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Science 20 December 1996: Vol. 274. no. 5295, pp. 2049 - 2052 DOI: 10.1126/science.274.5295.2049
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Reports
Design of Nonionic Surfactants for Supercritical Carbon
Dioxide
J. B. McClain,
D. E. Betts,
D. A. Canelas,
E. T. Samulski,
J. M. DeSimone,
*
J. D. Londono,
H. D. Cochran,
G. D. Wignall,
*
D. Chillura-Martino,
R. Triolo
Interfacially active block copolymer amphiphiles have been
synthesized and their self-assembly into micelles in supercritical carbon dioxide (CO2) has been demonstrated with small-angle
neutron scattering (SANS). These materials establish the design
criteria for molecularly engineered surfactants that can stabilize and disperse otherwise insoluble matter into a CO2 continuous
phase. Polystyrene-b-poly(1,1-dihydroperfluorooctyl
acrylate) copolymers self-assembled into polydisperse core-shell-type
micelles as a result of the disparate solubility characteristics of the
different block segments in CO2. These nonionic surfactants
for CO2 were shown by SANS to be capable of emulsifying up
to 20 percent by weight of a CO2-insoluble hydrocarbon into
CO2. This result demonstrates the efficacy of
surfactant-modified CO2 in reducing the large volumes of
organic and halogenated solvent waste streams released into our
environment by solvent-intensive manufacturing and process industries.
J. B. McClain, D. E. Betts, D. A. Canelas, E. T. Samulski, J. M. DeSimone, Department of Chemistry, University of North Carolina, CB
3290, Venable and Kenan Laboratories, Chapel Hill, NC 27599, USA.
J. D. Londono, H. D. Cochran, G. D. Wignall, Oak Ridge National
Laboratory, Oak Ridge, TN 37831, USA.
D. Chillura-Martino and R. Triolo, Departimento di Chimica
Fisica, University of Palermo, 90123 Palermo, Italy.
*
To whom correspondence should be addressed.
More than 30 billion pounds of organic and
halogenated solvents are used worldwide each year as process aids,
cleaning agents, and dispersants (1), and solvent-intensive
industries are considering alternatives that can reduce or eliminate
the negative impact that solvent emissions can have on the environment.
Because of its low cost, wide availability, and environmentally and
chemically benign nature (2, 3), CO2 is an
attractive solvent alternative for a wide variety of chemical and
industrial processes. Although CO2, in both its liquid and
supercritical (sc) states, readily dissolves many small molecules
(4), it is a very poor solvent--at easily accessible
conditions (temperature <100°C and pressure <300 bar)--for many
substances, and commercial applications of pure CO2 as a
solvent have been infrequent. Materials that have disappointingly low
solubilities in pure CO2 include most polymers [except
amorphous or low-melting fluoropolymers and silicones (2, 4,
5)], waxes, heavy oils, machine-cutting fluids, solder fluxes,
photoresists, proteins, salts, and metal oxides. The design and
characterization of surfactants that enhance the solubilizing
properties of CO2 is therefore crucial for its widespread application.
Block and graft copolymers composed of chain segments with
dissimilar solubility characteristics self-assemble into well-defined structures when placed in a medium that is a good solvent for one of
the segments (the lyophilic segment) and a poor solvent for the other
segment (the lyophobic segment) (6, 7, 8, 9). These nonionic
surfactants are typified by micelles or more complex aggregates in
which the lyophobic segments form a core surrounded by a shell of the
highly solvated lyophilic segments that extend into the continuous
phase (6). The core regions of such micelles are
technologically useful, as they are capable of emulsifying otherwise
insoluble materials into a microphase-separated environment within a
preferred continuous solvent phase (9). Here, we report the
direct structural characterization by SANS of well-defined, spherical
micelles resulting from a series of molecularly engineered block
copolymer surfactants in scCO2. Our results also
demonstrate the efficacy of these surfactants in emulsifying insoluble
solutes into CO2. This development may ultimately enable
surfactant-modified CO2 to be used as a replacement for conventional solvent systems currently used in manufacturing and service industries, such as precision cleaning (metal finishing, microelectronics, optics, or electroplating), medical device
fabrication, and dry (garment) cleaning, as well as in the chemical
manufacturing and coating industries.
Several laboratories have demonstrated progress in the micellization of
aqueous and polar materials in many dense sc fluids including alkanes,
chlorofluorocarbons, hydrofluorocarbons, and CO2
(10, 11, 12, 13, 14, 15). However, success in designing generic surfactants
for CO2 has been hindered by the challenge of identifying
lyophilic segments for CO2. A promising lead for the design
of highly effective surfactants for CO2 arose out of two
related discoveries: (i) that CO2 is thermodynamically a
good solvent for fluorinated acrylate polymers [positive second virial
coefficient (13, 16)], and (ii) that these same polymers could be synthesized under homogeneous conditions in CO2
(17). Therefore, the fluorinated acrylate segment can be
considered as a vehicle to bring insoluble components into
CO2. Recent evidence has shown that fluoroacrylate polymers
could be used to bring hydrated, water-soluble polyethylene glycol
segments into CO2 (10).
