Not available / text

Not available / text

Nitrogen-selective Carbon Molecular Sieve (CMS) membranes were developed for nitrogen/methane separation. Effects of pyrolysis conditions including pyrolysis temperature protocol and pyrolysis atmosphere were studied for Matrimid® and 6FDA:BPDA-DAM precursors. It was revealed that high pyrolysis temperature is essential to achieve attractive nitrogen/methane selectivity due to the subtle size difference between the two gas penetrants. Detailed study on one of the best performing CMS membranes showed that diffusion selection, more specifically, the entropic factor responsible for diffusion selection provides a significant contribution to the high selectivity. The effect of precursor was studied by considering nine carefully selected polymers. The structures and properties of these polymer precursors were compared and correlated with the separation performance of resulting CMS membranes. The translation of intrinsic CMS transport properties into the hollow fiber morphology was also explored. Substructure collapse and asymmetry lost during pyrolysis were observed, which resulted in significant increases of separation layer thickness and decreases in permeance. Vinyltrimethoxy silane (VTMS)-treatment was applied to polymer hollow fiber before pyrolysis to overcome the problem of substructure collapse. The effects of VTMS-treatment on both the substructure and skin layer are discussed.

South Africa is a land blessed with an abundance of mineral deposits. Yet, despite this, very little value adding of minerals exists. Most of the mined minerals are exported, where it is reworked into valued items. The country subsequently imports the valuable items at a much higher cost. In the 2006/7 financial year, the government made the decision to support several projects aimed at adding value to the mined minerals and by so doing, creating job opportunities. One such project was identified for the mineral Fluorite (CaF2). Fluorite is exposed to a controlled burn in a plasma reactor, producing an array of different fluorocarbon gases used in the electronics industry and for commercial polymers like Teflon®. Currently, fluorocarbon gases are separated using a series of cryogenic distillation columns. Although this technique has proven to be successful, it has several negative aspects such as the high cost involved when operating at cryogenic conditions as well as difficulty handling the gases at these sub–zero temperatures. It was proposed to study the possibility of using membranes to separate fluorocarbon gases at ambient conditions. Several membranes were screened to determine which one is best suited for this application. Two Teflon® based membranes were selected from this data. One of the membranes had a PAN support, while the other had a PEI support. Pure gas data for both membranes showed promising results. It yielded the highest flux for C3F6, followed by N2 and CF4. c–C4F8 was not used because it was demonstrated that the gas tends to condensate at low pressures. It is recommended to rather use pressure swing condensation to remove this gas from the mixture before the remainder is purified using membranes. Both membranes behaved similarly, with selectivity between C3F6 and CF4, and N2 and CF4; all above 10. By including the permeate pressure in the Solution–diffusion model, it was possible to model the pure gas data Binary feed gas mixture experiments showed a large amount of coupling existing between the feed gas mixtures. The result is a decrease in the selectivity as well as the total flux of the gas mixture. Partial fluxes were modelled by introducing a thermodynamic factor that was shown to follow a power law equation. The PAN–supported membrane outperformed the PEI–supported one; it was decided to use this membrane from this point onwards. Analysis of the ternary feed mixtures showed a strong selectivity towards the gas abundant in the feed blend. The existence of convective diffusion was proven, and included in the modelling, as well as a breakthrough pressure constant. This is indicative of strong interaction between the different gases and the membrane. Throughout the study it became clear that the difference in surface charge between the gases and the membrane were decisive. Opposite charges between a gas (C3F6) and the membrane aided in gas permeation. Membrane separation of fluorocarbon gases at ambient conditions is possible. Teflon® based membranes are recommended. It will be advantageous to study the effect of elevated temperatures on the separation efficiency of such a system. / Thesis (M.Ing. (Chemical Engineering))--North-West University, Potchefstroom Campus, 2012.

