Abstract

The conventional method for cadmium removal in aqueous solutions (1–100 mg/L) is ineffective and inefficient. Therefore, a batch biosorption reactor using a local freshwater microalga (originating from an urban lake, namely, Situ Rawa Kalong-Depok) as dried biosorbent was tested. Biosorbent made from three kinds of cyanobacterium Aphanothece sp. cultivars (A0, A8, and A15) were used to eliminate cadmium (Cd2+) ions in aqueous solution (1–7 mg/L). The biosorbents were harvested from a photobioreactor system enriched with carbon dioxide gas of 0.04% (atmospheric), 8%, and 15% under continuous light illumination of about 5700–6000 lux for 14 d of cultivation. Produced dried biosorbents had Brunauer–Emmet–Teller (BET) surface area ranges of 0.571–1.846 m2/g. Biosorption of Cd2+ was pH and concentration dependent. Sorption was spontaneous (ΔG = −8.39 to −10.88 kJ/mol), exothermic (ΔH = −41.85 to −49.16 kJ/mol), and decreased randomness (ΔS = −0.102 to −0.126 kJ/mol. K) on the interface between solid and liquid phases when the process was completed. The kinetic sorption data fitted best to the pseudo-second-order model (k2 = 2.79 × 10−2, 3.96 × 10−2, and 4.54 × 10−2 g/mg.min). The dried biosorbents of A0, A8, and A15, after modeling with the Langmuir and Dubinin–Radushkevich isotherm models, indicated that cadmium binding occurred through chemisorption (qmax, D-R = 9.74 × 10−4, 4.79 × 10−3, and 9.12 × 10−3 mol/g and mean free energy of 8.45, 11.18, and 11.18 kJ/mol) on the monolayer and homogenous surface (qmax, Langmuir of 12.24, 36.90, and 60.24 mg/g). In addition, the results of SEM, EDX, and FTIR showed that there were at least nine functional groups that interacted with Cd2+ (led to bond formation) after biosorption through cation exchange mechanisms, and morphologically the surfaces changed after biosorption. Biosorbent A15 indicated the best resilient features over three cycles of sorption–desorption using 1 M HCl as the desorbing eluent. These biosorbents can be a potent and eco-friendly material for treating aqueous wastewater.

Highlights

  • Cadmium (Cd) is one of the extreme acute toxic heavy metals and may present in industrial wastewater discharged by industries involved in dyes, electroplating, Ni–Cd batteries, and others.Water 2020, 12, 264; doi:10.3390/w12010264 www.mdpi.com/journal/waterPotential hazards will arise when bioaccumulation of Cd occurs in the aquatic food chain and is transferred into a human as the top consumer

  • Biosorption is sorption involving biomaterial as a sorbent, which is an alternative and cost-effective process for removing heavy metals ranging from 1–100 mg/L in wastewater [4]

  • This observed surface morphology was attributed to surface precipitation of Cd2+, which was to occur in Parachlorella sp. dried biosorbent when used to remove Cd from an aqueous solution reported to occur in Parachlorella sp. dried biosorbent when used to remove Cd from an aqueous containing 60 mg/L of Cd [16]

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Summary

Introduction

Cadmium (Cd) is one of the extreme acute toxic heavy metals and may present in industrial wastewater discharged by industries involved in dyes, electroplating, Ni–Cd batteries, and others.Water 2020, 12, 264; doi:10.3390/w12010264 www.mdpi.com/journal/waterPotential hazards will arise when bioaccumulation of Cd occurs in the aquatic food chain and is transferred into a human as the top consumer. Cadmium (Cd) is one of the extreme acute toxic heavy metals and may present in industrial wastewater discharged by industries involved in dyes, electroplating, Ni–Cd batteries, and others. Biosorption is sorption involving biomaterial as a sorbent, which is an alternative and cost-effective process for removing heavy metals ranging from 1–100 mg/L in wastewater [4]. Biosorption using this range (1−100 mg/L) of concentration is still lacking. A recent study using wheat straw biochar and acid-treated biochar made from agricultural solid waste reported adsorption capacities of the cadmium ion (Cd2+ ) of 30.65 and 74.63 mg/g, respectively [1]. Activated carbon derived from teak sawdust hydrochars (prepared through hydrothermal carbonization and activation using K2 CO3 or ZnCl2 ) resulted in maximum sorption capacities of 614, 208, and 182 mg/g of methylene blue, Cd2+ , and Cu2+ (concentration range of 50–900 mg/L), respectively [5]

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