Дисертації з теми "Iron industry and trade Waste disposal"
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Ng, Chiu-ue, and 吳昭榆. "Food waste management in Hong Kong." Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 2013. http://hdl.handle.net/10722/194571.
Повний текст джерелаpublished_or_final_version
Environmental Management
Master
Master of Science in Environmental Management
Leung, Oi-kwan Winnie. "A preliminary study on the Hong Kong external trade of non-ferrous metal waste (and scrap) and other potentially hazardous waste materials /." Hong Kong : University of Hong Kong, 1995. http://sunzi.lib.hku.hk/hkuto/record.jsp?B1470934X.
Повний текст джерелаShoko, Sipiwe. "Valorisation of industrial waste : extraction of bioactive compounds from Brewer’s spent grain." Thesis, Cape Peninsula University of Technology, 2018. http://hdl.handle.net/20.500.11838/2766.
Повний текст джерелаBrewer’s spent grain (BSG), a solid residue obtained from brewing beer, is gaining attention in the food, cosmetics and pharmaceutical industry due to its use as natural source of colorants, texturisers, functional ingredients and preservatives. It is therefore necessary to develop an economically viable method for the extraction, isolation or enrichment of these compounds. Although literature shows the technical feasibility of extraction of bioactive compounds from BSG at laboratory bench scale, none of the reviewed literature could provide adequate information necessary to determine the economic feasibility of the process at commercial scale. The aim of this study was to investigate the technical and economic viability of a commercial process for the recovery of antioxidant rich polyphenolic compounds from brewers spent grain using organic solvents and/or water. The objectives were to select the best solvent, perform the optimisation and kinetic study, as well as to model and simulate the extraction process with the aim of performing an economic analysis. In selecting the best solvent, maceration and soxhlet extraction were used for the recovery of polyphenolic compounds. Acetone and acetone: water mixtures, ethanol and ethanol: water mixtures as well as pure water were used as solvents. The evaluation of the best solvent was measured by the total phenolic content (TPC), flavonol content, the antioxidant activity using 2.2-diphenyl-1-picrylhydrazyl (DPPH) assay and ferric reducing antioxidant power (FRAP) assay. The study performed optimisation for various operational parameters (time, temperature, solvent to feed ratio and shaking speed) using response surface method. The effect of temperature on the extraction kinetics was also investigated with experiments being carried out at 20°C, 40°C and 80°C. Antioxidant activity was detected in all BSG extracts, but water showed the highest global yield and rates of extraction. The optimum conditions were found at 15 min reaction time, temperature of 40 °C, shaking speed of 185 rpm and solvent to solid ratio of 27.5: 1. So-Macdonald model was a suitable fit for the experimental data with a R2-value range of (0.85 < r2 < 0.995). A processing scenario was proposed as a base case, upon which subsequent scenarios were generated to improve the operation or the economics. SuperPro Designer® (Intelligen, Inc) was used for modelling the proposed process, for simulation and for the economic evaluation. Four alternative schemes from the base case simulation were developed for optimisation of the process. The process was found to be economically feasible and attractive with a return of investment (ROI) of 48.45 % for alternative scheme 4. The results in this thesis highlight the likely economic feasibility of the extraction of polyphenolic compounds from BSG at commercial scale by the maceration method.
Lam, Yik-man, and 林奕雯. "Partnership for sustainable waste management: a case study of the food waste recycling partnership scheme in HongKong." Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 2012. http://hub.hku.hk/bib/B48543263.
Повний текст джерелаpublished_or_final_version
Environmental Management
Master
Master of Science in Environmental Management
Mowat, Shaun Phillip. "Economic incentives in controlling pollution in the South African leather industry." Thesis, Rhodes University, 1996. http://hdl.handle.net/10962/d1002745.
Повний текст джерелаNtiribinyange, Mary Solange. "Degradation of textile wastewater using ultra-small Β-Feooh/Tio2 heterojunction structure as a visible light photocatalyst". Thesis, Cape Peninsula University of Technology, 2016. http://hdl.handle.net/20.500.11838/2467.
Повний текст джерелаThe worldwide high demand for drinking water has led to the development of numerous advanced wastewater treatment processes. Photocatalysis has recently become an alternative and attractive technique for green energy production and environmental remediation. It is also a wastewater treatment technique which is considered reliable and is expected to provide a sustainable solution to the scarcity of clean water. In particular, heterogeneous photocatalysts based on TiO2 nanoparticles and sunlight have been proposed as a powerful technique for degradation and mineralisation of persistent organic pollutants (POP`s). Although this method seems promising, some critical challenges are still to be addressed: namely, low photoefficiencies, faster electron and hole (𝑒−⁄ℎ+) pair recombination, utilisation of UV light and catalyst removal after treatment of pollutants.
Rademeyer, Sharon. "Poly(γ-glutamic) acid (PGA) production from confectionery waste using Bacillus species". Thesis, Cape Peninsula University of Technology, 2018. http://hdl.handle.net/20.500.11838/2840.
