Enzyme-catalyzed production of biodiesel by ultrasound-assisted ethanolysis of soybean oil in solvent-free system.

This work reports the transesterification of soybean oil with ethanol using a commercial immobilized lipase, Novozym 435, under the influence of ultrasound irradiation, in a solvent-free s. The experiments were performed in an ultrasonic water bath, following a sequence of experimental designs to evaluate the effects of temperature, enzyme and water concentrations, oil to ethanol molar ratio and output irradiation power on the reaction yield. Besides, a kinetic study varying the substrates molar ratio and enzyme concentration was also carried out. Results show that ultrasound-assisted lipase-catalyzed transesterification of soybean oil with ethanol in solvent-free system might be a potential alternative route to conventional alkali-catalyzed and/or traditional enzymatic methods, as high reaction yields (~78 wt%) were obtained at mild irradiation power supply (~132 W), and temperature (63 °C) in a relatively short reaction time, 1 h. Additionally, a study regarding the enzyme reuse was carried out at the experimental condition that afforded the best reaction yield.

Assessment of two immobilized lipases activity and stability to low temperatures in organic solvents under ultrasound-assisted irradiation.

Both stability and catalytic activity of two commercial immobilized lipases were investigated in the presence of different organic solvents in ultrasound-assisted system. In a general way, for Novozym 435, the use of ethanol as solvent led to a loss of activity of 35% after 10 h of contact. The use of iso-octane conducted to a gradual increase in lipase activity in relation to the contact time, reaching a maximum value of relative activity of 126%. For Lipozyme RM IM, after 5 h of exposure, the enzyme presented no residual activity when ethanol was used as solvent. The solvents tert-butanol and iso-octane showed an enhancement of about 20 and 17% in the enzyme activity in 6 h of exposure, respectively. Novozym 435 and Lipozyme IM presented high stability to storage after treatment under ultrasound-assisted system using n-hexane and tert-butanol as solvents.

Immobilization of inulinase from Kluyveromyces marxianus NRRL Y-7571 using modified sodium alginate beads.

An experimental design was carried out to evaluate the effect of the concentrations of sodium alginate, glutaraldehyde and activated coal on the immobilization of inulinase from Kluyveromyces marxianus NRRL Y-7571. The experimental condition of 20 g/L of sodium alginate, 50 mL/L of glutaraldehyde and 30 g/L of activated coal led to the highest specific activity (2,063.5 U/mg of protein), corresponding to an enhancement of about 26 times compared to the activity of the free enzyme (79.1 U/mg of protein). The effect of pH and temperature on the immobilized enzyme activity was also evaluated, showing optimal activities at pH of 5.5 and 55 °C. The study of storage of immobilized inulinase in different temperatures showed that the extract kept its initial activity after 43 days of storage at 40 and 50 °C and after 138 days of storage either at 4 or 25 °C.

Lipase-Catalyzed Glycerolysis of Soybean and Canola Oils in a Free Organic Solvent System Assisted by Ultrasound.

This work shows new and promising experimental data of soybean oil and canola oil glycerolysis using Novozym 435 enzyme as catalyst in a solvent-free system using ultrasound bath for the emulsifier, monoglyceride (MAG), and diacylglycerol (DAG) production. The experiments were conducted in batch mode to study the influence of process variables as temperature (40 to 70 °C), immobilized enzyme content (2.5 to 10 wt%, relative to substrates), molar ratio glycerol/oil (0.8:1 to 3:1), agitation (0 to 1200 rpm) and ultrasound intensity (0 to 132 W cm(-2)). Highest yields of DAG+MAG (75 wt%) were obtained with molar ratio glycerol/canola oil 0.8:1, 70 °C, 900 rpm, 120 min of reaction time, 10 wt% of enzyme concentration, and 52.8 W cm(-2) of ultrasound intensity. When soybean oil was used, the best results in terms of DAG+MAGs (65 wt%) were using molar ratio of glycerol/soybean oil 0.8:1, 70 °C, 900 rpm, 90 min of reaction time, 10 wt% of enzyme content, and 40 % of ultrasound intensity (52.8 W cm(-2)). The results showed that the lipase-catalyzed glycerolysis in a solvent-free system with ultrasound bath can be a potential route for high content production of DAGs and MAGs.

Gaseous emissions from sewage sludge combustion in a moving bed combustor.

