Thesis (Ph.D. 1974) from the Dept. of Physical and Inorganic Chemistry, University of Adelaide. / Reprints of 3 articles published by the author included in back of book.

Thesis (M. S.)--Materials Science and Engineering, Georgia Institute of Technology, 2008. / Committee Chair: Kenneth Gall; Committee Member: David Bucknall; Committee Member: Karl Jacob.

Thesis (M.S.)--University of Michigan, 1952.

Thesis (M.S.)--University of Wisconsin--Madison, 1983. / Typescript. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves 228-230).

No description available.

The objective of this study was to encapsulate cell lines that secrete marker proteins that cover a large molecular weight range (M^r from 45,000 to 300,000) and monitor the secretion of the marker proteins from alginate-poly-L-lysine-alginate (APA) microcapsules and hydroxyethyl methacrylatemethyl methacrylate (HEMA-MMA) thermoplastic capsules. Different parameters for the APA microcapsules, such as the duration of poly-L-lysine (PLL) and sodium citrate treatment, the initial cell density for encapsulation was studied, and their effects on secretion rate and cell proliferation were closely examined. Cell lines used for encapsulation secreted human growth hormone (hGH) (M^r 45,000), β-hexosaminidase (β-hexo.) (M^r 120,000) and β-glucuronidase (β-gluc.) (M^r 300,000). Monitoring the secretion rates, as well as the distribution of the marker proteins within the microcapsules following encapsulation enabled the permeability of the membrane to be assessed over one month in culture. Encapsulation of cell lines in both types of capsules was effective in producing viable cells capable of proliferating within a semi-permeable membrane. Encapsulating cells in single-coated APA microcapsules at 4°C, treated with 10 minutes PLL, 20 minutes sodium citrate and at a cell density of 2x10^6 cells/ml alginate was found to provide the most optimal conditions for prolonged viability of and stable secretion by the recombinant cells. Human growth hormone diffused readily across the capsule membrane into the culture media from both APA and HEMA-MMA capsules, at rates similar to the non-encapsulated cells. Human growth hormone did not accumulate in the intracapsular space in significant quantities. β-glucuronidase and β-hexosaminidase could diffuse across APA capsule membrane, but not across HEMA-MMA capsule membrane into surrounding media. β-glucuronidase secretion from APA microcapsules was 8-fold lower than non-encapsulated cells. β-hexosaminidase secretion from APA microcapsules was 4.5-fold lower than non-encapsulated cells. Slight retention of both β-glucuronidase and β-hexosaminidase was observed in the intracapsular space of APA capsules. HEMA-MMA capsules completely blocked the secretion of both β-glucuronidase and β-hexosaminidase out of the capsule. Massive accumulation of both kinds of secretory enzymes was found in the intracapsular space of HEMA-MMA capsules. This indicated APA microcapsules have a molecular weight cut-off of >300,000 whereas HEMA-MMA microcapsules have a molecular weight cut-off of <120,000. / Thesis / Master of Science (MS)

Environmentally friendly processing of materials is becoming an increasingly important consideration in a wide variety of emerging technologies. Polymer processing,in particular, has benefited tremendously in this venue from numerous advances achievedusing high-pressure carbon dioxide (CO2) as a viscosity modifier, plasticizing agent,foaming agent, and reaction medium. Polymer processing in supercritical fluids has been a major interest for a portfolio of materials processing applications including their impregnation into porous matrices. Also, SCF solvents are being examined as a media for polymerization processes, polymer purification and fractionation, and as environmentally preferable solvents for solution coatings. Pressurized CO2 isinexpensive, sustainable, relatively benign, and versatile due to its gas-like viscosity and liquid-like densities, which can be controllably tuned through appropriate choice of temperature and pressure. Addition of high-pressure CO2 to polymer systems can have a profound impact on their thermodynamic properties and phase behavior, since the number of interacting species increases due to the high-pressures, so that the compressibility also increases, as well as the plasticity effects. Even then, polymers are only sparingly soluble in CO2 unless one uses an entrainer or surfactant. An addition of a liquid monomer co-solvent results in greatly enhanced polymer solubility in the supercritical fluid at rather mild conditions of lower temperatures and reduced pressures.The focus of this research is to measure, evaluate and model the phase behavior of the methyl methacrylate-CO2 and the poly (methyl methacrylate)-CO2-methyl methacrylatesystem, where methyl methacrylate plays role of a co-solvent. Cloud-point data are measured in the temperature range of 30-80ʻC, pressures as high as 300 bar, co-solvent concentrations of 27 and 48.4 wt% MMA, and varying PMMA concentrations of 0.1, 0.2,0.5, and 2.5 wt%. Solubility data is reported for these systems. The experimental results are modeled accurately using the Statistical Associating Fluid Theory (SAFT) for multi component polymer/solvent mixtures. The measured solubility data appears to be significantly different than previously published results by McHugh et al, Fluid Phase Equilibria, 1999. Thorough investigation, re-calibration of the equipment, and repetition of the measurements has proved that the measured data is entirely correct and the reference data is significantly off, which indirectly gives credit to this work and opens room for amendments of those results.

