APREPRINT - OCTOBER 27, 2022
operation of the solvent recovery processes. Therefore, to respect the principles of green-chemistry, the search for an
alternative is necessary. [3, 4]
Switchable Hydrophilicity Solvents (SHSs) constitute a family of solvents that exhibits hydrophobic (immiscibility
with water) properties in their neutral form. However, when ionized (for example by contact with an acid such as
CO2
for a cationic SHS) they become hydrophilic (miscible with water). This switching process is also reversible, and SHS
can be "switched" back to their hydrophobic form by, for example, removing
CO2
by flushing with
N2
. [
5
] [
6
] The
mechanism behind this switching process is the acid-base chemical reaction described below:
SHSorg + H+
aq −−*
)−− SHSH+
aq
For the
CO2
trigger, it is the dissolution of
CO2
and the acidification of water that allows the SHS to switch. This
switching behavior can more generally be observed with other kinds of acid. [7, 8, 9]
SHSs present an economically viable and green alternative to VOCs due to the simplicity to "switch on" and "off" the
hydrophobicity of the solvent with high recoverability coming from the "switching off" process. Potential applications
of SHS have already been demonstrated in soybean oil extraction[
10
] [
11
], separation of bitumen from oil sands[
12
],
biofuel extraction from microalgae [
13
,
14
], polystyrene foam [
15
] and multi-layer packaging recycling[
16
,
17
],
liquid-liquid micro-extraction (SHS-LLME) for analytical chemistry [18, 19] or latex formation [20].
In latex formation, binary drops of SHS and dissolved polymer are made to deposit solid polymer particles by switching
off SHS hydrophobicity in an aqueous environment. A typical example is the formation of polystyrene particles by the
dissolution of N-N Dimethylcyclohexylamine (DMCHA) from binary drops of DMCHA and polystyrene. When the
DMCHA-polystyrene drop contacts an acidic phase, DMCHA reacts with protons producing the protonated counterpart
DMCHAH+ following the biphasic reaction below:
DMCHAorg + H+
aq )−
−−*DMCHAH+
aq
The produced DMCHAH
+
is solubilized in the aqueous environment at the surface of the binary drop. In this way,
the DMCHA in the DMCHA-polystyrene drop begins to dissolve into the aqueous phase and the drop shrinks with
time. Subsequently, the insoluble polystyrene part of the drop is left behind and forms a solid polystyrene particle.
Understanding of the dissolution dynamics of the binary drop is required to obtain the desirable morphology, size, and
properties of final polymer particles.
The dissolution process of drops with a low solubility in their environment is a problem that has already been studied
previously. In an early work, Duncan et al [
21
] showed experimentally that the diffusion-driven model for bulk
bubbles in an undersaturated liquid phase developed by Epstein [
22
] could be also applied to dissolution of a free oil
microdroplet. The diffusion-driven model was further developed to describe the dissolution of a drop deposited on
a substrate (i.e. sessile drop) with effects of the drop geometry taken into account. [
23
] The lifetime of a dissolving
sessile drop in various modes such as constant contact radius, constant contact angle, stick-slide, or stick-jump modes
of the drop have been experimentally and theoretically studied.[24, 25, 26]
To add to the diffusion-driven dissolution, the influence of gravity-induced convection in the bulk liquid on the
dissolution process has also been shown to speed up the dissolution dynamics.[
27
]. More recently, the dissolution
process of multicomponent drops, as opposed to pure liquid drops, has been found to exhibit complex dynamics. The
components in the drop may undergo preferential dissolution [
28
], phase separation [
29
], or self-assembling [
30
]. For
instance, dissolution of polymer solution drops may lead to formation of polymer capsules [
31
,
32
,
33
,
34
], while
snowballs of graphene oxide may develop from dissolution of colloidal drops. [35] [36]
The dynamic of the switching SHS and corresponding solvent extraction process has previously been shown to be time
consuming, in some cases reaching hours [
6
]. It is therefore important to understand what conditions may possibly
shorten the switching-extraction time and minimize residual solvent in a cost-effective manner. In the extraction process
assisted by
CO2
-switching SHS, two steps may play a role: (1) the slow mass transfer of
CO2
gas into the aqueous
phase, followed by the chemical reactions of dissociation and hydrolysis of
CO2
to
HCO−
3
,
CO2−
3
and
H+
, and (2)
the liquid phase reaction (switching) of neutral SHS (hydrophobic form) and dissolution of switched SHS (hydrophilic
form) into the aqueous solution. In previous work by Han et al the acceleration of the switching-extraction dynamics
was studied using a microfluidic device. The improved specific interfacial area between the aqueous phase and
CO2
gas
accelerated the extraction process inside the microfluidic device. [
37
,
38
] However, to the best of our knowledge, there
is no quantitative understanding on the SHS dissolution dynamics of the reaction-induced mass transfer of the SHS, and
in-particular inside a liquid drop and its impact on the final morphology of the polymer particles post solvent extraction.
2