published_or_final_version / Environmental Management / Master / Master of Science in Environmental Management

2 pp. / [Healthy Fats -- Guide for Improving the Quality of Fat Intake] / The fact sheet reviews healthy fats and how to incorporate a healthy amount of fat into our diet. Fats are necessary for our bodies to function properly. In fact, fats are an important part of a healthy diet and we can't live without them. Fats can be grouped into two groups: saturated and unsaturated. Unsaturated fats include polyunsaturated and monounsaturated fats. Both these fats, when eaten in moderation and used in place of saturated and trans fats, can help lower cholesterol levels and decrease the risk of heart disease. We provide a list of "Do's" and "Tips" which gives examples of how to select fats wisely and incorporate healthy changes into our diet. We also provide a guide for selecting an appropriate portion size of fat.

2 pp. / The fact sheet reviews healthy fats and how to incorporate a healthy amount of fat into our diet. Fats are necessary for our bodies to function properly. In fact, fats are an important part of a healthy diet and we can't live without them. Fats can be grouped into two groups: saturated and unsaturated. Unsaturated fats include polyunsaturated and monounsaturated fats. Both these fats, when eaten in moderation and used in place of saturated and trans fats, can help lower cholesterol levels and decrease the risk of heart disease. We provide a list of "Do's" and "Tips" which gives examples of how to select fats wisely and incorporate healthy changes into our diet. We also provide a guide for selecting an appropriate portion size of fat.

Scum is an integral component of solids management in MWWTP and is composed of fats, oils, grease and other entrained floatable materials that are collected during primary clarification. Lab scale BMP tests showed the addition of 14.5 g VS/L of scum exhibited the greatest increase in biogas production of 1.6 times per g VS added compared to the control, while a higher additional scum loading of 33.7 g VS/L reduced the biogas yield to 32% of the control reactor. Lab scale semi-continuous digestion measured the effects of scum loading and temperature of pretreatment in the scum concentrator. At 15 d and 20 d HRTs the greatest observed improvement in biogas was achieved by adding 3% scum by volume and pretreating the scum at 70°C in a scum concentrator with respective improvements of 24% and 16%.

O chocolate é conhecido mundialmente, proveniente do fruto do cacaueiro (Theobroma cacao) normalmente consumido em forma de barra, mas também podendo ser usado de inúmeras formas como coberturas, recheios dentre outras. Um importante componente na produção do chocolate é a gordura utilizada, uma vez que esta é responsável pela textura, brilho e características organolépticas do produto. O objetivo deste trabalho foi utilizar a manteiga de cupuaçu (proveniente do fruto da Theobroma grandiflorum) na elaboração de chocolate amargo. Para tanto a manteiga de cacau foi substituída de forma parcial e total. Foram desenvolvidas duas formulações de chocolate padrão com liquor de cacau (P1) e com cacau em pó (P2), e quatro formulações com substituição parcial da manteiga de cacau por manteiga de cupuaçu a partir de P2(F1 e F2) e de P1 (F3 e F4). As amostras elaboradas e os ingredientes (líquor de cacau, cacau em pó, manteiga de cacau e manteiga de cupuaçu) foram avaliadas por análise térmica (DSC-Differential Scanning Calorimetry), reologia, tamanho de partícula, composição em ácidos graxos e em triacilgliceróis, índice de temperagem e índice de resfriamento, bem como testes de acompanhamento de 112 dias como cor, atividade de água e textura. A manteiga de cupuaçu apresentou maior quantidade de ácido oleico quando comparada com a manteiga de cacau, aproximadamente 11,5%, e também características reológicas diferentes dos padrões: tensões iniciais variaram de 3,4 ± 0,3 a 7,9 ± 2,0 Pa para as amostras e 2,9 ± 1,4 a 6,2 ± 0,7 Pa para os padrões; viscosidade de 1,6 ± 0,1 a 2,9 ± 0,4 Pa*s para as amostras e 1,9 ± 0,8 a 2,9 ± 0,9 Pa*s