M. Tech. (Chemistry, Faculty of Applied and Computer Sciences), Vaal University of Technology. / Advanced oxidation processes (AOPs) are supposedly effective means for removal of low concentration of organic pollutants from waste water as compared to conventional treatment methods. However, TiO2 metal semiconductor is the most promising photocatalyst for degradation of organic pollutant under heterogeneous photocatalysis as compared to other metal semiconductors. Challenges such as aggregation in solution, low adsorptive ability for non-polar organic contaminants and recycling are limitations in application of TiO2 for commercial purposes. The other limitations of TiO2, is it only utilizes 4-6% of the solar energy reaching the earth's surface which is in the UV region and also rapid electron-hole recombination due its wide band gap. In this work, the limitations are overcome by synthesis of a new photocatalyst material and further applied on degradation of model organic contaminants. The first part of this work focused on preparation and characterization of photocatalyst material. The photocatalyst synthesized were characterized using X-ray diffraction (XRD), scanning electron microscopy (SEM), energy-dispersive X-ray analysis (EDAX), Fourier transform infrared spectroscopy (FTIR), thermal gravimetric analysis (TGA) and UV-VIS diffuse reflectance spectrophotometer (DRUV-VIS). Supporting characterization techniques revealed partly dispersion of TiO2 within the cavities of dealuminated Clinoptilolite (HCP). TiO2 exist as nanoparticles or clusters on the HCP surface ascribed to lower loading of TiO2. XRD analysis showed that the support material employed was mainly Clinoptilolite and absorption band of prepared photocatalyst was red-shifted into the visible region, with slight reduction in band gap of photocatalyst. The second part focused on adsorption and photocatalytic degradation of methyl orange solution (MO) conducted under UV-irradiation in the presence of TiO2/HCP. The influence of operational parameters on degradation efficiency of photocatalyst material on MO was carried out in this study. Parameters such as initial dye concentration, pH, calcination temperature, inorganic anions and peroxide concentration were varied during degradation activities of MO. Comparative degradation efficiency of TiO2/HCP, TiO2 and HCP were conducted on dye mixture (Methyl orange and Methylene Blue) under UV irradiation. Kinetic analysis employing Langmuir-Hinshelwood model on dependencies of organic contaminants degradation was also conducted at different operational parameters. The adsorption capacity of MO was highest in the presence of TiO2/HCP at lower loading, which is ascribed to good dispersion of TiO2 on HCP and increased surface area of dealuminated Clinoptilolite. The photocatalytic degradation of methyl orange in the presence of TiO2/HCP was optimized at low dye concentration (30 ppm), acidic condition (pH 4), and calcination temperature of 873 K. Nitrate ion of Sodium salt accelerates degradation activities on methyl orange as compared to other inorganic anions. Photocatalytic degradation of methyl orange was greatly enhanced upon addition of oxidant (H2O2) and the photocatalyst possessed good repeatability after 3 cycles. TiO2/HCP exhibit highest degradation activities, followed by HCP as compared to TiO2 during the degradation of dye mixture. The degradation of MO by the photocatalyst fits into pseudo-first order kinetic model, while for comparative analysis of photocatalyst on dye mixtures follows second order kinetic model.

Ph.D. (Chemistry) / This study addressed the incorporation of nanotechnology-based materials, either through incorporating nanomaterials or by introducing nanostructures onto the membrane matrix, to form nano-enabled polymeric membranes with high specific flux and better anti-fouling profile. The aim of the study was to integrate nanotechnology and membrane science in order to improve the performance of water filtration membranes by alleviating some of the specific shortcomings of water treatment membranes......