South Africa is a land blessed with an abundance of mineral deposits. Yet, despite this, very little value adding of minerals exists. Most of the mined minerals are exported, where it is reworked into valued items. The country subsequently imports the valuable items at a much higher cost. In the 2006/7 financial year, the government made the decision to support several projects aimed at adding value to the mined minerals and by so doing, creating job opportunities. One such project was identified for the mineral Fluorite (CaF2). Fluorite is exposed to a controlled burn in a plasma reactor, producing an array of different fluorocarbon gases used in the electronics industry and for commercial polymers like Teflon®. Currently, fluorocarbon gases are separated using a series of cryogenic distillation columns. Although this technique has proven to be successful, it has several negative aspects such as the high cost involved when operating at cryogenic conditions as well as difficulty handling the gases at these sub–zero temperatures. It was proposed to study the possibility of using membranes to separate fluorocarbon gases at ambient conditions. Several membranes were screened to determine which one is best suited for this application. Two Teflon® based membranes were selected from this data. One of the membranes had a PAN support, while the other had a PEI support. Pure gas data for both membranes showed promising results. It yielded the highest flux for C3F6, followed by N2 and CF4. c–C4F8 was not used because it was demonstrated that the gas tends to condensate at low pressures. It is recommended to rather use pressure swing condensation to remove this gas from the mixture before the remainder is purified using membranes. Both membranes behaved similarly, with selectivity between C3F6 and CF4, and N2 and CF4; all above 10. By including the permeate pressure in the Solution–diffusion model, it was possible to model the pure gas data Binary feed gas mixture experiments showed a large amount of coupling existing between the feed gas mixtures. The result is a decrease in the selectivity as well as the total flux of the gas mixture. Partial fluxes were modelled by introducing a thermodynamic factor that was shown to follow a power law equation. The PAN–supported membrane outperformed the PEI–supported one; it was decided to use this membrane from this point onwards. Analysis of the ternary feed mixtures showed a strong selectivity towards the gas abundant in the feed blend. The existence of convective diffusion was proven, and included in the modelling, as well as a breakthrough pressure constant. This is indicative of strong interaction between the different gases and the membrane. Throughout the study it became clear that the difference in surface charge between the gases and the membrane were decisive. Opposite charges between a gas (C3F6) and the membrane aided in gas permeation. Membrane separation of fluorocarbon gases at ambient conditions is possible. Teflon® based membranes are recommended. It will be advantageous to study the effect of elevated temperatures on the separation efficiency of such a system. / Thesis (M.Ing. (Chemical Engineering))--North-West University, Potchefstroom Campus, 2012.

Thesis (Ph. D.)--University of Texas at Austin, 2007. / Vita. Includes bibliographical references.

Thesis (Ph.D)--Chemical Engineering, Georgia Institute of Technology, 2008. / Committee Chair: Koros William; Committee Member: Hess Dennis; Committee Member: Jones Christopher; Committee Member: Meredith Carson; Committee Member: Wong CP. Part of the SMARTech Electronic Thesis and Dissertation Collection.

Thesis (Ph.D)--Chemical Engineering, Georgia Institute of Technology, 2009. / Committee Chair: Dr. William J. Koros; Committee Member: Dr. Amyn Teja; Committee Member: Dr. Christopher W. Jones; Committee Member: Dr. Haskell W. Beckham; Committee Member: Dr. Stephen J. Miller. Part of the SMARTech Electronic Thesis and Dissertation Collection.

