Overview
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Key numbers
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- H2 SO4 charring modification due to cross-linking reaction of betel nut cellulose, thereby creating suitable complexation sites for
- BaCrO4 precipitate (WHO, 0.05 mg/L) using charred BNW (CBNW). The negative value of ΔG◦ evaluated for all the temperatures
- notably reduced Cr(VI) uptake capacity of CBNW. More than 98% of adsorbed Cr(VI)
- est concentration of Cr(VI) levels as 0.05 mg/L in drinking water (9, biosorption research for Cr(VI) removal is carried out in batch mode
- barium chloride solution. g/L by using 0.56 mmol/L (29.54 mg/L) of Cr(VI) solution. The samples
- mg/L) was prepared by dissolving 1.415 g of K2 Cr2 O7 in a 500 mL 𝑊
- range of 0 to 80◦ using an X-ray diffraction spectrometer (Rigaku Co., of Cr(VI) solution (150 mg/L i.e., 2.89 mmol/L) at pH 2 and agitated
- the stable pink color complex when 1,5 diphenyl carbazide was mixed pared to HCl and NaCl. NaOH desorbed 99.72% whereas it was only
- 34.21%) even using 5M HCl, thus further optimization was carried out
- ( 𝑛 2) suitable for the adsorption reaction if it is amorphous compared to crys-
- tion reactions. FTIR analysis allows for the observation of various active adsorption as shown in Fig. 3(b). This can be reasonably attributable
- CBNW also provides suitable moiety for complexation (Scheme 1). With
- CBNW as shown in Fig. 3(a). Cr(VI) loaded CBNW shows intense peaks not suitable. So, the effect of other biosorption parameters was in-
- 0.97% of chromium in the sample of Cr(VI) loaded CBNW together with pens quickly, and the adsorption equilibrium is reached within 45 to
- 64.75% of carbon and 34.28% of oxygen provides direct evidence that 60 minutes. The fast uptake of Cr(VI) may be due to quick exposure of
- the biosorbent (34). Fig. 4 shows the % sequestration of Cr(VI) onto models. The exact equation of pseudo-first-order, pseudo-second-order,
- biosorption percentage of Cr(VI) ions (less than 50% even at optimum Pseudo-first-order (PFO) model
- ter modification or charring (>97%). The % sequestration of Cr(VI) was 𝑞𝑡 = 𝑞𝑒 1 − 𝑒−𝑘1 𝑡 (10)
- all three biosorbents. The high sequestration % of Cr(VI) onto CBNW 2.303
-
- Although the non-modified BNW sequestered around 50% of Cr(VI)
- H2 CrO4 which was hardly adsorbed onto CBNW reasonably causing the and Fig. 5(d). The correlation regression coefficient for PFO ranges
- = 20 mL, Cr(VI) concentration = 0.45 mmol/L, shaking time = 24 hrs, and
- the tested pHs as shown in Table 1. The Cr(VI) uptake capacity de- by equations (15) and (16) (38, 39).
- (d) intra-particle diffusion (IPD) plots. Condition: solid liquid ratio = 1 g/L, pH = 2, Cr(VI) ion = 0.45 mmol/L, shaking time = 24 hrs, and temperature = 298 ±
- equations can be used to express the nonlinear and linear forms of the are listed in Table 2. The experimental Cr(VI) adsorption capacity is in
- Table 1. Kinetics parameters evaluated for the adsorption of Cr(VI) using CBNW at different pH.
- Table 2. Investigated isotherm parameters for the adsorption of Cr(VI) using CBNW.
- Table 3. Comparisons of maximum adsorption capacities of CBNW for Cr(VI) investigated in this study with other biosorbents reported in the literature.
- Table 4. Estimated thermodynamic parameters for the adsorption of Cr(VI) using CBNW.
- tively. The evaluated thermodynamic parameters are listed in Table 4.
- tration. Condition: volume of solution = 10 mL, Cr(VI) concentration = 0.56
- set by WHO (0.05 mg/L) using only 0.6 g/L of CBNW at pH 2 whereas also other co-existing ions such as zinc, sulfate, chloride, phosphate,
- Fig. 9. Effect of interfering ions for the removal of Cr(VI) from water using CBNW. Condition: interfering ions = 0 to 200 mg/L, weight of CBNW = 40 mg, volume
- of solution = 20 mL, pH = 2, Cr(VI) concentration = 0.015 mmol/L, shaking time = 24 hrs, and temperature = 298 ± 2K.
- cationic species such as zinc and sodium ions are negligible because 3 mmol/L of BaCl2 solutions. The result shows that only 68.34% of
- the biosorption process. Monovalent nitrate anions caused moderate 87.76% at 0.5 mmol/L whereas the recovery reached 98.17% by using
- concentration, with 1M NaOH solution achieving over 96% desorption. of BaCrO4 is high as compared to BaCl2 (61).
- CBNW. Condition: Cr(VI) concentration = 0.083 mmol/L, weight of CBNW =
- of this figure that the CBNW removed greater than 97% of Cr(VI) even to the existence of reductive functional groups on the CBNW surface, a
- increasing repeated cycles and reached 87% at the 5th cycle. The reason boxyl or hydroxyl groups. Therefore, the biosorbent investigated in this
- However, the adsorption of Cr(VI) is higher than 87% even after the
- 5th cycle whereas desorption was higher than 95% in all the cycles.
Methods (brief)
- chu. The waste biomass of A. catechu (betel nut) was collected from the
- barium chloride solution. g/L by using 0.56 mmol/L (29.54 mg/L) of Cr(VI) solution. The samples
-
- Materials and method shaker. After stirring at pre-determined intervals of time, the samples
- the samples (SEM, JEOL model JSM 5900). X-ray diffractograms were 2.3.2. Desorption experiment of Cr(VI) from Cr(VI)-CBNW
- in the samples before and after sorption were determined by an atomic as Cr(VI) loaded CBNW and abbreviated as Cr(VI)-CBNW henceforth.
- glass column having a 0.8 mm internal diameter. For this, the column Fig. 1. Analysis of various functional groups in the sample of BNW, CBNW and
- a peristaltic pump and effluent samples were collected using the frac- changes/modifications to other active groups that may be involved in
- To investigate the reproducibility and validation of collected data, linking condensation reaction of betel nut cellulose with the aid of
- 0.97% of chromium in the sample of Cr(VI) loaded CBNW together with pens quickly, and the adsorption equilibrium is reached within 45 to
- of organic compounds from the CBNW (modified sample) was negligi- 𝑞 𝑡 𝑘2 𝑞 𝑒 2 𝑞 𝑒
- Zheng, Effective removal of Cr(VI) using 𝛽-cyclodextrin–chitosan modified biochars metals from wastewater, Bioresour. Technol. 98 (2007) 2243–2257.
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