The concentrations of chlorine dioxide (CI02), chlorine, chlorite (CIO2), and chlorate (CI03) were evaluated following pretreatment of raw water by CI02 at water treatment plants in New Castle, Pennsylvania; Charleston, West Virginia; Skagit, Washington; and Columbus, Georgia. Chlorite and chlorate concentrations were unaffected by any of the water treatment processes and did not vary as a function of time of travel in the distribution system. Chlorine dioxide, which was analyzed on-site at two water treatment plants, reformed in the clear well and in the distribution system following post chlorination. The chlorite-removal capability of powdered activated carbon (PAC) was evaluated in both laboratory- and pilot-scale studies. Chlorite removal by PAC in laboratory studies decreased with increasing pH over a range from pH 5.5 to 7.5 and varied with the type of PAC. Chlorite was reduced to chloride at pHs ranging from 5.5 to 7.5, but CI03- formed at the pH 5.5 through 6.0. The pilot plant study; which was conducted at Newport News, Virginia; evaluated CI02 removal by PAC enmeshed in a floc blanket in a pulsed-bed, solids-contact clarifier. An average of 27 percent of the CI02 was removed when the PAC dose was 10 mg/L PAC and 57 percent when it was 20 mg/L PAC. Chlorate was not removed by PAC, but the concentrations could be reduced if the CIOz generator was properly operated. / Master of Science