para os padrões; tamanho de partícula das amostras de 21 ± 2 a 22 ± 2 &#181;m, padrões de 20 ± 2 a 34 ± 4 &#181;m. Durante os 112 dias de estudo de prateleira: Aw variou de 0,405 ± 0,03 a 0,424 ± 0,02 nas amostras e 0,399 ± 0,03 no padrão; textura variou de 16,3 ± 1,2 a 31,6 ± 2,0 N para as amostras e 25,9 ± 3,0 a 28,6 ± 7,2 N para os padrões; WI variou de 24,1 ± 0,6 a 25,4 ± 0,3 para as amostras e 23,0 ± 0,4 a 23,9 ± 0,8 para os padrões; &#916;E variou de 0,4 a 2,2 para as amostras e de 0,5 a 1,2 para os padrões. Concluiu-se que: A variação do líquor de cacau para cacau em pó acarretou aumentando do tempo total de processo em aproximadamente 15 min. Os chocolates com maior teor de manteiga de cupuaçu apresentaram aumento em triacilglicerol C54, com redução de POP e POS. A faixa de fusão dos chocolates com maiores porcentagens de manteiga de cupuaçu (F3 e F4) foi maior do que para chocolates formulados apenas com manteiga de cacau (P1 e P2). A manteiga de cupuaçu tem relação direta com a queda da tensão inicial e da viscosidade (sem diferença significativa, p<0,05) nos chocolates produzidos. O baixo ponto de fusão do ácido oleico contido na manteiga de cupuaçu alterou a temperatura final e o valor do índice de temperagem nas amostras com maior teor de manteiga de cupuaçu (F3 e F4). / The chocolate is known worldwide, coming from the fruit of the cacao (Theobroma cacao) normally consumed in the form of a bar, but also can be used in countless ways like coverings, fillings among others. An important component in the production of chocolate is the fat used, since it is responsible for the texture, brightness and organoleptic characteristics of the product. The objective of this work was to use cupuassu butter (from the fruit of Theobroma grandiflorum) in elaboration of bitter chocolate. For this purpose, the cocoa butter was partially and totally replaced. Two formulations of standard chocolate with cocoa liquor (P1) and with cocoa powder (P2) were developed, and four formulations with partial replacement of cocoa butter by cupuassu butter from P2 (F1 and F2) and P1 (F3 and F4). The elaborated samples and the ingredients (cocoa liquor, cocoa powder, cocoa butter and cupuassu butter) were evaluated by DSC, rheology, particle size, fatty acid composition and triacylglycerol, temperature index and cooling index, as well as follow-up tests of 112 days such as color, water activity and texture. The cupuassu butter presented a higher amount of oleic acid when compared to cocoa butter, approximately 11.5%, and also different rheological characteristics of the standards: initial tensions ranged from 3.4 ± 0.3 to 7.9 ± 2, 0 Pa for the samples and 2.9 ± 1.4 to 6.2 ± 0.7 Pa for the standards; viscosity of 1.6 ± 0.1 to 2.9 ± 0.4 Pa*s for the samples and 1.9 ± 0.8 to 2.9 ± 0.9 Pa*s for the standards; sample particle size from 21 ± 2 to 22 ± 2 &#181;m, patterns from 20 ± 2 to 34 ± 4 &#181;m. During the 112 days of shelf study: Aw ranged from 0.405 ± 0.03 to 0.424 ± 0.02 in the samples and 0.399 ± 0.03 in the standard; texture ranged from 16.3 ± 1.2 to 31.6 ± 2.0 N for the samples and 25.9 ± 3.0 to 28.6 ± 7.2 N for the standards; WI ranged from 24.1 ± 0.6 to 25.4 ± 0.3 for the samples and 23.0 ± 0.4 to 23.9 ± 0.8 for the standards; &#916;E ranged from 0.4 to 2.2 for the samples and from 0.5 to 1.2 for the standards. It was concluded that: The variation of cocoa liquor to cocoa powder increased the total process time by approximately 15 min. The chocolates with higher content of cupuassu butter presented increase in triacylglycerol C54, with reduction of POP and POS. The melting range of chocolates with higher percentages of cupuassu butter (F3 and F4) was higher than for chocolates formulated with cocoa butter alone (P1 and P2). Cupuassu butter is directly related to the drop in initial tension and viscosity (without significant difference, p <0.05) in the chocolates produced. The low melting point of the oleic acid contained in the cupuassu butter altered the final temperature and the temperature index value in the samples with the highest cupuassu butter content (F3 and F4).

