Thesis (M.S.)--Missouri University of Science and Technology, 2009. / Vita. The entire thesis text is included in file. Title from title screen of thesis/dissertation PDF file (viewed August 31, 2009) Includes bibliographical references (p. 51-56).

Thesis (M.S.)--Humboldt State University, 2007. / Includes bibliographical references (leaves 42-46). Also available via Humboldt Digital Scholar.

Thesis (M.A. Sc.)--University of Ottawa, 2003. / Includes bibliographical references. Abstract and 24 page preview available online.

Thesis (M. A. Sc.)--University of Toronto, 2003. / Includes bibliographical references (p. 76-80 of photocopy). Abstract and 24 page preview available online.

Submitted in fulfillment of the requirements for the Degree of Master of Technology: Chemical Engineering, Durban University of Technology, 2014. / Biodiesel is a renewable fuel that can be produced from animal fats, vegetable oils or recycled used cooking oil. From the 1970’s, biodiesel received increased focus as an alternative to crude oil and its component products. Among various processes used for biodiesel production, transesterification of glyceride and alcohol in the presence of a catalyst to produce ester (biodiesel) and glycerin remains the most common. In Africa, biodiesel is currently produced industrially in a number of ways via different methods. In South Africa, there are a number of biodiesel production plants that are continuous processes with feed samples from different sources. Reviewing the batch systems for developing economies, various observations were made. Some produced biodiesel using batch systems at room or day temperatures, another used different temperatures, some also used flat based buckets for their mixing and so on. This becomes difficult for local producers who desired to produce biodiesel on a very small scale for their farms or business. Hence, the study was aimed at evaluation batch biodiesel systems and to come up with a simplified approach for a producer in a developing economy or a local user. The objectives of this study were as follows; To evaluate biodiesel production options, and hence develop a simplified process that can be used to produce biodiesel in developing economies. The criteria for evaluation will include: ease of operation, non-specialist equipment, range of feedstock, product quality and product yield. To evaluate various factors that affect these criteria and make recommendations that will enable a local producer to remain within an optimum range Compare the produced biodiesel properties against general biodiesel and petroleum diesel ASTM standard range Recommend simplified equipment design for a local producer Perform economic evaluation to establish cost required both for equipment and raw materials for a local producer. After literature review on the existing processes, base catalyzed transesterification was selected. This is because of the simplicity as well as ease of operation. Experimental trials commenced using feeds from pure vegetable oil (PVO) and waste vegetable oil (WVO) to familiarize biodiesel production, as well as study the behavior of each having the research criteria in focus. Various variables that affect ease of operation, product quality, and yield were also investigated. These include temperature, type of catalyst (KOH or NaOH), type of alcohol (Methanol or Ethanol), concentration of catalyst, and purity of alcohol, and nature of feed (PVO or WVO). The effect of temperature was compared against product quality, yield, and ease of operation. Other variables were also compared against the same criteria. Treatment of WVO because of impurity and moisture contamination associated with such samples was also studied. The product was then tested using some ASTM procedures to compare biodiesel quality to acceptable standards. Efficient reaction time is paramount for a quality biodiesel. It was observed that biodiesel required between 25 and 30 minutes for a complete reaction. Lower temperatures clearly affected the quality of biodiesel produced. Best operating range was found to be between 55 oC – 75 oC is usually recommended for a transesterification reaction to obtain optimum yield and quality. The use of KOH compared to NaOH yields similar results even though NaOH is usually selected because of the reduced cost. The use of methanol compared to ethanol also yields similar results, even though methanol is usually preferred due to cost. Purity of available alcohol is vital as its reduction from 99.5 % to 75 % during experimental trials, yielded poor quality biodiesel. This is mainly due to moisture content that usually gives room for bacteria growth and corrosion of fuel lines in engines. As long as a titration test is carried out on the feed, the use of WVO is a good option. Varying catalyst concentrations from 0.5 % to 1.75 % were considered and the best regimes identified. This test will enable a producer from a growing economy to use the appropriate reagent, which will ensure the transesterification reaction is complete. After comparing appleseed and cone based design, the latter was selected as it will eliminate any difficulty that a local producer might encounter in making the biodiesel batch. In terms of costs, it was discovered that the major costs to a local producer will be the biodiesel mixer and fittings which will be fixed costs. Other variable costs are considered to be affordable, as the cost of waste vegetable oil is very low as well as other industrial reagent grade that will be required. In summary, batch biodiesel production for a local user or developing economy is a very feasible exercise. One needs to ensure that the recommendations regarding pre-treatment of feed oil, basic reaction criteria and other generic parameters are considered during production.

