10 research outputs found
Surfactant-Free Polymerization Forming Switchable Latexes That Can Be Aggregated and Redispersed by CO<sub>2</sub> Removal and Then Readdition
Polystyrene latexes prepared using the bicarbonate salt
of initiator
2,2′-azobis[2-(2-imidazolin-2-yl)propane] via surfactant-free
emulsion polymerization can be aggregated using only argon and gentle
heat and redispersed using carbon dioxide and sonication. The bicarbonate
and hydrochloride salts of the initiator have similar thermal decomposition
behavior, but only the bicarbonate salt of 2,2′-azobis[2-(2-imidazolin-2-yl)propane]
can be switchable between ionic and nonionic forms by addition and
removal of CO<sub>2</sub>. Measurements of particle size and zeta
potential were used to study the aggregation and redispersion of the
latexes. The latex is aggregated by heating and bubbling with argon
to remove CO<sub>2</sub> and convert the active cyclic amidinium groups
to their neutral form. When treated with sonication and bubbling with
CO<sub>2</sub>, the aggregated polystyrene latex can be redispersed
successfully, as evidenced by restoration of the original latex particle
size and zeta potential from the large aggregated polymer particles.
This is the simplest method to date to prepare a redispersible latex
stabilized by CO<sub>2</sub>
Aryl Amidine and Tertiary Amine Switchable Surfactants and Their Application in the Emulsion Polymerization of Methyl Methacrylate
The switchability and bicarbonate formation of CO<sub>2</sub> triggered
aryl amidine and tertiary amine switchable surfactants have been investigated.
Despite the lower basicity of these compounds compared to alkylacetamidine
switchable surfactants, it was found that amidinium and ammonium bicarbonates
could be formed in sufficiently high enough concentrations to perform
emulsion polymerization of methyl methacrylate and stabilize the resulting
colloidal latexes. Particle sizes ranging from 80 to 470 nm were obtained,
and the effects of surfactant concentration, surfactant basicity,
initiator type, initiator concentration, and CO<sub>2</sub> pressure
on particle size and ζ-potential have been examined. Destabilization
of latexes is traditionally achieved by addition of salts, strong
acids for anionically stabilized latexes, or alkalis for cationically
stabilized latexes. However, with CO<sub>2</sub>-triggered switchable
surfactants, only air and heat are required to destabilize the latex
by removing CO<sub>2</sub> from the system and switching the active
amidinium or ammonium bicarbonate surfactant to a surface inactive
neutral compound. This process occurs much more rapidly in the case
of these less basic aryl amidine and tertiary amine based surfactants
compared to previously reported alkyl amidine surfactants
Shuttling Catalyst for Living Radical Miniemulsion Polymerization: Thermoresponsive Ligand for Efficient Catalysis and Removal
In this report, we
demonstrate the use of a thermoresponsive ligand
for the ruthenium-catalyzed living radical polymerization of butyl
methacrylate (BMA) in miniemulsion. A phosphine-ligand-functionalized
polyethylene glycol chain (PPEG) in conjunction with a Cp*-based ruthenium
complex (Cp*: pentamethylcyclopentadienyl) provided thermoresponsive
character as well as catalysis for living polymerization: the complex
migrated from the water phase to the oil phase for polymerization
upon heating and then migrated from the oil to water phase when the
temperature was decreased to quench polymerization. Consequently,
simple treatment (i.e., water washing or methanol reprecipitation)
yielded metal-free polymeric particles containing less than 10 μg/g
(by ICP-AES) of ruthenium residue
Microalgae Recovery from Water for Biofuel Production Using CO<sub>2</sub>‑Switchable Crystalline Nanocellulose
There is a pressing
need to develop efficient and sustainable approaches
to harvesting microalgae for biofuel production and water treatment.
CO<sub>2</sub>-switchable crystalline nanocellulose (CNC) modified
with 1-(3-aminopropyl)imidazole (APIm) is proposed as a reversible
coagulant for harvesting microalgae. Compared to native CNC, the positively
charged APIm-modified CNC, which dispersed well in carbonated water,
showed appreciable electrostatic interaction with negatively charged Chlorella vulgaris upon CO<sub>2</sub>-treatment.
The gelation between the modified CNC, triggered by subsequent air
sparging, can also enmesh adjacent microalgae and/or microalgae-modified
CNC aggregates, thereby further enhancing harvesting efficiencies.