Typescript (photocopy). / Digitized by Kansas Correctional Industries

Call number: LD2668 .T4 1984 K55 / Master of Science

Thesis (MEng)--University of Stellenbosch, 2000. / ENGLISH ABSTRACT: Peach and apricot shells are agricultural waste products. These waste products accumulate around canneries and food-processing plants in South Africa. No effort is being made to utilise these waste products. This study is the first part of the product development from these products i.e. peach shell activated carbon and apricot shell activated carbon. By producing activated carbon from peach and apricot shells the solid waste problem is addressed, but most of all a profit can be made. But why activated carbon? Activated carbons are unique and versatile adsorbent with a vast amount of adsorption applications. It can be produced via a simple oxidation reaction with steam and the nature of peach and apricot shells are such that it is expected that activated carbons with good adsorption properties can be produced from it. The single largest consumer of activated carbon in South Africa is the gold mining industry that uses imported coconut shell activated carbon for gold adsorption in the gold recovery process. Activated carbon is also used as water purification adsorbents. During this study activated carbons were produced in a fluidized bed reactor at various activation conditions: 700 - 900°C, 0.0425 - 0.0629 g steamlg char.min and 30 - 60 min. This was done in order to find the optimum activation conditions within the activation parameter range. The optimal activated carbons were defined as peach and apricot shell activated carbons that showed good microporous as well as mesoporous character. The optimal activated carbons produced are: peach shell activated at 875°C, 0.0533 g stearnlg char. min, 60 min and apricot shell activated carbon at 850°C, 0.0533 g steamlg char.min, 60min. The possible use of these optimal activated carbons and two other activated carbons produced (Peach shell activated carbon 900°C, 0.0425 g steamlg char. min, 60 min and apricot shell activated carbon 900°C, 0.0425 g steamlg char.min, 60min) were tested in gold recovery and water purification. The gold adsorption properties of peach and apricot shell activated carbons were found to be better than two commercial coconut shell activated carbons (Chemquest 650 and GRC 22). No definite conclusions could, however, be drawn about the replacement of coconut shell activated carbon with peach or apricot shell activated carbon, because abrasion test work and thermal regeneration of the experimental carbons still have to be performed. The experimental activated carbons displayed good phenol adsorption characteristic, although further test work is required. / AFRIKAANSE OPSOMMING: Perske- en appelkoospitte is landbouafvalprodukte. Hierdie afvalprodukte versamel rondom inmaakfabrieke en voedselververkingsaanlegte. Tans word daar geen poging in Suid-Afrika aangewend om hierdie afvalprodukte te benut nie. Hierdie studie is die eerste deel van die ontwikkeling van die produkte: Perskepitdop-geaktiveerde koolstof en appelkoospitdop-geaktiveerde koolstof. Deur geaktiveerde koolstof van die perske- en appelkoospitdoppe te maak, word nie net 'n antwoord op die vastestofafvalsprobleem gevind nie, maar daar kan ook geld gemaak word. Hoekom geaktiveerde koolstof? Aktiveerde koolstowwe is veelsydige en unieke adsorbente met 'n groot verskeidenheid adsorpsie toepassings. Dit kan vervaardig word via 'n eenvoudige oksidasie reaksie met stoom en die aard van die perske- en appelkoospitdoppe is sodanig, dat verwag kan word om geaktiveerde koolstowwe met goeie adsorpsie eienskappe daarvan te kry. Die grootste enkelverbruiker van geaktiveerde koolstof in Suid-Afrika is die goudmynbedryf, wat kokosneutdop geaktiveerde koolstof invoer om goud te herwin. Geaktiveerde koolstof word ook gebruik vir watersuiwering. Tydens hierdie studie IS geaktiveerde koolstowwe by verskillende aktiveeringskondisies in 'n gevloeïdiseerde bed vervaardig: 700 - 900oe, 0.0425 - 0.0629g stoornlg gepiroliseerde pitdoppe.min en 30 - 60 mm. Die aktiveringskondisies is gevarieer om sodoende die optimale aktiveringskondisies binne die aktiveringsparameterreeks te kry. 'n Geaktiveerde koolstof is as optimaal geklassifiseer as dit 'n goeie mikro- sowel as mesostruktuur getoon het. Die optimaal geaktiveerde koolstowwe is: geaktiveerde koolstof vervaardig van perskepitdoppe by 875°e, 0.0533 g stoornlg gepiroliseerde pitdoppe.min, 60 mm en geaktiveerde koolstof vervaardig van appelkoospitdoppe by 850oe, 0.0533 g stoornlg gepiroliseerde pitdoppe.min, 60min. Die gebruik van die twee optimale geaktiveerde koolstowwe sowel as twee ander geaktiveerde koolstowwe (perskepitdop-geaktiveerde koolstof, 900oe, 0.0425 g stoornlg gepiroliseerde pitdoppe.min, 60 min en appelkoospitdop-geaktiveerde koolstof, 850°C, 0.0533 g stoom/g gepiroliseerde pitdoppe.min, 60min) is VIr goudadsorpsie en watersuiwering ondersoek. Die goudadsorpsie eienskappe van die perske-en appelkoospitdop-geaktiveerde koolstowwe was beter as die van twee kommersiële kokosneutdop-geaktiveerde koolstowwe (Chemquest 650 and GRC 22). Daar kan egter geen definitiewe gevolgtrekkings gemaak word oor die vervanging van kokosneutdop geaktiveerde koolstowwe met dié van perske of appelkoospitdoppe nie, aangesien daar nog toetsresultate oor die slytweerstand en reaktiverings eienskappe van die eksperimentele geaktiveerde koolstowwe uitstaande is. Die eksperimentele geaktiveerde koolstowwe toon goeie adsorpie ten opsigte van fenol, maar verdere toetswerk is egter nodig.

A collaborative pilot study of the microflora on biological activated charcoal (BAC) filters employed in the tertiary treatment of drinking water revealed the principle bacterial genera to be Pseudomonas, Alcaligenes, Achromobacter, Bacillus, Micrococcus, Corynebacterium, Chromobacterium, Microcyclus and Paracoccus. The microbial population of the filters paralleled seasonal carbon dioxide production. Of particular interest were the effects of the BAC miroorganisms upon precursors of trihalomethanes (THMs). Mixed populations of BAC microorganisms were cultivated for 50 days in a mineral salts-humic acid medium. It was concluded that (1) the BAC microflora enhances the absorptive capacity of the filters; (2) chemico-physical and biological processes operate in concert to lower the concentration of precursors of THMs; and (3) few bacterial pathogens establish themselves on the filters.

