Abstract The increasing awareness of the depletion of fossil fuel resources and the environmental benefits of biodiesel fuel has made it more attractive in recent times. The cost of biodiesel, however, is the major hurdle to its commercialization in comparison to petroleum-based diesel fuel. The high cost is primarily due to the raw material, mostly neat vegetable oil. Used cooking oil is one of the economical sources for biodiesel production. However, the products formed during frying, can affect the transesterification reaction and the biodiesel properties. This paper attempts to review various technological methods of biodiesel production from used cooking oil. The analytical methods for high quality biodiesel fuel from used cooking oil like GC, TLC, HPLC, GPC and TGA have also been summarized in this paper. In addition, the specifications provided by different countries are presented. The fuel properties of biodiesel fuel from used cooking oil were also reviewed and compared with those of conventional diesel fuel.

Soybean oil, palm oil and waste cooking oil as feedstock were used to measure the effects of different heating methods, reaction time, molar ratio of methanol to oil, temperature, power, catalyst type and catalyst concentration on the biodiesel yield in this study. Additionally, reducing reaction time for the transesterification reaction used microwave heating to make more complete. The optimized operating conditions of conventional heating used palm oil, concentration for 0.75 wt% sodium methoxide, molar ratio of methanol to oil for 6:1, reaction time for 90 min and reaction temperature for 60 ¢J offered the best yield of 98.1%. the microwave heating used palm oil, concentration for 0.75 wt% sodium methoxide, molar ratio of methanol to oil for 6:1, reaction time for 3 min and power for 750 W offered the best yield of 99.5% Used soybean oil and palm oil as biodiesel feedstock production, its yield was higher than the waste cooking oil. This reason is caused by composition complex and high viscosity of waste cooking oil compare with pure vegetable oil. The catalyst of sodium methoxide is higher effective than sodium oxide used in transesterification reaction, because the reaction process will not formation of water and saponification. Use ionic liquid [Pyr12CN][Cl], [MorEtH][HSO4], [MorMeMe][MeSO4], [PyrMeH][HSO4] and [MorMeEt][EtSO4] as biodiesel catalyst, the optimized operating conditions of concentration for 2.00 wt% [Pyr12CN][Cl], molar ratio of methanol to oil for 6:1, reaction time for 6 min and power for 750 W offered the best yield of 98.1%.

Poor sleep quality is an important symptom of many medical or psychiatric disorders. However, the impact of cooking oil fumes (COFs) on sleep quality has not been studied. This population-based cross-sectional study was conducted to examine the association between COFs of Chinese household cooking and sleep quality. Individual sleep quality assessment was completed in 2197 participants with an average age of 37.52 years, through Pittsburgh Sleep Quality Index (PSQI). Information about their cooking practice were also collected by self-reported questionnaire. As an internal biomarker of COFs, urinary 1-hydroxypyrene (1-HOP) (n = 562) was further measured using high-performance liquid chromatography. Binary logistic regression models were performed to evaluate the association between exposure to COFs and individual sleep quality. We found that, subjective poor kitchen ventilation, preheating oil to smoking, and cooking for over 30 minutes were positively associated with overall poor sleep quality (global PSQI score >5) [odds ratio (OR) = 1.75, 95% confidence interval (CI) = 1.43–2.16; 1.25, (1.03–1.52); 1.42, (1.15–1.76), respectively]. After adjusting for potential confounders, subjective poor kitchen ventilation still tend to increase the risk of long sleep latency, sleep disturbances, and daytime dysfunction [OR = 1.37, 95% CI = 1.09–1.73; 1.91, (1.39–2.61); 1.54, (1.23–1.93), respectively]. Similar results were observed in participants who preheated oil to smoking [OR = 1.36, 95% CI = 1.08–1.72; 1.55, (1.14–2.14); 1.25, (1.02–1.55), respectively] and cooked for over 30 minutes [OR = 1.34, 95% CI = 1.05–1.72; 1.46, (1.03–2.06); 1.36, (1.08–1.72), respectively]. Furthermore, high urinary 1-HOP level was also positively associated with overall poor sleep quality (OR = 2.30, 95% CI = 1.31–4.05). The results indicated that exposure to COFs from Chinese household cooking may be a risk factor for poor sleep quality among middle-aged Chinese population.

