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The optimum conditions for preparing activated carbon from OPF were found as follows: activation temperature of 850 °C, activation time of 1 h and KOH char ratio of 3.75:1.
The optimum conditions for preparing activated carbon from coconut husk were found as follows: activation temperature of 816 °C, activation time of 1 h and KOH char ratio of 3.9.
Treatment of nickel aluminum alloy with sodium hydroxide solution is one of the typical techniques for preparing activated Raney nickel.
The most ideal conditions for preparing activated carbon from Prosopis africana seed hulls (PASH-AC) were investigated using sodium acetate (CH3COONa) as an activating agent.
The optimum conditions for preparing activated carbon from EFB for adsorption of 2,4,6-TCP were found as follows: CO2 activation temperature of 814 °C, CO2 activation time of 1.9 h and IR of 2.8, which resulted in 168.89 mg/g of 2,4,6-TCP uptake and 17.96% of activated carbon yield.
The optimum conditions for preparing activated carbon from coconut husk for adsorption of 2,4,6-TCP were found as follow: CO2 activation temperature of 750 °C, CO2 activation time of 2.29 h and KOH char impregnation ratio of 2.91, which resulted in 191.73 mg/g of 2,4,6-TCP uptake and 20.16 % of activated carbon yield.
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Bamboo waste was used to prepare activated carbon by chemical activation using phosphoric acid (H3PO4) as chemical agent.
Coconut husk was used to prepare activated carbon using physiochemical activation method, consisted of potassium hydroxide (KOH) treatment and carbon dioxide (CO2) gasification.
Oil palm fibre was used to prepare activated carbon using physiochemical activation method which consisted of potassium hydroxide (KOH) treatment and carbon dioxide (CO2) gasification.
Oil palm fronds (OPF) were used to prepare activated carbon (PFAC) using physiochemical activation method, which consisted of potassium hydroxide (KOH) treatment and carbon dioxide gasification.
Palm oil fronds were used to prepare activated carbon using the physiochemical activation method, which consisted of potassium hydroxide (KOH) treatment and carbon dioxide (CO2) gasification.
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