Literature DB >> 30426059

Data of adsorption of Basic Blue 41 dye from aqueous solutions by activated carbon prepared from filamentous algae.

Shirin Afshin1,2, S Ahmad Mokhtari1, Mehdi Vosoughi1,3, Hadi Sadeghi1, Yousef Rashtbari1,2.   

Abstract

For this data article the adsorption of Basic Blue 41 (BB 41) dye by activated carbon derived from filamentous algae (AAC) of available in agriculture waste as cheap adsorbents were examined. Activated carbon has been widely used as an adsorbent regard to its massive specific surface area, high porosity, reusability and thermal stability for the removal of pollutants from effluent. These filamentous algae grow widely in irrigation streams, causing decreasing speed of water flow and are not even eaten by livestock so are considered agricultural wastes. They can be used as precursors for activated carbon preparation and as adsorbent for the dye removal. The data of initial dye concentration (50-200 mg//L), pH of dye solution (3-9), adsorbent dosage (0.25-2 g/L), and contact time (5-200 min), were assessed. The structure of AAC was characterized by X-ray diffraction and Fourier transforms infrared spectroscopy. Activated carbon with a 94% removal of dye at concentration of 100 mg/L, pH 9, and adsorbent dose 1 g/L after 90 min. The data of isotherms and Kinetics indicated that the experimental data are fitted to Langmuir and second-pseudo-order models. Under the optimum conditions, maximum adsorption capacity of the AAC in Langmuir model enhanced to amount of 125 mg/g. According to the experimental data, filamentous algae are a suitable raw material for activated carbon production.

Entities:  

Keywords:  Activated carbon; Adsorption; Basic Blue 41; Filamentous algae

Year:  2018        PMID: 30426059      PMCID: PMC6222081          DOI: 10.1016/j.dib.2018.10.023

Source DB:  PubMed          Journal:  Data Brief        ISSN: 2352-3409


Specifications table Value of the data The data provides information about the adsorption process of BB 41 dye from aqueous solution by activated carbon under room temperature. Activation method can be used to prepare activated carbon from algae powdered using H3PO4 and data will be advantageous for scale up and design the adsorption experimental set up for removing dyes. The adsorption process by activated carbon can be used as a convenient and environmentally friendly method for removing of different concentrations of dye.

Data

FTIR spectra was recorded in the range 400–4000 cm−1 using a Fourier transform infrared spectrometer (PerkinElmer, USA), and Philips X’Pert Pro instrument (the Netherlands) was used to get XRD patterns of the activated carbon, respectively. The obtained data are shown in Fig. 1(a) and (b). The data of pH solution and contact time on removal efficiency are presented in Figs. 2 and 3. The kinetic and isotherm data and equation are calculated and listed in Table 1, Table 2, Table 3. Comparison the adsorption capacity of AAC with the other adsorbents is presented in Table 4.
Fig. 1

FTIR (a) and XRD (b) patterns of AAC.

Fig. 2

Data of initial pH on the adsorption of BB 41 by the AAC.

Fig. 3

Data of the contact time on the adsorption of BB 41 by AAC.

Table 1

Equations of isotherm and kinetic models [11], [12], [13], [14].

Model typesModel nameEquation
Isotherm modelsLangmuir1/qe = 1/(qmK1Ce) + (1/qm)
FreundlichLog qe = log kf + (1/n)log Ce
Kinetic modelsPseudo-first-orderLog(qeqt) = log qe−(k1/2.303)t
Pseudo-second-ordert/qe = 1/(k2qe2) + 1(1/qe)t
Table 2

Kinetic parameters of BB 41 adsorption onto AAC obtained using of the pseudo-first order and pseudo-second order models [11].

ModelPseudo-first-order
Pseudo-second-order
Co (mg/L)qe,exp (mg/g)k1 (1/min)qe,cal (mg/g)R2k2 (g/mg/min)qe,cal (mg/g)R2
50500.02612.070.86440.008350.5050.9996
10096.40.02859.080.9790.00121000.9968
1501240.02673.890.94040.0008131.570.9962
200137.90.031125.370.97960.0004147.050.994
Table 3

Langmuir and Freundlich isotherms parameters for adsorption of BB 41 onto AAC [15], [16], [17].

Isotherm modelLangmuir isotherm
Freundlich isotherm
ParameterKL (L/mg)qm (mg/g)R2Kf [(mg/g) (mg/L)1/n]nR2
Value1.8181821250.957463.885166.3251110.9493
Table 4

Comparison of the adsorption capacity of BB 41 onto various adsorbents.