Повний текст джерелаApproximately 9 million tonnes of food waste is generated annually in South Africa. Its treatment, including treatment of confectionery waste, is costly because of the high chemical oxygen demand (COD) loads; as a result much of this waste is sent to landfill. South Africa’s confectionery industry contributes to a significant proportion of the country’s economy. Among the confectionery waste entering landfills are defective material, expired sweets and returns. This high COD waste can create breeding grounds for pathogenic microorganisms and anaerobic methanogens, causing negative environmental impacts. Part of the Department of Science and Technology (DST) Waste Research, Development and Innovation (RD&I) roadmap initiative is to minimise waste entering landfills by identifying waste sources from which to produce value that will contribute to social and economic growth. Confectionery waste has a high sugar content which can be used for feedstock to bioprocesses. By placing this bioproduction into a waste biorefinery framework, bio-based raw materials can be used to produce competitively priced products with low environmental impact, thereby optimising remediation and value generation simultaneously. Ongoing research at the Centre for Bioprocess Engineering Research (CeBER) at the University of Cape Town has shown that a wastewater biorefinery approach can use wastewater as feedstock for the generation of products of value. Previous studies have investigated potential products of value based on nutrient loads found in wastewater as well as the nature of the product. Among the organisms selected was the Bacillus species, producing the potential product poly-γ-glutamic acid (PGA), an extracellular poly-amino acid when there is an excess of nutrients. Similarly, this product could potentially be produced from sugar-rich waste candy. The aim of this study was to explore the use of hard candy waste as a feedstock for PGA, and Bacillus licheniformis JCM 2505 was selected as it was characterised in terms of the nutrients needed. The most attractive attribute of this strain was that it did not need L-glutamic acid to synthesise PGA but could do so from sugar. L-glutamic acid is costly. Using a cheaper nitrogen alternative would make the process more cost effective. To investigate this potential, the confectionery waste was characterised to identify the nutrients, namely, sugars, organic nitrogen and key trace elements needed for cell function and PGA production. Results showed that the nitrogen content and trace element concentrations were insignificant, as it was determined that the waste consisted mostly of sucrose. This therefore had to be supplemented with a basal medium containing the supplementation needed for cell function and PGA production. The growth of B. licheniformis was profiled in Erlenmeyer shake flasks using candy waste supplemented with the basal medium, with sucrose supplemented with basal medium as a control. The results showed similar trends on candy waste and sucrose.
Ngai, Ho-yee, and 危可兒. "Food waste management in a Hong Kong secondary school campus." Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 2012. http://hub.hku.hk/bib/B4854341X.
Повний текст джерелаpublished_or_final_version
Environmental Management
Master
Master of Science in Environmental Management
Chan, Yip-wai Edward. "A preliminary study on cooking oil waste management in Hong Kong /." Hong Kong : University of Hong Kong, 1998. http://sunzi.lib.hku.hk/hkuto/record.jsp?B2012613X.
Повний текст джерелаJoyce, Jim. "Color and TOC removal from pulp and paper wastes by ultrafiltration." Thesis, Virginia Polytechnic Institute and State University, 1986. http://hdl.handle.net/10919/91035.
Повний текст джерелаM.S.
Tse, Yin-man Jacky. "An independent progress review of the Chemical Waste Treatment Centre in Hong Kong /." Hong Kong : University of Hong Kong, 1995. http://sunzi.lib.hku.hk/hkuto/record.jsp?B1472361X.
Повний текст джерелаTaljaard, Adriana Cecilia. "Critical perspectives on the definition of waste in South Africa : experiences within the steelmaking industry / Taljaard A.C." Thesis, North-West University, 2011. http://hdl.handle.net/10394/7625.
Повний текст джерелаThesis (M. Environmental Management)--North-West University, Potchefstroom Campus, 2012.
Johnson, Hailey E. "Co-utilisation of microalgae for wastewater treatment and the production of animal feed supplements." Thesis, Rhodes University, 2011. http://hdl.handle.net/10962/d1003999.
Повний текст джерелаNdobeni, Afika. "Effect of temperature and carbon to nitrogen ratio on the performance of an upflow anaerobic sludge blanket reactor treating sugarcane molasses." Thesis, Cape Peninsula University of Technology, 2017. http://hdl.handle.net/20.500.11838/2622.
Повний текст джерелаThe sugar industry contributes to the development of the economy in many countries, including South Africa. The wastewater generated by this industry has a high pollution load, and therefore requires treatment before discharge to the environment. The primary aims of this study were to determine the performance of an upflow anaerobic sludge blanket (UASB) reactor treating sugarcane molasses and to develop an empirical model to predict the behaviour of the UASB in terms of chemical oxygen demand (COD) removal and biogas production. A UASB (46 L working volume) was inoculated with granular sludge from the brewery industry and was used to investigate the treatment of synthetic sugar industry wastewater with an average COD of 4101 mg/L. The experiments were designed using Design-Expert® Software Version 10. The analysis of variance for the models and the optimisation of reactor temperature and feed carbon to nitrogen (C/N ratio) were carried out using response surface methodology. The UASB was operated at constant hydraulic retention time and organic loading rate of 2.04 days and 2.01 kg/m3.d, respectively. A start-up period of 22 days was required to reach steady-state. The developed empirical models for total COD removal efficiency and biogas production rate were found to be statistically significant with Prob > F values of 0.0747 and 0.0495 and the determination coefficients (R2) were found to be 0.80 and 0.65, respectively. The optimal conditions were found to be at a temperature of 38oC and C/N ratio of 22 mgTOC/mgTN. The corresponding removal efficiencies in terms of total COD, five day biological oxygen demand, total nitrogen, total phosphorus, and sulphate was 77.7, 85.9, 99.2, 44.4 and 57.2%, respectively. Biogas was produced at a rate of 0.832 L/L.d with a methane, carbon dioxide and molecular oxygen content of 65.2, 32.8 and 0.6%. Results suggest that UASBs may offer a feasible option for reducing the organic strength of sugar industry wastewater, while simultaneously generating methane-rich biogas.
Yee, Lai-wan. "The efficiency of the charging system for industrial wastewater management in Hong Kong /." Hong Kong : University of Hong Kong, 1997. http://sunzi.lib.hku.hk/hkuto/record.jsp?B18976566.
