Catalizadores heterogéneos básicos para a produção de biodiesel

O consumo de energia é um requisito fundamental para a existência humana. Grande parte da energia é gerada a partir de combustíveis fósseis. Os problemas ambientais e a instabilidade dos mercados de crude, agravados pela conscencialização de que as reservas de crude são finitas, motivaram a procura de combustíveis alternativos. Entre os vários estudados, o biodiesel é apontado como uma alternativa viável ao diesel de origem fóssil por apresentar propriedades de combustão similares. O biodiesel apresenta um balanço de carbono praticamente nulo sendo por isso visto como uma arma na batalha contra o aquecimento global. O biodiesel compreende uma mistura de mono-ésteres alquílicos de ácidos gordos de cadeia longa. A transesterificação ou esterificação de óleos vegetais ou gorduras animais, com um álcool de baixo peso molecular (metanol ou etanol) é o principal processo usado para produzir biodiesel. Presentemente os processos industriais usam catalisadores homogéneos em processos. No entanto, os catalisadores heterogéneos têm surgido como promissores para a produção de biodiesel, já que são ambientalmente benignos e podem ser regenerados e reutilizados. Deste modo, a catálise heterogénea torna a produção de biodiesel potencialmente mais barata, permitindo a utilização em processos contínuos. Neste contexto, foram preparados e testados, na metanólise de óleo de soja, vários catalisadores heterogéneos básicos. Os melhores desempenhos catalíticos foram obtidos utilizando catalisadores sólidos preparados por deposição de SrO sobre MgO (razão atómica Sr/Mg entre 0.05 e 0.35). Os catalisadores com razão atómica Sr/Mg superior a 0.10 permitem obter um rendimento em ésteres metílicos superior a 90%, para a temperatura de refluxo do metanol. Os resultados das diferentes técnicas de caracterização mostraram que a temperatura de calcinação tem uma forte influência sobre o comportamento catalítico. Para temperaturas de calcinação inferiores a 625 ºC o carbonato de estrôncio permanece na superfície dos catalisadores. A solubilidade desta espécie no meio reaccional, principalmente no metanol, promove a rápida lixiviação do estrôncio e assim a desactivação do catalisador. A fim de optimizar a produção de biodiesel, foi estudado o efeito de vários parametros do processo tais como a temperatura da reacção, a razão molar metanol/óleo, razão mássica catalisador/óleo e o tempo de reação. Este estudo incluiu igualmente a estabilidade dos catalisadores.

Advances on the development of novel heterogeneous catalysts for transesterification of triglycerides in biodiesel

This paper describes experimental work done towards the search for more profitable and sustainable alternatives regarding biodiesel production, using heterogeneous catalysts instead of the conventional homogenous alkaline catalysts, such as NaOH, KOH or sodium methoxide, for the methanolysis reaction. This experimental work is a first stage on the development and optimization of new solid catalysts, able to produce biodiesel from vegetable oils. The heterogeneous catalytic process has many differences from the currently used in industry homogeneous process. The main advantage is that, it requires lower investment costs, since no need for separation steps of methanol/catalyst, biodiesel/catalyst and glycerine/catalyst. This work resulted in the selection of CaO and CaO modified with Li catalysts, which showed very good catalytic performances with high activity and stability. In fact FAME yields higher than 92% were observed in two consecutive reaction batches without expensive intermediate reactivation procedures. Therefore, those catalysts appear to be suitable for biodiesel production.

