Gas-expanded liquids (GXLs) are a new and benign class of pressure-tunable liquid solvents which show tremendous promise as the next sustainable processing medium. In order to realize the potential of GXLs fully, it is necessary to elucidate their cybotactic region and gain an understanding of where properties are different in the bulk and micro-scales and how local structure and order affect both reactions and separations. This work explores the cybotactic region of GXLs and probes the existence and implications of those differences. This study is started by exploring the cybotactic region of ambient liquid mixtures. Thermodynamic models based on intermolecular forces are used to predict the solubility of multi-functional solids in a variety of solvent mixtures. While this part does not lend any insight into GXLs directly, it acts as a stepping stone in both understanding the intermolecular forces that govern the cybotactic region and by opening the gateway to studying solid solubility in GXLs. The rest of the study focuses on the differences between bulk and local properties of GXLs. Different probes of polarity in the cybotactic region are compared and the solute dependence of the local structure is explored. Bulk transport properties are measured with different probes in an effort to see if molecular interactions play a role in governing diffusion processes in GXLs.

Sustainable technologies are vital to reducing the environmental impact of chemical enterprises. Solvents are often seen as just a medium in which a reaction takes place; however they can also play a dominant role in the overall toxicity of a typical pharmaceutical/fine chemicals batch chemical operation. Further, careful solvent selection for a reaction may also lead to more facile separation and purification of products, thus reducing the overall cost of a chemical process. This thesis presents an environmentally benign processing technique for sustainable biocatalytic reactions coupled with facile built-in separation. An organic aqueous tunable solvent (OATS) system allows access to a hydrophobic substrate which is transformed with a homogeneous enzymatic catalyst in a single liquid phase. Subsequent CO2 addition produces a biphasic mixture where the hydrophobic product partitions preferentially into the organic rich phase for separation while the hydrophilic enzyme catalyst partitions into the aqueous rich phase, where it is recyclable. Processing parameters in OATS systems are discussed and an overall product recovery of 80% is observed after six reaction cycles. Additionally, greater than 99% enantiomeric excess (ee) is shown for catalyzed hydrolysis of rac-1-phenylethyl acetate with Candida antarctica lipase B (CAL B) both before and after CO2-induced separation.

Solvent selection is an important factor in chemical process efficiency, profitability, and environmental impact. Prediction of solvent phase behavior will allow for the identification of novel solvent systems that could offer some economic or environmental advantage. A modified cohesive energy density model is used to predict the solid-liquid-equilibria for multifunctional solids in pure and mixed solvents for rapid identification of process solvents for design of crystallization processes. Some solubility data at several temperatures are also measured to further test the general applicability of the model. Gas-expanded liquids have potential environmentally advantageous applications as pressure tunable solvents for homogeneous and heterogeneous catalytic reactions and as novel solvent media for anti-solvent crystallizations. The phase behavior of some carbon dioxide/organic binary systems is measured to provide basic process design information. Solvent selection is also an important factor in the anti-solvent precipitation of solid compounds. The influence of organic solvent on the solid-liquid equilibria for two solid pharmaceutical compounds in several carbon dioxide expanded solvents is explored. A novel solvent system is also developed that allows for homogeneous catalytic reaction and subsequent catalyst sequestration by using carbon dioxide as a miscibility switch. The fundamental biphasic solution behavior of some polar organics with water and carbon dioxide are investigated.

The work conducted in this thesis is two-fold. First, binary vapor liquid equilibria of several solvent/CO2 systems are measured at 40 ?? The systems analyzed are all gas-expanded liquids (GXLs) characterized with a Jerguson Cell apparatus. A Jerguson cell is a windowed pressure vessel that allows one to measure the height of the condensed liquid. Using this height and the known overall contents in the cell, one can calculate the liquid composition without using any external sampling. Secondly, this same setup is attached to a sampling system, and solid solubility (fractional crystallization) is measured for various GXL systems. The CO2 acts as an antisolvent in what is commonly known as a gaseous antisolvent (GAS) system. Essentially, this work shows that expansion of the tested solvents with CO2 will cause the precipitation of the solid solute. This work also analyzes the affect two solutes have on each other in a quaternary GAS system. Gas-expanded liquids combine desirable gaseous properties and liquid properties to yield a very useful solvent for many applications. An advantage of GXLs is that a relatively small change in pressure or temperature can greatly affect the solvation properties. The tunability of GXLs increases as the amount of the gas (usually CO2) increases in the liquid phase. With the benign chemical nature and environmental impact of CO2 processing, GXLs and supercritical fluids (SCFs) have garnered a lot of attention for industry and academia. Supercritical fluids in this work refer to pure CO2 above its critical temperature and pressure.

