Separation Bubble
Mostrando 1-12 de 20 artigos, teses e dissertações.
-
1. Effect of calcium concentration on calcite flotation from apatite using carbonic gas
Abstract The flotation process currently considered for apatite concentration from the Santa Quitéria phosphate deposit (Brazil), involves bulk flotation of apatite and calcite with anionic collector at pH=10 followed by calcite flotation at pH=5.5, adjusted with H3PO4. Although this concept is efficient from the point of view of separation between apatite
REM, Int. Eng. J.. Publicado em: 2020-06
-
2. GUILHERME, Alexandre Anselmo; MORGAN, W. John. Philosophy, dialogue, and education. Nine Modern European Philosophers [Filosofia, diálogo e educação: nove filósofos europeus modernos]. London: Routledge, 2018. 190 p.
Abstract The flotation process currently considered for apatite concentration from the Santa Quitéria phosphate deposit (Brazil), involves bulk flotation of apatite and calcite with anionic collector at pH=10 followed by calcite flotation at pH=5.5, adjusted with H3PO4. Although this concept is efficient from the point of view of separation between apatite
Bakhtiniana, Rev. Estud. Discurso. Publicado em: 2020-06
-
3. Ultrastructural study of morphological changes in Schistosoma mansoni after in vitro exposure to the monoterpene rotundifolone
ABSTRACT INTRODUCTION: Schistosomiasis, a parasitic disease caused by trematode flatworms of the genus Schistosoma, affects more than 200 million people worldwide, and its control is dependent on a single drug, praziquantel. Here, we report the in vitro effect of rotundifolone, a monoterpene isolated from Mentha x villosa (Lamiaceae), on Schistosoma manson
Rev. Soc. Bras. Med. Trop.. Publicado em: 2017-02
-
4. Direct Numerical Simulation of the Onset of Vortex Shedding for Blunt Elongated Bodies
ABSTRACT: This research project focuses upon the wake behind a two-dimensional blunt-trailing-edged body. Data are obtained numerically by means of a Direct Numerical Simulation code. The body has an elliptical nose followed by a straight section that ends in a blunt base. The present paper is dedicated to the analysis of the onset of the shedding process. T
J. Aerosp. Technol. Manag.. Publicado em: 2014-09
-
5. Hydrodynamic and absorption studies of carbon dioxide absorption in aqueous amide solutions using a bubble column contactor
The present work analyses the carbon dioxide absorption process in aqueous n-alkylpyrrolidones solutions, from the point of view of hydrodynamic studies as well as mass transfer, using a bubble column contactor. An analysis of the influence of solute concentration and gas flow-rate is complemented by the study of the effect caused by the alkyl group on the h
Braz. J. Chem. Eng.. Publicado em: 2013-12
-
6. Fracionamento de surfactina em coluna de bolhas e espuma / Fractionation of surfactin on a bubble and foam column
Foam fractionation of biosurfactant surfactin solutions obtained from fermentation with Bacillus subtilis bacteria was experimentally studied. A bubble and foam column system was mounted and operated in a semi-batch mode aiming at to optimize the concentration enrichment and the recovery of the bioproduct. The process involves the injection of gaseous nitrog
Publicado em: 2010
-
7. NUMERICAL INVESTIGATION OF THE TURBULENT FLOW SEPARATION BUBBLE OVER INCLINED THIN FLAT PLATE / ANÁLISE NUMÉRICA DA BOLHA DE SEPARAÇÃO DO ESCOAMENTO TURBULENTO SOBRE PLACA PLANA FINA INCLINADA
A estabilização de mísseis e projéteis é normalmente realizada através de aletas, que podem ser representadas por placas planas finas. O escoamento sobre placas finas é de difícil previsão por apresentar diversos fenômenos, tais como transição da camada cisalhante para regime turbulento, recolamento, relaminarização e geração de bolhas primá
Publicado em: 2009
-
8. SIMULAÇÃO DE GRANDES ESCALAS DA BOLHA DE SEPARAÇÃO EM PLACAS FINAS A PEQUENO ÂNGULO DE INCIDÊNCIA / LARGE EDDY SIMULATIONS OF THE THIN PLATE SEPARATION BUBBLE AT SHALLOW INCIDENCE
Escoamentos aerodinâmicos externos sobre membranas e aerofólios finos representam um enorme desafio para simulações numéricas, tendo em vista os diversos e complexos regimes de escoamento presentes, que incluem separa ção da camada limite, transição da camada de mistura para regime turbulento, recolamento, relaminarização da camada limite, e forma
Publicado em: 2006
-
9. NUMERICAL SIMULATION OF A PROCESS SEPARATOR FOR OIL AND WATER / SIMULAÇÃO NUMÉRICA DE UM FLOTADOR PARA SEPARAÇÃO DE ÓLEO DA ÁGUA
This work refers to an application for the treatment of produced water in oil and gas production platforms. It focuses on the analysis of flotation cells design and geometry influence in the oil-water separation process, in order to optimize their performance. Examples of application for the simulation tool are: internal retrofitting of existing equipments a
Publicado em: 2003
-
10. Optimizing dissolved air flotation design system
Dissolved Air (Pressure) Flotation-DAF, is a well-established separation process that employs micro-bubbles as a carrier phase. This work shows results concerning bubble generation at low working pressures in modified DAF-units to improve the collection of fragile coagula by bubbles. DAF of Fe (OH)3 (as model) was studied as a function of saturation pressure
Brazilian Journal of Chemical Engineering. Publicado em: 2000-12
-
11. Conversion of a deasphalting unit for use in the process of supercritical solvent recovery
In order to reduce energy consumption and to increase deasphalted oil yield, an old PETROBRAS deasphalting unit was converted for use in the process of supercritical solvent recovery. In-plant and pilot tests were performed to determine the ideal solvent-to-oil ratio. The optimum conditions for separation of the supercritical solvent from the solvent-plus-oi
Brazilian Journal of Chemical Engineering. Publicado em: 2000-09
-
12. Avaliação de metodos de contribuição de grupos para uso em calculos de equilibrio liquido-vapor
A methodology for predicting vapour-liquid equilibrium curves using group contribution methods is proposed. From the molecular structure of the compound, values of normal boiling temperature, critical properties, acentric factor, second virial coefficients, vapor pressure, activity coefficients and molar liquid volume are required since they are necessary in
Publicado em: 1992