Produção de biodiesel a partir de matérias-primas ácidas e de gorduras animais

A produção de energia a partir de fontes renováveis tornou-se num objectivo essencial para a sustentabilidade económica, social e ambiental do mundo actual. O biodiesel é uma dessas fontes renováveis que pode substituir o diesel fóssil. A principal via de produção do biodiesel é através de uma reacção de transesterificação de óleos vegetais, óleos alimentares usados ou gorduras animais por reacção com um álcool na presença de um catalisador alcalino. Contudo, a utilização de matérias-primas com um teor em ácidos gordos livres superior a cerca de 4% (8mg KOH/g óleo) inviabiliza a possibilidade de efectuar directamente a reacção de transesterificação básica das gorduras e obriga à realização de um pré-tratamento para redução da acidez inicial da amostra. Assim, este trabalho teve como principal objectivo estudar a possibilidade de produzir diesel a partir de matérias-primas alternativas como as gorduras vegetais com elevados teores em ácidos gordos livres após esterificação com glicerina e uma gordura animal de baixa acidez, conseguindo-se assim a valorização de um resíduo e ao mesmo tempo a diminuição do custo de produção do biodiesel. Após ensaios preliminares, a esterificação com glicerina foi estudada aplicando a metodologia do planeamento factorial dos ensaios. Nos ensaios preliminares foi analisado o efeito da temperatura, da percentagem de catalisador, da velocidade de agitação, da percentagem de excesso de glicerina e do tipo de catalisador na acidez da amostra. Os resultados obtidos mostraram que é possível reduzir o índice de acidez de 30% (60 mg KOH/g gordura) para 8% (4 mg KOH/g gordura) trabalhando a 220° C, 10% de excesso de glicerina e 0,2% de catalisador (zinco) em apenas 90 minutos de reacção. A transesterificação básica do produto obtido na esterificação com glicerina não permitiu produzir um biodiesel que cumprisse a Norma Europeia de qualidade do biodiesel no que diz respeito à pureza, acidez e teor em água. De facto, nas condições mais favoráveis, que corresponderam à utilização da razão molar de metanol/gordura de 12:1 e 1% de catalisador, foi possível produzir um biodiesel com um teor em ésteres metílicos de 94.7% e 1.1% de ácidos gordos livres. Por último, os ensaios de transesterificação com a gordura animal mostraram que estas gorduras são uma matéria-prima com grandes potencialidades para serem utilizadas na produção de biodiesel. Assim, utilizando condições operatórias idênticas às utilizadas para os óleos virgens (0.6% de metóxido de sódio catalisador e uma razão molar de metanol de 6:1) foi possível produzir em apenas 30 minutos de reacção um biodiesel com um teor em ésteres superior a 98%.

Implementação e validação do método de determinação de metais e fósforo por ICP-OES (inductively coupled plasma-optical emission spectometry) em biodiesel

O objectivo do presente trabalho foi desenvolver, implementar e validar métodos de determinação de teor de cálcio (Ca), magnésio (Mg), sódio (Na), potássio (K) e fósforo (P) em biodiesel, por ICP-OES. Este método permitiu efectuar o controlo de qualidade do biodiesel, com a vantagem de proporcionar uma análise multi-elementar, reflectindo-se numa diminuição do tempo de análise. Uma vez que o biodiesel é uma das principais fontes de energia renovável e alternativa ao diesel convencional, este tipo de análises revela-se extremamente útil para a sua caracterização. De acordo com a análise quantitativa e qualitativa e após a validação dos respectivos ensaios, apresentam-se, na Tabela 1 as condições optimizadas para cada elemento em estudo. As condições de trabalho do ICP-OES foram escolhidas tendo em conta as características do elemento em estudo, o tipo de equipamento utilizado para a sua análise, e de modo a obter a melhor razão sinal/intensidade de fundo. Para a validação dos ensaios foram efectuados ensaios de recuperação, determinados limites de detecção e quantificação, ensaios de repetibilidade e reprodutibilidade, e verificação das curvas de calibração. Na tabela 2 apresentam-se os comprimentos de onda escolhidos (livres de interferências) e respectivos limites de detecção e quantificação dos elementos analisados por ICP-OES, na posição radial e radial atenuado.