A dissertation submitted to the Faculty of Engineering and the Built Environment, University of the Witwatersrand, Johannesburg, in fulfilment of the requirements for the degree of Master of Science in Engineering September 2017 / Owing to the ongoing advancement in technology, escalating population sizes and urbanization rate, fossil fuels (coal, petroleum oil and natural gas) remain attractive as an energy source to run most of the daily operations. Consequent to heavy consumption of fossil fuels, the world faces detrimental challenges such as future energy security and environmental concerns. Combustion of fossil fuels results in emission of greenhouse gases such as CO2 and SO2 thereby contributing to global warming and acid rain problems. These alarming challenges drive the need for exploration of alternative energy sources to reduce dependence on fossil fuels. Presented in this dissertation is a study of biodiesel, a biodegradable, non-toxic and environmentally benign energy source as an alternative to petroleum-based fuels. Chemically known as fatty acid alkyl ester (FAAE), biodiesel is commonly produced from vegetable oils or animal fats in addition to methanol by a catalysed transesterification reaction. Currently, biodiesel is more expensive than petroleum diesel due to high operation costs incurred during the production process. Despite the high prices, biodiesel production continues to grow on an industrial scale across the world as supported by policy measures and biofuel targets. Researchers have identified two main factors that contribute to high costs of biodiesel production; 1) type of feedstock and 2) type of catalyst used in the production process. Conventional methods of production use edible oils as feedstock. This becomes unjustified due to the potential price hikes in the food market owing to the prospective competition between fuel and food industries. As a result, numerous researchers reported on the use of cheap and non- edible feedstock oils such as waste cooking oil and animal fat. However, the challenge with the use of non-edible oils is their high content of free fatty acids (FFA) which is unattractive for a smooth transesterification process, more especially when homogeneous base catalysts are used. Homogeneous base catalysts are widely used in current industrial biodiesel production methods because they yield faster transesterification processes due to increased reaction rates. However, these types of catalysts are much sensitive to FFA, so when high FFA content feedstock is used, a saponification reaction occurs which consequently reduces the yield of biodiesel. An additional process unit is required to reduce the FFA content via esterification process prior to the main transesterification reaction. Furthermore, since the reaction mixture is homogeneously combined with the product, an additional process unit for product separation is required to recover the resulting biodiesel from the mixture, translating into additional production costs. Researchers are currently exploring the use of heterogeneous catalysts, which tend to avoid the saponification reaction and reduce the need for an esterification reaction used as oil pre-treatment step to reduce FFA content. This dissertation is therefore dedicated to attaining a economic and environmentally attractive process for biodiesel production using cheap non-edible beef tallow oil (BTO) and a heterogeneous hydroxy sodalite (H-SOD) catalyst. Some industrial operations such as zeolite manufacturing processes produce a low grade H-SOD as by products, which is in turn disposed as chemical waste and therefore induces ground water contamination concerns. Exploration on the use of H-SOD as catalyst can largely contribute to the environmental protective measures as a waste management process among other benefits. The use of H-SOD is extensively reported in current research development on membrane separation; limited research reports on the use of H-SOD material to catalyse chemical processes are present in literature. For the first time in open literature, H-SOD is reported as the solid catalyst for biodiesel production in this dissertation. The investigative study commenced with a preliminary study to gauge the feasibility of using H-SOD as a catalyst where a