Catalisadores a base de guanidinas, suporte compreendendo catalisadores a base de guanidina, processo de produção de produção de suporte com guanidinas, e, uso de guanidinas para obtenção de biodiesel

Colorminas Colorifício e MineraçãoUniversidade Federal do Rio Grande do SulQuímicaDepositad

Processo de obtenção de biocarvão e de bio-óleo cru, processo de obtenção de carvão ativado magnético, carvão ativado magnético e seu uso, uso do bio-óleo cru ou da fração de destilado de bio-óleo e uso do biocarvão

Universidade Federal do Rio Grande do SulQuímicaDepositad

Production of analytical grade 2-ethoxy-2-methylpropane from a commercial product

Ethyl tert-butyl ether (ETBE) is produced by commercial processes to a purity of up to 96%. In recent years, several companies have started to produce ETBE, increasing the demand for standards with higher grades of purity in the area of production control and final product certification. The present work involved the development of a purification protocol for obtaining high purity ETBE from the commercial product used in the formulation of automotive gasolines, using a spinning band distillation column. The ETBE thus produced showed a purity of over 99.5%, its main contaminant being its isomer, ethyl-sec-butyl ether (ESBE)

Production of analytical grade 2-ethoxy-2-methylpropane from a commercial product

Ethyl tert-butyl ether (ETBE) is produced by commercial processes to a purity of up to 96%. In recent years, several companies have started to produce ETBE, increasing the demand for standards with higher grades of purity in the area of production control and final product certification. The present work involved the development of a purification protocol for obtaining high purity ETBE from the commercial product used in the formulation of automotive gasolines, using a spinning band distillation column. The ETBE thus produced showed a purity of over 99.5%, its main contaminant being its isomer, ethyl-sec-butyl ether (ESBE)

Development of a device to valuate the effect of ethanol on the vapor pressure and vaporization enthalpy of fuel gasolines

The quality of the gasoline utilized for fueling internal combustion engines with spark ignition is directly affected by the gasoline’s properties. Thus, the fuel’s properties must be in perfect equilibrium to allow the engine to perform optimally, not only insofar as fuel consumption is concerned, but also in order to reduce the emission of pollutants. Vapor pressure and vaporization enthalpy are important properties of a gasoline determining the fuel’s behavior under different operating conditions in internal combustion engines. The study reported here involved the development of a device to determine the vapor pressure and the vaporization enthalpy of formulations containing volumes of 5, 15 and 25% of ethanol in four base gasolines (G1, G2, G3 and G4). The chemical composition of these gasolines was determined using a gas chromatographer equipped with a flame ionization detector (FID)

Development of a device to valuate the effect of ethanol on the vapor pressure and vaporization enthalpy of fuel gasolines

The quality of the gasoline utilized for fueling internal combustion engines with spark ignition is directly affected by the gasoline’s properties. Thus, the fuel’s properties must be in perfect equilibrium to allow the engine to perform optimally, not only insofar as fuel consumption is concerned, but also in order to reduce the emission of pollutants. Vapor pressure and vaporization enthalpy are important properties of a gasoline determining the fuel’s behavior under different operating conditions in internal combustion engines. The study reported here involved the development of a device to determine the vapor pressure and the vaporization enthalpy of formulations containing volumes of 5, 15 and 25% of ethanol in four base gasolines (G1, G2, G3 and G4). The chemical composition of these gasolines was determined using a gas chromatographer equipped with a flame ionization detector (FID)

Sampling of particulate matter and of the volatile organic fraction of emissions from a diesel cycle engine without the use of dilution tunnel

Using a sampling method of particulate matter (PM) without the use of a dilution tunnel allows for evaluations of the volatile hydrocarbons (HC) in the emissions of diesel cycle engines. The procedure in this work applied a heated filter with temperature controlled. The volatile compounds are condensed at low temperature, allowing for evaluation of the HC by thermal desorption of the PM and for analysis of the condensed compounds of the exhaust gases

Sampling of particulate matter and of the volatile organic fraction of emissions from a diesel cycle engine without the use of dilution tunnel

Using a sampling method of particulate matter (PM) without the use of a dilution tunnel allows for evaluations of the volatile hydrocarbons (HC) in the emissions of diesel cycle engines. The procedure in this work applied a heated filter with temperature controlled. The volatile compounds are condensed at low temperature, allowing for evaluation of the HC by thermal desorption of the PM and for analysis of the condensed compounds of the exhaust gases

Catalisadores baseados em CeO2/ZrO2/Al2O3 para controle de emissões gasosas

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Using GC-MS to analyze bio-oil produced from pyrolysis of agricultural wastes : discarded soybean frying oil, coffee and eucalyptus sawdust in the presence of 5% hydrogen and argon

Pyrolysis is a thermal process for converting various biomasses, wastes and residues to produce high-energydensity fuels (bio-oil). In this paper, we have done some important analysis of bio-oil which is obtained from the pyrolysis of agricultural wastes - discarded soybean frying oil, coffee and eucalyptus sawdust in the presence of 5% Hydrogen and Argon. The bio oil was obtained in one step pyrolysis in which temperature of the system kept 15°C and then increased up to 800°C but in two step condensation processes. 1st condensation step is done on temperature 100°C and 2nd is done on 5°C. So we got two types of fractions, HTPO (Oil condensed at high temperature 100°C after pyrolysis) and LTPO (Oil condensed at low temperature 5°C after pyrolysis). After pyrolysis the thermal cracking is done for both types of oil on the same two temperatures, then we again got two type of fractions HTCO (high temperature 100°C condensed oil after cracking) and LTCO (Low temperature 5°C condensed oil after cracking), these fractions are distillated and analyzed in GC-MS. The resulted compounds are given in the paper and are explained with the help of graphs and tables. The ultimate aim of hydrogenation and Argon is to improve stability and fuel quality by decreasing the contents of organic acids and aldehydes as well as other reactive compounds, as oxygenated and nitrogenated species because they not only lead to high corrosiveness and acidity, but also set up many obstacles to applications