Progress in the microelectronics industry is driven by smaller and faster transistors. As feature sizes in integrated circuits become smaller and liquid chemical waste becomes an even greater environmental concern, gas expanded liquids (GXLs) may provide a possible solution to future device fabrication limitations relative to the use of liquids. The properties of GXLs such as surface tension can be tuned by the inclusion of high pressure gases; thereby, the reduced surface tension will allow penetration of cleaning solutions into small features on the nanometer scale. In addition, the inclusion of the gas decreases the amount of liquid necessary for the photoresist and etch residue removal processes. This thesis explores the role of CO2-based GXLs for photoresist and etch residue removal. The gas used for expansion is CO2 while the liquid used is methanol. The cosolvent serving as the removal agent is tetramethyl ammonium hydroxide (TMAH) which upon reacting with CO2 becomes predominantly tetramethyl ammonium bicarbonate (TMAB).

Gas-expanded liquids (GXLs) are novel and environmentally benign solvent systems with applications in reactions, separations, nanotechnology, drug delivery, and microelectronics. GXLs are liquid mixtures consisting of an organic solvent combined with a benign gas, such as CO2, in the nearcritical regime. In this work, molecular dynamics simulations have been combined with experimental techniques to elucidate the cybotactic region or local environment in gas-expanded liquids. Molecular dynamics simulations show clustering of methanol molecules in carbon dioxide-methanol mixtures. This clustering was not observed in carbon dioxide-acetone mixtures. Furthermore, addition of carbon dioxide enhances diffusivity of solutes in gas-expanded media as shown by both simulations and Taylor-Aris dispersion experiments. Finally, local structure and local compositions around pyrene in carbon dioxide-methanol and carbon-dioxide acetone were investigated using simulations and UV-vis spectroscopy.

Developing greener, more efficient, and less energy-intensive processes will lead the chemical industry into a more sustainable future. Gas-expanded liquids (GXLs) form a unique class of environmentally benign and tunable solvents that can be used in a variety of applications. Through the series of studies presented in this thesis, we have investigated both the properties and applications of GXLs. We have developed a more complete understanding of the interactions between the gas, the organic liquid, and solutes at the molecular level through kinetic and solvatochromic experiments. We have examined a Diels-Alder reaction and an SN2 reaction and have described the kinetic results in terms of intermolecular interactions and local composition enhancement. We have also demonstrated the use of Organic-Aqueous Tunable Solvents, a special case of GXLs, to recycle homogeneous hydroformylation catalysts. The results of this research can be used to guide future applications of GXLs as green reaction solvents.

Gas-expanded liquids (GXLs) are a unique class of tunable solvents with unlimited potential. A wide range of solvent properties and solvent interactions and complexes are possible by adjusting the amount of the gas component (in situ) or changing the organic liquid. Aside from solvent tunability, there are environmental and processing benefits to using GXLs. Organic solvent use is decreased, the gas component can be vented off facile separations, and the gas can act as an antisolvent for selective solute precipitation. As a result there are numerous reaction and extraction schemes and materials processing applications that could benefit from GXL use. Unfortunately, important molecular-level details that can drive a chemical process are largely unknown and limit GXL use in industrial and specialty applications. The work presented in this uses a synergistic study of experiments and computer simulations to explore solvation processes and molecular interactions in GXLs and the effects on macroscopic observables like spectroscopy, transport, and reactions. Steady-state solvation of a laser dye is studied with spectroscopy (UV/vis and fluorescence) and molecular dynamics simulations (MD). Both experiment and theory show that organic enrichment occurs in the vicinity of the solute called the cybotactic region. Subsequently, the solvent dynamics arising by electronically perturbing the solute are studied with MD simulation. Unexpected dynamics are observed and are dependent on the organic component and gas composition. The diffusion of heterocyclic compounds is studied with MD simulations and compared to the Taylor-Aris diffusion study of former group members. The experiments and simulations do not agree, but solvent structures obtained by simulation are shown to provide valuable insight into solvent-dependent absorption spectroscopy, or solvatochromism. Finally, dissociation constants of alkylcarbonic acids that form in situ in CO2/alcohol mixtures are presented from spectroscopic measurements. Spectroscopic techniques to measure dissociation constants are well known; however, the high-pressure and multiple equilibria associated with alkylcarbonic acids hinder straight-forward measurement and analysis.