Moreover, the surface charges and dispersion/gelation of APIm-modified
CNC could be reversibly adjusted by alternatively sparging CO<sub>2</sub>/air. This CO<sub>2</sub>-switchability would make the reusability
of redispersed CNC for further harvesting possible. After harvesting,
the supernatant following sedimentation can be reused for microalgal
cultivation without detrimental effects on cell growth. The use of
this approach for harvesting microalgae presents an advantage to other
current methods available because all materials involved, including
the cellulose, CO<sub>2</sub>, and air, are natural and biocompatible
without adverse effects on the downstream processing for biofuel production
Compositional analysis of lignocellulosic biomass: conventional methodologies and future outlook
<p>The composition and structural properties of lignocellulosic biomass have significant effects on its downstream conversion to fuels, biomaterials, and building-block chemicals. Specifically, the recalcitrance to modification and compositional variability of lignocellulose make it challenging to optimize and control the conditions under which the conversion takes place. Various characterization protocols have been developed over the past 150 years to elucidate the structural properties and compositional patterns that affect the processing of lignocellulose. Early characterization techniques were developed to estimate the relative digestibility and nutritional value of plant material after ingestion by ruminants and humans alike (e.g. dietary fiber). Over the years, these empirical techniques have evolved into statistical approaches that give a broader and more informative analysis of lignocellulose for conversion processes, to the point where an entire compositional and structural analysis of lignocellulosic biomass can be completed in minutes, rather than weeks. The use of modern spectroscopy and chemometric techniques has shown promise as a rapid and cost effective alternative to traditional empirical techniques. This review serves as an overview of the compositional analysis techniques that have been developed for lignocellulosic biomass in an effort to highlight the motivation and migration towards rapid, accurate, and cost-effective data-driven chemometric methods. These rapid analysis techniques can potentially be used to optimize future biorefinery unit operations, where large quantities of lignocellulose are continually processed into products of high value.</p
Polymerization Induced Self-Assembly of Alginate Based Amphiphilic Graft Copolymers Synthesized by Single Electron Transfer Living Radical Polymerization
Alginate-based
amphiphilic graft copolymers were synthesized by
single electron transfer living radical polymerization (SET-LRP),
forming stable micelles during polymerization induced self-assembly
(PISA). First, alginate macroinitiator was prepared by partial depolymerization
of native alginate, solubility modification and attachment of initiator.
Depolymerized low molecular weight alginate (∼12 000
g/mol) was modified with tetrabutylammonium, enabling miscibility
in anhydrous organic solvents, followed by initiator attachment via
esterification yielding a macroinitiator with a degree of substitution
of 0.02, or 1–2 initiator groups per alginate chain. Then,
methyl methacrylate was polymerized from the alginate macroinitiator
in mixtures of water and methanol, forming poly(methyl methacrylate)
grafts, prior to self-assembly, of ∼75 000 g/mol and
polydispersity of 1.2. PISA of the amphiphilic graft-copolymer resulted
in the formation of micelles with diameters of 50–300 nm characterized
by light scattering and electron microscopy. As the first reported
case of LRP from alginate, this work introduces a synthetic route
to a preparation of alginate-based hybrid polymers with a precise
macromolecular architecture and desired functionalities. The intended
application is the preparation of micelles for drug delivery; however,
LRP from alginate can also be applied in the field of biomaterials
to the improvement of alginate-based hydrogel systems such as nano-
and microhydrogel particles, islet encapsulation materials, hydrogel
implants, and topical applications. Such modified alginates can also
improve the function and application of native alginates in food and
agricultural applications
4‑Dimensional Modeling Strategy for an Improved Understanding of Miniemulsion NMP of Acrylates Initiated by SG1-Macroinitiator
For the first time, a kinetic model
considering four-dimensional Smith–Ewart equations is presented
to simultaneously calculate the time evolution of the conversion,
number-average chain length, dispersity, end-group functionality (EGF),
and short chain branching (SCB) content for the miniemulsion NMP of <i>n</i>-butyl acrylate (nBuA), initiated by poly(nBuA)-(<i>N</i>-<i>tert</i>-butyl-<i>N</i>-(1-diethylphosphono-2,2-dimethylpropyl)
at 393 K ([nBuA]<sub>0</sub>:[poly(nBuA)-SG1]<sub>0</sub> = 300). On the basis of literature