In this paper, we discuss the effect of the hydrogen-bonding on the photoluminescent(PL) properties of 1-pyrenecarboxylic acid (PCA)/ poly(methyl methacrylate) (PMMA). Isolated fluorophore can be obtained when PCA molecules were blended and septrated by PMMA, i. e. excimer emission can be more efficiently prevented. With the use of non-solvent, toluene, in the preparation step, excimer emission of PCA can be more effeiciently prevented as compared to the good solvent, tetrahydrofuran(THF). With a high PMMA/PCA ratio of 1000/1, emission spectra show no sign of excimer formation. Intermolecular hydrogen bonding between PMMA and PCA helps to prevent the excimer formation. Solvents used in the preparative state play important role on the final PL properties of the solid film. In the blend, partial carbonyl groups in PMMA band with carboxylic acid group in PCA, this causes the appearance of a stretching band at 1718 cm-1 in infrared spectroscopy. The hydrogen-bond interactions help to the prevention of excimer formation in the PMMA/PCA blending systems.

The work presented herein focuses on expanding the use of CO2-triggered switchable surfactants in emulsion polymerization of hydrophobic and hydrophilic monomers. Bicarbonate salts of the following compounds were employed as surfactants in the emulsion polymerization of styrene, methyl methacrylate (MMA) and/or butyl methacrylate (BMA): N’-hexadecyl-N,N-dimethylacetamidine (1a), N’-dodecyl N,N-dimethylacetamidine (2a) and N’-(4-decylphenyl)-N,N-dimethylacetamidine (3a). A systematic study of the effects of surfactant and initiator concentrations and solids content on the resulting particle size and ζ-potential was carried out, showing that a wide range of particle sizes (40 – 470 nm) can be obtained. It was found that as the basicity of the surfactant decreased, the particle size generated from emulsion polymerization increased. Destabilization of these latexes did not require the addition of salts and was carried out using only non-acidic gases and heat. It was shown that solids content, temperature, particle size and surfactant basicity greatly affect the rate of destabilization of latexes. The area occupied by N’-dodecyl-N,N-dimethylacetamidinium acetate on PMMA particles was determined to be 104 Å2. The monomer-D2O partition coefficient of 2a was determined to be 21 for styrene and 2.2 for MMA. The monomer-D2O partition coefficient of the bicarbonate salt of 2a was determined to be 1.2 for styrene and 0.85 for MMA. An initial assessment of the use of switchable surfactants in the generation of inverse emulsions was carried out. It was determined that butylated polyethyleneimine (BPEI) can successfully stabilize inverse emulsions of cyclohexane and aqueous 2-(dimethylamino)ethyl methacrylate. Upon CO2 introduction, this emulsion separates into two distinct phases. / Thesis (Master, Chemistry) -- Queen's University, 2011-09-26 11:10:14.053

Experimental data on the solubility of CO2 in methyl methacrylate (MMA) and butyl methacrylate (BMA) are reported at temperatures from 308 to 333 K and pressures in the range of 1 to 10 MPa. The corresponding measurements of the volumetric expansion of the liquid phase are also presented. The solubility data are correlated with the Peng-Robinson equation of state using two interaction parameters. Solubilities of CO2 as high as 80 mol% can be attained in both monomers in the range of pressure considered. A near-linear relationship is observed between pressure and liquid-phase composition. The Peng-Robinson equation of state provides a satisfactory correlation of the solubility data. The average absolute relative deviations with respect to the calculated values of pressure are less than 2%. For a given monomer, the expansion isotherms coincide when plotted as a function of the liquid - phase composition. Catalytic chain transfer (CCT) polymerisation of CO2-expanded MMA, BMA and styrene is then described. Experimental values of the chain transfer constant are determined at 323 K and 333 K and in the range of pressure from 0.1 to 6 MPa. A cobaloxime complex is used as the chain transfer catalyst. The effect of small quantities of polymer on the volumetric expansion of the corresponding monomer is considered. The chain transfer constants for the expanded monomers are significantly higher than those obtained in the bulk monomers. It is demonstrated that a linear relationship exists between the chain transfer rate coefficient and the inverse of liquid-phase viscosity. These results provide significant evidence that the rate-determining step in the CCT process is diffusion-controlled. Finally, molecular weight evolution in CCT polymerization of CO2-expanded MMA is reported. Experimental molecular weight and polydispersity index data are presented at 323 K in the range of conversion from 1 to 25%, and at pressures of 5 and 6 MPa. Both molecular weight and polydispersity increase with conversion at conditions below the homogeneous expansion limit. Predici simulations suggest that either irreversible catalyst deactivation or cobalt-carbon bond formation is the most likely mechanism for the increase in molecular weight with conversion.