M.Ing. / Rietvlei Dam was completed in 1933, and has been utilized as a drinking water source for the City of Pretoria since then. The original process configuration operated for almost 50 years before being upgraded in 1988. This upgrading was mainly due to the eutrophication of the impoundment. The new plant worked excellently under normal conditions but certain serious problems did occur and full production could not be maintained at all times. Activated Carbon and Ozone are two possible solutions to these problems. This study was directed at investigating the possible implementation of Preozonation, Granular Activated Carbon, and Ozone and Granular Activated Carbon in combination (case study), and it was shown that: All these processes are beneficial to the final water quality. Pre-ozonation proved to be the most cost effective process, but the least effective process in improvement of the water quality. Ozone and Granular Activated Carbon in combination proved to be the least cost effective process, but should be the most effective in improvement of the water quality. Granular Activated Carbon proved to be the optimun process with regard to cost and water quality improvement. The final recommendation is the implementation of Granular Activated Carbon with an empty bed contact time of 10 minutes.

本論文主要探討銠卟啉和銥卟啉絡合物，分別與酮類與醛類進行的鍵活化化學。 / 第一部分主要介紹由β-乙基羥基銠卟啉絡合物(Rh{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH)與酮類進行的羰基碳及α-碳(C(CO)-C(α)) 鍵活化(下稱碳碳鍵活化)。於室溫至50ºC時，在非溶劑的條件下，Rh{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH選擇性地斷裂芳香酮和脂肪酮類的C(CO)-C(α)鍵，生成相對應的銠卟啉酰基絡合物(Rh{U+1D35}{U+1D35}{U+1D35}(ttp)COR, R = 烷基或芳基)，產率最高可達80%。作為銠卟啉羥基絡合物(Rh{U+1D35}{U+1D35}{U+1D35}(ttp)OH)的前體，Rh{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH的活性展示出Rh{U+1D35}{U+1D35}{U+1D35}(ttp)OH是碳碳鍵活化的重要中間體。 / 第二部分主要介紹由β-乙基羥基銥卟啉絡合物(Ir{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH)與芳香醛類進行，具選擇性的醛碳氫鍵活化。在160ºC和非溶劑的條件下，Ir{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH與芳香醛類反應，生成相對應的銥卟啉酰基絡合物(Ir{U+1D35}{U+1D35}{U+1D35}(ttp)COAr)作為碳氫鍵活化產物，產率最高可達72%。銥卟啉羥基絡合物(Ir{U+1D35}{U+1D35}{U+1D35}(ttp)OH)和乙烯配位銥卟啉絡合正離子((CH₂=CH₂)Ir{U+1D35}{U+1D35}{U+1D35}(ttp)⁺)被推斷為醛碳氫鍵活化的可能中間體。 / This research focuses on the bond activation chemistry by rhodium and iridium porphyrin complexes with ketones and aldehyde respectively. / Part 1 describes the C(CO)-C(α) bond activation (CCA) of ketones by Rh{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH (ttp = 5,10,15,20-tetratolylporphyrinato dianion). Rh{U+1D35}{U+1D35}{U+1D35}(ttp)- CH₂CH₂OH selectively cleaved the C(CO)-C(α) bond of aromatic and aliphatic ketones in solvent-free conditions at room temperature to 50ºC, giving the corresponding rhodium(III) porphyrin acyls (Rh{U+1D35}{U+1D35}{U+1D35}(ttp)COR, R = alkyl or aryl) up to 80% yield. The activity of the Rh{U+1D35}{U+1D35}{U+1D35}(ttp)OH precursor, Rh{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH, demonstrates Rh{U+1D35}{U+1D35}{U+1D35}(ttp)OH as the key intermediate in the CCA of ketones. / [With images]. / Part 2 describes the selective aldehydic carbon-hydrogen bond activation (CHA) of aryl aldehydes by Ir{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH. Ir{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH reacted