Cork processing wastewater treatment/valorisation by nanofiltration

Nanofiltration process for the treatment/valorisation of cork processing wastewaters was studied. A DS-5 DK 20/40 (GE Water Technologies) nanofiltration membrane/module was used, having 2.09 m(2) of surface area. Hydraulic permeability was determined with pure water and the result was 5.2 L.h(-1).m(-2).bar(-1). The membrane presents a rejection of 51% and 99% for NaCl and MgSO4 salts, respectively. Two different types of regimes were used in the wastewaters filtration process, total recycling mode and concentration mode. The first filtration regime showed that the most favourable working transmembrane pressure was 7 bar working at 25 degrees C. For the concentration mode experiments it was observed a 30% decline of the permeate fluxes when a volumetric concentration factor of 5 was reached. The permeate COD, BOD5, colour and TOC rejection values remained well above the 90% value, which allows, therefore, the concentration of organic matter (namely the tannin fraction) in the concentrate stream that can be further used by other industries. The permeate characterization showed that it cannot be directly discharged to the environment as it does not fulfil the values of the Portuguese discharge legislation. However, the permeate stream can be recycled to the process (boiling tanks) as it presents no colour and low TOC (< 60 ppm) or if wastewater discharge is envisaged we have observed that the permeate biodegradability is higher than 0.5, which renders conventional wastewater treatments feasible.

Estudo do uso de hidrotalcites de Mg-Al como catalisadores heterogéneos para produção de biodiesel

A transesterificação de óleos vegetais ou gorduras animais com um álcool de baixo peso molecular é o principal processo utilizado na produção de biodiesel. Actualmente os processos industriais utilizam catalisadores homogéneos para acelerar a reacção. No entanto a utilização de catalisadores heterogéneos, no processo de transesterificação, tem sido sugerido por vários investigadores pois, são amigos do ambiente e podem ser regenerados e reutilizados portanto possibilitam a utilização de processos contínuos. Neste contexto, a utilização de hidrotalcites Mg-Al, como catalisadores heterogéneos para produção de biodiesel foi investigada neste trabalho experimental. As hidrotalcites com diferentes razões molares Mg/Al (Mg/Al=1, 2, 3 e 4) foram preparadas pelo método de co-precipitação. As diversas matrizes catalíticas obtidas, calcinadas a diferentes temperaturas, foram caracterizadas por difracção de raios X (DRX), análise térmica (TG-DSC), espectroscopia de infravermelhos (MIR), microscopia electrónica de varrimento (SEM) e isotérmicas de adsorção com azoto (BET). Estes catalisadores foram testados na metanólise de óleos vegetais para produzir biodiesel. As hidrotalcites Mg/Al=2, HT2A e HT2B (preparada com metade da quantidade de NaOH) calcinadas a 507 ºC e 700 ºC, respectivamente, foram as que apresentaram melhores resultados ao catalisar a reacção com um rendimento em éster superior a 97%, utilizando 2.5% da massa de catalisador, em relação à massa do óleo, razão molar metanol/óleo igual a 12, temperatura reaccional de 65 ºC durante 4h. Foi também investigada a reutilização do catalisador e o efeito da temperatura de calcinação. Constatou-se que o catalisador hidrotalcite HT2B apresentou melhor comportamento catalítico pois permitiu catalisar a reacção de transesterificação até três ciclos reaccionais, convertendo em ésteres 97%, 92% e 34% no primeiro, segundo e terceiro ciclos reaccionais, respectivamente. A análise de, algumas propriedades do biodiesel obtido como, o índice de acidez, a viscosidade e o índice de iodo mostraram que os resultados obtidos estão dentro dos valores limite recomendados pela norma EN 14214. Em anexo apresenta-se uma comunicação à First International Conference on Materials for Energy, Karlsruhe, 2010.