The research aimed to develop chemically modified PIM-1s for use in adsorption and gas separation processes. In particular, the nitrile group in PIM-1 was converted to several different functional groups to manipulate the interaction ability of PIM-1 with different species. Synthesis of PIM-1 was achieved by two different methods, using both the low (72h, 65 °C) and the high temperature (40 min, 160 °C) methods. Hydrolysis of PIM-1 was performed in the presence of 20% and 10% NaOH solutions (1:1 H2O/ethanol) at 120 and 100 °C, respectively. The reaction resulted in a mixture of hydrolysis products. The composition of the polymer has a profound effect on the final performance of the polymer. Powder samples of hydrolysed PIMs were used in the research. The reduction of nitrile to primary amine was achieved using borane dimethyl sulphide complex, resulting in amine PIM-1. Both membrane and powder forms of amine PIMs were studied. The reaction of PIM-1 with ethanolamine and diethanolamine produced hydroxyalkylaminoalkylamide PIMs. The combination of all available techniques (ATR-IR, solution and solid state NMR, TGA, Elemental analysis, UV, GPC, MALDI-ToF, low pressure N2 sorption) was used to characterise the polymers. Gas sorption studies of modified PIMs showed that the sorption capacities of polymer altered depend on the modification. Hydrolysed PIMs showed reduced CO2 uptake. Ethanolamine modified PIM showed reduced CO2 uptake along with even more reduced N2 uptake, leading to enhanced CO2/N2 ideal selectivity at 1 bar. Amine modification increased the CO2 uptake of the polymer, while showing the same N2 uptake. Enhanced sorption selectivity was also achieved by amine PIM-1. Although chemical modifications reduced the permeability of the membranes, enhanced gas selectivity was obtained. Enhanced H2/CO2 selectivity placed amine PIM-1 above the 2008 Robeson upper bound. The relationship between the degree of conversion and permeability of amine PIM-1 was studied in detail. The effect of temperature and pressure on the permeability of amine PIM was studied, using several different temperatures and pressures. Ethanolamine modified PIM showed size selective behaviour by enhanced H2/N2 and H2/CH4 selectivities, and it crossed the 2008 Robeson upper bounds. Dye adsorption studies revealed that chemical modification manipulated the interaction ability of PIM-1. PIM-1 showed high affinity for neutral dye. While hydrolysed PIMs showed high affinity for cationic species, amine and ethanolamine modified PIMs displayed high affinity for anionic dyes. The factors affecting the uptake capacity of PIM-1, including temperature and pH, were studied along with kinetics of dye adsorption. Thermal treatments of modified PIMs and their structural characterisation were performed. The adsorption and separation performances of thermally treated and untreated modified PIMs were compared.

This research aimed to develop new polymeric materials for use in membrane or adsorption processes for carbon dioxide capture. In particular, it explored the synthesis, characterization and properties of polymers incorporating a spiro-center. A dianhydride containing a spiro-center (An-1), suitable for use in the preparation of polyimides, was synthesized using a previously reported procedure. The spiro-center makes the structure of the resulting polymers (PIM-PIs) similar to polymers of intrinsic microporosity (PIMs), which are known for their high internal surface area and outstanding membrane permeation properties. PIM-polyimides PIM-PI-1 and PIM-PI-5 were successfully synthesized and characterized, and membranes prepared for permeation studies. For PIM-PI-5, gas permeation data were obtained for the first time and were shown to be in reasonable agreement with values predicted by a group contribution method. To produce membranes with even better gas permeation properties, hydroxyl-containing PIM-polyimides were introduced. The presence of a hydroxyl group in the ortho position of the imide linkage made it possible to thermally rearrange the PIM-polyimide to a PIM-polybenzoxazole (PIM-PBO) at 450 oC in an inert atmosphere. PIM-PI-OH-1 with high enough molecular weight to form a freestanding membrane was successfully synthesized using two different synthetic methods: thermal imidization and one-step polycondensation. The PIM-PI-OH-1 polymers prepared by both synthetic methods were compared in terms of gas permeation properties and CO2 uptake capacity, before and after thermal rearrangement. As expected, for polymers prepared by both methods, a significant enhancement was observed in the membranes gas permeation properties upon thermal rearrangement. Ethanol treatment was also performed on the thermally rearranged polymers, which resulted in a large increase in their permeability. The effect of aging was investigated on the ethanol treated PIM-PBO-1 membranes. It was observed that the membranes gradually lose the extra permeability created upon ethanol treatment and return to close to their original permeability value. To increase the concentration of thermally rearrangeable sites in the polymers, a dianhydride (An-2) with a smaller structure and lower molecular weight comparing to the An-1 was synthesized. A copolymer (copolymer-OH(1-2)), was synthesized using An-1 and An-2 (1:1). Gas permeation measurements were performed on the thermally rearranged polymer before and after ethanol treatment. A slight enhancement in the polymer’s selectivity toward CO2/N2 and CO2/CH4 gas pairs was observed, while maintaining the permeability. Having the same aim, PIM-PI-OH-3 was prepared using a smaller and a more rigid diamine, compared to the diamine used in the preparation of PIM-PI-OH-1. Gas permeation studies of the thermally rearranged membrane before and after ethanol treatment showed a significant increase in O2/N2 selectivity, which passed the Robeson 2008 upper bound. In adsorption experiments, CO2 uptake was higher than for PIM-PI-OH-1 and its thermally rearranged product.