Sample preparation is a key step in chemical analysis, and includes isolation of target analytes, removal of interferences, preconcentration, and/or modification of target analytes (if needed). Sample preparation is also the most time-consuming and error-prone step in the whole analytical process. Traditional sample preparation techniques involve hazardous solvents. Considering the environmental and health safety, it is desirable to reduce or eliminate organic solvents in sample preparation. Solid phase microextraction (SPME) was introduced as a solvent free sample preparation technique. Capillary microextraction (CME) is one of the formats of SPME that can be easily coupled to high performance liquid chromatography (HPLC). In SPME and CME a solvent free sample preparation is accomplished by using a sorbent coating instead of hazardous organic solvents commonly used in conventional extraction techniques. This research is focused on the development and systematic examination of novel niobia-, titania- and silica-based organic-inorganic hybrid sol-gel sorbents for CME. Conventionally silica and titania based precursors were used in organi-inorganic hybrid sol-gel sorbents for CME, here novel niobia based precursor was used in creating organic-inorganic hybrid sol-gel sorbents. Poly tetrahydrofuran (polyTHF) as well as electrically neutral and charged organic ligands were used to prepare the sorbents for CME coupled to HPLC. Characterization of created sol-gel sorbents, evaluation of extraction performance, and enrichment of environmentally and biomedically important analytes including organophosphorus compounds were performed. CME performances of the created sorbents were characterized by specific extraction (SE) (a measure of extraction efficiency) and desorption efficiency (DE) (a measure of completeness desorption of extracted analytes). Scientific findings of this research has shown that sol-gel niobia-polyTHF sorbent provides 60 to 70 % higher SE values for different environmentally important analytes compared to analogously prepared silica-polyTHF sorbent. This superior extraction performance can be attributed to the presence of surface Lewis acid sites undergoing Lewis acid-base interactions with analytes representing Lewis bases. The prepared sorbents also have the ability to undergo van der Waals interactions due to the presence of polyTHF. Absence of Lewis acid sites on silica surface resulted in inferior extraction efficiency compared to niobia-polyTHF sorbents. Extraction efficiency of the created sol-gel based niobia-polyTHF was also explored in the enrichment of organophosphorus pesticides and compared with that of the state-of-the-art titania-based sorbent. Sol-gel niobia-polyTHF sorbent has provided 40 to 50 % higher SE values in the enrichment of organophosphorus pesticides compared to sol-gel titania-polyTHF sorbent which can be attributed to the presence of bronsted acid sites on niobia surface (but lacking on titania) along with Lewis acid sites. To explore relative contributions of electrostatic, Lewis acid-base and van der Waals interactions between sol-gel sorbents and analytes, two sol-gel sorbents, one containing a positively charged octadecyl ligand and the other a neutral octadecyl ligand were created. Positive charge was imparted by using N-octadecyldimethyl [3-(trimethoxysilyl) propyl] ammonium chloride (C18 (+ve)) as ligand bearing co-precursor. Similarly N-octadecyl trimethoxysilane was used to impart a neutral C18 ligand in sol-gel coating. Experimental results have shown that sol-gel Nb2O5-C18 (+ve) sorbent has superior extraction efficiency compared to sol-gel based Nb2O5-C18 and purely inorganic Nb2O5 sorbents in enrichment of organophosphorus compounds (nucleotides and organophosphorus pesticides). Electrostatic interactions between the positive charge of organic ligand (C18 (+ve)) and negative charge of phosphate group has contributed to the higher extraction performance of sol-gel based Nb2O5-C18 (+ve) sorbent. TiO2-C18 (+ve) sorbent was also created to compare with the novel sol-gel niobia based sorbents, since titania-based sorbents are considered as the state-of-the-art extraction material in the enrichment of organophosphorus compounds. Established research results has shown that sol-gel based Nb2O5-C18 (+ve) sorbent has provided 40 to 50 % higher specific extraction values for organophosphorus compounds compared to sol-gel based TiO2-C18 (+ve) sorbent. Desorption efficiency of sol-gel Nb2O5-C18 (+ve) and TiO2-C18 (+ve) sorbents were 96% vs 90%. This superior DE of sol-gel Nb2O5-C18 (+ve) sorbent can be attributed the higher Lewis acid strength of titania than nioiba. The developed sol-gel niobia based sorbents have also shown high pH stability compared to traditional sol-gel silica based sorbents. The created sol-gel sorbents were characterized by less than 5% run to run RSD values and also less than 5% capillary to capillary RSD values which indicated the high reproducibility of developed method. The developed sol-gel niobia sorbents are applicable to sample preparation in different fields including biomedical, environmental, forensic, defense etc.

