ra03254g |
| This journal is © The Royal Society of Chemistry 2015 |