scholarly journals Adsorption kinetics of colour removal from palm oil mill effluent using wastewater sludge carbon in column studies

Heliyon ◽  
2019 ◽  
Vol 5 (10) ◽  
pp. e02439 ◽  
Author(s):  
S.R.M. Kutty ◽  
N.M.Y. Almahbashi ◽  
A.A.M. Nazrin ◽  
M.A. Malek ◽  
A. Noor ◽  
...  
2012 ◽  
Vol 512-515 ◽  
pp. 1515-1519 ◽  
Author(s):  
Nipon Pisutpaisal ◽  
Saowaluck Hoasagul

Kinetics of mesophilic biohydrogen production from ozone-pretreated palm oil mill effluent (POME) using C. butyricum and C. acetobutylicum co-culture was investigated. All experiments were setup in 0.5-L batch reactors under mesophilic condition (37°C), pH 6, and POME concentration of 5,000-30,000 mg COD L-1. At the concentration of 15,000 mg COD L-1, maximum hydrogen production yield for non-ozone pretreated POME and ozone pretreated POME were 318 and 122 mL g-1 CODremoved, respectively. Acetic and butyric acids were dominant fermentation products in liquid phase. Ozone-pretreatment of POME showed no significant improvement on the hydrogen production by the co-culture.


2021 ◽  
Author(s):  
Arezoo Fereidonian Dashti ◽  
Hamidi Abdul Aziz ◽  
Mohd Nordin Adlan ◽  
Ali Huddin Ibrahim

Abstract Palm oil wastewater treatment was investigated via a filtration process using raw and calcinated limestone. The column studies were conducted using different limestone sizes (4, 12, and 20 mm), calcination temperature (800°C and 600°C) and various filtration rates (20, 60, and 100 mL/min) and a comparison was made with raw limestone under similar conditions. The response surface methodology using central composite design was employed to optimize the process parameter. The experimental data was analyzed via the analysis of variance to identify the interaction between the parameters and the dependent parameter. The results showed that the colour removal increased with an increase in temperature (800 ºC) for filtration rate of 20 mL/min, the retention time of 317 min and the smaller size (4 mm) of limestone and decreased with an increase in the filtration rate and size of raw limestone. Based on the achieved results, the optimum condition for colour removal was at temperature 800°C (61%), 600 oC (56%) and raw limestone (49%) respectively with the same experimental setup (flow rate of 20 mL/min and limestone size of 4 mm). According to the statistical analysis, quadratic models demonstrated significant values (0.000) for the response (colour). Freundlich and Langmuir isotherms also provided good correlation coefficient for the colour removal. The data conforms to the Langmuir isotherm with the best fit model (R2 = 0.7).


Author(s):  
Arezoo Fereidonian Dashti ◽  
Hamidi Abdul Aziz ◽  
Mohd Nordin Adlan ◽  
Ali Huddin Ibrahim

2016 ◽  
Vol 78 (5-6) ◽  
Author(s):  
Hathaikarn Thongpan ◽  
Rachadaporn Thongnan ◽  
Nirattisai Rakmak ◽  
Chairat Siripatana

In this work, both models for batch and continuous anaerobic digestion of palm oil mill effluent were developed based on Monod’s kinetics. Then the authors attempt to understand the effect of wastewater-sludge (WW:S) ratio on the biogas production efficiency in batch digesters. The experiments were carried out at a controlled temperature of 35±0.5 °C. Two series of the experiment were conducted. In the first series, the wastewater-sludge ratios covered 1:1 (add sodium bi-carbonate), 1:1, 1:2 and 2:1. It was found that the ratio of 1:2 gave the highest biogas producing efficiency followed by the ratio 1:1 (add sodium bi-carbonate). At 1:1 ratio, sodium bi-carbonate addition was required to start anaerobic digestion at a workable pH range whereas at 1:2 ratio the initial pH is in the workable range without the need of its addition. However, at the ratio of 2:1 the starting pH was too low to adjust pH economically by adding sodium bi-carbonate. The second series was to confine experiments to a narrower ratio range, namely: 1:1 (add sodium bi-carbonate), 1:1.5, 1:2, 1:2.5. In both sets of experiment, the ratio 1:2 gave the best biogas production potential of 76.62 and 78.52 ml of biogas/g COD removed respectively. In all treatments, the process was able to remove more than 80% of wastewater initial COD. The modified Gompertz equation was used to estimate the maximum specific biogas production rate (MBPR or Rm/S0). It was also found that the ratio of 1:2 gave the best MBPR in both experimental series (26.87 ml biogas/g COD-day). A modified Monod-type Model was also developed to describe the microbial growth, substrate consumption and biogas production in continuous operation. In general, sludge recycle provided active biomass which can use the substrate in the wastewater instantly without significant lag phase or delay. Furthermore, continuous-flow model developed, with parameters estimated from batch experiments, predicted the experimental kinetics of the actual continuous experiments satisfactory.  


Sign in / Sign up

Export Citation Format

Share Document