Orientador: Délson Luiz Módolo / Banca: Vicente Luiz Scalon / Banca: Elson Avallone / Resumo: A reação de transesterificação de óleos vegetais com álcool etílico ou metílico dá origem a ésteres metílicos ou etílicos de ácidos graxos, conhecidos como biodiesel. Este apresenta propriedades próximas do óleo diesel mineral como o número de cetano, massa específica, poder calorífico e relação ar-combustível. Porém, problemas decorrentes de sua maior viscosidade resultam em uma pulverização deficiente pelos bicos injetores levando a uma combustão de qualidade inferior, e com isso, formação de depósitos indesejáveis no interior do motor, alterações nas propriedades do óleo lubrificante e na composição dos gases de escape. Frente a essa questão se faz necessário o estudo da utilização de um aditivo capaz de tornar as características do biodiesel mais adequadas à sua utilização em motores de ignição por compressão e também o acompanhamento das alterações na composição dos gases de escape. O aditivo estudado nesse trabalho foi o d-limoneno, um hidrocarboneto obtido como subproduto da citricultura, que foi adicionado ao óleo diesel à ser utilizado como combustível do conjunto moto-gerador utilizado nos ensaios. Neste sistema foram aplicadas diferentes cargas e coletados os dados relativos à emissão do motor. Resultados relevantes como a redução de material particulados foram observados mesmo com a adição de pequenas quantidades de d-limoneno / Abstract: The transesterification of vegetable oils with methanol or ethanol results in methyl esters or ethyl esters of fatty acid, known as biodiesel. This one presents similar features of diesel oil, such as cetane number, specific weight, heat of combustion and air-fuel ratio. However, arising problems from its higher viscosity leads to a poor spraying by the fuel injectors and so to a low-grade combustion, causing formation of undesirable deposits inside the engine, changes in the properties of the lubricating oil and in the composition of the exhaust gas. Owing to this issue, it is necessary to study an additive able to make biodiesel characteristics more appropriate to be used in compression ignition engines, as well as a monitoring of changes in exhaust gas composition. The chosen additive was d-limonene, a hydrocarbon obtained as a byproduct of citriculture, which was added to diesel fuel to be used as fuel for the motor-generator set used in the tests. Different loads were applied to this system and the engine emission data were collected. Relevant results such as the reduction of particulate material were observed even with small amounts of d-limonene added / Mestre

No description available.

Orientador: Ricardo Alan Verdú Ramos / Banca: João Batista Campos Silva / Banca: Jhon Jairo Ramirez Behainne / Resumo: Na produção de biodiesel em pequena escala são comumente empregados os decantadores para separar o glicerol do biodiesel após a reação química de transesterificação do óleo com um álcool e um catalisador. Na maioria das vezes, esse processo de separação é realizado de forma manual e subjetiva por um operador que está sujeito a erros de interpretação, podendo, com isso, aumentar o custo de produção e/ou comprometer a qualidade do combustível produzido. Neste trabalho é proposta uma metodologia para o desenvolvimento e teste de um sistema eletrônico micro controlado, capaz de distinguir as fases formadas após o processo de decantação por meio de um sensor de condutividade elétrica, o qual permite o acionamento de válvulas para controle automático do direcionamento do biodiesel e do glicerol para reservatórios distintos. Essa metodologia contém a técnica de desenvolvimento abrangendo modelagem, simulação computacional, seleção de materiais, usinagem, projeto eletrônico, calibração e obtenção das características do desempenho do sensor. O sistema é composto por um painel elétrico que permite observar características do processo, através de um visor de LCD, e permite alterar as configurações do micro controlador, através da comunicação USB do equipamento com um computador. O sistema se mostrou eficiente nos testes com o biodiesel e glicerol, em processos produtivos com óleo de soja refinado, sendo que o glicerol apresentou valor de condutividade superior ao biodiesel, conforme esperado / Abstract: In the production of biodiesel on a small scale decanters are commonly utilized to separate the glycerol from biodiesel produced after a chemical reaction of oil with some alcohol and a catalyst. In most cases, this separation process is done manually and subjectively by an operator that can make mistakes in interpretation, increasing the cost of production and/or compromising the quality of the fuel produced. This work presents a methodology for developing and testing of a micro controlled electronic system, capable of distinguishing the phases formed after the decanting process by means of an electrical conductivity sensor, which permits the actuation of valves in order to have an automatic control of the direction of biodiesel and glycerol for different reservoirs. This methodology contains the technical development including modeling, computer simulation, materials selection, manufacturing, electronic project, calibration and obtains the performance characteristics of the sensor. The system consists of an electrical panel, which allows to observe the process through features an LCD display and permits change the settings of microcontroller through the USB communication device with a computer. The system proved effective in tests with biodiesel and glycerol production processes with refined soybean oil, and glycerin showed conductivity value higher than biodiesel as expected / Mestre