水資源缺乏引起的一系列問題在世界上已建得到廣泛關注，因此，確保提供潔淨衛生的水在保護人類健康和環境方面起著重要作用。近來，光催化作為頗有前景的替代方法被廣泛應用殺菌除污。二氧化鈦是目前研究最多應用最廣的光催化劑。基於紫外光譜照射，催化劑表面產生活性氧化物種，這些物種具有強氧化性能殺滅細胞。 / 本文首次研究了母體菌種大腸桿菌BW25113和它的同源單基因缺陷變異體對光催化殺菌的靈敏度差異。母體菌種和變異菌種表現出不同的耐受性。基於此，能幫助發掘出重要的變種。通過生物化學方法，可以檢測出不同菌種的生理性特徵。結合其他方法，可以進一步揭示光催化殺菌的生理性機理。 / 首先，我們篩選出了兩種重要的變異體。一種是大腸桿菌JW1081，即脂肪酸變異體，該菌種缺乏脂肪酸合成調節的關鍵基因。一種是大腸桿菌JW3942，即乙酰輔酶A變異體，該菌種缺乏乙酰輔酶A合成調控得到關鍵激酶。我們發現脂肪酸變異體對光催化處理的耐受性稍低，而乙酰輔酶A變異體則耐受性較高。 同時發現，溫度可以調節細胞膜的不飽和酸和飽和酸的比例。因此，我們提出脂肪酸和乙酰輔酶A是光催化殺菌中的重要影響因子。 / 更進一步研究發掘了細胞內酶和光催化產生的活性氧物種間的關係。大腸桿菌JW3914，即過氧化氫酶變異體，是發現的另一個重要的變異體。通過對母體和變異體的淬滅劑實驗，主要的殺菌活性氧物種是光催化產生的雙氧水，而不是羥基自由基。細胞體內的過氧化氫酶誘導在母體菌體內發現，而未在變異體內檢測到。 / 本課題採用母體/單基因變異體的研究方法，為全面深刻理解光催化殺菌的深層機理提供一種全新的研究思路。 / Many problems associated with the lack of clean, fresh water worldwide are well known. Developing countries will particularly be affected by water availability problems and there will be further pressure on water demand resulting from economic development and population growth. Therefore, the provision of safe and clean water plays a key role in protecting human health and the environment. Recently, photocatalytic oxidation (PCO) has been widely accepted as a promising alternative method of water disinfection. Titanium dioxide (TiO₂) has been investigated extensively and is the most widely used photocatalyst. Upon the irradiation of UVA lamp, reactive charged and oxidative species are generated on TiO₂ surface and can inactive the bacterial cells. / In this study, the photocatalytic performances of a parental strain (E.coli BW25113) and its isogenic single-gene deletion mutant strains have been investigated for the first time. These bacterial strains exhibited different sensitivies towards photocalytic inactivation. Based on this, it can help reveal some important mechanism from the mutations. Biotic factors were confirmed by physiological biochemical measurement. / Firstly, we screened out the potential mutation fabF⁻ mutant (E. coli JW1081, carrying the mutation of fabF759(del)::kan) and coaA⁻ mutant (E. coli JW3942, carrying the mutation of coaA755(del)::kan). The isogenic fabF⁻ mutant is slightly more susceptible, and coaA⁻ mutant is less susceptible to photocatalytic inactivation. Through conditioning temperature, it adjusts the ratio of unsaturated to saturated fatty acid (FA) of cell membrane. We propose that FA profile and coenzyme A level significantly affect photocatalytic inactivation of bacteria. Moreover, we show photogenerated electrons (e⁻) can directly inactivate the cells of E. coli. / Furthermore, we report the relationship between the bacterial intracellular enzyme and the reactive charged and oxidative species (ROSs) generated during photocataltic inactivation. The katG⁻ mutant, E. coli JW3914, carrying the mutation of katG729(del)::kan is another important mutation. The parental and katG⁻ mutant strains reveal that photogenerated H₂O₂ but not OH[subscript free] is another important reactive oxygen species to inactivate bacteria. The inducible catalase (CAT) corresponding to H₂O₂can be detected in parental strain but not in katG⁻ mutant. / The research methodology using parental/single-gene deletion mutant strains is expected to shed light on fully understanding of the fundamental mechanism of photocatalytic inactivation of E. coli. / Detailed summary in vernacular field only. / Detailed summary in vernacular field only. / Detailed summary in vernacular field only. / Detailed summary in vernacular field only. / Detailed summary in vernacular field only. / Gao, Minghui. / Thesis (Ph.D.)