Повний текст джерелаKagaba, James. "Bioprospecting for novel lipases from indigenous olive wastewater biofilms." Thesis, Cape Peninsula University of Technology, 2019. http://hdl.handle.net/20.500.11838/2828.
Повний текст джерелаLipase-catalysed chemical transformations are today routinely considered by synthetic organic chemists as economical and competitive “green chemistry” alternatives. Although lipases can effortlessly be produced on a large-scale by fermentation, their industrial application was, until recently, limited to the detergent, oleo-chemistry and dairy industry. However, during the last few decades, the biotechnological application of lipases has expanded significantly, becoming indispensable in the manufacture of pharmaceuticals, pesticides, single cell protein production, biosensor preparations and waste management. Similarly, lipases have become a vital ingredient in the contemporary food processing industry with applications ranging from fruit juice production to baked foods, vegetable fermentations and dairy enrichment. Furthermore, lipases are routinely used as flavour development agents in cheese, butter and margarine products. Lipases are also applied in the leather industry for processing hides and skins and for treatment of activated sludge and other aerobic waste product treatments where its action enhances oxygen transfer. While lipases currently account for less than 21 % of the enzyme market, a growing interest in lipases is reflected by the publication of an average of 1000 research papers per year and the growing number of available lipases since the 1980s. There is a sustained interest to bioprospect for novel lipase enzymes from available unexplored biodiversity. This study aimed to screen for lipase-producing microorganisms resident in olive wastewater biofilms. Lipase activity of positive isolates was subsequently also quantitatively determined to select for the highest producers of true lipases. A Geotrichum candidum isolate from olive mill wastewater biofilms was selected for subsequent studies based on its superior lipase production phenotype. Using a yeast mediated ligation approach the G. candidum GCL1 lipase gene was cloned and heterologously expressed in Saccharomyces cerevisiae as an enzyme production host. The recombinant lipase was purified and analysed in terms of substrate specificity, pH optima, temperature optima and stability as well as organic solvent tolerance. The G. candidum gcl1 lipase presented enhanced thermo- and organic solvent-stability that are highly sought after traits for industrial application.
Huen, Clay. "Would adopting the ISO 14000 make Hong Kong's solid waste management system more sustainable?" Thesis, Hong Kong : University of Hong Kong, 1998. http://sunzi.lib.hku.hk/hkuto/record.jsp?B19945528.
Повний текст джерелаHoekstra, Dirk Tjalling. "Microbial population dynamics in indigenous olive wastewater biofilms." Thesis, Cape Peninsula University of Technology, 2007. http://hdl.handle.net/20.500.11838/829.
Повний текст джерелаThe olive industry in South Africa, although small compared to the rest of the world, is rapidly expanding and producing increased volumes of wastewater on an annual basis that could in future develop into a major environmental problem. Olive mill wastewater (OMWW) and table olive wastewater (TOWW) are characterised by high chemical oxygen demand (COD), biological oxygen demand (BOD) and phenolic content that are toxic to the environment. Due to the nature of olive wastewater (OWW), its irresponsible and unregulated environmental release will result in oxygen depletion, nutrient enrichment and accumulation of toxic compounds in receiving water bodies that ultimately disrupts aquatic and terrestrial ecosystems. An estimated 3500 - 4500 tons of olives are processed on an annual basis by 51 farmers .in the Western Cape. Economic forecasts predict a steady growth, i.e. increased production and processing of olives in the South African olive industry, in the future due to consumer demand. These production increases will consequently lead to increased volumes of wastewater production, which would, in tum, require an expansion of treatment capacity of the wastewater prior to release. Two South African olive factories were chosen for this study: Buffet Olives, situated in Dal Josefat (Paarl), that produces table olives and Vesuvio Estate on Sorento farm (Wellington) that produce extra-virgin olive oil. Preliminary COD determinations showed that indigenous OWW biofilms within a rotating biological contactor set-up reduced the COD from TOWW and OMWW by 47% and 32%, respectively, over a l0-day period. These preliminary results strongly suggested that biofilms indigenous to OWW have the potential to remediate the pollution problems of OWW. However, the overall aim of this study was to determine how sustainable the application of indigenous biofilms in the OWW are over two production seasons and whether it would be feasible to apply and develop these naturally occurring biofilms as an effective bioremediation tool to reduce the COD and polyphenol content of OWW.
Griessel, Wilmare. "Anaerobic bioconversion of the organic fraction from the fruit processing industry." Thesis, Stellenbosch : Stellenbosch University, 2002. http://hdl.handle.net/10019.1/52651.
