粉煤灰和稻壳在蜡染废渣中作为金属铬吸附剂的研究

H. Oktavianty, S. Sunardi, K. Amri
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摘要

作为棕榈油厂锅炉废渣的飞灰含有63.4%的二氧化硅(sio2)。稻壳灰是一种具有特殊性能的大米废料,也含有约94-96%的二氧化硅(sio2)。这两种废物都含有二氧化硅,可用作吸附剂。本研究的目的是利用棕榈油厂的飞灰锅炉和稻壳灰生产吸附剂作为蜡染废料的吸附剂。研究设计采用全块式设计,设计2个因素,即稻壳灰分质量与粉煤灰锅炉的比值为3个水平,分别为A1(25%:75%)、A2(50%:50%)、A3(75%:25%)和HCl浓度因子为3个水平,即B1 (1M);B2 (2M) B3 (3M),重复2次。实验阶段包括锅炉粉煤灰预处理、稻壳灰预处理、吸附剂的合成与活化以及蜡染废水的吸附试验。此外,还进行了COD、TSS和Chromium的分析。结果表明,A3B2样品对COD、TSS和金属铬离子的吸附量最佳,分别为57.62 mg/L、1.43 mg/L和3.24 ppm,其中COD降低74%,TSS降低97.56%,金属铬离子降低80.43%。这是由于使用更多的稻壳灰和使用HCl溶液作为活化剂可以增加吸附剂上的二氧化硅活性基团,从而增加吸附剂的表面积,其中A3B2样品的表面积为118.24 m2 /g。这是一篇基于CC-BY-SA许可的开放获取文章。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Utilization of Fly Ash and Rice Husk as Chromium Metal Adsorbent in Batik Waste
Fly ash boiler as a waste of palm oil mill containing 63.4% of silica (SiO 2 ). Rice husk ash is a waste material from rice that has special properties, also containing about 94-96% of silica (SiO 2 ). Both of these wastes contain silica which can be used as an adsorbent. This study aims to produce adsorbents from fly ash boilers for palm oil mills and rice husk ash as adsorbents for batik waste. The research design used was Complete Block Design with 2 factors, namely the ratio of rice husk ash mass to fly ash boiler with 3 levels, namely A1 (25%:75%), A2 (50%:50%), A3 (75%:25%), and the concentration factor of HCl with 3 levels, namely B1 (1M); B2 (2M), B3 (3M), which is done 2 times repetition. The experimental stages include boiler fly ash pretreatment, rice husk ash pretreatment, synthesis and activation of adsorbents and adsorption tests on batik wastewater. Furthermore, analysis of COD, TSS and Chromium was carried out. The results showed that the A3B2 sample provided optimal adsorption capacity for the analysis of COD, TSS and Chromium metal with values of 57.62 mg/L, 1.43 mg/L and 3.24 ppm, respectively, where there was a decrease in COD of 74%, a decrease in TSS of 97.56% and a decrease in Chromium metal ion of 80.43%. This is due to the use of more rice husk ash with the use of HCl solution as an activator can increase the silica active group on the adsorbent thereby increasing the surface area of the adsorbent, where the surface area of the A3B2 sample is 118.24 m 2 /g. This is an open access article under the CC–BY-SA license.
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