batch transesterification of waste cooking oil (WCO) was studied. The reaction was conducted at 60 ᵒC for 12 h at a methanol-to-WCO ratio of 7.5:1 using 3 wt. % H-SOD catalyst with a particle size of just below 300 Å, the stirring intensity was kept at 1000 rpm to ensure uniform mixing throughout the reaction. The product obtained after the reaction was analysed using a pre-calibrated Chromatography-Mass Spectrometer (GC-MS) described in Chapter 5, and the results demonstrated the possibility of catalysing a transesterification reaction using solid H-SOD. Under the same reaction conditions, the study was then extended to an investigation on the use of H-SOD to catalyze transesterification of BTO (4.53 % FFA) to FAME. The results showed that FAME was produced, at a yield of 39.6% and a conversion of 68.4%. Seeing that the yield and conversion obtained is relatively small compared to literature findings, the effect of some process conditions on the conversion and biodiesel yield were studied. The transesterification reaction was conducted with variations in the mixing intensity (700 – 1250 rpm), catalyst particle size (200 – 300 Å), reaction time (6 – 24 h) and reaction temperature (40-60 °C). The maximum performance of H-SOD catalyst for a transesterification of BTO was achieved with a conversion of 78.3% and biodiesel yield of 62.9% obtained at optimum conditions: a stirrer speed of 1000 rpm, with the smallest catalyst particle size of 200 Å at maximum temperature of 60 °C and 24 h reaction time. The values of activation energy, reaction constants and frequency factor obtained from the kinetic study were 0.0011 min-1, 5.52 x108 min-1 and 79.20 kJ/mol, respectively, and are within the range of the results reported in literature. As a result, solid H-SOD is recommended as a catalyst for the batch transesterification of BTO in a biodiesel production process. / MT2018

Thesis (M.Sc. (Eng.))--University of the Witwatersrand, Faculty of Engineering and the Built Environment, School of Chemical and Metallurgical Engineering, 2016. / The world is gradually shifting to renewable clean energy and away from fossil fuels which are considered to have a finite reserve and have negative impact on the environment. Many alternatives have been developed including biofuels. Of the biofuel family, not all products are produced at the same level given the differences in technological advancements. Commonly produced biofuels which are commercialised are bioethanol and biodiesel. Given that a large number of vehicles operate using gasoline, there is a need to develop biogasoline specific processes to produce biogasoline. Bioethanol is used as a blending agent and has a drawback of engine corrosion. Biogasoline can be used for blending or to substitute gasoline in existing motors. The main objective of the project was to produce biogasoline from waste cooking oil using nano-particle catalyst for better performance. A Co-Mo/Al2O3 catalyst was synthesized and tested in two processes namely thermal cracking and hydrocracking. The waste cooking oil used in this study was pre-treated to remove salts and excess water prior to cracking process. Various analytical techniques were then used to characterize the catalyst, waste cooking oil and the products. Waste cooking oil was successfully pre-treated for salt removal with salt dropping from 13.18% to 4.37%. Effect of catalyst performance on thermal cracking proved to be minimal with temperature being the major factor in cracking. The catalyst performed better under hydrocracking with effects of catalyst calcination temperature and catalyst/oil ratio being more apparent as opposed to thermal cracking. Highest percentage biogasoline achieved under thermal cracking was 81.6% at a reaction temperature of 600°C. The highest percentage biogasoline achieved under hydrocracking was 75.7% at a reaction temperature of 210°C, using calcined catalyst at 700°C, catalyst/oil mass ratio of 1/75 and reaction time of 1hr. The biogasoline produced had low sulphur content. The highest sulphur containing product for hydrocracking was 7.4% and that for thermal cracking was 1.3%. It is recommended that the hydrocracking and thermal cracking methods be used for biogasoline production and that further research be done on the optimization of the biogasoline production process and synthesis of nano Co-Mo catalyst. / MT2016