Resource-efficient technologies are essential for economically viable biodiesel production. This work focuses on conversion of microalgal lipids and vegetable oils into fatty acid alkyl esters or biodiesel. Transesterification of waste cooking oil (WCO) and extractive-transesterification of wet microalgal biomass were investigated using microwave and ultrasound irradiations through several process parametric evaluation studies to elucidate the effects of different alcohols and catalyst types (homogeneous and heterogeneous), reaction time, and reaction temperatures. First, a brief overview of process steps involved in microalgal biodiesel production and associated energy consumption and research needs were discussed. Next, energy analysis of microalgal biocrude production via extractive-transesterification under microwave and ultrasound irradiations (individually) was performed. Then, the synergistic effect of microwave and ultrasound irradiations on extractive-transesterification of microalgal lipids was evaluated through a process optimization study using response surface methodology to determine the best process conditions. For this study, a maximum biocrude conversion of 51.2% was obtained when 20 g of algal paste was treated with 30 mL methanol, 1 wt.% catalyst, 7 min reaction time, and 140 W for MW and US (280 W total). Further, biocrude yield kinetics study revealed that the activation energy for this reaction was around 17, 298 J mol-1 K-1. A series of experimental studies were conducted to understand the roles and effects of various process related conditions including the power output and power density of microwave and ultrasound irradiations in biodiesel production. The two non-conventional heating techniques were compared for their process intensification effects. Ultrasound was applied either in continuous or pulse mode. Pulse sonication was found to be more suitable for simple transesterification reaction of WCO with a 98% biodiesel yield in 2.5 min (9:1 methanol to oil ratio, 1.25% catalyst, and 150 W power output) over 82% yield for continuous sonication under the same conditions. Followed by this, a detailed study was conducted to determine optimum pulse (ON and OFF time) sonication conditions. A 99% conversion yield was obtained for a pulse ON-OFF combination of 7s-2s. Additionally, the effect of different alcohols (ethanol, methanol, and ethanol-methanol mixtures) using pulse sonication was evaluated.

Research and experience has shown that vegetable oil can be processed, by transesterification, into a useable fuel for compression ignition engines. Earlier research examined using straight vegetable oil as a fuel, but found it to cause detrimental engine problems. Trial and error has shown that heating the vegetable oil prior to injection, is a viable option. A diesel vehicle engine was operated for over 188 hours or approximately 7,000 miles, using waste cooking oil as fuel. The longevity of the vehicle engine was limited by an undetermined engine failure. Using stationary testing, with no engine load and various power settings, engine emissions of several engines operating on waste cooking oil were compared to emissions from two other fuels, diesel and Biodiesel, and found to be very positive. Waste vegetable oil (WVO) had lower overall emissions than diesel and lower levels of nitrogen species than Biodiesel. Agricultural yield predictions estimate that currently only 5% and at most 20% of all diesel fuel needs can be met with vegetable oil. Currently WVO is a disposal problem. It is primarily used as a feedstock. WVO is not a commodity and has disposal fees associated with it. If WVO is used as a fuel, it would not only provide another source for disposal, but it may also increase the value of WVO making it a commodity instead of a disposal burden.

This study used jatropha oil, waste cooing oil, and soybean oil as the raw materials for investigating effects of catalyst concentration, reaction time, reaction temperature, methanol-to-oil ratio, and catalyst types on biodiesel yield. The authors also heated up the oil to speed up the transesterification and to make the reaction more complete. Jatropha oil, waste cooing oil, and soybean oil were used as the raw materials, and three types of ionic liquid or zwitterionic liquid, [PyrMe][HSO4], [PyrMeBuS][HSO4], and [MorMeA][Br], were added as catalysts for co-catalysis while heating the oil raw materials to create the best operational condition for biodiesel production. For soybean oil used as the raw material, the best catalyzing effect (a 99.4% yield) was achieved by adding [MorMeA][Br] while the reaction time was 6min, reaction temperature was 70 ¢J, and the methanol-to-oil ratio was 9:1. Under the best reaction condition, catalyzing effect was compared between the addition of sulfate-containing ionic liquid and sulfate-containing zwitterionic liquid. The yield of the addition of sulfate-containing ionic liquid and sulfate-containing zwitterionic liquid were 97.2% and 98.7% respectively. It can be found from this study that for increasing biodiesel yield, the addition of zwitterionic liquid for co-catalysis is more effective than the addition of homogeneous ionic liquid. Comparing the best operational condition between jatropha oil and soybean oil, the best yield of jatropha oil and soybean oil was 98.5% and 99.4% respectively, while the concentration of sodium hydroxide was 0.75 wt%, [MorMeA][Br] of 1.00 wt% was added, the methanol-to-oil ratio was 9:1, the reaction time was 6 min, and the reaction temperature was 70¢J. As for disposed cooking oil, the best operational condition rendered a yield of 98.1% when the concentration of sodium hydroxide was 0.75 wt%, [MorMeA][Br] of 1.00 wt% was added, the methanol-to-oil ratio was 9:1, the reaction time was 7 min, and the reaction temperature was 70¢J. For waste cooking oil, because of the containing of impurities from frying, the yield was slightly lower and the reaction time was longer.