Substantial increase in sewage sludge generation in recent years requires suitable destination for this residue. This study evaluated the gaseous emissions generated during combustion of an aerobic sewage sludge in a pilot scale moving bed reactor. To utilize the heat generated during combustion, the exhaust gas was applied to the raw sludge drying process. The gaseous emissions were analyzed both after the combustion and drying steps. The results of the sewage sludge characterization showed the energy potential of this residue (LHV equal to 14.5 MJ kg(-1), db) and low concentration of metals, polycyclic aromatic hydrocarbons (PAH), polychlorinated dibenzo-p-dioxins (PCDD) and polychlorinated dibenzofurans (PCDF). The concentration of CO, NOx, BTEX (benzene, toluene, ethylbenzene and xylenes) emitted from the sludge combustion process were lower than the legal limits. The overall sludge combustion and drying process showed low emissions of PCDD/PCDF (0.42 ng I-TEQ N m(-3)). BTEX and PAH emissions were not detected. Even with the high nitrogen concentration in the raw feed (5.88% db), the sludge combustion process presented NOx emissions below the legal limit, which results from the combination of appropriate feed rate (A/F ratio), excess air, and mainly the low temperature kept inside the combustion chamber. It was found that the level of CO emissions from the overall sludge process depends on the dryer operating conditions, such as the oxygen content and the drying temperature, which have to be controlled throughout the process in order to achieve low CO levels. The aerobic sewage sludge combustion process generated high SO2 concentration due to the high sulfur content (0.67 wt%, db) and low calcium concentration (22.99 g kg(-1)) found in the sludge. The high concentration of SO2 in the flue gas (4776.77 mg N m(-3)) is the main factor inhibiting PCDD/PCDF formation. Further changes are needed in the pilot plant scheme to reduce SO2 and particulate matter emissions, such as the installation of exhaust gas-cleaning systems. According to previous studies, the efficient operation of such cleaning systems is also effective for metals emission control, which makes the combustion of sewage sludge a feasible treatment method from both energetic and environmental perspectives.

Ultrasound-assisted lipase-catalyzed transesterification of soybean oil in organic solvent system.

This work reports the transesterification of soybean oil with ethanol using two commercial immobilized lipases under the influence of ultrasound irradiation. The experiments were performed in an ultrasonic water bath, following a sequence of experimental designs to assess the effects of temperature, enzyme and water concentrations, oil to ethanol molar ratio and output irradiation power on the reaction yield. Results show that ultrasound-assisted lipase-catalyzed transesterification of soybean oil with ethanol might be a potential alternative route to conventional alkali-catalyzed method, as high reaction yields (~90 wt.%) were obtained at mild irradiation power supply (~100 W), and temperature (60 °C) in a relatively short reaction time, 4h, using Lipozyme RM IM as catalyst. The repeated use of the catalyst under the optimum experimental condition resulted in a decay in both enzyme activity and product conversion after two cycles. The use of Novozym 435 led to lower conversions (about 57%) but the enzyme activity was stable after eight cycles of use, showing, however, a reduction in product conversion after the forth cycle.

Extração e recuperação de prata e mercúrio em efluentes gerados na determinação de DQO empregando métodos físico-químicos / Extraction and recovery of silver and mercury from COD-test residues using physico-chemical methods

Durante as análises de Demanda Química de Oxigênio (DQO) é gerado um efluente líquido que se caracteriza pela presença de elevadas concentrações de metais pesados (Hg, Ag, Cr e Fe). Visando à remoção seletiva destes metais, possibilitando suas reutilizações, foram avaliados diferentes agentes precipitantes (Cl-, Br-, I- e S= para a Ag e o Hg e NaOH, NH4OH e NaHCO3 para o Cr e o Fe). Para a Ag e o Hg os melhores resultados em termos de remoção e recuperação seletiva foram obtidos quando do emprego seqüencial dos íons cloreto e sulfeto. Devido à presença de Hg(I), se fez necessário o emprego de NH4OH para separar seletivamente a Ag, presente na forma de AgCl, precipitada concomitantemente com Hg(I) como Hg2Cl2. Para o Cr e o Fe foram obtidas remoções que satisfazem à legislação (FEPAM) para ambos os elementos, somente quando do emprego do NaOH como agente precipitante.

In the analysis of Chemical Oxygen Demand (COD) a liquid residue rich in heavy metals (Hg, Ag, Cr, Fe) is obtained. This work aimed to remove, in a selective way, such metals from the residue using chemical precipitation, also creating a possibility to recover and reuse the heavy metals,. Different precipitants were evaluated (Cl-, Br-, I- and S= for Ag and Hg, and NaOH, NH4OH and NaHCO3 for Cr and Fe). The best results for selective recovery of Ag and Hg were obtained using chloride followed by sulphide. Due to the presence of Hg(I) it is necessary the use of NH4OH to separate Ag and Hg(I) that are both precipitated as AgCl and Hg2Cl2. Removal of Cr and Fe that attends the local limits set by the official control agency (FEPAM) was only obtained when NaOH was used as precipitating agent.