Caracterizar um quadro experimental que representa excesso de glicocorticoides e verificar esse efeito sobre o metabolismo dos carboidratos no tecido adiposo branco. Ratos foram divididos aleatoriamente em grupo controle (CON) e dexametasona (DEX), e após 4 semanas de tratamento foram sacrificados e os tecidos retirados e analisados. O tratamento foi capaz de bloquear o eixo hipotálamo-hipófise-adrenal, como verificado pela menor concentração de corticosterona plasmática e atrofia das glândulas adrenais no grupo DEX. Além disso, os animais do grupo DEX apresentaram resistência à insulina, intolerância à glicose, dislipidemia e alterações hormonais; além de adipócitos hipertrofiados. Apresentaram também maior lipogênese nos coxins retroperitoneal e mesentérico, sendo que houve maior incorporação de glicose na porção ácido graxo dos triacilgliceróis. Houve maior atividade e expressão das enzimas lipogênicas no grupo DEX. Os resultados mostram que a maior atividade e expressão de enzimas lipogênicas podem justificar o acúmulo de gordura na região visceral. / To characterize an experimental condition of glucocorticoid excess and to verify this effect in carbohydrate metabolism in white adipose tissue. Rats were divided at random into control (CON) and dexamethasone (DEX) groups, and after 4 weeks of treatment they were sacrificed and tissues were excised and analysed. The treatment was able to block hypothalamic-pituitary-adrenal axis, as verified by lower corticosterone plasma levels and adrenal glands atrophy in DEX group. Furthermore, animals from DEX group presented insulin resistance, glucose intolerance, dyslipidemia and hormonal alterations; besides hypertrophied adipocytes. They also presented increased lipogenesis in retroperitoneal and mesenteric fat pads, with increased incorporation into fatty acids of triacylglycerol. There was increased activity and gene expression of lipogenic enzymes in DEX group. The data show that the increased lipogenic enzyme activity and expression could justify increased lipid accumulation in visceral depots.

Investigar os efeitos do consumo de leucina sobre a adiposidade e a funcionalidade do tecido adiposo branco em ratos alimentados com dietas controle ou hiperlipídicas (HL). Ratos obesos foram submetidos a 6 semanas de suplementação com leucina. Ao final, podemos observar que a leucina exerceu efeitos distintos, dependente da condição metabólica em vários parâmetros relacionacidos como a adiposidade. Estas respostas foram pronunciadas no grupo de animais alimentados com dieta HL e suplementados com leucina, principalmente pela maior massa adiposa em diferentes coxins adiposos, maior hipertrofia de adipócitos da região subcutânea (SC), incremento na síntese de novo de ácidos graxos em adipócitos SC, bem como, aumento na incorporação de ácidos graxos em adipócitos SC. Além disso, observamos efeitos da leucina sobre a expressão gênica de PPAR<font face=\"symbol\">g, GPAT, FABP e PEPCK no tecido adiposo SC. Assim, foi demonstrado que a leucina quando utilzada em modelo de obesidade e resistência à insulina acaba favorecendo maior incremento da massa de gordura SC via PPAR<font face=\"symbol\">g. / Investigate the effects of leucine consumption on adiposity and functionality of white adipose tissue in rats fed with control or hyperlipidic (HL) diets. After obesity characterization, animals were submitted to 6 weeks of leucine supplementation. At the end, we could observe that leucine exerted distinct effects, depending on the metabolic condition in several parameters related to adiposity. These responses were more pronounced in animalsfed with HL diet and supplemented with leucine, mainly due to higher adipose mass in different fat pads, larger adipocytes in subcutaneous fat (SC), increase of de novo fatty acids synthesis, as well as, an increase in fatty acids incorporation in SC adipocytes. Furthermore, we observed effects of leucine supplementation on PPAR<font face=\"symbol\">g, GPAT, FABP and PEPCK gene expression in SC fat. Thus, it was demonstrated that leucine supplementation, when used in an obesity and insulin resistance model, favors the increase of adipose mass in SC fat via PPAR<font face=\"symbol\">g.