Recently, restaurant employees exposing to cooking oil fume with potential lung cancer was highly concerned, indicating cooking oil fume emitted from restaurants might cause tremendous hazard to human health. This study combined photocatalytic oxidation and ozone oxidation technology to decompose VOCs from the exhaust of cooking oil fume from restaurants. Firstly, this study selected three different types of restaurants to implement air pollutant measurements in the indoor dinning room and stack emission. Indoor TVOCs continuous monitoring data showed that the highest TVOCs concentration was generally observed in the dining peak time. In this study, photocatalyst coated fiberglass filter was prepared by impregnation procedure and its characteristics was analyzed by SEM and XRD. Experimental results showed that the particle size of photocatalyst ranged from 25 to 50 nm and had high percentage of Anatase, suggesting that it had high photocatalytic reactivity. This study designed a continuous-flow reaction system combined nano-sized TiO2 photocatalysis with ozone oxidation technology to decompose VOCs from cooking oil fume. After passing through a fiberglass filter to remove oil droplets, the cooking oil fume then coated with nano-sized titanium oxide (UV/TiO2) fiberglass filter purification system, and then injected ozone into the system to decompose residual VOCs. This study further investigated the influences of operating parameters, including TVOCs initial concentration, O3 injection concentration, and reaction temperature on the decomposition efficiency of TVOCs by using the UV/TiO2/O3 technology. When the photocatalytic reaction temperature was 35~50¢J, the TVOC decomposition efficiency slightly increased with reaction temperature, however, when the reaction temperature went up to 55¢J, the TVOC decomposition efficiency increased only slightly, but did not increased linearly. Combination of photocatalysis and ozone oxidation system performance test results showed that ozone could decompose approximately 34% VOCs, and followed by the photocatalytical reaction of residual pollutants, achieving an overall decomposition efficiency of about 75%; while photocatalytic reaction can remove 64% of TVOCs and followed by O3 for the decomposition of residual pollutants, achieving an overall decomposition efficiency up to 94%. It showed that the combined UV/TiO2+O3 system could effectively remove VOCs in the cooking oil fume from the exhaust of restaurants. By using GC/MS to qualitatively analyze the speciation of TVOCs from cooking oil fume before and after UV/TiO2/O3, the results showed that the composition of VOCs had a decreasing trend. The peak area and dilution factor were applied to estimate the decomposition efficiency of different VOCs species. The decomposition efficiencies of pentane, 2-acrolein, acrolein, heptane, pentanal, hexanal, 2-hexenal, heptanal, heptenal and ethylhexenal were 56.21%, 72.88%, 51.33%, 32.23%, 59.04%, 69.22%, 73.53%, 41.37%, 92.57%, and 96.02%. Finally, a Langmuir-Hinshelwood kinetic model was applied to simulate the photocatalytic decomposition efficiency with the initial concentration of cooking oil fume. Model simulation results showed that the reaction rate increased with the initial TVOCs concentration. However, when TVOCs concentration increased gradually, the reaction rate became constant since the activated sites on the photocatalyst¡¦s surface was limited and cannot allow more VOC molecules diffuse to the activated sites for further photocatalytic reaction.

