Water Pollution Control in Asia 1988
DOI: 10.1016/b978-0-08-036884-9.50066-1
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Recovery of Nickel by Crystallization of Nickel Carbonate in a Fluidized-Bed Reactor

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Cited by 16 publications
(15 citation statements)
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“…ln q e = ln q m − Kε 2 (10) where q e is the amount of the metal ion adsorbed at the equilibrium, K a constant related to the adsorption energy, q m the theoretical saturation capacity, ε is the Polanyi potential, equal to RT ln(1 + 1/C e ). The slope of the plot of ln q e versus ε 2 gives K (mol 2 (kJ 2 ) −1 ) and the intercept yields the sorption capacity, q m (mol g −1 ).…”
Section: Dubinin and Radushkevich Isothermmentioning
confidence: 99%
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“…ln q e = ln q m − Kε 2 (10) where q e is the amount of the metal ion adsorbed at the equilibrium, K a constant related to the adsorption energy, q m the theoretical saturation capacity, ε is the Polanyi potential, equal to RT ln(1 + 1/C e ). The slope of the plot of ln q e versus ε 2 gives K (mol 2 (kJ 2 ) −1 ) and the intercept yields the sorption capacity, q m (mol g −1 ).…”
Section: Dubinin and Radushkevich Isothermmentioning
confidence: 99%
“…A number of technologies have been used to remove Ni(II) from wastewater streams, such as adsorption onto activated carbon [6][7][8], filtration of precipitate [9] and by crystallization in the form of nickel carbonate [10]. However, these technologies are most suitable in situations where the concentrations of the heavy metal ions are high.…”
Section: Introductionmentioning
confidence: 99%
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“…While the nickel(II) ion concentration in plating rinse can approach 2-900 mg −1 , wastewater from paint and ink formulation, porcelain enameling, copper sulphate manufacture industries record effluent nickel(II) ion concentrations that varies from 0 to 40, 0.25 to 67 and around 22 mg l −1 [3]. A number of conventional methods have been used to remove nickel(II) ion from wastewater streams, such as adsorption on activated carbon [4]; chemical precipitation [5]; crystallization in the form of nickel carbonate [6]. However, these methods are ineffective or expensive when initial metal concentrations in wastewaters are low, or when very * Fax: +90 388 2250114.…”
Section: Introductionmentioning
confidence: 99%
“…The technology was initially employed for the softening of drinking water by calcium carbonate precipitation 7) and the removal of phosphates from waste water, producing calcium phosphate 8) . More recently, fluidised bed reactors have been used for the removal of metals (nickel, copper and zinc) from solution 9,10,11,12) as carbonates or as sulphides. Kaksonen and co-workers 13) used biologically generated sulphide and alkalinity as the reagents to precipitate zinc and iron from acidic waste water in a fluidised bed reactor, whilst Esposito and co-workers 14) used the same sulphide source but precipitated only zinc from acidic waste water.…”
Section: Introductionmentioning
confidence: 99%