--Chinese University of Hong Kong, 2012. / Includes bibliographical references (leaves 130-177). / Electronic reproduction. Hong Kong : Chinese University of Hong Kong, [2012] System requirements: Adobe Acrobat Reader. Available via World Wide Web. / Abstract also in Chinese. / Acknowledgements --- p.i / Abstract --- p.v / Table of contents --- p.ix / List of Figures --- p.xiii / List of Plates --- p.xvii / List of Tables --- p.xviii / List of Equations --- p.xix / Abbreviations --- p.xxi / Chapter 1. --- Introduction --- p.1 / Chapter 1.1 --- Water crisis --- p.1 / Chapter 1.2 --- Traditional disinfection methods --- p.3 / Chapter 1.2.1 --- Chlorination --- p.4 / Chapter 1.2.2 --- Ozonation --- p.6 / Chapter 1.2.3 --- Ultraviolet irradiation --- p.8 / Chapter 1.2.4 --- Multiple disinfectants --- p.10 / Chapter 1.3 --- Advanced oxidation process (AOPs) --- p.10 / Chapter 1.3.1 --- Hydrogen Peroxide/Ozone (H₂O₂/O₃) --- p.11 / Chapter 1.3.2 --- Ozone/Ultraviolet Irradiation (O₃/UV) --- p.12 / Chapter 1.3.3 --- Hydrogen Peroxide/ Ultraviolet Irradiation (H₂O₂/UV) --- p.12 / Chapter 1.3.4 --- Fenton's --- p.Reaction / Chapter 1.4 --- Solar photocatalytic disinfection (SPC-DIS) --- p.14 / Chapter 1.4.1 --- Photocatalyst-TiO₂ --- p.31 / Chapter 1.4.2 --- Irradiation sources --- p.35 / Chapter 1.4.3 --- TiO₂ photocatalytic process --- p.35 / Chapter 1.4.4 --- The role of photogenerated reactive charged and oxidative species (ROSs) --- p.38 / Chapter 1.5 --- Bacteria --- p.40 / Chapter 1.5.1 --- E. coli BW25113 --- p.40 / Chapter 1.5.2 --- E. coli Keio Collection --- p.41 / Chapter 1.5.3 --- Bacterial defense mechanism towards oxidative stresses --- p.44 / Chapter 1.6 --- Photocalytic applications --- p.53 / Chapter 1.7 --- Significance of the project --- p.55 / Chapter 2. --- Objectives --- p.58 / Chapter 3. --- Genetic studies of the roles of fatty acid and coenzyme A in photocatalytic inactivation of Escherichia coli --- p.61 / Chapter 3.1 --- Introduction --- p.61 / Chapter 3.2 --- Materials and methods --- p.65 / Chapter 3.2.1 --- Photocatalyst --- p.65 / Chapter 3.2.2 --- Bacterial nutrient --- p.66 / Chapter 3.2.3 --- Bacterial strains --- p.67 / Chapter 3.2.4 --- Photocatalytic inactivation --- p.69 / Chapter 3.2.5 --- Fatty acid profile --- p.72 / Chapter 3.2.6 --- Fluorescent measurement of bacterial coenzyme A content --- p.74 / Chapter 3.2.7 --- The role of photogenerated electrons (e⁻) to bacterial inactivation --- p.74 / Chapter 3.2.8 --- Transmission Electron Microscopic (TEM) --- p.75 / Chapter 3.2.9 --- Photoelectrochemical measurement --- p.77 / Chapter 3.3 --- Results --- p.77 / Chapter 3.3.1 --- Photocatalytic inactivation --- p.77 / Chapter 3.3.2 --- Effects of pre-incubation at different temperatures --- p.80 / Chapter 3.3.3 --- Fatty acid profile --- p.83 / Chapter 3.3.4 --- Fluorescent measurement of bacterial coenzyme A content --- p.84 / Chapter 3.3.5 --- The role of electron (e⁻) in photocataytic inactivation --- p.84 / Chapter 3.3.6 --- Transmission electron microscopy (TEM) --- p.89 / Chapter 3.3.7 --- Photocurrent measurement --- p.90 / Chapter 3.4 --- Discussion --- p.90 / Chapter 3.5 --- Conclusions --- p.96 / Chapter 4 --- Genetic and physiological studies of the role of Catalase and H₂O₂ in photocatalytic inactivation of E. coli --- p.98 / Chapter 4.1 --- Introduction --- p.98 / Chapter 4.2 --- Materials and methods --- p.101 / Chapter 4.2.1 --- Bacterial strains --- p.101 / Chapter 4.2.2 --- Photocatalytic performance --- p.102 / Chapter 4.2.3 --- Scavenger studies --- p.103 / Chapter 4.2.4 --- Effects of different pHs on photocatalytic inactivation --- p.104 / Chapter 4.2.5 --- Measurement of bacterial catalase activity and H₂O₂ --- p.104 / Chapter 4.2.6 --- Transmission electron microscopy (TEM) --- p.105 / Chapter 4.2.7 --- Atomic absorption spectrophotometer (AAS) --- p.105 / Chapter 4.3 --- Results and discussion --- p.106 / Chapter 4.3.1 --- Photocatalytic performance --- p.106 / Chapter 4.3.2 --- Scavenger studies --- p.108 / Chapter 4.3.3 --- Contribution of hydrogen peroxide (H₂O₂) --- p.111 / Chapter 4.3.4 --- Effects of different pHs on photocatalytic inactivation --- p.114 / Chapter 4.3.5 --- Bacterial catalase (CAT) activity --- p.116 / Chapter 4.3.6 --- Destruction model of bacterial cells --- p.118 / Chapter 4.4 --- Conclusions --- p.120 / Chapter 5. --- General conclusions --- p.122 / Chapter 6. --- Prospectives --- p.125 / Chapter 7. --- Appendix --- p.127 / Chapter 8. --- References --- p.130