Повний текст джерелаENGLISH ABSTRACT: South Africa is a developing country that relies heavily on its agricultural sector for economical welfare especially in the Western Cape Province. However, development gives rise to new technologies, new products, economical stability and unfortunately also to the production of larger volumes of liquid and solid waste. Anaerobic composting is becoming a very attractive treatment option for solid waste disposal because of its unique operational advantages and two valueadded by-products, compost and biogas. Over the last decade progress has been made in anaerobic digestion of solid wastes, but no literature could be found on the anaerobic composting of apple and peach pomace. The main objective of this study was to develop a method to anaerobically compost apple and peach pomace. In the first phase important operational parameters were identified and a method was developed to optimise the parameters. In the second phase of the study, the scaling-up and optimisation of the process were the major objectives. During the first phase of this research 2 L modified glass containers were used as composting units. The most important operational parameters (leachate pH, inoculum source and size, and initial moisture levels) were identified. Anaerobic compost from previous tests, brewery granules and anaerobic sludge were also used as inocula and evaluated for the best source of microbes. After optimising all the identified parameters, good results were obtained, which included higher biogas production, good volume reductions, less bad aromas and a compost product with a neutral pH. After developing the 2 L laboratory-scale method to compost the apple pomace anaerobically, the next step was to ascertain if the method would work if larger volumes of solid fruit waste were composted. A special 20 L composting unit made of PVC was designed to suit the operational requirements of the anaerobic composting process. It was also decided to mix apple pomace and peach pulp together and to use this solid waste source as part of the composting substrate. Different inocula, including cattle manure, anaerobic sludge, brewery granules and anaerobic compost produced in the previous tests, were used. Although good results were obtained with the anaerobic compost and cattle manure as inoculum, the aim was also to decrease the composting period by shortening the pH stabilisation period. To achieve this, it was decided to add NaHC03 to the substrate to be composted to facilitate a faster pH stabilisation. The composting period was subsequently shortened to 25 days with satisfactory results, which included a volume reduction, biogas production and faster pH stabilisation. An upflow anaerobic sludge blanket (UASB) bioreactor was also used to assist the composting process by facilitating the removal of the VFA's present in the composting leachate. This proved to be a valuable addition to the composting process as the UASB bioreactor also provided the composting units with a 'moisturising liquid', which was 'enriched' with a consortium of active anaerobic bacteria when the effluent from the bioreactor was re-added to the composting units. With all the operational parameters in place, good results were obtained and these included a volume reduction of 60% (m/m), a good biogas production, a composting period of only 25 days, a compost that was free of bad aromas, a final compost pH of > 6.5, final leachate COD values of less than 3 000 rnq.l", and a final leachate VFA's concentration of between 0 and 250 rnq.l". If in future research further scaling-up is to be considered, it is recommended that the composting unit be coupled directly to the UASB bioreactor, thus making the process continuous and more practical to operate. If the operational period of the anaerobic composting set-up could be further shortened and the inoculum adapted so that the process could be used for the treatment of other difficult types of solid wastes, it would probably be advantageous for the fruit processing industry to use this method as an environmental control technology.
AFRIKAANSE OPSOMMING: Suid-Afrika is 'n ontwikkelende land wat baie afhanklik is van die sukses van die landbousektor vir ekonomiese welstand, veral in die Wes Kaap Provinsie. Ontwikkeling gaan gepaard met nuwe tegnologie, nuwe produkte, ekonomiese stabiliteit en daarmee saam gaan die produksie van groter volumes vlooiebare en soliede afvalprodukte. Anaërobiese kompostering is tans besig om opgang te maak as en doeltreffende behandelingstegnologie vir vaste afvalstowwe. Tydens die laaste dekade is baie vooruitgang gemaak in die veld van anaërobiese vertering asook kompostering van afvalmateriaal met en hoë vaste stof inhoud. Anaërobiese kompostering van appel- en perskepulp, afkomstig van die versappingsindustrie, het tot dusver min aandag geniet. Die hoofdoel van hierdie navorsing was om 'n anaërobiese komposterings metode te ontwikkel vir die beheer van vrugte afval om sodoende die basis neer te lê vir en nuwe tegnologie wat baie voordele (biogas en kompos) inhou. In die eerste fase is die belangrikste operationele parameters geïdentifiseer om sodoende beter beheer oor die anaërobiese proses uit te oefen. In die tweede fase is die anaërobiese proses wat gedurende die eerste fase ontwikkel is, opgeskaal om optimum resultate te verkry. Gedurende die eerste fase van hierdie verhandeling was 2 L gemodifiseerde glas houers gebruik as komposteringseenhede. Die belangrikste operasionele parameters (pH beheer, inokulasie grootte, vloeistofvlakke en hoeveelheid vog asook vlugtige vetsuur produksie en verwydering) vir die beheer van die anaërobiese komposteringsproses was geïdentifiseer en gebruik as uitgangspunt om 'n anaërobiese komposteringsmetode te ontwikkel. Anaërobiese slyk, brouery granules en anaërobiese kompos van vorige eksperimente was as inokula gebruik. Gedurende hierdie studies was goeie resultate verkry en het 'n hoë biogas produksie, goeie volume reduksies, vermindering van slegte aromas en kompos met 'n neutrale pH ingesluit. . Nadat hierdie goeie resultate met die 2 L laboratorium-skaal metode verkry was, was groter volumes vaste vrugte afval gebruik om te bepaal of dieselfde metode toegepas kan word op en groter skaal. Spesiale 20 L komposteringseenhede was ontwerp om aan die operasionele vereistes van 'n anaërobiese proses te voldoen. Dit was ook besluit om appel pulp met perske pulp te meng en te gebruik as deel van die komposteringssubstraat. Verskeie inokula was weereens gebruik en het die volgende ingesluit: vars beesmis, anaërobiese slyk, brouery granules en anaërobiese kompos van vorige eksperimente. Hoewel baie goeie resultate met vars beesmis en anaërobiese kompos as inokula verkry was, was 'n volgende doel gewees om die kompoterings tydperk te verkort deur die pH vinniger te stabiliseer. Daar was besluit om NaHC03 by die komposteringssubstraat te voeg en so 'n vinniger pH stabilisasie te fasiliteer. 'n UASB ('upflow anaerobic sludge blanket') bioreaktor was ook gebruik om die komposteringsproses aan te help deur die vlugtige vetsure wat in die kompostloog teenwoordig was, te verwyder. Die insluiting van die bioreaktor in die anaërobiese komposteringsproses het bygedra tot die sukses van die proses deurdat die uitvloeisel as 'n vogmiddel vir die komposteringseenhede gebruik was en 'n konsortium van aktiewe anaërobiese bakterieë bevat het. Nadat al die operationele parameters in plek was, was goeie resultate bereik en het die volgende ingesluit: 'n volume reduksie van 60% (m/m), goeie biogas produksie, 'n komposteringstyd van 25 dae, 'n kompos wat vry was van slegste aromas, 'n finale kompos pH van >6.5, finale loog CSB van <3 000 rnq.l' en 'n finale vetsuur konsentrasie van tussen 0 en 250 mq.l'. lndien verdere navorsing onderneem word, word dit aanbeveel dat die UASB bioreaktor direk aan die komposteringseenheid gekoppel word om sodoende die proses meer aaneenlopend en die proses prakties makliker uitvoerbaar te maak. Indien die operationele tydperk nog korter gemaak kan word en die inokulum aanpasbaar kan wees om moeilik verteerbare afvalprodukte te akkomodeer, sal hierdie tegnologie baie voordelig wees as 'n metode om omgewingsbesoedeling te beheer
De, Lange Ruan. "The effectiveness of implementing eco initiatives to recycle water and food waste in selected Cape Town hotels." Thesis, Cape Peninsula University of Technology, 2012. http://hdl.handle.net/20.500.11838/1607.
