Abstract:In this study, a commercial granular activated carbon was modified with sodium hydroxide followed by a cationic surfactant to increase its efficiency for nitrate removal from water. Physicochemical properties of untreated activated carbon and treated activated carbons were characterized in the terms of FTIR spectroscopy, N 2 adsorption-desorption, and SEM analyses. The surface properties of ACs were determined by N 2-adsorption isotherm data and modeled with several mathematical models. The results showed that… Show more
“…However, treatment with NaOH or HNO 3 prior to surfactant modification has been shown to minimise the reduction in the BET specific surface surface or micro pore volume and ultimately increase the net surface charge of the modified activated carbons. Mazarji et al [27] recorded that the BET specific surface area and micro pore volume of a virgin activated carbon, 888 m 2 /g and 0.376 cm 3 /g increased to 901 m 2 /g and 0.400 cm 3 /g respectively after NaOH treatment but slightly reduced to 722 m 2 /g and 0.310 cm 3 /g after CTAB modification of the NaOH treated activated carbon. They obtained percentage nitrate removal of NaOH-CTAB modified activated carbon, 80%, >NaOH-pre-treated activated carbon, 16% > virgin activated carbon, 8%.…”
Section: Adsorption Of Inorganic Contaminantsmentioning
confidence: 99%
“…However, increase in initial concentration increases the driving force causing more adsorbate to bind onto the adsorbent. Hence, for a fixed mass of adsorbent, increase in initial concentration of adsorbate increases the specific adsorbate uptake until equilibrium is attained [26] [27].…”
“…In addition, reduction of the micro-pore volume above CMC has high tendency of masking the active binding sites originally present on the virgin activated carbon thereby reducing their contribution to physical adsorption, surface complexation and electrostatic interaction to the main ion exchange. Few researchers fixed surfactant concentration below CMC [17] [27] or above CMC [21] during adsorption experiments. Such approach may prevent optimising the capacity of the modified activated carbons.…”
Effluents containing inorganic contaminants are releasing into the environment untreated despite being hazardous to man and environment. It is costly and unsustainable to use conventional methods to remove them from dilute aqueous solution. Adsorption involving granular activated carbon is an alternative method for treating such effluents. Granular activated carbon is structurally strong, highly resistance to attrition and wearing, large and can easily separate from the effluents. However, its surface is highly hydrophobic and has little surface charge thereby reducing its adsorption capacity for anion or cation. This article reviews surfactant modification of activated carbon to enhance its adsorption capacity for inorganic contaminants and key factors affecting the adsorption efficiency. They include initial concentration of contaminants, contact time, solution pH, solution temperature, adsorbent concentration, ionic strength, competing ions, type of surfactant, and surfactant concentration. The modified activated carbon usually shows maximum contaminant uptake around its critical micelles concentration. Surfactant modification reduces specific surface area and/or micro pore volume but hot NaOH or HNO 3 treatment before surfactant modification minimises this drawbacks and increases the net surface charge. Overall, surfactant modification is a simple but efficient method of enhancing adsorption capacity of activated carbon for removing anion or cation from aqueous solution. However, a handful publication is available on the regeneration of the spent (saturated) surfactant modified activated carbons. Hence, more research efforts should be directed towards proper regenerating reagents and the optimise conditions such as contact time, concentration, and temperature for regenerating spent modified activated carbons.
“…However, treatment with NaOH or HNO 3 prior to surfactant modification has been shown to minimise the reduction in the BET specific surface surface or micro pore volume and ultimately increase the net surface charge of the modified activated carbons. Mazarji et al [27] recorded that the BET specific surface area and micro pore volume of a virgin activated carbon, 888 m 2 /g and 0.376 cm 3 /g increased to 901 m 2 /g and 0.400 cm 3 /g respectively after NaOH treatment but slightly reduced to 722 m 2 /g and 0.310 cm 3 /g after CTAB modification of the NaOH treated activated carbon. They obtained percentage nitrate removal of NaOH-CTAB modified activated carbon, 80%, >NaOH-pre-treated activated carbon, 16% > virgin activated carbon, 8%.…”
Section: Adsorption Of Inorganic Contaminantsmentioning
confidence: 99%
“…However, increase in initial concentration increases the driving force causing more adsorbate to bind onto the adsorbent. Hence, for a fixed mass of adsorbent, increase in initial concentration of adsorbate increases the specific adsorbate uptake until equilibrium is attained [26] [27].…”
“…In addition, reduction of the micro-pore volume above CMC has high tendency of masking the active binding sites originally present on the virgin activated carbon thereby reducing their contribution to physical adsorption, surface complexation and electrostatic interaction to the main ion exchange. Few researchers fixed surfactant concentration below CMC [17] [27] or above CMC [21] during adsorption experiments. Such approach may prevent optimising the capacity of the modified activated carbons.…”
Effluents containing inorganic contaminants are releasing into the environment untreated despite being hazardous to man and environment. It is costly and unsustainable to use conventional methods to remove them from dilute aqueous solution. Adsorption involving granular activated carbon is an alternative method for treating such effluents. Granular activated carbon is structurally strong, highly resistance to attrition and wearing, large and can easily separate from the effluents. However, its surface is highly hydrophobic and has little surface charge thereby reducing its adsorption capacity for anion or cation. This article reviews surfactant modification of activated carbon to enhance its adsorption capacity for inorganic contaminants and key factors affecting the adsorption efficiency. They include initial concentration of contaminants, contact time, solution pH, solution temperature, adsorbent concentration, ionic strength, competing ions, type of surfactant, and surfactant concentration. The modified activated carbon usually shows maximum contaminant uptake around its critical micelles concentration. Surfactant modification reduces specific surface area and/or micro pore volume but hot NaOH or HNO 3 treatment before surfactant modification minimises this drawbacks and increases the net surface charge. Overall, surfactant modification is a simple but efficient method of enhancing adsorption capacity of activated carbon for removing anion or cation from aqueous solution. However, a handful publication is available on the regeneration of the spent (saturated) surfactant modified activated carbons. Hence, more research efforts should be directed towards proper regenerating reagents and the optimise conditions such as contact time, concentration, and temperature for regenerating spent modified activated carbons.
