2 research outputs found
Coal bottom ash for palm oil mill effluent (POME) decolourization
The utilization of coal bottom ash (CBA) from thermal power plant for palm oil mill effluent (POME) decolourization was studied. CBA is prepared using chemical activation with hydrochloric acid (HCl) to increase adsorption performance. Physico-chemical characterizations of CBA-HCl was analysed using BET for surface area, FTIR for its surface chemistry, SEM for morphology and EDX for elemental analysis. The effectiveness of CBA-HCl for colour adsorption of POME was investigated as a function of pH, initial concentration, adsorbent dosage and contact time by batch experiments. Adsorption increased with increasing contact time and the equilibrium states could be achieved in range of 18 to 24 hr. Results showed that CBA-HCl perform with maximum colour removal of 93% at pH 6 with 10% (w/v) adsorbent dosage in 24 hr. It was shown that the isotherm for adsorption of colour from POME on CBA-HCl was well fitted by Freundlich equation (correlation coefficient, R2 = 0.9636). Based on the results, CBA showed potential adsorbent candidate for POME decolourization
Utilization and optimization of industrial bottom ash for palm oil mill effluent decolourization
The increasing demand of crude palm oil (CPO) has resulted in the enormous increases in palm oil
mills operation in Malaysia and hence the palm oil mill effluent (POME) discharges. Thus, existing
treatment facilities have difficulties to comply the discharge limit for this excess POME from the
running plants. In this case, colour of POME was one of the major concerns as it will be
incorporated in the current regulation. Various adsorbents (i.e POMBA, treated POMBA, CBA, treated
PKS) had been screened for POME decolourization. Coal bottom ash (CBA) showed highest
colour removal percentage among others and hence selected for the consequence
investigations. The raw CBA were then chemically (ACBA) and physically treated
(PCBA) for comparison study. Furthermore, response surface methodology (RSM) was used
for optimization. As results, the optimum parameters of ACBA and PCBA for POME colour
adsorption proposed the followings: 14.20 hr and 15.37 hr contact time, 13.16 g and 13.84 g
adsorbent dosage, 27.97% and 57.52% POME concentration, pH 6.24 and pH 6.04, respectively. Both
predicted and experimental percentage removal of POME colour for ACBA and PCBA were
significantly correlated with the R² values for ACBA and PCBA were 0.9793 and
0.9755, respectively. Physico-chemical characterizations of both treated CBA were
performed using BET for surface area, FTIR for its surface chemistry, SEM for morphology and
EDX for elemental analysis. It was shown that the isotherms for adsorption of colour from POME onto
treated CBA were well fitted by Freundlich model. Furthermore, pseudo-second order was identified
to be governing mechanism for both treated CBA. Other pollutants i.e COD, BOD3 and NH3-N removal
are also evaluated. It was found that percentage removal of COD, BOD3 and NH3-N using
ACBA were 61.33%, 58.33% and 61.43%, respectively. Meanwhile, percentage removal of COD,
BOD3 and NH3-N using PCBA were 38.39%, 33.33% and 31.10%, respectively. Upon these findings, CBA
has potential not only in
POME decolourization also in POME treatment as adsorbent