Dispersed niobia catalysts were prepared via a non-aqueous synthesis route. The effects of the type of oxide support, the support thermal pre-treatment, the calcination temperature and the niobia loading on the activity and selectivity for mesityl oxide (MO) synthesis at 160C were investigated in an autoclave reactor. The morphological and chemical properties of the catalysts were characterized via EDXRF, XRD, BET and Raman spectroscopy. The strength and nature of the acid sites were elucidated via in situ DRIFT spectra of the adsorption of pyridine as well as the temperature programmed desorption of NH3 interacting with the surface oxide phase. All four catalyst parameters had significant effects on the catalytic properties. Significantly, the nature of the acidity was clearly linked to the catalyst activity and particularly the catalyst stability. Catalysts exhibiting predominantly Lewis acidity invariably deactivated despite good initial activity, with the final acetone conversion dependent on the catalyst formulation. In contrast, catalysts exhibiting Bronsted acidity showed no evidence of catalyst deactivation after 8 hours of reaction. A plausible mechanism which explains these observations is proposed. Catalysts exhibiting Lewis acidity were more active when the supports were first activated at elevated temperature, likely due to a stronger support-surface oxide interaction as a consequence of increased surface coordinative unsaturation of the support. SiO¬2 supported catalysts exhibiting Bronsted acidity were more active if the supports were initially activated at 100C. Evidently, the hydroxyl groups on the oxide support contribute to the generation of Bronsted acidity. Different oxide supports gave rise to distinct acidic and catalytic properties in the niobia overlayer. The most striking example of this was the direct comparison of niobia dispersed onto two kinds of silica supports following the same preparative method. Unique and very strong acid sites were observed in niobia dispersed onto a commercial SiO¬2 catalyst carrier that were not observed in niobia dispersed onto fumed SiO¬2. For SiO2 catalysts, the activity increased linearly with niobia loading regardless of calcination temperature. In contrast, Al2O3 catalysts exhibited an initial increase in activity for MO synthesis with niobia loading followed by a decrease in activity after reaching a maximum activity below 1/3 monolayer coverage. The effect was more pronounced for catalysts exhibiting Bronsted acidity. It is proposed that adlineation sites are primarily responsible for catalytic activity in Nb2O5/-Al2O3 catalysts exhibiting Bronsted acidity. Niobia catalysts were developed using commercially available catalyst carriers as supports. The macrokinetics of MO and MIBK syntheses were investigated in a benchtop fixed bed flow reactor. The catalysts showed excellent activity for MO and MIBK syntheses at 160°C, typically 0.9 to 1.3 [g/hr*gcat]. However, the MIBK selectivity was constrained from 82 to 85% due to the coproduction of 2-propanol and diisobutyl ketone. The productivity for MO synthesis was found to be strongly dependent on the space velocity suggesting product inhibition. The intrinsic kinetics of the one-step synthesis of MIBK over a 15.2 wt% Pd/Nb2O5/SiO2 catalyst was investigated in an autoclave reactor. A kinetic model was developed and is reported. The one step synthesis of MIBK was investigated at the pilot plant scale via catalytic distillation (CD). An important finding was that while operating at 100% reflux, the accumulation of water in the reactive section resulted in the suppression of the DAA dehydration reaction. The in situ removal of water from the reactive section via an overhead distillate stream operating at 83 to 97% reflux directly resulted in an increase in MIBK productivity and hydrogen uptake efficiency by factors of about 20 yielding a moisture free reboiler product stream with as high as 53 wt% MIBK. The process was found to be controlled by the external mass transfer of hydrogen. Interestingly, the results suggest that the catalyst wetting efficiency affects the transport of hydrogen to the active sites as evidenced by the dependence of MO conversion on the reflux flow rate. The condition of minimum reflux flow rate and maximum hydrogen flow rate resulted in 97% MO conversion and 90 wt% MIBK selectivity.

