Kemampuan Hydrochar dari Pelepah Kelapa Sawit Teraktivasi Asam Fosfat (H3PO4) sebagai Adsorben untuk Pemurnian Gliserol
Ability of Hydrochar from Palm Fronds Activated with Phosphoric Acid (H3po4) as Adsorbent for Glycerol Purification
Abstract
Crude glycerol is obtained as a by-product of the biodiesel production process in
an impure state and contains many impurities, so it needs to be purified. Glycerol
purification can be achieved by neutralization and adsorption processes using
activated carbon. Palm fronds contain high levels of cellulose lignin and can be
used as activated carbon. Hydrothermal carbonization is a rapid combustion
method in which biomass and water are introduced under high temperature and
pressure conditions. This study aims to evaluate the ability of hydrochar from
phosphoric acid-activated palm fronds and to analyze the effect of temperature,
time and water to biomass weight ratio on glycerol purification. The stages of this
research consisted of experimental design, preparation of raw materials,
hydrothermal carbonization process, determination of iodine absorbency, analysis
of hydrochar products, characterization of hydrochar texture and surface,
neutralization and adsorption procedures of crude glycerol, determination of
glycerol content by titrimetry and using GC-MS equipment, analysis of glycerol
purity and color analysis of glycerol. Hydrochar was prepared with process
temperature variations of 160 oC, 180 oC, 200 oC and 220 oC, process time of 20,
40, 60 and 80 minutes and biomass: water ratio of 1:6, 1:8, 1:10 and 1:12. The
adsorption process was carried out with adsorbent mass variation (m/v) of 1%, 2%,
3% and 4%. The results showed that the adsorbent variation at a process
temperature of 220 oC for 80 minutes with a biomass: water ratio of 1:10 had the
highest iodine number value of 980.68 mg/g. The highest glycerol content was
92.50% with 4% adsorbent mass variation. Color analysis of the best glycerol
showed a yellow parameter value that decreased from 70 to 2 on the scale at 4%
adsorbent mass variation.
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