2014
DOI: 10.1371/journal.pone.0095162
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Removal of Emulsified Oil from Water by Fruiting Bodies of Macro-Fungus (Auricularia polytricha)

Abstract: The aim of this study was to investigate the feasibility of utilizing the fruiting bodies of a jelly macro-fungus Auricularia polytricha as adsorbents to remove emulsified oil from water. The effects of several factors, including temperature, initial pH, agitation speed, and adsorbent dosage, were taken into account. Results showed that the optimized conditions for adsorption of A. polytricha were a temperature of 35°C, pH of 7.5, and agitation speed of 100 rpm. The adsorption kinetics were characterized by th… Show more

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Cited by 22 publications
(9 citation statements)
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“…The adsorption process rate and its effect on the equilibrium time are often determined by kinetic models. The mass transport process and chemical and/or physical characteristics of the adsorbent affect the adsorption mechanism [34]. In order to explore the mechanism of biosorption and potential rate controlling steps, such as chemical reaction processes and mass transport, the distinguished pseudo-first-order, pseudo-second-order models have been applied to evaluate the experimental data.…”
Section: Resultsmentioning
confidence: 99%
“…The adsorption process rate and its effect on the equilibrium time are often determined by kinetic models. The mass transport process and chemical and/or physical characteristics of the adsorbent affect the adsorption mechanism [34]. In order to explore the mechanism of biosorption and potential rate controlling steps, such as chemical reaction processes and mass transport, the distinguished pseudo-first-order, pseudo-second-order models have been applied to evaluate the experimental data.…”
Section: Resultsmentioning
confidence: 99%
“…9 ) 49 models were used to describe the adsorption equilibrium. where q m is the maximum adsorption capacity (mg g −1 ), K L is the Langmuir adsorption equilibrium constant (L mg −1 ), K F and n are Freundlich constants representing the adsorption capacity (L −1/n mg −(1−n) g −1 ) and the adsorption intensity varying with the degree of heterogeneity, respectively, and K L ’ and n ’ are the Langmuir adsorption equilibrium constant (L mg −1 ) and the adsorption intensity, respectively 50 .…”
Section: Methodsmentioning
confidence: 99%
“…Two kinetic models, a pseudo-first-order model and a pseudo-second-order model, were used to characterize the adsorption kinetics of chromium (Cr or Cr 6+ ) on the loaded activated carbon composites (NZVI/GAC). The integrated forms of the two models are as follows:where q e is the amount of chromium ions adsorbed at equilibrium (mgg −1 ), and k 1 (s −1 ) and k 2 (gmg −1 s−1 ) are the rate constants of the pseudo-first and pseudo-second-order adsorptions, respectively 57 .…”
Section: Methodsmentioning
confidence: 99%