The development of structured macroporous hydrogels are of great interest in many industries due to their high permeabilities, large surface areas and large pore volumes. In drug delivery and wound healing applications, these macropores may theoretically be utilized as large drug reservoirs to deliver anti-inflammatory drugs to a wound site, while simultaneously absorbing exudate and maintaining a hydrated environment in which the wound may heal. However, current methods of generating macroporous structured hydrogels are low-throughput, expensive, and require the use of organic solvents, salts, and other additives that are difficult to remove from the crosslinked hydrogel scaffold. In contrast, the Pressurized Gas eXpanded liquid (PGX) processing technology, patented by the University of Alberta and licensed for all industrial applications by Ceapro Inc., has been shown to generate purified and exfoliated biopolymer scaffolds in a less expensive and more efficient way. Herein, the tunability of the PGX processing method was investigated in depth, varying solvent/anti-solvent ratios, nozzle mixing volume, polymer molecular weight, and polymer concentration to examine the resulting effects on produced polymer morphologies. PGX-processed chitosan and alginate scaffolds were stabilized as bulk hydrogels through post-processing crosslinking methods using anti-solvents, solid-state chemistries, and/or rapid gelation kinetics. The mechanical strength, swelling/degradation kinetics, affinity for protein uptake, and cytotoxicity of these stabilized scaffolds were subsequently examined and compared to hydrogels produced without the use of PGX processing. Furthermore, in situ crosslinking methods were explored, in which alginate and poly(oligoethylene glycol methacrylate) polymers were shown to form stable aerogels during the standard PGX processing method. Finally, the PGX apparatus was reconfigured to enable the impregnation of a model hydrophobic drug into pre-processed polymer scaffolds via circulation of supercritical CO2. The total loading was calculated and the release kinetics from loaded-scaffolds examined. In conclusion, this work outlines a novel method of creating structured macroporous hydrogels from PGX processed biopolymers with the potential to provide improved drug loadings and sustained release profiles. It is expected that this work will provide a basis for a great deal of research into the further stabilization of scaffolds for use in other applications, the investigation of a larger range of bioactive molecules for impregnation and release, and the exploration of PGX hydrogel scaffolds for in vivo wound healing. / Thesis / Master of Applied Science (MASc)

The focus of this research was to improve the sustainability of various processes by employing tunable solvents, switchable solvents, and catalysis. In Chapter 2, we report applications of tunable solvents to metal and enzyme catalyzed reactions of hydrophobic substrates. Tunable solvents are defined as solvent that change properties rapidly but continuously upon the application of an external physical stimulus and we utilize these solvents to couple homogeneous reactions with heterogeneous separations. We developed organic-aqueous tunable solvents that utilize propane for efficient phase separation at moderate pressures around 1 MPa; for example the water contents in the propane-expanded THF is 3 wt% at 0.8MPa at 30°C. Also, we extended the use of CO2-organic-aqueous tunable solvents to a pharmaceutically-relevant reaction--the hydroformylation of p-methylstyrene. The homogeneous reactions provide fast rates with excellent yields. At 60°C, the reaction reaches completion after 180 minutes with 95% branched aldehyde yield. The CO2-induced heterogeneous separation of the product from the catalyst provides an efficient and simple way to remove 99% of the product, to retain 99.9% of catalyst, and to recycle the Rh-TPPMS catalyst for five consecutive reactions. In chapter 3, we investigated the use of reversible ionic liquids (RevILs) for synthesis of nanoparticles. RevILs are formed by the reversible reaction of compounds with basic nitrogen functionalities (molecular liquid) with CO2 at ambient pressure to form a liquid salt (ionic liquid). We demonstrated that RevILs form microemulsions that can be switched-on by bubbling CO2 and switched-off by heating. These microemulsions solubilize ionic compounds such as chloroauric acid. We utilized these microemulsions as a template for controlled synthesis of gold nanoparticles. With 2-component RevILs, [TMBGH]+[O2COCH3]-/N-propyl-octylsulfonamide/hexane were used to form particles in the size range of 6-20 nm with an average particles size of 11.4±3.3. With 1-component RevILs, (3-aminopropyl)-tripropylsilane was used to prepare semi-spherical gold particles with an average size of about 20nm. The 1-component RevILs systems provide a simpler method to form microemulsions when compared to the 2-componenet RevILs systems since they eliminate the need for alcohols and surfactants. In chapter 4, we developed a catalyst that efficiently decomposes hydrazine to selectively produce ammonia. This enables the use of the chemical propulsion hydrazine for electric propulsion as well. We prepared nickel, copper, cobalt, ruthenium, rhodium, and iridium nanoparticles that were supported on silica and we tested these silica-supported metals for the decomposition of hydrazine. To study the catalytic activity, we designed and constructed a continuous flow reactor. The results show that nano-nickel supported on silica is the most active and selective catalyst with 100% conversion of hydrazine and 94±3% yield of ammonia.