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An Investigation Into Activated CarbonKyriakakis, G 02 July 2015 (has links)
The extraction of aurocyanide by activated carbon
probably involves the adsorption of neutral ion-pair
species [M ^jAuCCN)^. The large hydrophobic
aurocyanide anion associates with the cation in
order to minimize the disruption of the water
structure whereby lowering its free energy
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Organic solvent regeneration of granular activated carbonRollor, Michael Alan 12 1900 (has links)
No description available.
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Activated carbon adsorption techniqueKumke, Gordon W. January 1963 (has links)
Thesis (M.S.)--University of Wisconsin--Madison, 1963. / Typescript. eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references (leaves [141-155]).
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Modelling and control of wastewater treatmentGhavipanjeh, Farideh January 2001 (has links)
No description available.
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The numerical simulation of two phase flows in settling tanksBrennan, Daniel January 2001 (has links)
No description available.
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Development of a device for monitoring metal pollutants in seawaterSolbra, Susan Tanja January 2001 (has links)
No description available.
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The role of microbial polysaccharides and filamentous bacteria in activated sludge bioflocculationEccles, C. R. H. January 1987 (has links)
No description available.
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The chemistry of the carbon-in-pulp processAdams, Michael David 26 August 2014 (has links)
Several conflicting theories of the adsorption of
aurocyanide onto activated carbon presently exist. To
resolve the mechanism, adsorption and elution of
aurocyanide are examined by several techniques, including
Mossoauer spectroscopy, X-ray photoelectron spectroscopy,
X-ray diffractometry, Fourier Transform Infrared
spectrophotometry, ultraviolet-visible spectrophotometry
and scanning electron microscopy.
The evidence gathered indicates that, under normal plant
conditions, aurocyanide is extracted onto activated carbon
in the form of an ion pair M n+ [Au(CN) 2 ] n, and eluted by
hydroxide or cyanide. The hydroxide or cyanide ions react
with the carbon surface, rendering it relatively
hydrophilic with a decreased affinity for neutral species.
Additional adsorption mechanisms are shown to operate
under other conditions of ionic strength, pH, and
temperature. The poor agreement in the literature
regarding the mechanism of adsorption of aurocyanide onto
activated carbon is shown to be due to the fact that
different mechanisms operate under different experimental
conditions. The AuCN produced on the carbon surface by acid
treatment is shown to react with hydroxide ion via the
reduction of AuCN to metallic gold with formation of
Au (CN) 2 , and the oxidation of cyanide to cyanate. Other
species, such as An(CN)5 and Ag(CN)g adsorb onto
activated carbon by a similar mechanism to that postulated
for Au(CN)2 .
Ion association of MAu(CN) 2 salts in aqueous solution is
demonstrated by means of potentiometric titration and
conductivity measurements, and various associated
species of KAu(CN), salts are shown to occur in organic
solvents by means of infrared spectrophoteaietric and
distribution measurements.
A kinetic model was developed for elution of aurocyanide
from activated carbon and was found to predict gold elution
performance successfully using the Zadra procedure.
The influence of the surface chemistry and structure of
activated carbon on adsorption of aurocyanide was
investigated by characterization of activated carbons that
were synthesized or oxidized under various conditions.
Synthetic polymeric adsorbents with characteristics
similar to activated carbons were also studied. The
evidence suggests that a large micropore volume is
important in providing suitable active sites for
adsorption. Another important factor is the presence of
basic functional groups within the micropore, which act as
solvating agents for the ion pair.
The aim is to provide a self-consistent adsorption
mechanism that accounts for all observations presented in
the literature. Interpretation of results in terms of
preconceived ideas, and neglect of observations of other
authors has greatly contributed to current disagreement in
the literature.
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Obtenção e caracterização, em laboratório, do carvão ativo de bagaço de cana, visando sua utilização no tratamento de água de lavagem de cana-de-açúcar. / Obtaining and caracterization in laboratory of active charcoal of sugar cane bagasse, aiming its use in the sugar cane washing water treatment.Wiebeck, Hélio 16 November 1987 (has links)
As amostras de carvão ativo de bagaço de cana-de-açúcar foram preparadas em temperaturas de carbonização de 500, 600 e 700 ºC, com tempos de ativação de 60 e 120 minutos e concentração de agente ativante (ZnC12) 30 e 60% em relação ao bagaço seco original. Foi utilizado como padrão, para verificação de eficiência, um carvão ativo alemão (Riedel). Estas amostras foram caracterizadas pelas seguintes análises: rendimento; teor e umidade; teor de cinzas; pH; teor de substâncias solúveis em água. Foi também estudado o desempenho destas amostras no descoramento de água de lavagem de cana-de-açúcar, utilizando 1% e 1,5% em peso de carvão ativo. Amostras preparadas a 500 ºC, 60 minutos e concentração de agente ativamente 0%, 30% e 60% em relação ao peso de bagaço seco original foram utilizadas no tratamento de água de lavagem de cana-de açúcar visando a diminuição do potencial poluidor, essas mesmas amostras foram utilizadas para determinação de poder de adsorção, equação e isoterma de Freundlich. Os resultados mostraram ser viável, em escala de laboratório a obtenção de carvão ativo de bagaço de cana-de-açúcar, para utilização no tratamento de água de lavagem de cana-de-açúcar visando diminuir o seu potencial poluidor. / Samples of activated carbon from cane-thrash were prepared in carbonization temperatures of 500, 600 and 700 ºC; activation times of 60 and 120 minutes, and concentrations of activating agent (ZnC12) 30 and 60% in relation to the original dry bagasse. A German activated carbon, was used a standard (Riedel). The samples were characterized by the following analysis: yield, proportion (5) of humidity, proportion of ashes; pH; proportion of solubles in water substances. It was also studied the performance in discolouring sugar-cane washing water using 1% and 1,5% in weight of activated carbon. Samples prepared in 500 ºC, 60 minutes and activating agent concentration of 0%, 30% and 60% in relation to the weight of the original dry bagasse were used in the treatment of sugar-cane washing water the purpose of reducing the polluter potential. They were used to determine the adsorption power, equation and Freundlish isotherm. The results showed it is possible to obtain active carbon from cane-thrash in laboratory scale, to be used in the treatment of sugar-cane washing water with the purpose of reducing its polluter potential.
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Adsorption of acetaldehyde vapour in low concentration in air with fixed-beds of charcoalChun, Heungwoo January 2010 (has links)
Digitized by Kansas Correctional Industries
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