Study on the glycerolysis reaction of high free fatty acid oils for use as biodiesel feedstock

Biodiesel is the main alternative to fossil diesel and it may be produced from different feedstocks such as semi-refined vegetable oils, waste frying oils or animal fats. However, these feedstocks usually contain significant amounts of free fatty acids (FFA) that make them inadequate for the direct base catalyzed transesterification reaction (where the FFA content should be lower than 4%). The present work describes a possible method for the pre-treatment of oils with a high content of FFA (20 to 50%) by esterification with glycerol. In order to reduce the FFA content, the reaction between these FFA and an esterification agent is carried out before the transesterification reaction. The reaction kinetics was studied in terms of its main factors such astemperature, % of glycerin excess, % of catalyst used, stirring velocity and type of catalyst used. The results showed that glycerolysis is a promising pretreatment to acidic oils or fats (> 20%) as they led to the production of an intermediary material with a low content of FFA that can be used directly in thetransesterification reaction for the production of biodiesel. (C) 2011 Elsevier B.V. All rights reserved.

Study on the use of MgAl hydrotalcites as solid heterogeneous catalysts for biodiesel production

This paper, reports experimental work on the use of new heterogeneous solid basic catalysts for biodiesel production: double oxides of Mg and Al, produced by calcination, at high temperature, of MgAl lamellar structures, the hydrotalcites (HT). The most suitable catalyst system studied are hydrotalcite Mg:Al 2:1 calcinated at 507 degrees C and 700 degrees C, leading to higher values of FAME also in the second reaction stage. One of the prepared catalysts resulted in 97.1% Fatty acids methyl esters (FAME) in the 1st reaction step, 92.2% FAME in the 2nd reaction step and 34% FAME in the 3rd reaction step. The biodiesel obtained in the transesterification reaction showed composition and quality parameters within the limits specified by the European Standard EN 14214. 2.5% wt catalyst/oil and a molar ratio methanol:oil of 9:1 or 12:1 at 60 -65 degrees C and 4 h of reaction time are the best operating conditions achieved in this study. This study showed the potential of Mg/Al hydrotalcites as heterogeneous catalysts for biodiesel production. (C) 2011 Elsevier Ltd. All rights reserved.

Cork industry wastewater partition by ultra/nanofiltration: A biodegradation and valorisation study

Wastewater from cork processing industry present high levels of organic and phenolic compounds, such as tannins, with a low biodegradability and a significant toxicity. These compounds are not readily removed by conventional municipal wastewater treatment, which is largely based on primary sedimentation followed by biological treatment. The purpose of this work is to study the biodegradability of different cork wastewater fractions, obtained through membrane separation, in order to assess its potential for biological treatment and having in view its valorisation through tannins recovery, which could be applied in other industries. Various ultrafiltration and nanofiltration membranes where used, with molecular weight cut-offs (MWCO) ranging from 0.125 to 91 kDa. The wastewater and the different permeated fractions were analyzed in terms of Total Organic Carbon (TOC), Chemical Oxygen Demand (COD), Biochemical Oxygen Demand (BOD), Total Phenols (TP), Tannins, Color, pH and Conductivity. Results for the wastewater shown that it is characterized by a high organic content (670.5-1056.8 mg TOC/L, 2285-2604 mg COD/L, 1000-1225 mg BOD/L), a relatively low biodegradability (0.35-0.38 for BODs/COD and 0.44-0.47 for BOD20/COD) and a high content of phenols (360-410 mg tannic acid/L) and tannins (250-270 mg tannic acid/L). The results for the wastewater fractions shown a general decrease on the pollutant content of permeates, and an increase of its biodegradability, with the decrease of the membrane MWCO applied. Particularly, the permeated fraction from the membrane MWCO of 3.8 kDa, presented a favourable index of biodegradability (0.8) and a minimized phenols toxicity that enables it to undergo a biological treatment and so, to be treated in a municipal wastewater treatment plant. Also, within the perspective of valorisation, the rejected fraction obtained through this membrane MWCO may have a significant potential for tannins recovery. Permeated fractions from membranes with MWCO lower than 3.8 kDa, presented a particularly significant decline of organic matter and phenols, enabling this permeates to be reused in the cork processing and so, representing an interesting perspective of zero discharge for the cork industry, with evident environmental and economic advantages. (C) 2010 Elsevier Ltd. All rights reserved.