with aryl aldehydes in solvent-free conditions at 160ºC to give the corresponding iridium(III) porphyrin acyls (Ir{U+1D35}{U+1D35}{U+1D35}(ttp)COAr) as the CHA products up to 72% yield. Ir{U+1D35}{U+1D35}{U+1D35}(ttp)OH and (CH₂=CH₂)Ir{U+1D35}{U+1D35}{U+1D35}(ttp)⁺ were proposed as the possible intermediate for the CHA reaction. / [With images]. / Detailed summary in vernacular field only. / Detailed summary in vernacular field only. / Detailed summary in vernacular field only. / Chan, Chung Sum. / "November 2012." / Thesis (M.Phil.)--Chinese University of Hong Kong, 2013. / Includes bibliographical references. / Abstracts also in Chinese. / Abstract --- p.i / Acknowledgement --- p.iii / Table of Contents --- p.iv / Abbreviations --- p.vii / Structural Abbreviations of Porphyrin --- p.viii / Chapter Part 1 --- Carbon-Carbon Bond Activation of Ketones with Rhodium(III) Porphyrin β-Hydroxyethyl --- p.1 / Chapter Chapter 1 --- Introduction --- p.1 / Chapter 1.1 --- Properties of Ketones --- p.1 / Chapter 1.2 --- Carbon(CO)-Carbon(α) Bond Activation (CCA) of Ketones --- p.2 / Chapter 1.2.1 --- CCA of Ketones by Transition Metal Complexes --- p.2 / Chapter 1.2.2 --- CCA of Ketones by Metalloporphyrins --- p.5 / Chapter 1.3 --- Porphyrin Ligands and Rhodium(III) Porphyrins --- p.7 / Chapter 1.3.1 --- Porphyrin Ligands --- p.7 / Chapter 1.3.2 --- Rhodium(III) Porphyrins --- p.8 / Chapter 1.4 --- Rhodium(III) Porphyrin Hydroxide --- p.10 / Chapter 1.4.1 --- Nature of Bonding in Late Transition Metal Hydroxides --- p.10 / Chapter 1.4.1.1 --- Hard-Soft Acid-Base principle --- p.11 / Chapter 1.4.1.2 --- dπ-pπ Interaction Model --- p.11 / Chapter 1.4.1.3 --- E-C Model --- p.12 / Chapter 1.4.2 --- Attempted Preparation of Rhodium(III) Porphyrin Hydroxides --- p.13 / Chapter 1.4.3 --- Chemistry of Rhodium(III) Porphyrin Hydroxides --- p.15 / Chapter 1.5 --- Rhodium(III) Porphyrin β-hydroxyethyl as Rhodium(III) Hydroxide Precursor --- p.18 / Chapter 1.6 --- Objective --- p.20 / Chapter Chapter 2 --- Carbon-Carbon Bond Activation of Ketones with Rhodium(III) Porphyrin β-Hydroxyethyl --- p.21 / Chapter 2.1 --- Preparation of Starting Materials --- p.21 / Chapter 2.1.1 --- Synthesis of Porphyrin --- p.21 / Chapter 2.1.2 --- Synthesis of Rhodium(III) Porphyrins --- p.21 / Chapter 2.2 --- CCA of Diisopropyl Ketone by Rh{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH --- p.22 / Chapter 2.3 --- Optimization of Reaction Conditions --- p.22 / Chapter 2.3.1 --- Atmosphere Effect --- p.22 / Chapter 2.3.2 --- PPh3 Effect --- p.23 / Chapter 2.3.3 --- Solvent Effect --- p.24 / Chapter 2.4 --- Substrate Scope --- p.26 / Chapter 2.4.1 --- CCA of Isopropyl Ketones --- p.26 / Chapter 2.4.2 --- CCA of Non-Isopropyl Ketones --- p.28 / Chapter 2.5 --- Proposed Mechanism --- p.29 / Chapter 2.6 --- Comparison on CCA of Ketones by Different Rh{U+1D35}{U+1D35}{U+1D35}(por)OH Sources --- p.31 / Chapter 2.6.1 --- Reaction Conditions --- p.31 / Chapter 2.6.2 --- Substrate Scope --- p.32 / Chapter 2.6.3 --- Regioselectivity --- p.33 / Chapter 2.7 --- Comparison on Bond Activation of Carbonyl Compounds by Rhodium Porphyrin β-Hydroxyethyl --- p.34 / Chapter 2.8 --- CCA of Ketones with Ir{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH --- p.36 / Chapter 2.9 --- Conclusion --- p.37 / Chapter Chapter 3 --- Experimental Sections --- p.39 / References --- p.54 / List of Spectra I --- p.59 / Spectra --- p.60 / Chapter Part 2 --- Aldehydic Carbon-Hydrogen Bond Activation with Iridium(III) Porphyrin β-Hydroxyethyl --- p.63 / Chapter Chapter 1 --- Introduction --- p.63 / Chapter 1.1 --- Properties of Aldehydes --- p.63 / Chapter 1.2 --- Carbon-Hydrogen Bond Activation (CHA) of Aldehydes --- p.64 / Chapter 1.2.1 --- CHA of Aldehydes by Transition Metal Complexes --- p.64 / Chapter 1.2.2 --- Aldehydic CHA by Metalloporphyrins --- p.74 / Chapter 1.3 --- Iridium(III) Porphyrins --- p.77 / Chapter 1.4 --- Iridium(III) Porphyrin Hydroxide --- p.78 / Chapter 1.4.1 --- Attempted Preparation of Iridium(III) Porphyrin Hydroxides --- p.78 / Chapter 1.4.2 --- Chemistry of Iridium(III) Porphyrin Hydroxides --- p.81 / Chapter 1.5 --- Iridium(III) Porphyrin β-hydroxyethyl as Iridium(III) Hydroxide Precursor --- p.83 / Chapter 1.6 --- Objective --- p.85 / Chapter Chapter 2 --- Aldehydic Carbon-Hydrogen Bond Activation with Iridium(III) Porphyrin β-Hydroxyethyl --- p.86 / Chapter 2.1 --- Preparation of Iridium(III) Porphyrins --- p.86 / Chapter 2.2 --- Aldehydic CHA of Benzaldehyde by Ir{U+1D35}{U+1D35}{U+1D35}(ttp)CH₂CH₂OH --- p.87 / Chapter 2.3 --- Optimization of Reaction Conditions --- p.87 / Chapter 2.3.1 --- Temperature Effect --- p.87 / Chapter 2.3.2 --- Solvent Effect --- p.88 / Chapter 2.3.3 --- PPh₃ Effect --- p.90 / Chapter 2.4 --- Substrate Scope --- p.93 / Chapter 2.5 --- Proposed Mechanism --- p.94 / Chapter 2.6 --- Conclusion --- p.96 / Chapter Chapter 3 --- Experimental Sections --- p.97 / References --- p.108 / List of Spectra II --- p.112 / Spectra --- p.112

Abstract not available

M. Tech. Chemical Engineering. / Discusses the objectives of the research project are to: 1. Develop a cost effective technique for modifying the surface groups of ACs with a view to induce selectivity properties towards PGMs. 2. Characterize the chemically treated ACs. 3. Determine adsorption capacities and selectivity of Amine treated ACs by performing batch adsorption tests. 3. Investigate the adsorption of Pt (IV) in a Continuous stirred tank reactor. The data generated according to the project objectives will assist in obtaining the following informations. 1. Adsorption isotherms - Find the maximum adsorption capacity of ACs for different solution concentrations, and temperature. Determine the effect of base metals on adsorption and hence extend the adsorption isotherm equation from single component to a multi-component adsorption isotherm. 2. Kinetics data - Determine the rate of change of metals in solution with time at various initial concentration, temperature and acid strength. 3. Characterization of modified ACs - Determine surfaces morphology of ACs using SEM-EDS.

M. Tech. Chemical Engineering. / Discusses the reactive properties of oxalate molecules on the surface of activated carbons (ACs) so that they can bind selectively with base metals. Therefore, the experimental plan covered three main axes of study: Chemical modification of AC adsorbent and characterization, adsorption studies in batch and continuous modes, and adsorption modelling.