Lipídeos contidos em resíduos de laticínios além de representarem uma perda industrial importante, interferem negativamente nos sistemas de tratamento de efluentes inibindo a atividade microbiana do consórcio (Mendes, 2005). O objetivo do presente trabalho foi estudar a degradação anaeróbia de gorduras do leite hidrolisadas com duas enzimas: lipase comercial de Candida rugosa (éster-inespecífica), e preparado enzimático de Geotrichum candidum (lipase éster-específica). Determinaram-se condições ótimas de hidrólise de gorduras do leite no tocante a tempo e temperatura de processo. Após esta etapa, determinou-se a produção metanogênica advinda da estabilização de esterco bovino combinado com gorduras de laticínios hidrolisadas e in natura. As condições ótimas de ação de lipase comercial de C. rugosa em gorduras do leite foram obtidas com temperatura de 40ºC e pH de 6,5. As condições ótimas de ação de preparado enzimático de G. candidum foram obtidas com temperatura de 40ºC e pH de 7,5. Os tempos de processo hidrolítico para a produção máxima de ácidos graxos foram de 8 horas e 16 horas quando se utilizaram preparado enzimático de G. candidum e solução de lipase comercial de C. rugosa respectivamente. As velocidades de processo, bem como os valores de biodegradabilidade anaeróbia, produção metanogênica específica e coeficiente de conversão (Yp/s) indicaram ser muito mais eficiente a utilização lipase de C. rugosa na hidrólise das gorduras do leite, quando o objetivo do processo é a produção de biogás. Além disso, o preparado enzimático de G. candidum ocasionou inibição da atividade metanogênica acetoclástica. Quando se realizou um estudo variando-se a concentração de gordura no tratamento enzimático, obteve-se a maior produção de ácido oléico quando se utilizaram 42 gramas de gordura por grama de enzima. Por outro lado, o melhor fator de conversão entre produto e substrato foi verificado quando a relação entre a massa de gordura e a massa de enzima foi igual a 6g/g. / Lipids in dairy waste as well as representing an important industrial loss, interfere negatively in wastewater treatment systems by inhibiting microbial activity of the consortium. The aim of this work was to study the anaerobic degradation of hydrolyzed milk fats using two enzymes: lipase from Candida rugosa, which is an ester unspecific enzyme; and other specific lipase obtained from Geotrichum candidum. Optimal conditions for hydrolysis of milk fat regarding pH, time and temperature were determined. After that, the methanogenic production from the stabilization of cattle manure combined with fats (hydrolyzed and in nature) was evaluated. The optimum conditions for the action of commercial C. rugosa lipase were obtained at 40ºC and pH 6.5. The optimum conditions for the action of G. candidum preparation were obtained at 40ºC and pH 7.5. Maximum product concentrations were obtained within 8 hours and 16 hours when preparation of G. candidum and C. rugosa lipase were used, respectively. The initial methanogenic production rate, the values of anaerobic biodegradation, the specific methanogenic production and the methane yield as well, showed that the use of C. rugosa lipase in the hydrolysis of fats is more efficient when the goal of the process is the production of biogas. The use of the enzymatic preparation of G. candidum did not cause any benefits, and in addition, caused bigger inhibition of acetoclastic methanogenic activity. When the initial concentration of substrate was varied for the enzymatic treatment, it was possible to verify higher oleic acid accumulated production when 42 grams of fat where used per gram of enzyme. On the other hand, the higher conversion factor between product and substrate was obtained when the relation between the mass of fat and the mass of enzyme was 6g/g.