Повний текст джерелаThe objective of the research study was to investigate how effective an eco initiative to recycle water and food waste would be when implemented in selected Cape Town hotels. Earthworm farms are able to convert organic food waste into usable compost as an alternative to landfills. Harvesting rainwater as a direct method for the reuse of waste water makes it possible to store captured rainwater for future use. This serves as an alternative source of surface water. The study further investigated whether implementing these initiatives would be successful as a future endeavour. Environmental movements were the instigators of the high demand for recycling initiatives. These movements aimed to address the deteriorating quality of water supplies, as well as growth in landfills. In South Africa, a decrease in the availability and quality of surface water has been coupled with an annual increase of 3.7 % in the demand for water. Landfills furthermore release toxic smoke when burned. Within the Hospitality Industry, travelers are increasingly seeking out environmentally friendly hotels as part of their corporate travel policy. This has occurred as a result of the increased focus on environmental initiatives by the International community. The researcher therefore aimed to provide practical examples of how existing theory regarding these initiatives is applicable to operations within hotels. The research methodology was determined through analysing the research strategy, the design and the research instruments. The research strategy was based on gathering facts relevant to the theory of the study. A descriptive approach was therefore adopted as the “-what-” question that was asked when measuring data to answer the research questions. The research design utilised a multi-strategy approach whereby both quantitative and qualitative data were gathered. This resulted in questionnaires, interviews and case studies forming part of the research instruments. The researcher found it effective to corroborate the findings from both quantitative and qualitative data: that is, the findings from the questionnaires were enhanced by the findings from the interviews. The case studies were conducted to provide a practical context to the theory. Recommendations have been made according to technological and social developments. Ultimately, this study illustrates the success of eco initiatives aimed at recycling water and food waste produced by selected hotels in Cape Town and a reduction in the waste generated by the hotels.
De, Jager Debbie. "Membrane bioreactor application within the South African textile industry: pilot to full-scale." Thesis, Cape Peninsula University of Technology, 2013. http://hdl.handle.net/20.500.11838/926.
Повний текст джерелаTo date, limited information has been published on textile wastewater treatment, for re-use, in South Africa (SA), with treatment processes focusing on conventional wastewater treatment methods. A large contributor to the contamination of water within textile industries is from dyehouse processes. A major concern in textile wastewater treatment is the release of azo dyes and their metabolites, some of which are carcinogenic and mutanogenic, into the environment since they are xenobiotic and aerobically recalcitrant to biodegradation. A necessity therefore exists to find an effective treatment method capable of removing both the strong colour and the toxic organic compounds from textile wastewater. Membrane bioreactors (MBRs) are favoured when treating high-strength wastewater, since the membrane area is determined by the hydraulic throughput and not the biological load; no sludge is wasted and all bacteria are retained within the reactor, including specific bacteria capable of degrading the toxic, non-biodegradable constituents present in textile wastewater. MBR systems, using various configurations have been utilised extensively in the rest of the world to treat textile wastewater at both lab and pilot-scale. This DTech project formed part of a collaborative Water Research Commission (WRC) funded project K5/1900 - Pilot application of a dual-stage membrane bioreactor (dsMBR) for industrial wastewater treatment. The main purpose of this study was the on-site evaluation of a pilot-scale dsMBR incorporating two ultrafiltration (UF) sidestream membrane modules for the treatment, recovery and re-use of textile wastewater. The objectives of this project were to determine the treatment efficiency of the system; to evaluate the degree of colour removal from the textile wastewater; to improve residual colour removal within the system using treatment processes, such as NF and RO, as well as to propose a design and cost for a full-scale plant. A textile industry located in Bellville, Western Cape, was chosen as the industrial partner for the on-site evaluation of a semi-automated pilot wastewater treatment MBR plant using two 5.1 m2 Norit X-flow AirliftTM membrane modules. Since the wastewater treatment system was located on the premises, real continuously changing industrial wastewater was being treated. The industrial textile wastewater was treated in a series of tanks: 1) an anaerobic tank, which cleaved the azo bonds of the reactive dyes; 2) an anoxic tank containing reduced amounts