ADSORPTION OF LA(III) USING ALGINATE MAGNETITE COMPOSITES WITH BORIC ACID CROSSLINKER
The increase in demand for rare earth metals (Rare Earth Metals) continues to increase every year, rare earth metals have similar physical and chemical properties, making it difficult to separate them. The need for Rare Earth Metals (REE) continues to increase every year. Lanthanum is one of the...
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Format: | Final Project |
Language: | Indonesia |
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Online Access: | https://digilib.itb.ac.id/gdl/view/71595 |
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Institution: | Institut Teknologi Bandung |
Language: | Indonesia |
Summary: | The increase in demand for rare earth metals (Rare Earth Metals) continues to increase
every year, rare earth metals have similar physical and chemical properties, making it
difficult to separate them. The need for Rare Earth Metals (REE) continues to increase
every year. Lanthanum is one of the REE used in hybrid car batteries, flint in cigarette
lighters, substance to improve optical properties and alkali resistance of glass, as well as
catalysts in oil refining processes. The increasing need for and use of rare earth is
accompanied by an increase in the potential for pollution of rare earth ions in the
environment. Adsorption is one of the most popular separation techniques because it is
easier and cheaper. In this study, a Magnetite Alginate composite with a Boric Acid
crosslinker (MAB) was prepared for the adsorption of La3+ ions. In this study, the Magnetite
Alginate composite with Boric Acid (MAB) crosslinker was used as an adsorbent. The
FTIR spectrum of the adsorbent shows the absorption of Fe-O bonds at wave number 588
cm#$. The typical absorption of alginate is found at wave number 3380 cm#$, which is the
vibration of the O-H bond, 1605 cm#$ for C=O asymmetry vibration, 1394 cm#$ for C=O
symmetry vibration, and 1030 cm#$ for C-O-C vibration. The adsorbent diffractogram
showed peaks corresponding to the magnetite JCPDS, which identified the presence of
magnetite in the MAB composite. Adsorption of La (III) ions using the batch method
reached its optimum conditions at pH 4 and contact time of 4 hours with the adsorbent mass
of 0.05 gram. The adsorption process of La (III) ions followed the Langmuir isotherm
model with a maximum adsorption capacity (qm) of 30.87 mg g-1 and a pseudo-secondorder
kinetic model. Adsorption of La (III) using MAB was an endothermic process, with
a value of ?H = 59 kJ/mol, accompanied by an increase in system entropy and took place
spontaneously |
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