“…Adsorption, in general, is the removal process of soluble substances that are in solution on a suitable interface [1]. Activated carbon has gained wide attention as an efficient adsorbent which can adsorb various pollutants in aquatic phase especially organic pollutants [12]. However, it shows poor adsorption towards anionic pollutants.…”
Coconut granular activated carbon (CGAC) was modified by impregnating with ZnCl 2 solution to remove nitrate from aqueous solutions. Sorption isotherm and kinetic studies were carried out in a series of batch experiments. Nitrate adsorption of both ZnCl 2 -modified CGAC and CGAC fitted the Langmuir and Freundlich models. Batch adsorption isotherms indicated that the maximum adsorption capacities of ZnCl 2 -modified CGAC and CGAC were calculated as 14.01 mgN·g −1 and 0.28 mgN·g −1 , respectively. e kinetic data obtained from batch experiments were well described by pseudo-second-order model. e column study was used to analyze the dynamic adsorption process. e highest bed adsorption capacity of 1.76 mgN·g −1 was obtained by 50 mgN·L −1 inlet nitrate concentration, 20 g adsorbents, and 10 ml·min −1 flow rate. e dynamic adsorption data were fitted well to the omas and Yoon-Nelson models with coefficients of correlation R 2 > 0.834 at different conditions. Surface characteristics and pore structures of CGAC and ZnCl 2 -modified CGAC were performed by SEM and EDAX and BET and indicated that ZnCl 2 had adhered to the surface of GAC after modified. Zeta potential, Raman spectra, and FTIR suggested the electrostatic attraction between the nitrate ions and positive charge. e results revealed that the mechanism of adsorption nitrate mainly depended on electrostatic attraction almost without any chemical interactions.
“…Urbanization, industrialization, high usage of agricultural fertilizers, combined with inappropriate treatment of wastewater, have led to contamination of the environment and groundwater resources by toxic pollutants including organic, and inorganic ions like nitrate and phosphate. Nitrogen and phosphorous are used in agriculture due to their high solubility in water and nutritious values for the plants [1][2][3]. However, excessive release of nitrate and phosphate to the environment adversely affects the ecosystem and human health [4,5].…”
In the present study, Glycyrrhiza glabra residues (GGR) were used for the preparation of activated carbon, with a surface area of 959.22 m 2 g −1 . Activated carbon was prepared through chemical activation using ZnCl 2 at optimum carbonization temperature, and impregnation ratio for nitrate, and phosphate removal. The effect of contact time and adsorbent dosage on the removal efficiency was investigated, and the pseudo-second-order kinetic model correlated well with the adsorption data. The response surface methodology was applied for the determination of the effect of initial concentration, pH, and temperature and their interaction on the removal efficiency in the batch adsorption system. The Langmuir isotherm generated a satisfactory fit with the experimental data, and the maximum adsorption capacity was 142.5 mg g −1 at 308 K and 92.5 mg g −1 at 298 K for nitrate and phosphate removal, respectively. The high adsorption capacity reveals the applicability of the GGR activated carbon for nitrate and phosphate removal. Furthermore, the fixed-bed column adsorption studies were carried out, and the effect of flow rate and influent concentration on the behavior of the breakthrough curve was studied. The breakthrough time decreased by increasing the flow rate and inlet concentration. The Thomas and Yoon-Nelson models were suitable models for the design of GGR activated carbon fixed-bed column. The LUB of 0.44 cm and 4.35 cm was obtained for nitrate and phosphate with the inlet concentration of 20 mg L −1 and a flow rate of 40 mL min −1 , respectively. GGR is a new adsorbent that has not been previously utilized for adsorption of phosphate and nitrate.
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