This study analyzes the sustainability of various energy sources including micro hydro power and biodiesel in the context of Nepal. The main focus is on the development of biodiesel fuels from non-edible oil resources including waste cooking oil, jatropha and soapnut oil feedstocks grown on the marginal lands of Nepal. Biodiesel fuel samples were prepared by acid and/or base catalyst transesterification. Both single stage and dual stage transesterification processes were employed depending on the free fatty acid content of the oil feedstock. The oil to biodiesel conversion rate and total yield were monitored. The quality of the biodiesel fuels including viscosity etc was confirmed by an external laboratory and all fuels met the ASTM fuel quality requirements. Canola, jatropha and soapnut biodiesel fuels were tested to determine some atomization properties - density, surface tension and viscosity - at elevated temperatures and pressures. The density of three biodiesel fuels and diesel were determined up to 523 K and 7 MPa using a capacitance type densitometer. The results showed a linear relationship with temperature and pressure over the measured range. The experimental data were well within the range of canola and other biodiesel fuels found in the literature. Kay’s mixing rule was used to predict the density of some biodiesel blends and the results were found to be in agreement with less than 5% error with the measured data. The surface tension was measured using a pendant drop apparatus for all three biodiesel and diesel fuels for temperatures and pressures up to 473K and 7 MPa. Results showed a linear relationship with temperature as well as with pressure. Temperature has a higher effect on surface tension than pressure. The viscosity of all three biodiesel and diesel fuels were measured using a torsional vibration viscometer up to 523 K and 7 MPa. Results showed that the viscosity-temperature relationship of all three biodiesel fuels tested followed a modified Andrade equation which was also applicable when temperature and pressure were both applied simultaneously. The measured and regressed kinematic and dynamic viscosities obtained were comparable with values in the literature. / This thesis is focused on sustainability analysis of alternative fuels in Nepal and presents the resullts of the tests on fuel and atomization characterisation of different biodiesel feedstocks including canola, jatropha, soapnut and waste cooking oil. A new model to evaluate sustainability of renewable alternatives energy resources has been developed and tested.

L'objectif de cette thèse est de proposer un réacteur continu et intensifié pour la transformation d’huiles végétales de récupération en produits ou intermédiaires qui seront ensuite utilisés ou formulés en applications destinées au BTP. Ce travail s’inscrit dans le cadre du FUI AGRIBTP, projet de recherche collaboratif qui a pour finalité la création d'un outil industriel de valorisation des sous-produits de l'agro-industrie. Le réacteur se veut pluri-réactionnel, c’est-à-dire adapté et efficace pour réaliser les réactions de transestérification ou d’estérification par le méthanol ou par le glycérol, pour une consigne de production fixée à 100 kg/h. Pour parvenir à cet objectif, une revue de la littérature a permis de dégager une liste de technologies de réacteurs adaptés à ces réactions. L’analyse comparative de ces systèmes a conduit à sélectionner trois types de réacteurs intensifiés existant dans le commerce et qui ont été ensuite testés expérimentalement: les réacteurs microstructurés (type Corning®), les réacteurs micro-ondes et les réacteurs pulsés à chicanes (type NiTech®). De bonnes conversions sont obtenues pour les réactions de transestérification et d’estérification par le méthanol, montrant une meilleure efficacité de ces réacteurs intensifiés par rapport aux réacteurs conventionnels; en revanche les résultats sont encore insuffisants pour l’estérification avec le glycérol en raison de limitations en température. Concernant le réacteur micro-ondes, les excellents résultats rapportés dans la littérature sont à modérer en raison d’une imprécision de mesure de la température. La technologie de réacteurs pulsés à chicanes a finalement été retenue : leur flexibilité, l’indépendance entre le débit et le mélange généré, et enfin leur diamètre suffisamment étendu pour ne pas générer de blocage éventuel dû à l’encrassement du réacteur par la matière entrante sont les principaux arguments qui ont guidé ce choix. Le système disponible construit en verre a tout de même montré ses limites en montée en température et en pression et il a donc été envisagé d’étoffer nos investigations dans des gammes de fonctionnement plus larges. Ainsi une collaboration avec le laboratoire TNO de Delft, aux Pays-Bas a permis d’avoir accès à un réacteur pulsé à chicanes en acier inoxydable. Les résultats obtenus pour la réaction d’estérification par le glycérol - qui n’offrait pas jusqu’à présent des données concluantes - sont satisfaisants, et même de qualité supérieure comparés à ceux obtenus avec un réacteur tubulaire hélicoïdal lui aussi pulsé. Parallèlement à ces études, des simulations numériques des écoulements dans le réacteur ont permis de proposer des améliorations de la forme des chicanes, celle-ci étant déterminante pour la bonne capacité de dispersion liquide-liquide des réactifs immiscibles et la qualité du mélange. Ces simulations ont été comparées à des mesures de vitesses obtenues sur un pilote expérimental conçu pour permettre la visualisation par technique laser des écoulements dans un élément du réacteur à chicanes. Pour terminer, l’extrapolation des résultats obtenus sur les pilotes étudiés à une échelle de production de 100 kg/h a été initiée, aboutissant à la proposition d’un procédé permettant la production sélective de monoglycérides via l’estérification par le glycérol, mais également la fabrication de biodiesel par la transestérification, incluant un réacteur intensifié pulsé dont la géométrie de chicanes a été optimisée, et ce afin de répondre à l’objectif initial de la thèse. / The objective of this thesis is to propose a continuous and intensified reactor to transform waste cooking oil into products that will be used in applications in the building and public works sector. This work is part of the FUI AGRIBTP, a collaborative research project whose finality is to the creation of an industrial tool for the reuse of co-products from agroindustries. The reactor must be able to handle transesterification and esterification (with methanol or with glycerol) reactions efficiently with a total flow rate of 100 kg/h. To achieve this objective, a literature review has identified a list of suitable reactor technologies for these reactions. The comparative analysis of these different technologies has led to the selection of three types of intensified reactors microstructured reactors (Corning® type), microwave reactors and oscillatory baffled reactors (NiTech® type). The performance of these reactors for transesterification and esterification reactions has then been investigated experimentally. High conversions have been obtained for transesterification and esterification with methanol reactions, thereby showing the improved performance of these intensified reactors compared with conventional reactors; however results obtained with esterification with glycerol reaction are still rather low due to limitations in operating temperature. Concerning the microwave reactor, the excellent results previously reported in the literature should be taken with care because of the inaccuracy of temperature measurements, as proven in this work. The oscillatory baffled reactor technology has been selected has the most industrially viable equipment for the considered reactions. The flexibility of this reactor, the independency of the flow rate and mixing, as well as the diameter ,which is large enough to avoid fouling caused by the quality of the feed line, are the main reasons for this choice. The commercial available system, built in glass, has nevertheless shown limitations in terms of operating temperature and pressure. As a result, further work has focused on reactor operation in a wider range of operating conditions. To do this, a collaboration with the TNO laboratory in Delft, Netherlands, was set up in order to investigate reaction performance an oscillatory baffled reactor made of stainless steel. The reaction performance obtained for esterification with glycerol is more than satisfactory, being significantly greater that that obtained in the glass Nitech reactor and even of higher quality compared to that obtained with a oscillatory helicoidal tubular reactor. In parallel to these studies, CFD simulations of flow in the reactor have enable the investigation of new baffle designs, which play a major role in the capacity to generation liquid-liquid dispersions of the immiscible reactants and in the quality of the mixing. These simulations have been compared with velocity measurements and flow patterns obtained in a transparent experimental rig using Particle Image Velocimetry. Finally, the results obtained on the pilot-scale rigs have been used to size a the oscillatory flow reactor for a total flow rate of 100 kg/h, which would be dedicated to the selective production of monoglycerides by esterification with glycerol reaction and also biodiesel production by transesterification reaction.

