Olive stones have been carbonized under a flow of nitogen in the temperature range from 700 to 900Β°C and activated in a CO2 flow in the range from 675 to 875Β°C. ZnCI, was used in some of the activation processes. The adsoptive characteristics of the carbonized and activated samples have been determ
Preparation and Characterization of Active Carbon Adsorbents for Wastewater Treatment from Elutrilithe
β Scribed by Xiaohu Deng; Yinghong Yue; Zi Gao
- Publisher
- Elsevier Science
- Year
- 1997
- Tongue
- English
- Weight
- 100 KB
- Volume
- 192
- Category
- Article
- ISSN
- 0021-9797
No coin nor oath required. For personal study only.
β¦ Synopsis
2. EXPERIMENTAL
Active carbon adsorbents were prepared from natural elutrilithe by chemical activation with K 2 CO 3 . The effect of pyrolysis temper-
2.1. Preparation of Adsorbent
ature and time and K 2 CO 3 /elutrilithe ratio on the surface area, porosity, and ash content of the adsorbents was studied. Various The black elutrilithe was from Shanxi province, China. It prior and post treatments have been tried to improve the quality contained 29.1% C, 36.0% SiO 2 , 18.2% Al 2 O 3 , and 16.7% of the adsorbents. An ideal active carbon adsorbent with a BET
Ca, Mg, Fe, Mn, Cr, Ni, Ti, and Na oxides. The BET surface surface area of 1236 m 2 /g and a total pore volume of 0.679 cm 3 / g has been obtained. The adsorbent is hydrophobic in nature and area of the original elutrilithe was 5.7 m 2 /g. exhibits large adsorption capacities for various phenolic com-Elutrilithe with a particle size smaller than 100 mesh, 3 pounds from aqueous solutions.
π SIMILAR VOLUMES
Preparation of activated carbons from eucalyptus kraft lignin has been investigated. A pretreatment method has been established to avoid partial fusion and swelling in the carbonization stage. Carbonization has been studied at different temperatures and the structure of the microporous chars has bee
Powdered activated carbon has been prepared from lignitic coal of Lakhra (Pakistan) by a chemical activation method using ZnCl, as an activating agent. Different process variables have been established after a series of experiments and an impregnation ratio of 1: 2, an activation temperature of 650Β°
## Abstract The polymeric precursor polystyrene sulphonate beads were used to produce activated carbon spheres (ACSs). ACSs were prepared by carbonization of polymeric precursor at 800Β°C followed by activation of resultant char with steam and carbon dioxide activation processes. The resulting ACSs
Graft copolymerization of acrylamide onto coconut husk (CH), initiated by the ferrous ammonium sulfate/H 2 O 2 redox initiator system, was studied. To determine the optimum conditions of grafting, the effect of the concentrations of ferrous ammonium sulfate, the monomer, and H 2 O 2 and the time and