of dissolved oxygen, in which denitrification occurred; and 3) an aerobic tank, in which i) nitrification, as well as ii) mineralisation of the aromatic amines occurred. The UF-membrane modules would account for the removal of any organic material. The wastewater stream was characterised by a chemical oxygen demand (COD) range of between 45 to 2,820 mg/L and an average biological oxygen demand (BOD) of 192.5 mg/L. The dsMBR achieved an average COD reduction of 75% with a maximum of 97% over the 220 day test period. The COD concentration obtained after dsMBR treatment averaged at 191 mg/L, which was well within the City of Cape Town industrial wastewater discharge standard. The average reduction in turbidity and TSS was 94% and 19.6%, respectively, during the UF-MBR stage of the system. Subsequent treatment of the UF permeate with nanofiltration (NF) for 4 days, alternated with reverse osmosis (RO) for 14 days removed both the residual colour and salt present in the UF permeate. A consistent reduction in the colour of the incoming wastewater was evident. The colour in the wastewater was reduced from an average of 659 ADMI units to ~12 ADMI units in the NF permeate, a lower American dye manufacturing index (ADMI) (i.e. method of colour representation) compared to the potable water (~17 ADMI units) utilised by the industrial partner in their dyeing processes. The colour was reduced from an average of 659 to ~20 ADMI units in the RO permeate, a lower ADMI and therefore colour when compared to the potable water. An average conductivity rejection of 91% was achieved with conductivity being reduced from an average of 7,700 to 693 μS/cm and the TDS reduced from an average of 5,700 to 473 mg/L, which facilitated an average TDS rejection of 92%. Based on the composition of the UF permeate fed to the RO membrane a maximum removal of 98.7% was achieved for both conductivity and total dissolved solids (TDS). The proposed full-scale plant would incorporate a UF-MBR system, followed by NF, RO, flocculation and a filter press. Therefore, the two waste products produced during operation of the proposed full-scale plant, would be the solid filter cakes and the liquid filtrate from the filter press. Implementing the proposed full-scale plant it would cost the industrial partner an operating cost of ZAR 113.85 and ZAR 3,415.49 to treat 97.1 m3 and 2,913 m3 of textile wastewater, respectively, per day and per month. This results in an annual saving of ZAR 845,848 on potable water expenses. This research, would provide SA textile industries, with an option to: 1) reduce their water consumption, thereby utilising less of a valuable decreasing commodity; 2) meet the SA government discharge standards and reduce their discharge costs; 3) reduce their carbon footprint (i.e. reduce their impact on the environment) by re-using their treated wastewater and therefore using less water from the municipality; and 4) decrease their annual expenditure on water, since the treated wastewater would be available for re-use.
Yee, Lai-wan, and 余麗容. "The efficiency of the charging system for industrial wastewater management in Hong Kong." Thesis, The University of Hong Kong (Pokfulam, Hong Kong), 1997. http://hub.hku.hk/bib/B30101062.
Повний текст джерелаRadoll, Geni Portela. "Avaliação da genotoxicidade em efluentes líquidos da indústria frigorífica." Universidade Tecnológica Federal do Paraná, 2013. http://repositorio.utfpr.edu.br/jspui/handle/1/947.
Повний текст джерелаThe degradation of water quality by the discharge of industrial wastewater, even treated to some degree, has been affecting the health of aquatic organisms, including being able to affect the health of humans, featuring a global environmental problem. Liquid effluents from the food industries A and B, the object of this study with recognized genotoxic potential, are only monitored through physical and chemical analyses. Thus, the present study aimed to evaluate the treatment system of wastewater from two food companies and their genotoxic effects in Astyanax sp. Fish were exposed to wastewater pre and post treatment as well as upstream and downstream of the release. The genotoxicity was evaluated according to the technique of the comet assay and micronucleus test in piscine. Physical, chemical and biological parameters of: temperature, pH, dissolved oxygen, alkalinity, volatile acids, COD, BOD5.20, total nitrogen, total phosphorus and coliforms were analyzed. Genotoxic analysis in 600 specimens of Astyanax sp, which exposed for 96 hours to raw wastewater, after treatment, and downstream water body in the two industries were used. The results obtained from this study indicated that in all samples, including post processing and downstream of the release, statistically significant damages were observed in the genetic material of the fish analyzed, with (p<0,0001). The results showed that the wastewater from industries A and B evaluated in this study, have genotoxic potential to cause harm to living organisms in the ecosystems in which they are embedded.
Hinojosa, Eduardo Alberto Lazo. "Remoção de matéria orgânica e cor de efluente kraft por adsorção usando carvão ativado e argila." Universidade Tecnológica Federal do Paraná, 2014. http://repositorio.utfpr.edu.br/jspui/handle/1/1302.