Conselho Nacional de Desenvolvimento CientÃfico e TecnolÃgico / O Ãleo de fritura à um resÃduo amplamente produzido em todo o mundo. No entanto, somente alguns paÃses mais desenvolvidos possuem polÃticas de descarte ambiental correto desse resÃduo, o que o torna um poluente em potencial em naÃÃes menos esclarecidas em relaÃÃo à questÃo ambiental. Portanto, este trabalho tem como objetivo principal apresentar uma tecnologia de produÃÃo de biodiesel a partir de Ãleo de fritura como forma de aproveitamento energÃtico, aliado a uma forma ambientalmente correta de destinaÃÃo final para esse resÃduo. O trabalho se inicia com uma revisÃo bibliogrÃfica bÃsica do estado da arte da produÃÃo de biodiesel. Em seguida, apresenta-se a proposiÃÃo de um processo quÃmico para a produÃÃo de biodiesel a partir de Ãleo de fritura e por fim, tem-se uma discussÃo da tecnologia, na forma como ela foi inserida no ambiente computacional utilizado para sua elaboraÃÃo. AlÃm da apresentaÃÃo da tecnologia propriamente dita, uma avaliaÃÃo ambiental do processo à feita para mensurar a capacidade do processo de produÃÃo de biodiesel proposto de diminuir o impacto causado pelo Ãleo de fritura no ambiente. / Waste cooking oil is a residue widely produced around the world. However, only a few developed countries have policies of environmental correct disposal of this waste, which makes it a potential pollutant in less enlightened nations about the environmental issues. Therefore, this work aims to present a technology for producing biodiesel from waste cooking oil as a form of energy recovery, combined with an environmentally correct disposal for this waste. The work begins with a basic review of the state of the art in biodiesel production. Then, it presents a proposition of a chemical process to produce biodiesel from waste cooking oil and finally has a discussion of the technology the way it was inserted in the computing environment used for its elaboration. Besides the presentation of the technology itself, an environmental assessment of the process is performed to measure the ability of the proposed biodiesel production process to reduce the impact caused by the waste cooking oil in the environment.