No description available.

The capacity and efficiency of melter slag (provided by New Zealand Steel) to remove heavy metals and suspended solids from stormwater samples are studied in this thesis. A series of batch tests were carried out to investigate the adsorption-desorption mechanism of the slag to remove heavy metals (Cd2+, Zn2+ and Cu2+) from working solutions. The results showed that all the tested metallic ions could be removed by mixing the melter slag with the working solutions. Adsorption and ion exchange are the dominant mechanisms in this process. The adsorption capacity follows the descending order of Cu2+ > Zn2+ = Cd2+. Varied binding energy of different metallic ions to the slag resulted in competitive adsorption between ions.A variety of substances: inorganic salts (KCl, NaCl, KNO3 and sea water), organic acids (citric and tartaric) and inorganic acids (nitric and carbonic), were tested as desorbing agents to recover the used slag. Citric acid in sea water was found to be the best in terms of desorption efficiency and cost-effectiveness.The column tests were carried out to simulate the filtration bed in laboratory conditions. Stormwater samples were collected from residential and commercial areas in Auckland. The synthetic stormwater samples were prepared from clay and metallic ion solution. Both samples were used as feeding solutions in the tests. The removal efficiencies of suspended solids and metallic ions (Zn2+, Cd2+ and Cu2+) vary depending on different operation conditions. They are in inverse proportion to the grain size of the melter slag and the influent flow rate. The higher removal efficiency of Zn2+ than that of suspended solids infers that metallic ions are removed by both precipitation and adsorption.

published_or_final_version / Civil Engineering / Doctoral / Doctor of Philosophy

M. Tech. Water Care / Aims of the study was to recommend probable management procedures that could be used in small water treatment plants in order to produce safe drinking water.

No description available.

No description available.

The capacity and efficiency of melter slag (provided by New Zealand Steel) to remove heavy metals and suspended solids from stormwater samples are studied in this thesis. A series of batch tests were carried out to investigate the adsorption-desorption mechanism of the slag to remove heavy metals (Cd2+, Zn2+ and Cu2+) from working solutions. The results showed that all the tested metallic ions could be removed by mixing the melter slag with the working solutions. Adsorption and ion exchange are the dominant mechanisms in this process. The adsorption capacity follows the descending order of Cu2+ > Zn2+ = Cd2+. Varied binding energy of different metallic ions to the slag resulted in competitive adsorption between ions.A variety of substances: inorganic salts (KCl, NaCl, KNO3 and sea water), organic acids (citric and tartaric) and inorganic acids (nitric and carbonic), were tested as desorbing agents to recover the used slag. Citric acid in sea water was found to be the best in terms of desorption efficiency and cost-effectiveness.The column tests were carried out to simulate the filtration bed in laboratory conditions. Stormwater samples were collected from residential and commercial areas in Auckland. The synthetic stormwater samples were prepared from clay and metallic ion solution. Both samples were used as feeding solutions in the tests. The removal efficiencies of suspended solids and metallic ions (Zn2+, Cd2+ and Cu2+) vary depending on different operation conditions. They are in inverse proportion to the grain size of the melter slag and the influent flow rate. The higher removal efficiency of Zn2+ than that of suspended solids infers that metallic ions are removed by both precipitation and adsorption.