Cork industry wastewater characterization assessment of the biodegradability, reuse and of the relationship between BOD, COD and tannins with TOC

Cork processing involves a boiling step to make the cork softer, which consumes a high volume of water and generates a wastewater with a high organic content, rich in tannins. An assessment of the final wastewater characteristics and of the boiling water composition along the boiling process was performed. The parameters studied were pH, color, total organic carbon (TOC), chemical and biochemical oxygen demands (COD, BOD5, BOD20), total suspended solids (TSS), total phenols and tannins (TP, TT). It was observed that the water solutes extraction power is significantly reduced for higher quantities of cork processed. Valid relationships between parameters were established not only envisaging wastewater characterization but also to provide an important tool for wastewater monitoring and for process control/optimization. Boiling water biodegradability presented decreasing values with the increase of cork processed and for the final wastewater its value is always lower than 0.5, indicating that these wastewaters are very difficult to treat by biological processes. The biodegradability was associated with the increase of tannin content that can rise up to 0.7 g/L. These compounds can be used by other industries when concentrated and the clarified wastewater can be reused, which is a potential asset in this wastewater treatment.

Biodiesel production from waste frying oils over lime catalysts

Biodiesel production from semi-refined oils (SRO) and waste frying oils (WFO) was studied using commercial CaO as heterogeneous catalyst. The methanolysis tests were carried out in mild reaction conditions (62 A degrees C, atmospheric pressure). With such conditions, SRO (soybean and rapeseed) allowed to produce a biodiesel containing 97-98 % of methyl esters (FAME), whereas WFO only provided 86-87 % of FAME. The lower FAME yield for WFO oil is ascribable to the partial neutralization of the catalyst by free fatty acids. Also, soaps formation from the WFO oil reduced the weight yield of the oil phase (containing FAME) obtained and increased the MONG content of the glycerin phase. The catalysts stability tests showed high stability even when WFO oil was processed. Catalytic tests performed with blends of WFO/semi-refined oils showed blending as a good strategy to process low value raw oils with minor decay of the catalyst performance. Both WFO and semi-refined oils showed S-shape kinetics curves thus discarding significant differences of the reaction mechanisms.

Fungal contamination in two Portuguese wastewater treatment plants

The presence of filamentous fungi was detected in wastewater and air collected at wastewater treatment plants (WWTP) from several European countries. The aim of the present study was to assess fungal contamination in two WWTP operating in Lisbon. In addition, particulate matter (PM) contamination data was analyzed. To apply conventional methods, air samples from the two plants were collected through impaction using an air sampler with a velocity air rate of 140 L/min. Surfaces samples were collected by swabbing the surfaces of the same indoor sites. All collected samples were incubated at 27°C for 5 to 7 d. After lab processing and incubation of collected samples, quantitative and qualitative results were obtained with identification of the isolated fungal species. For molecular methods, air samples of 250 L were also collected using the impinger method at 300 L/min airflow rate. Samples were collected into 10 ml sterile phosphate-buffered saline with 0.05% Triton X-100, and the collection liquid was subsequently used for DNA extraction. Molecular identification of Aspergillus fumigatus and Stachybotrys chartarum was achieved by real-time polymerase chain reaction (RT-PCR) using the Rotor-Gene 6000 qPCR Detection System (Corbett). Assessment of PM was also conducted with portable direct-reading equipment (Lighthouse, model 3016 IAQ). Particles concentration measurement was performed at five different sizes: PM0.5, PM1, PM2.5, PM5, and PM10. Sixteen different fungal species were detected in indoor air in a total of 5400 isolates in both plants. Penicillium sp. was the most frequently isolated fungal genus (58.9%), followed by Aspergillus sp. (21.2%) and Acremonium sp. (8.2%), in the total underground area. In a partially underground plant, Penicillium sp. (39.5%) was also the most frequently isolated, also followed by Aspergillus sp. (38.7%) and Acremonium sp. (9.7%). Using RT-PCR, only A. fumigatus was detected in air samples collected, and only from partial underground plant. Stachybotrys chartarum was not detected in any of the samples analyzed. The distribution of particle sizes showed the same tendency in both plants; however, the partially underground plant presented higher levels of contamination, except for PM2.5. Fungal contamination assessment is crucial to evaluating the potential health risks to exposed workers in these settings. In order to achieve an evaluation of potential health risks to exposed workers, it is essential to combine conventional and molecular methods for fungal detection. Protective measures to minimize worker exposure to fungi need to be adopted since wastewater is the predominant internal fungal source in this setting.

