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a ¼ 0.0485P ꢀ 2.75 ꢀ 0.46p*
b ¼ 0.358 ꢂ (31.10 ꢀ nmax,NA) ꢀ 1.125p*
(3)
(4)
The derived solvatochromic parameters (p*, a and b) as well
as the viscosity (h) of the binary IL mixtures are shown in Fig. 2.
It is seen that, with the increase of the mole fraction of [Bmim]
Cl (x), the absorption maximum of EMCPI moves towards
longer wavelength, which indicates the polarity of the binary IL
mixtures decreases (the ground state of EMCPI is more polar
than its excited state). As for a and b values, Fig. 2A shows that
they are both proportional to the x value; with the increase of
3 3
Scheme 1 Structures of [Bmim]Cl and [HNMP][CH SO ].
[Bmim]Cl content, b increases from 0.46 to 0.91, but a decreases
from 0.81 to 0.44. This is because in the present binary IL
ꢀ
[
CH SO ], respectively. The discrepancy between the melting mixtures, Cl is
a
better hydrogen-bond acceptor than
3
3
27
ꢀ
+
and the freezing temperatures is due to supercooling. As for [CH SO ] , while [HNMP] is a better hydrogen-bond donor
3
3
ꢁ
+
6,11
neat [Bmim]Cl, it melts at 68 C, but aer heated, the molten than [Bmim] . For the viscosity of the binary mixtures, Fig. 2B
Bmim]Cl has no crystallization peak and only glass transition shows that it rises nonlinearly as a function of the x value. This
[
ꢁ
ꢁ
phenomenon (at ca. ꢀ39 C and ꢀ48 C) was observed in the trend could be explained using a similar rationale to that for the
ꢁ
ꢀ1
course of cooling and reheating at the rate of 4 C min (as composition-dependent T , i.e., the ions interaction is the major
g
ꢁ
ꢁ
28
6,32
reported in literature they are at ꢀ41 C and ꢀ48 C). This factor, the larger the force, the larger the viscosity.
phenomenon indicates that the crystallization of [Bmim]Cl is
kinetically much slower than that of [HNMP][CH SO ].
29,30
For
3
3
their mixture, a thermal behaviour similar to the neat [Bmim]Cl Fructose conversion into HMF in binary IL mixtures
was also observed, but the glass-transition temperature (T
g
) was
Fig. 3 shows the time-dependent HMF yield in IL mixtures of
different mole fractions under the reaction conditions of 25 C
ꢁ
shied to lower temperature (ca. ꢀ63 C). The present thermal
ꢁ
behaviours of the binary IL mixture are very similar to those
and 600 rpm. For a given amount of fructose, the HMF yield in
a given time interval increases with the increase of x. Speci-
cally, the HMF yield in 1.0 h varies from the lowest 24.6% to the
highest 73.0%, which indicates that the composition of the
binary IL mixtures affects the formation rate. Based on the
physicochemical properties of the binary mixture (characterized
in the previous section), we speculate that the change may be
related to the viscosity and/or the hydrogen-bond donating/
accepting ability of the medium.
To explore the effect of the viscosity on the formation rate,
a less viscous IL mixture (x ¼ 0.33) and a more viscous IL
mixture (x ¼ 0.86) were selected as media for fructose dehy-
dration, and the HMF yield at a given time in the two media
under different stirring speeds were compared (see Fig. 4). As
shown in Fig. 4, the formation rate of HMF under unstirred
condition is low in both media. The HMF yields in 1.0 h and
2
7,31
reported elsewhere.
Bmim]Cl, the T
It is noteworthy that with the increase of
ꢁ
ꢁ
[
g
of IL mixture rose from ꢀ63 C to ꢀ52 C. This
composition-dependent phenomenon could be rationalized as
ꢀ
follows: on the one hand, more Cl anions, which have smaller
size and higher charge density, result in an enhancement of the
coulombic interaction between ions; on the other hand, the
+
hydrogen-bond donating ability of [HNMP] is stronger than
+
+
that of [Bmim] , so the decrease of [HNMP] content results in
weaker hydrogen bonds and therefore more ordered ionic
32
structure, thereby enhancing ion–ion interaction. However,
the reason why the T values of the binary mixtures in [HNMP]
g
[
CH SO ]-rich region change little is not clear and it need
3 3
further investigation.
Physicochemical properties of the binary IL mixtures
5
.0 h were 10.2% and 23.7% (x ¼ 0.33) and 13.0% and 19.9% (x
The polarity (P), hydrogen-bond donating ability (a) and
¼
0.86), respectively. Relatively speaking, the increment in HMF
hydrogen-bond accepting ability (b) of the binary IL mixtures at
ꢁ
yield in the less viscous mixture is larger than that in the more
viscous mixture. This result indicates that the more viscous the
binary IL mixture is, the greater the mass transfer resistance
and the slower the HMF formation rate. To eliminate the mass
transfer resistance, the reaction system was subjected to agita-
tion. Under the conditions of 600 rpm and 1200 rpm, HMF
yields aer 5.0 h were 45.4% and 48.9% (x ¼ 0.33) and 87.4%
and 88.0% (x ¼ 0.86), respectively. Compared with that under
2
5 C were determined using solvatochromic dyes as probes.
The P parameter is calculated based on eqn (1), where lmax,EMCPI
is the wavelength corresponding to the absorption maximum of
EMCPI in the binary IL mixtures (see Table 1). The a and
b parameters are calculated based on eqn (2)–(4), where
nmax,DENA and nmax,NA are the wavenumbers converted based on
the absorption maxima of DENA and NA in binary IL mixtures
33,34
(see Table 1).
600 rpm, further increase of stirring speed could not enhance
the HMF formation rate signicantly. It follows that without
stirring, the viscosity of the media has signicant negative effect
(2) on the fructose dehydration due to the mass transfer resistance.
P ¼ 28591/lmax,EMCPI
p* ¼ 0.314 ꢂ (27.52 ꢀ nmax,DENA
(1)
)
18786 | RSC Adv., 2018, 8, 18784–18791
This journal is © The Royal Society of Chemistry 2018