## Abstract **BACKGROUND:** The removal of cationic dyes from wastewater is of great importance. Three zeolites synthesized from coal fly ashes (ZFAs) were investigated as adsorbents to remove methylene blue (MB), a cationic dye, from aqueous solutions. Experiments were conducted using the batch ad
Zeolite synthesis from coal fly ash for the removal of lead ions from aqueous solution
β Scribed by Jason Scott; Deyan Guang; Kornrat Naeramitmarnsuk; Mallika Thabuot; Rose Amal
- Publisher
- Wiley (John Wiley & Sons)
- Year
- 2001
- Tongue
- English
- Weight
- 142 KB
- Volume
- 77
- Category
- Article
- ISSN
- 0268-2575
- DOI
- 10.1002/jctb.521
No coin nor oath required. For personal study only.
β¦ Synopsis
Abstract
Fly ash samples from the Bayswater and Eraring power plants, located in New South Wales, Australia, were used in a preliminary study on zeolite synthesis by hydrothermal treatment with sodium hydroxide under various conditions. The treated fly ash was tested for the ability to remove lead ions from aqueous solution. Both fly ashes were partially converted to zeolite. The zeolites formed under the experimental conditions were zeolite NaβP1 and sodalite octahydrate for the Bayswater ash and phillipsite, zeolite X, zeolite NaβP1 and sodalite octahydrate for the Eraring ash. The type of zeolite formed was dependent on the treatment time and sodium hydroxide concentration. In the case of the Bayswater ash, zeolite NaβP1 was formed by treatment with 4βmolβ dm^β3^ NaOH for 48βh while treatment with 5βmolβ dm^β3^ NaOH for 96βh produced sodalite octahydrate at the expense of zeolite NaβP1. In the case of the Eraring ash, phillipsite was formed following treatment with 3βmolβ dm^β3^ NaOH, zeolite X and zeolite NaβP1 were formed following treatment with 4βmolβ dm^β3^ NaOH and sodalite octahydrate was formed following treatment with 5βmolβ dm^β3^ NaOH. A maximum cation exchange capacity of βΌ400βmeq/100βg was achieved by both treated ash samples. Treatment of a solution with a lead ion concentration of 120βppm using 0.5βg of both treated ash samples (S/L ratioβ=β0.25βg/100βcm^3^) achieved complete removal in 5βmin, whereas treatment with 0.1βg of each material (S/L ratioβ=β0.05βg/100βcm^3^) achieved complete lead ion removal after 24βh.
Β© 2001 Society of Chemical Industry
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