Hong Kong is vulnerable to energy and economic security due to the heavy dependence on imported fossil fuels. Waste has also been a major environmental management problem due to the amount of rubbish produced every year but lacking the technology and capital to manage different types properly. The objective of the dissertation is to study the feasibility of the use of biofuel in Hong Kong by recycling local waste. Current government policies in Hong Kong and overseas are being investigated on the appropriateness for domestic use. Literature reviews and stakeholders’ questionnaires are accounted to analyse the adaptability and popularity of the biodiesel application. The methodology of the dissertation is to firstly examine literature reviews regarding biodiesel’s environmental aspect, technical efficiencies, economic aspect, government incentives and tax constraints. The consensus outcome of these researches advocated high popularity of biodiesel consumption and production in Europe and U.S. due to lower environmental impact, equivalent output efficiency and strong government support. Their successful implementation is a good example to improvise biodiesel domestically in Hong Kong. Secondly, interviews were conducted with Hong Kong’s limited stakeholders. Respondents such as Hong Kong International Airport, Hong Kong Jockey Club, Fairwood Fastfood MTR Maritime Square were interviewed as these participants have been the pioneers in Hong Kong by recycling waste into biodiesel. On the production side, two out of three bio-refineries in Hong Kong provided their business sustainability and feasibility comments to pursue a long term goal. The limitation on responses might be focused solely on a few peer groups, and not the appropriate stakeholders with proper sampling size. However, the results are concurrent that biodiesel is one of the best alternative energy in Hong Kong. The dissertation draws positive results based on the following factors. Biodiesel can diminish the tremendous cost on waste management and landfill dumping. Using local food waste and industrial wastes from restaurants and food factories as feedstock to produce biodiesel is positive. This will also minimise the heavy reliance on imported fossil fuels to diversify energy sources. Refuelling of biodiesel fuel can be performed in any gas stations with the use of the existing infrastructure without any further requirement of new investment. Nonetheless, in order to facilitate the use of biodiesel, incentives programmes initiated by Hong Kong Government and the biofuel producers have to coherently promote this alternative fuel. The conclusion states that Hong Kong is completely feasible to adopt the use of biodiesel in medium to heavy sized vehicles and vessels in the commercial sector. The environmental benefit of Hong Kong using biodiesel stood out compared to other form of renewable energy. / published_or_final_version / Environmental Management / Master / Master of Science in Environmental Management

Biodiesel is a promising renewable alternative fuel to fossil energy. For the biodiesel production from low-cost feedstock, a pretreatment step is essential, which is the esterification of free fatty acids (e.g. oleic acid) in the feedstock in order to avoid soap formation and minimize catalyst deactivation. Sulfuric acid modified zirconia (H2SO4-ZrO2) is known as an effective heterogeneous catalyst for esterification. However, due to rapid 〖SO〗_4^(2-) leaching, its reusability is low and its practical use is thus largely hindered. Zirconia supported on silica (ZrO2-SiO2) serves as a kind of non-sulfated zirconia catalyst against the leaching of the active species. Moreover, the silica support offers a large surface area and excellent thermal stability, which can accommodate a number of active zirconia species. Furthermore, there are Zr-O-Si bondings at the contact area between ZrO2 and SiO2, which might result in the formation of a new strong acid species and induce an increase of the zirconia acidity accordingly. Herein, two types of ZrO2-SiO2 catalysts were prepared, by using the reverse microemulsion method and sol-gel-hydrothermal method, denoted as ZrO2-SiO2-ME and ZrO2-SiO2-SG, respectively. The as synthesized ZrO2-SiO2 were characterized by TEM, SEM, EDX, XRD, BET and IR. ZrO2-SiO2-ME demonstrated a good dispersion of ZrO2 nanoparticles, encapsulating in the monodispersed SiO2 host matrix, while ZrO2-SiO2-SG possessed the SiO2 support with a mesoporous structure, with an average pore size of ~7 nm and a surface area of 418 m2/g. The catalysts both exhibited excellent catalytic activity and stable performance in the esterification of oleic acid. Besides non-sulfated zirconia, sulfated zirconia catalysts other than traditional H2SO4-ZrO2 were also developed as solid acid catalysts for biodiesel production. Two sulfur-containing strong acids, chlorosulfonic acid (HClSO3) and (NH4)2SO4, were employed to acidify ZrO2, and two sulfated zirconia catalysts were prepared accordingly, namely HClSO3-ZrO2 and S-ZrO2. They were characterized by SEM, EDX, XRD, BET, IR, TGA and NH3-TPD. Comparing with H2SO4-ZrO2, HClSO3-ZrO2 and S-ZrO2 contained higher sulfur content and more acid sites. More importantly, both HClSO3-ZrO2 and S-ZrO2 demonstrated high catalytic activity and excellent durability in the esterification of oleic acid. It is known that consecutive esterification and transesterification reactions are suitable for direct biodiesel production and acetylation of glycerol enables the conversion of this biodiesel byproduct to a biofuel additive. Therefore, all the above mentioned catalysts were examined to compare their catalytic abilities in these reactions. Among the four catalysts, HClSO3-ZrO2 exhibited the highest catalytic activity in both reactions under optimal conditions. The thesis work here described the preparation and characterization of four types of ZrO2-based solid acid catalysts. Their catalytic activities were thoroughly investigated upon the several essential steps in biodiesel production. In addition, the synthesis condition-activity relation was studied and the synthesis and reaction conditions were delicately tuned. / published_or_final_version / Chemistry / Doctoral / Doctor of Philosophy