Adsorbentsqm(mg/g)References
Sodium alginate12[18]
Raw rice husk24.4[19]
Modified rice husk34.6[19]
Untreated antibiotic waste111[20]
N, F-codoped flower-like TiO2143[21]
Activated carbon125This data article
FTIR (a) and XRD (b) patterns of AAC. Data of initial pH on the adsorption of BB 41 by the AAC. Data of the contact time on the adsorption of BB 41 by AAC. Equations of isotherm and kinetic models [11], [12], [13], [14]. Kinetic parameters of BB 41 adsorption onto AAC obtained using of the pseudo-first order and pseudo-second order models [11]. Langmuir and Freundlich isotherms parameters for adsorption of BB 41 onto AAC [15], [16], [17]. Comparison of the adsorption capacity of BB 41 onto various adsorbents.

Experimental design, materials and methods

Materials

For this data article, all chemicals materials were purchased from Merck in analytical grade. Basic Blue 41 (Empirical Formula: C20H26N4O6S2, purity ≥ 98%) was the commercial product supplied from Alvan Sabet Hamadan Co (Iran) and used without further purification. The algae were collected from river in Ardabil, Iran. The pH of the solution was adjusted by mixing with the appropriate amount of 0.1 M (H2SO4/NaOH). A stock solution of dye solutions with a concentration of 1000 mg/L was prepared by dissolving the required quantity of the dye in distilled water. Distilled water was used throughout in all the experiments.

Preparation of activated carbon

The algae were collected from the streams in Ardabil, Iran. The algae were washed with using distilled water several times to remove the contamination and impurities such as dust and stones. The algae were dried at 60 °C in oven for 72 h. Then dried algae were powdered to size 100 meshes. Chemical activation of the powdered precursor was accomplished with phosphoric acid (H3PO4). Powdered algae were impregnated with 30 wt% diluted H3PO4 in 3:1 (activating agent/ powdered algae) ratio and soak time of one hour. The achieved product was placed in an electric furnace (5 °C/min) for 3 h at 650 °C in a nitrogen flow rate of 94.4 mL/min. The samples were washed with HCl, hot water and distilled water respectively, to remove residual organic and mineral matters, and then dried in an oven at 105 °C for 2 h. At the final preparation step, activated carbon samples were crushed and sieved in mesh size 100 to obtain homogenous particle size [4], [5].

Experimental procedure

Batch adsorption experiments were performed in 100 mL Erlenmeyer, in different concentrations of the BB 41 solutions and requested amount of AAC were placed. The pH of the solution was adjusted by mixing with the appropriate amount of 0.1 M H2SO4 or NaOH. Then a specific amount of adsorbent was added to the Erlenmeyer flasks. The mixtures were continuously shaken in different times (agitation rate = 250 rpm) at room temperature. After adsorption experiments, immediately the suspensions were separated by centrifuge. Then concentration of the remaining BB 41 was analyzed with a UV–vis spectrophotometer by monitoring the intensity of the peaks at wavelength of 617 nm [6] and comparing the values with those in the calibration curve. The experiments were repeated three times in during the process. The adsorption rate R (%) and the equilibrium adsorption capacity qe (mg/g) were calculated using the Eqs. (1) and (2), respectively [7], [8], [9], [10].Where CO and Ce are the initial and the final concentration of BB 41 (mg/L), respectively, V is the volume of dye solution (L), and M is the dry weight of adsorbent used (g).
Subject areaEnvironmental Engineering
More specific subject areaWastewater technology
Type of dataTables, Figures and Images
How data was acquiredAlga powdered was used to preparation activated carbon.
All experiments were done using UV–vis spectrophotometer (model DR 5000, HACH). Characterization of structure AAC were determined by Philips X’Pert Pro instrument for X-ray Powder Diffraction (Netherlands) and Fourier transforms infrared (PerkinElmer, USA). The pH meter (Sense Ion 378, Hack model) and centrifuge (Eppendorf versatile 5810 model) were used.
The obtained data were analyzed using isotherm and kinetic models.
Data formatAnalyzed
Experimental factorsAll dyes samples were performed in contact time and various solution pH at room temperature.
Experimental featuresThe optimum contact time and pH were determined for adsorption of BB 41 from aqueous solutions by AAC.
Data source locationArdabil city, Ardabil province, Iran
Data accessibilityData are included in this article
Related research articleJ. Torres-Pérez, Y. Huang, P. Hadi, H. Mackey, G. McKay, Equilibrium, Kinetic and Optimization Studies for the Adsorption of Tartrazine in Water onto Activated Carbon from Pecan Nut Shells, Water, Air, and Soil Pollution. 229 (2018) 73 [1].
I.A.W. Tan, A.L. Ahmad, B.H. Hameed, Adsorption of basic dye on high-surface-area activated carbon prepared from coconut husk: Equilibrium, kinetic and thermodynamic studies, J. Hazard. Mater. 154 (2008) 337–346 [2].
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