Batch Study of Cadmium Biosorption by Carbon Dioxide Enriched <i>Aphanothece</i> sp. Dried Biomass

The conventional method for cadmium removal in aqueous solutions (1&#8722;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. Biosorben...

Full description

Bibliographic Details
Main Authors: Awalina Satya, Ardiyan Harimawan, Gadis Sri Haryani, Md. Abu Hasan Johir, Saravanamuthu Vigneswaran, Huu Hao Ngo, Tjandra Setiadi
Format: Article
Language:English
Published: MDPI AG 2020-01-01
Series:Water
Subjects:
Online Access:https://www.mdpi.com/2073-4441/12/1/264
Description
Summary:The conventional method for cadmium removal in aqueous solutions (1&#8722;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 <i>Aphanothece</i> sp. cultivars (A0, A8, and A15) were used to eliminate cadmium (Cd<sup>2+</sup>) ions in aqueous solution (1&#8722;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&#8722;6000 lux for 14 d of cultivation. Produced dried biosorbents had Brunauer&#8722;Emmet&#8722;Teller (BET) surface area ranges of 0.571&#8722;1.846 m<sup>2</sup>/g. Biosorption of Cd<sup>2+</sup> was pH and concentration dependent. Sorption was spontaneous (&#916;G = &#8722;8.39 to &#8722;10.88 kJ/mol), exothermic (&#916;H = &#8722;41.85 to &#8722;49.16 kJ/mol), and decreased randomness (&#916;S = &#8722;0.102 to &#8722;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 (k<sub>2</sub> = 2.79 &#215; 10<sup>&#8722;2</sup>, 3.96 &#215; 10<sup>&#8722;2</sup>, and 4.54 &#215; 10<sup>&#8722;2</sup> g/mg.min). The dried biosorbents of A0, A8, and A15, after modeling with the Langmuir and Dubinin&#8722;Radushkevich isotherm models, indicated that cadmium binding occurred through chemisorption (<i>q<sub>max</sub></i><sub>, D-R</sub> = 9.74 &#215; 10<sup>&#8722;4</sup>, 4.79 &#215; 10<sup>&#8722;3</sup>, and 9.12 &#215; 10<sup>&#8722;3</sup> mol/g and mean free energy of 8.45, 11.18, and 11.18 kJ/mol) on the monolayer and homogenous surface (<i>q<sub>max</sub></i><sub>, Langmuir</sub> 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 Cd<sup>2+</sup> (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&#8722;desorption using 1 M HCl as the desorbing eluent. These biosorbents can be a potent and eco-friendly material for treating aqueous wastewater.
ISSN:2073-4441