Повний текст джерелаAtualmente há preocupação da sociedade em relação aos impactos gerados pelas indústrias ao meio ambiente. Para produção de celulose e de papel é usada grande quantidade de água, madeira e produtos químicos, sendo gerado efluente nos diferentes processos produtivos da indústria. A matéria orgânica e a cor do efluente do processo Kraft se devem à presença de moléculas derivadas da lignina que são difíceis de serem removidas ou biodegradadas. Com vistas à remedição deste efluente, o presente trabalho busca avaliar a remoção de cor e matéria orgânica residual de efluente de celulose Kraft pré-tratado biologicamente, usando carvão ativado de casca de coco e argila montmorilonita pelo método de adsorção através de delineamentos experimentais. Para remoção de cor e matéria orgânica foram avaliados os fatores: a) pH do efluente; b) massa do material adsorvente no processo de adsorção e c) temperatura. A capacidade de adsorção de matéria orgânica e cor no carvão ativado e argila montmorilonita foram determinados pelo modelo matemático de Langmuir e Freundlich, por meio de ensaios de construção de isotermas de adsorção em efluente Kraft. O efluente foi caracterizado quanto a DQO, DBO5,20, COT e cor verdadeira antes e depois do tratamento terciário. Para o tratamento do efluente foram empregadas duas temperaturas: 25 e 40°C, seguiu-se planejamento fatorial completo 32 em triplicata com ponto central tendo como variáveis pH (5,0; 6,0 e 7,0) e massa de material adsorvente (0,5; 1,0 e 1,5 g). O planejamento experimental utilizado permitiu obter os melhores resultados com carvão ativado em 40 °C, pH 7,0 e 1,5 g de adsorvente com remoção de: 98% de COT, 83% de DQO, 97% de DBO5,20 e 95% de cor verdadeira e para argila em temperatura de 40 oC, pH 7, e 1,5 g de adsorvente com remoção de: 55% de COT, 50% de DQO, 90% de DBO5,20, e 56% de cor verdadeira. A principal variável responsável pela remoção de cor e matéria orgânica foi a massa de adsorvente seguida do pH. Também foi avaliada a possibilidade de aproveitamento do resíduo obtido a partir do processo de adsorção na incorporação de cinzas de carvão na produção de argamassas com teores de 0,4%, 1,0% e 1,2%; em cimento portland, areia e água com tempos de cura de 7 e 28 dias fazendo testes de resistência à compressão. Para a reutilização da argila foram utilizados 15% de argila do processo de adsorção, 25% de vidro e 60% de argila vermelha, para a confecção de corpos de prova cerâmico à temperatura de 1100 oC a 1150 oC. De modo geral, o processo de tratamento proposto neste trabalho utilizando carvão ativado, demostrou ser boa alternativa comparado com argila montmorilonita para redução de cor e matéria orgânica residual do efluente de processo Kraft, tendo-se em vista a utilização da cinza do carvão utilizado no processo de adsorção como um agregado para formação de argamassas na construção civil e argila utilizada na adsorção como material cerâmico.
Nowadays, there is a concern of society regarding the impacts caused by the industries on the environment. Large amounts of water, wood and chemichal are used to produce cellulose and paper, and contaminated effluents are generated through the various industrial processes associated. The organic matter and the color of the Kraft effluent are due to the presence of lignin-derived molecules that are difficult to be removed or biodegraded. With intent to remediate this effluent, this study aim to evaluate the removal of color and residual organic matter from biologically pretreated Kraft effluent, using activated carbon from coconut shell and montmorillonite clay by adsorption method through experimental designs. For the color and organic matter removal, the following factors were evaluated: a) pH of the effluent; b) the mass of the adsorbent material in the adsorption process and c) temperature. The adsorption capacity of organic matter and color in the activated carbon and in the montmorillonite clay were determined by the mathematical model of Langmuir and Freundlich, by means of isotherm adsorption construction in Kraft effluent.The effluent was characterized by COD, DBO5,20, COT and true color before and after the tertiary treatment. For it treatment two temperatures were employed: 25 °C and 40 °C, followed by a 32 full factorial design with center point in triplicate, using pH (5.0, 6.0 and 7.0) and masses of adsorbent material (0.5, 1.0 and 1.5 g) as variables. The experimental design used showed that the best results with activated carbon are obtained at 40 ° C, pH 7.0 and 1.5 g of adsorbent with removals of 98% of TOC, 83% of COD, 97% of BOD5,25 and 95% of true color. With clay, the best results occurred at temperature of 40 ° C, pH 7, and 1.5 g of adsorbent to remove 55% of COT, 50% of COD, 90% of BOD5,20 and 56% of true color. The main responsible for the removal of color and organic matter was the mass of adsorbent, followed by the pH. It was also evaluated the possibility of using the residue obtained from the adsorption process in the incorporation of carbon ash to produce mortars with levels of 0.4%, 1.0% and 1.2% in Portland cement, sand and water, with curing times of 7 and 28 days, for which compressive strength tests were performed. To reuse the clay, 15% of the clay from the adsorption process was used, together with 25% of glass and 60% of red clay, in order to construct ceramics bodies specimen generated at temperatures from 1100 °C to 1150 °C. The treatment process proposed in this work using activated carbon demonstrated to be, in general, a good alternative compared to montmorillonite clay for the color reduction and residual organic matter removal from Kraft process effluent, while residues from both process can be used as aggregates for mortars and ceramic body production.
Ngenda, Banka Richard. "Etude de valorisation des rejets des usines à zinc de Kolwezi, République démocratique du Congo." Doctoral thesis, Universite Libre de Bruxelles, 2010. http://hdl.handle.net/2013/ULB-DIPOT:oai:dipot.ulb.ac.be:2013/210144.
Повний текст джерелаA l’aide des techniques modernes de caractérisation (physico–chimique, minéralogique et morphologique), nous sommes arrivés à cibler, à adapter et à justifier l’utilisation d’une technique de valorisation des matières minérales existantes. Les minéraux utiles contenus dans les rejets UZK ont été sulfatés par digestion et sélectivement mis en solution après un grillage. La sulfatation s’est avérée l’étape déterminante du procédé et un intérêt particulier a été focalisé sur cette étape en réalisant une étude cinétique approfondie.
Les données et informations récoltées tout le long de cette recherche nous ont permis de réaliser une simulation du procédé par le logiciel ASPEN PLUS. Ce qui a permis de faire une ébauche d’un schéma de traitement industriel. Ce dernier s’est avéré souple vis-à-vis de l’utilisation d’autres matières comme les calcines des concentrés sulfurés cuivre-zinc.