kinetic and diffusion parameters, model analysis reveals that backbiting
cannot be neglected for an accurate description of the NMP characteristics,
despite the low number of SCBs formed per chain (ca. 2) and that the
small loss of EGF at low conversions is mainly caused by chain transfer
to monomer. SG1 partitioning (partitioning coefficient Γ = 50)
between the organic and aqueous phase increases the dispersity and
polymerization rate at low particle diameters (dp < ca. 50 nm)
with a limited effect on the EGF profile. However, the extent of these
increases is very sensitive to the Γ value, highlighting the
relevance of its accurate experimental determination in future studies
Anionic Polymerizable Surfactants from Biobased ω‑Hydroxy Fatty Acids
Biobased ω-hydroxytetradecanoic
acid prepared via an efficient
yeast-catalyzed ω-hydroxylation reaction was converted by a
one-step reaction to the polymerizable surfactants ω-acryltetradecanoic
acid (MA-1) and ω-maleate tetradecanoic acid (MA-2). MA-1 is
a single polar-headed surfactant, whereas MA-2 is a bolaamphiphile
with carboxylic acid polar groups at both chain ends. MA-1 gave a
distinct critical micelle concentration (cmc) at 253 mg/L, whereas
for MA-2, the surface tension decreased monotonically and a distinct
cmc was not observed even up to 1800 mg/L. Experimental determination
of the reactivity ratios for MA-1 and MA-2 with styrene showed that
for MA-1 copolymers that approximate random structures were formed
while MA-2 tends to form copolymers with an alternating nature. Emulsion
polymerizations conducted with varying amounts of MA-1 and MA-2 (1–10
wt % with respect to styrene) gave colloidally stable latexes with
particle sizes ranging from 52 to 155 nm. In emulsion polymerizations
using either MA-1 or MA-2 at more than 5 wt % to monomer, a linear
increase in latex particle volume with conversion was observed and
the particle number remained constant, establishing that the polymerizations
proceeded without significant aggregation or secondary particle nucleation.
Potentiometric titration and <sup>1</sup>H NMR were used to measure
MA-1 and MA-2 conversions during polymerization as well as how the
surfactants were distributed between the particle surface, aqueous
phase, and particle interior. Observed differences were rationalized
based on the comparative structures of MA-1 and MA-2 and their corresponding
partitioning behavior
Amphiphilic Block Copolymers as Stabilizers in Emulsion Polymerization: Effects of the Anchoring Block Molecular Weight Dispersity on Stabilization Performance
Poly(sodium acrylate)-<i>b</i>-polystyrene block copolymers were employed as stabilizers in the
emulsion polymerization of styrene. Previous work by our group has
shown that the molecular weight dispersity of the stabilizing block
is an important design parameter of block copolymer stabilizers; herein,
the molecular weight dispersity of the anchoring polystyrene block, <i>Đ</i><sub>PS</sub>, was investigated. Stabilization performance
was evaluated by the critical aggregation concentration, aggregation
number, and surface activity of the block copolymers and the size,
distribution, and zeta potential of the polystyrene latex particles.
It was observed that <i>Đ</i><sub>PS</sub> had a strong
effect on aggregation number, which led to a change in the number
of latex particles in the seeded emulsion polymerization of styrene.
Surface activity decreased with increasing <i>Đ</i><sub>PS</sub> due to a greater diversity of copolymer compositions,
supporting the idea that copolymers of different composition play
different roles in the stabilization of an emulsion. The performance
of block copolymer stabilizers, evaluated by the stability and size
distribution of latex particles, was indistinguishable over the range
of <i>Đ</i><sub>PS</sub> studied; narrow stabilizer
molecular weight distributions were not necessary for satisfactory
performance
ARGET ATRP of Butyl Methacrylate: Utilizing Kinetic Modeling To Understand Experimental Trends
A comprehensive kinetic Monte Carlo
(kMC) model is used to interpret and better understand the results
of a systematic experimental investigation of activators regenerated
by electron transfer atom transfer radical polymerization (ARGET ATRP)
of butyl methacrylate (BMA) using Sn(EH)<sub>2</sub> as reducing agent,
ethyl 2-bromoisobutyrate (EBiB) as ATRP initiator, and CuBr<sub>2</sub>/TPMA (TPMA: tris[(2-pyridyl)methyl]amine) as deactivator. The model
demonstrates the importance of slow initiation, with distinct activation
and deactivation rate coefficients for the initiator and polymeric
species required to match the experimental data. In addition, the
model incorporates a second reduction step for the reducing agent
and accounts for diffusional limitations on chain-length-dependent
termination. The effect of temperature on the slow ATRP initiation
is limited, and a sufficiently high initial reducing agent concentration
is crucial to obtain a high conversion, although achieved at the expense
of decreased end-group functionality