The block copolymers that we have molecularly engineered to be
interfacially active in CO2 are composed of a
CO2-insoluble polystyrene (PS) segment and a
CO2-soluble poly(1,1-dihydroperfluorooctyl acrylate) (PFOA)
segment. Because of these solubility differences in CO2,
such block copolymers are predisposed to self-assemble spontaneously
into micellular structures in CO2. We synthesized PS-b-PFOA diblock copolymers (Fig. 1) with
the "iniferter" technique developed by Otsu (18, 19, 20). We
first synthesized the lyophobic PS segment of the surfactant by using
tetraethylthiuram disulfide as the initiator. We determined the
functionality of the telechelic PS segment by using ultraviolet-visible
spectroscopy, and the number-average molecular weight
( Mn ) was determined from gel permeation
chromatography. This functionalized PS segment was then used as a
macroinitiator in the photopolymerization of the second monomer, FOA,
to form the second lyophilic segment of the diblock copolymer (for
simplicity, we will henceforth refer to the block copolymers by listing
Mn for each block,
Mn styrene-b- Mn FOA).
Fig. 1.
PS-b-PFOA synthesis and structure
(18). Rf = CH2(CF2)6CF3 and
contains 25% CF3 branches per molecule.
[View Larger Version of this Image (18K GIF file)]
During the past two decades, SANS has emerged as a powerful technique
for studying the self-assembly of amphiphiles in aqueous media
(21). Experiments to determine the characteristics of PS-b-PFOA micelles in scCO2 were performed on
the W. C. Koehler 30-m SANS facility at the Oak Ridge National
Laboratory (22). The neutron wavelength was 4.75 Å ( / 5%), and the sample detector distance ranged from 6.3 to 10 m, resulting in a range of momentum transfer
0.006 < Q = 4  1 sin < 0.1 Å 1, where 2 is the angle of scatter. Instrumental
procedures and calibration as well as the procedure for SANS
measurements from scCO2 systems have been described
(23, 24, 25, 26, 27).
Neutron scattering curves (Fig. 2) from
PS-b-PFOA in CO2 were fitted to a spherical
"core plus shell" model based on a solid PS core and a
uniform-thickness shell containing PFOA chains swollen by
CO2 solvent molecules. Parameters of the model include the aggregation number Nagg (the number of block
copolymer units forming each micelle), the number of CO2
molecules NCO2 (that swell the PFOA corona
per FOA unit), and the polydispersity parameter Z (related
to the variance of the Schultz distribution of the particle sizes:
increasing polydispersity with decreasing Z). The radius of
the core (Rcore) and of the total particle
(Rtotal) can be easily derived from these
parameters. If we assume no orientational correlations, the coherent
differential cross section,
d (Q)/d , for such a model is
given by
|
(1)
|
(28), where
Np is the number density of particles,
S(Q) is the structure function arising from interparticle
scattering, B is the background, and F(Q) is the
scattering amplitude of the spherical particle.
Fig. 2.
Plot of
d (Q)/d versus Q
for 3.7k-b-16.7k
PS-b-PFOA in scCO2 (65°C, 340 bar) with
fitting to a monodisperse and polydisperse core-shell
model.
[View Larger Version of this Image (36K GIF file)]
A series of PS-b-PFOA surfactants having differing lyophilic
PFOA segment lengths and lyophobic PS segment lengths were dissolved in
CO2 at 65°C and 340 bar (density = 0.842 g
cm 3) and characterized by SANS (Table 1).
If we rely on calibrated SANS curves, the fit of the scattering results
to the core-shell model indicates that the block copolymers
self-assemble into spherical core-shell structures (see Fig. 2). A
systematic increase of the PFOA block length (the first three entries
in Table 1) results in a variation of only the "shell-dependent"
properties: an increase in Rtotal and a decrease
in the swelling of the corona, evident in
NCO2. The "core-dependent" properties,
Rcore and Nagg, remain essentially constant for surfactants of constant PS length. Control of
the core-dependent properties is evident in the smooth increases in
Rcore with increasing PS segment length. The
behavior of PS-b-PFOA surfactants in CO2 follows
the expected scaling laws of micelles composed of block copolymers with
variable segment lengths in traditional solvents (29, 30).