Residues from the Kolwezi Zinc Plant (Usines à Zinc de Kolwezi UZK) essentially contain zinc in a refractory (ferrite) form, which is difficult to recover by conventional hydrometallurgical methods. « Heavy» metals are also present that make them hazardous towards the environment in which they are currently stored. Most of these metals are valuable; thus, the UZK residues are a real secondary deposit. It is therefore imperative to develop an appropriate method of treatment, hence the theme of the present thesis: « Recovery study of values metals from Kolwezi Zinc Plant residues, DRC ».
Using modern techniques of characterization (physical and chemical, mineralogical and morphological), we focused, adapted and justified the use of a technique for efficient recovery of the existing valuable minerals. The minerals contained in UZK residues have been sulphated by digestion and thereafter selectively dissolved after roasting. Sulphatation proved to be the decisive step of the process and a particular attention has been given to this step by performing a detailed kinetic study.
The data and information collected throughout this research allowed a simulation of the developed method by using the « Aspen Plus » software. This allowed us to propose a draft scheme of industrial processing. The latter proved flexible towards the use of other materials such as calcines of copper-zinc sulphide concentrates.
Doctorat en Sciences de l'ingénieur
info:eu-repo/semantics/nonPublished
"Chemical monitoring and waste minimisation audit in the electroplating industry." Thesis, 2004. http://hdl.handle.net/10413/2157.
Повний текст джерелаThesis (M.Sc.)-University of KwaZulu-Natal, Pietermaritzburg, 2004.
"Application of chemical analysis as an aid to waste minimisation in the electroplating industry." Thesis, 2009. http://hdl.handle.net/10413/2613.
Повний текст джерелаThesis (M.Sc.)-University of KwaZulu-Natal, Pietermaritzburg, 2009.
Hunt, Neil Adrian. "Application of acidogenic solids removal in the biological treatment of wastewater from a Bagasse based pulp and paper mill." Diss., 2002. http://hdl.handle.net/2263/29080.
Повний текст джерелаOtieno, Dennis Ouma. "Treatment of tea industry effluents using a combined adsorption and advanced oxidation process." 2014. http://encore.tut.ac.za/iii/cpro/DigitalItemViewPage.external?sp=1001708.
Повний текст джерелаDiscusses the general objective of this research is to study the application of a combined advanced oxidation and adsorption process, with a view to developing a novel technique for the treatment of tea industry effluents prior to discharge into receiving water bodies. The specific objectives of the research are: a) To tailor natural zeolite physico-chemical properties in attempt to enhance its adsorptive performance ; b) To evaluate the decolourization efficiency of functionalized zeolite in tea industry effluent treatment. c) To evaluate the effect of the following operational parameters: pH, initial concentration,temperature and the sorbent mass, on the removal of colour in tea industry effluent. d) To apply adsorption and advanced oxidation independently and to combine the two into one process.
Ndlovu, Vuyani. "Waste water treatment of effluents from corn processing plant." Thesis, 2013. http://hdl.handle.net/10413/11095.
Повний текст джерелаThesis (M.Sc.Eng.)-University of KwaZulu-Natal, Durban, 2013.
Chamane, Ziphathele. "The effect of biomass acclimation on the co-digestion of toxic organic effluents in anaerobic digesters." Thesis, 2008. http://hdl.handle.net/10321/592.
Повний текст джерелаCurrently KwaZulu-Natal (KZN) province is populated with textile industry, which produces wastewater, some of which is not biodegradable. Due to the stringent environmental regulations the wastewater cannot be discharged into the rivers or public owned treatment systems. The alternative solution is to co-dispose this wastewater with easily biodegradable waste (labile effluent). The aim of this investigation was to develop a process protocol for the codigestion of high strength and toxic organic effluents under mesophilic conditions (35°C ± 2°C), with emphasis on the effect of biomass acclimation. A total of four effluents were chosen for this study, two labile (distillery and size) and two recalcitrant (scour dye and reactive dye). Two anaerobic batch experiments and two pilot scale trials were performed. The first batch anaerobic experiment investigated the influence of biomass source in anaerobic treatability. The second batch test investigated, whether biomass acclimation enhanced the biodegradability of pollutants. The pilot scale trials were the scale up version of the biomass acclimation test. The results showed sludge from Umbilo Wastewater Treatment Works was a superior biomass source, producing more gas and methane compared to Mpumalanga waste. For the high strength organic waste, the acclimated size and distillery samples produced 50% more biogas and methane compared to non-acclimated samples. This confirms that the biomass acclimation enhances the biodegradability. The biomass acclimation did not enhance the biodegradability of the recalcitrant effluent (scour dye). The pilot scale trials did not yield meaningful data; therefore it could not be proven if acclimation works on a larger scale.
Thambiran, Namo. "An investigation of a waste minimisation club for the metal finishing industry." Thesis, 2002. http://hdl.handle.net/10413/4819.
Повний текст джерелаThesis (M.Sc.Eng.)-University of Natal,Durban, 2002.
West, D. W. "Responses of wild freshwater fish to anthropogenic stressors in the Waikato River of New Zealand." 2007. http://adt.waikato.ac.nz/public/adt-uow20070828.145414/index.html.
Повний текст джерелаNdhlovu, Maanda Luxious. "Frantz Fanon and critique of the post-apartheid South Africa in relation to socio-economic development." Diss., 2017. http://hdl.handle.net/10500/26871.
Повний текст джерелаDevelopment Studies
M.A. (Development Studies)
Mahlangu, Mpanyana Lucas. "Waste tyre management problems in South Africa and the possible opportunities that can be created through the recycling thereof." Diss., 2009. http://hdl.handle.net/10500/1307.
Повний текст джерелаEnvironmental Sciences
M.A. (Environmental Management)