Aspergillus flavus contamination in two Portuguese wastewater treatment plants

Filamentous fungi from genus Aspergillus were previously detected in wastewater treatment plants (WWTP) as being Aspergillus flavus (A. flavus), an important toxigenic fungus producing aflatoxins. This study aimed to determine occupational exposure adverse effects due to fungal contamination produced by A. flavus complex in two Portuguese WWTP using conventional and molecular methodologies. Air samples from two WWTP were collected at 1 m height through impaction method. Surface samples were collected by swabbing surfaces of the same indoor sites. After counting A. flavus and identification, detection of aflatoxin production was ensured through inoculation of seven inoculates in coconut-milk agar. Plates were examined under long-wave ultraviolet (UV; 365 nm) illumination to search for the presence of fluorescence in the growing colonies. To apply molecular methods, air samples were also collected using the impinger method. Samples were collected and collection liquid was subsequently used for DNA extraction. Molecular identification of A. flavus was achieved by real-time polymerase chain reaction (RT-PCR) using the Rotor-Gene 6000 qPCR detection system (Corbett). Among the Aspergillus genus, the species that were more abundant in air samples from both WWTP were Aspergillus versicolor (38%), Aspergillus candidus (29.1%), and Aspergillus sydowii (12.7%). However, the most commonly species found on surfaces were A. flavus (47.3%), Aspergillus fumigatus (34.4%), and Aspergillus sydowii (10.8%). Aspergillus flavus isolates that were inoculated in coconut agar medium were not identified as toxigenic strains and were not detected by RT-PCR in any of the analyzed samples from both plants. Data in this study indicate the need for monitoring fungal contamination in this setting. Although toxigenic strains were not detected from A. flavus complex, one cannot disregard the eventual presence and potential toxicity of aflatoxins.

Construção de curvas binodais para sistemas ternários, contendo biodiesel, álcool e água

Trabalho Final de Mestrado para obtenção do grau de Mestre em Engenharia Química

Biodiesel production over lithium modified lime catalysts: activity and deactivation

Biodiesel production by methanolysis of semi-refined rapeseed oil was studied over lime based catalysts. In order to improve the catalysts basicity a commercial CaO material was impregnated with aqueous solution of lithium nitrate (Li/Ca = 03 atomic ratio). The catalysts were calcined at 575 degrees C and 800 degrees C, for 5 h, to remove nitrate ions before reaction. The XRD patterns of the fresh catalysts, including the bare CaO, showed lines ascribable to CaO and Ca(OH)(2). The absence of XRD lines belonging to Li phases confirms the efficient dispersion of Li over CaO. In the tested condition (W-cat/W-oil = 5%; CH3OH/oil = 12 molar ratio) all the fresh catalysts provided similar biodiesel yields (FAME >93% after 4 h) but the bare CaO catalyst was more stable. The activity decay of the Li modified samples can be related to the enhanced, by the higher basicity, calcium diglyceroxide formation during methanolysis which promotes calcium leaching. The calcination temperature for Li modified catalysts plays an important role since encourages the crystals sinterization which appears to improve the catalyst stability. (C) 2013 Elsevier B.V. All rights reserved.