The solvent strength of scCO2 is easily tunable with
changes in the system density (directly related to temperature and
pressure) (2, 13, 16, 31). Thus, the association of
amphiphiles in CO2 should be strongly dependent on the
CO2 density because of changes in polymer solubility as a
function of solvent quality. As the density of CO2 is
increased (32), the solvation of both segments becomes
greater, which decreases aggregation and creates more dynamic micelles.
Thus, we anticipate the existence of a critical micelle density,
analogous to a critical micelle concentration, to describe the
phenomenon of unimer-to-aggregate transitions for amphiphilic materials
in sc fluids with changing solvent (quality) density. Table
2 shows the effect of two experimental
conditions--65°C, 340 bar, = 0.842 g cm 3 and
40°C, 340 bar, = 0.934 g cm 3 (31)--on
the association of PS-b-PFOA surfactants. With increasing solvent strength (density), smaller and more polydisperse micelles are
evident, especially for surfactants with a higher PS/PFOA ratio. When
the PFOA segment length is increased to 135 repeat units, the
micelles are essentially unaffected by CO2 density over
this range of conditions.
We demonstrated the ability of a PS-b-PFOA micellar solution
in CO2 to emulsify CO2-insoluble materials by
adding model CO2-insoluble hydrocarbon oligomers (500 g per
mole of oligomers of both deuterated and hydrogenated PS, referred to
as D-oligomer and H-oligomer, respectively) to the system and
monitoring by SANS (33). We used both H- and D-oligomer
samples to take advantage of different neutron scattering contrasts and
to quantify the fraction of oligomer inside the micelle core versus
oligomer free in solution or stabilized by free surfactant
(25). SANS characterization of micelles of PS-b-PFOA surfactants in CO2 (65°C, 340 bar,
= 0.842 g cm 3) with added H-oligomer and D-oligomer
display stabilization of >99% of the added oligomer into the core of
the micelle. The micellar core volume increases with added H-oligomer
and D-oligomer as a function of oligomer concentration for the
3.7k-b-39.8k surfactant
(20) (Fig. 3). By a comparison of the
unswollen surfactant micelles with the swollen system containing added
oligomer in Table 3, we see an approximately eightfold
increase in the volume of the micelle core with the addition of up to
20% (w/w) oligomer.
Fig. 3.
The swelling of
3.7k-b-39.8k surfactant micelles in
CO2 (65°C, 340 bar, = 0.842 g cm 3) with
PS oligomers. Surfactant concentration = 4% (w/v).
[View Larger Version of this Image (22K GIF file)]
The density of CO2, over the same range studied for
unswollen aggregates, seems to have little effect on the structure of oligomer-swollen micelles (Table 3). Highly swollen systems were observed for three different surfactants at CO2 densities
ranging from 0.842 to 0.934 g cm 3 with less than 5%
change in the dimensions or characteristics of the micelles. This is
very different from the association behavior of similar unswollen
surfactant micelles. In the oligomer-swollen system, the surfactant
molecules are forced to an interface between insoluble PS oligomer and
CO2. This effect results in diminished changes in the
overall structural dimensions with solvent strength so long as
CO2 remains a good solvent for the PFOA shell segments. Earlier work has shown that PFOA is in a thermodynamically favorable solvent at both densities (16) and therefore retains its
propensity to stabilize a larger CO2-insoluble core.
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Summary of data from the synthesis of PS-b-PFOA
diblock copolymers: Telechelic PS:
Mn = 3.7 kg mol 1, polydispersity index (PDI) = 1.6, functionality = 1.6;
3.7k-b-16.6k diblock copolymer:
Mn = 20.4 kg mol 1, 49.4 mol
% styrene, and 50.6 mol % FOA;
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% styrene, and 71.1 mol % FOA;
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The model CO2-insoluble oligomers were PS (500 g
mol
1) made by living anionic polymerization. Also, to
simplify the experimental system and to ensure minimal free oligomer
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extracted oligomer samples in advance with CO2 at 50°C
and 400 bar.
-
The research at the University of North Carolina was supported
by the Environmentally Benign Chemical Synthesis and Processing
Initiative of NSF and the U.S. Environmental Protection Agency; the
Presidential Faculty Fellowship Program (J.M.D.); and the Consortium
for the Synthesis and Processing of Polymeric Materials at the
University of North Carolina (sponsored by Air Products and Chemicals,
Bayer, B. F. Goodrich, DuPont, Eastman Chemical, General Electric,
Hoechst-Celanese, and Xerox). The research at Oak Ridge National
Laboratory was supported by Laboratory Directed Research and
Development Program and the Division of Material Science, U.S.
Department of Energy, under contract DE-AC05-96OR22464 with Lockheed
Martin Energy Research Corp.
12 June 1996; accepted 25
September 1996
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