壳聚糖和氧化铁吸附剂去除砷的析因设计

Marianela Batistelli, Julián Bultri, Mayra Hernandez Trespalacios, María Florencia Mangiameli, Lina Gribaudo, Sebastián Bellú, María Inés Frascaroli, Juan Carlos González
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摘要

砷具有剧毒,影响着世界许多地区的数百万人。这就是为什么必须发展经济和有效的技术来消除它。吸附技术是有吸引力的,因为高效和廉价的吸附剂可以使用。壳聚糖是一种丰富的、天然存在的、可生物降解的、低成本的生物聚合物,可以与金属氧化物结合以提高其可去除性。本工作旨在合成一种新型壳聚糖-磁铁矿基吸附剂,用于除砷。合成的吸附剂不存在孔洞,利用红外光谱(FT-IR)鉴定了壳聚糖的官能团和砷处理后吸附剂中As(V)的存在。用XRD对合成的磁铁矿进行了表征。应用中心复合设计模型表明,在pH为6.0时,0.22 g的吸附剂可去除27.6%的As(V)。动力学数据符合准一级和准二级模型,离子交换吸附和活化能为28.1 ~ 31.4 kJ mol−1。等温线符合Langmuir模型,表明具有良好的单层吸附和高亲和力。Dubinin Radushkevich法计算的吸附能为9.60 ~ 8.80 kJ mol−1,证实了离子交换介导的吸附机制。热力学参数分别为ΔG°(−21.7/−19.7 kJ mol−1)、ΔH°(16.7 kJ mol−1)和ΔS°(123.3 J mol−1 K−1)。
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Elimination of Arsenic Using Sorbents Derived from Chitosan and Iron Oxides, Applying Factorial Designs
Arsenic is highly toxic, affecting millions of people in many regions of the world. That is why developing economic and efficient technologies is imperative to eliminate it. Sorption techniques are attractive as efficient and inexpensive sorbents can be used. Chitosan is an abundant, naturally occurring, biodegradable, low-cost biopolymer that can be combined with metal oxide to enhance its removability. This work aimed to synthesize a new chitosan–magnetite-based sorbent for arsenic removal. The synthesized sorbent does not present pores, and when using FT-IR, functional groups of the chitosan and the presence of As(V) in the sorbent treated with arsenic were identified. The synthesized magnetite was characterized using XRD spectroscopy. Application of the central composite design model showed that 0.22 g of the sorbent at pH 6.0 could remove 27.6% of As(V). Kinetic data, fitted with the pseudo-first and -second order models, indicated an ion exchange sorption and activation energy of 28.1–31.4 kJ mol−1. The isotherms were fitted with the Langmuir model, indicating favorable monolayer adsorption with high affinity. The sorption energy calculated using Dubinin Radushkevich, 9.60–8.80 kJ mol−1, confirms a sorption mechanism mediated by ion exchange. The thermodynamic parameters of the process were ΔG° (−21.7/−19.7 kJ mol−1), ΔH°(16.7 kJ mol−1) and ΔS°(123.3 J mol−1 K−1).
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