Wolfson et al.
241
Table 1. Glycerol and triacetin properties.
Table 2. Nucleophilic substitution in representative glycerol−triacetin
mixtures.
Property
Glycerol
Triacetin
259
0.0023
Product yield (%)
Boiling point (°C)
290
0.00025a
12 600
400
b
Vapor pressure at 20–25 °C (mmHg)
LD50 oral-mouse (mg/kg)
Autoignition temperature (°C)
Flash point (°C)
Dielectric constant at 25 °C
log P
BzCl + NaOAc
(1 h)
BzCl + NaOAc
(2 h)
BzCl + NH OAc
(1 h)
4
3000
433
140
Solvent (wt%)
Glycerol
30
32
74
25
0
60
62
96
42
0
100
76
74
71
193
42.5a
b
Gly-Tri (70/30)
Gly-Tri (50/50)
Gly-Tri (30/70)
Triacetin
7.3
−4.15
1410
221.9
91.7
0.25
23
389.0
85.7
1.1562
Viscosity at 20 °C (cP)
Heat capacity at 25 °C (J/(mol K))
Heat of vaporization (kJ/mol)
Density at 25 °C (g/mL)
a
0
Note: Reaction conditions: 0.8 mmol of benzyl chloride, 0.88 mmol of salt,
5.0 g of solvent, 80 °C.
1.4746
2
5 °C.
uously generated by the biodiesel industry are increasing, it is
vital that we search for economical uses for glycerol to defray the
cost of biodiesel production.
b20 °C.
Fig. 1. Representative reactions.
While the key property of a reaction solvent is its solvation
capability, i.e., its ability to facilitate the combination of reactants
and catalysts, many organic reactions also require salts and or-
ganic compounds or hydrophilic and hydrophobic molecules to
2
0,21
be dissolved simultaneously.
Hence, it was suggested that the
drawbacks outlined above in the use of glycerol as a solvent for
the dissolution of a hydrophobic substrate can be overcome by
using mixtures of glycerol and triacetin, both of which are inex-
pensive and commercially available and sustainable solvents
whose use enables the polarity of the reaction medium to be
tailored to the reaction requirements. The properties of glycerol
and triacetin as solvents are summarized in Table 1.
To examine this hypothesis, catalyst-free nucleophilic substitu-
tion of benzyl halides with sodium or ammonium acetate22 was
employed as the first example of organic transformation in a
glycerol−triacetin (Gly-Tri) mixture (Fig. 1a). Because this reaction
requires the dissolution of a nonpolar organic compound with a
polar ionic salt, reaction medium polarity is expected to have an
influence. The investigation began by testing the yields of benzyl
acetate in the nucleophilic substitution of benzyl chloride with
sodium and ammonium acetate in several Gly-Tri mixtures and in
the two pure solvents (Table 2). As illustrated in Table 2, the reac-
tion proceeded in pure glycerol, but no reaction was detected in
pure triacetin. This outcome may be attributed to the fact that for
the substitution to occur, the salt must split into ions, a phenom-
enon that occurs only in polar solvents. Likewise, performing the
reaction in different Gly-Tri mixtures also yielded benzyl acetate.
In addition, replacing sodium acetate with ammonium acetate
produced higher yields in glycerol and in all Gly-Tri mixtures, a
result possibly due to the lower ionization energy of ammonium
acetate due to the higher ionic radius of the ammonium ion.
Finally, the product extraction resulted in highly pure benzyl ac-
etate (>98%).
The effect of the glycerol to triacetin ratio on the yield of benzyl
acetate was also dissimilar with the two different salts. When
sodium acetate was the salt, maximum product yield was detected
in a mixture of 50%–50% Gly-Tri, while the highest product yield
with ammonium acetate was in pure glycerol. Furthermore, al-
though addition of triacetin to glycerol (up to 70 wt%) when am-
monium acetate was used as the salt resulted in lower product
yields compared to running the reaction in pure glycerol, the
amount of triacetin in the mixture did not significantly affect
product yield. These results can also be explained by the lower
ionization power of ammonium acetate and the fact that it may
also form hydrogen bonds with glycerol, which enhances its sep-
aration into ions relative to sodium acetate in all reaction mix-
tures.
pressure and the resulting crude was analyzed to determine prod-
uct yield by GC using an HP-1 column.
Transfer hydrogenation
In a typical procedure, 0.1 g of 1-octene and 0.01 g of palladium
acetate were added to a vial with 5.0 g of reaction mixture. The
mixture was placed in a preheated oil bath and heated to 80 °C,
after which it was magnetically stirred for 48 h. At the end of the
reaction, the reaction mixture was cooled and extracted with 3 mL
of petroleum ether (60–80 °C). Finally, the ether phase was re-
duced under vacuum and analyzed by GC analysis using an HP-5
column (30 m × 0.25 mm, 0.25 m thick) to determine the product
yield.
Results and discussion
Organic chemistry is traditionally carried out in solution to
dissolve reactants and (or) catalysts and to affect the transfer of
mass, heat, or momentum.14 However, solvents are responsible
for a large part of the waste and pollution generated by chemical
processes, as their discharge into the environment leads to their
accumulation in the air, water, and land. Thus, various green
solvents have been introduced and studied during the last three
decades, some of them specific to particular reactions and others
for more general use.1
5–19
The most commonly used and accepted
green solvent families comprise water, ionic liquids, fluorous phase,
supercritical solvents, especially super critical CO , and bio-based
2
solvents such as ethanol and glycerol and its derivatives.
As a nontoxic, nonhazardous, nonvolatile, biodegradable, and
recyclable liquid produced as a by-product in the transesterifica-
tion of oil from renewable sources, glycerol has been shown to be
a promising alternative and sustainable solvent for organic trans-
The effect of the glycerol to triacetin ratio on reaction perfor-
mance was also studied in the palladium-catalyzed Suzuki−Miyaura
cross-coupling reaction of iodobenzene and phenylboronic acid
1
–11
23
formations.
Moreover, as the amounts of glycerol being contin-
(Fig. 1b). This reaction requires the simultaneous dissolution of
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