Dispersed niobia catalysts were prepared via a non-aqueous synthesis route. The effects of the type of oxide support, the support thermal pre-treatment, the calcination temperature and the niobia loading on the activity and selectivity for mesityl oxide (MO) synthesis at 160C were investigated in an autoclave reactor. The morphological and chemical properties of the catalysts were characterized via EDXRF, XRD, BET and Raman spectroscopy. The strength and nature of the acid sites were elucidated via in situ DRIFT spectra of the adsorption of pyridine as well as the temperature programmed desorption of NH3 interacting with the surface oxide phase. All four catalyst parameters had significant effects on the catalytic properties. Significantly, the nature of the acidity was clearly linked to the catalyst activity and particularly the catalyst stability. Catalysts exhibiting predominantly Lewis acidity invariably deactivated despite good initial activity, with the final acetone conversion dependent on the catalyst formulation. In contrast, catalysts exhibiting Bronsted acidity showed no evidence of catalyst deactivation after 8 hours of reaction. A plausible mechanism which explains these observations is proposed. Catalysts exhibiting Lewis acidity were more active when the supports were first activated at elevated temperature, likely due to a stronger support-surface oxide interaction as a consequence of increased surface coordinative unsaturation of the support. SiO¬2 supported catalysts exhibiting Bronsted acidity were more active if the supports were initially activated at 100C. Evidently, the hydroxyl groups on the oxide support contribute to the generation of Bronsted acidity. Different oxide supports gave rise to distinct acidic and catalytic properties in the niobia overlayer. The most striking example of this was the direct comparison of niobia dispersed onto two kinds of silica supports following the same preparative method. Unique and very strong acid sites were observed in niobia dispersed onto a commercial SiO¬2 catalyst carrier that were not observed in niobia dispersed onto fumed SiO¬2. For SiO2 catalysts, the activity increased linearly with niobia loading regardless of calcination temperature. In contrast, Al2O3 catalysts exhibited an initial increase in activity for MO synthesis with niobia loading followed by a decrease in activity after reaching a maximum activity below 1/3 monolayer coverage. The effect was more pronounced for catalysts exhibiting Bronsted acidity. It is proposed that adlineation sites are primarily responsible for catalytic activity in Nb2O5/-Al2O3 catalysts exhibiting Bronsted acidity. Niobia catalysts were developed using commercially available catalyst carriers as supports. The macrokinetics of MO and MIBK syntheses were investigated in a benchtop fixed bed flow reactor. The catalysts showed excellent activity for MO and MIBK syntheses at 160°C, typically 0.9 to 1.3 [g/hr*gcat]. However, the MIBK selectivity was constrained from 82 to 85% due to the coproduction of 2-propanol and diisobutyl ketone. The productivity for MO synthesis was found to be strongly dependent on the space velocity suggesting product inhibition. The intrinsic kinetics of the one-step synthesis of MIBK over a 15.2 wt% Pd/Nb2O5/SiO2 catalyst was investigated in an autoclave reactor. A kinetic model was developed and is reported. The one step synthesis of MIBK was investigated at the pilot plant scale via catalytic distillation (CD). An important finding was that while operating at 100% reflux, the accumulation of water in the reactive section resulted in the suppression of the DAA dehydration reaction. The in situ removal of water from the reactive section via an overhead distillate stream operating at 83 to 97% reflux directly resulted in an increase in MIBK productivity and hydrogen uptake efficiency by factors of about 20 yielding a moisture free reboiler product stream with as high as 53 wt% MIBK. The process was found to be controlled by the external mass transfer of hydrogen. Interestingly, the results suggest that the catalyst wetting efficiency affects the transport of hydrogen to the active sites as evidenced by the dependence of MO conversion on the reflux flow rate. The condition of minimum reflux flow rate and maximum hydrogen flow rate resulted in 97% MO conversion and 90 wt% MIBK selectivity.