利用稻壳快速热解产生的副产品活性炭去除重金属的优化方法

Peter Wilberforce Olupot , Joel Wakatuntu , Medard Turyasingura , Joseph Jjagwe , Emmanuel Menya , Mackay Okure
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引用次数: 0

摘要

要实现循环经济,就必须最大限度地利用现有资源,并且在工艺循环后不产生可回收的废物。在快速热解生物质以生产生物油用作能源的过程中,会产生生物炭形式的固体残留物。在这项研究中,稻壳热解榨油后的残炭在 800 °C 的温度下用蒸汽活化,生成活性炭(AC)。对所生成的活性炭进行了表征和评估,以去除受污染水体中的重金属。采用盒式响应面设计法对去除水中的 Cu2+、Co2+、Zn2+、Pb2+ 和 Ni2+ 进行了优化。工艺条件为:吸附剂剂量(2-12 克/升)、接触时间(30-180 分钟)和温度(25-70 °C)。AC 的表征显示,其表面积和孔体积分别为 407 m2g-1 和 0.22 m3g-1。在所有建立的模型中,吸附剂剂量和接触时间是最重要的条件。线性模型最适合 Cu2+ 的去除,而二次模型最适合 Co2+、Zn2+、Pb2+ 和 Ni 2+ 的去除。重金属去除率随着吸附剂剂量、接触时间和温度的增加而提高。最佳处理参数为:吸附剂剂量(11.90 克/升)、接触时间(172.5 分钟)、温度(54 °C),对 Cu2+、Co2+、Zn2+、Pb2+ 和 Ni2+ 的去除率分别为 98.2%、84.1%、75.3%、98.1% 和 75.7%。吸附数据最符合 Langmuir 等温线和伪二阶模型。这些结果证实了热解石油残炭中的 AC 可用于吸附重金属。在水处理中使用来自残炭的 AC 有助于实现循环经济。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Optimization of heavy metal removal by activated carbon obtained as a co-product from fast pyrolysis of rice husks

Optimization of heavy metal removal by activated carbon obtained as a co-product from fast pyrolysis of rice husks

The realization of a circular economy calls for maximum utilization of existing resources with no recoverable waste after the process cycle. During fast pyrolysis of biomass to produce bio-oil for energy purposes, solid residues in form of bio-char are generated. In this study, residual char after pyrolytic-oil extraction from rice husks was activated using steam at 800 °C to produce activated carbon (AC). The formed AC was characterized and evaluated for removal of heavy metals from contaminated water. Box Behnken Design of Response Surface Methodology was used to optimize the removal of Cu2+, Co2+, Zn2+, Pb2+, and Ni2+ from water. The process conditions were: adsorbent dose (2–12 g/L), contact time (30–180 min) and temperature (25–70 °C). Characterization of AC revealed surface area and pore volume of 407 m2g-1 and 0.22 m3g-1, respectively. For all developed models, adsorbent dose, and contact time were the most significant terms. A linear model best fits Cu2+ remediation, while quadratic models best-fit removals of Co2+, Zn2+, Pb2+, and Ni 2+. Heavy metal removal efficiency increased with increasing adsorbent dose, contact time and temperature. Optimum treatment parameters were: adsorbent dose (11.90 g/L), contact time (172.5 min), temperature (54 °C) with removal efficiencies of 98.2%, 84.1%, 75.3%, 98.1%, 75.7% for Cu2+, Co2+, Zn2+, Pb2+, and Ni2+, respectively. Adsorption data best fitted Langmuir isotherm and pseudo second order models. These results confirm the applicability of AC from pyrolytic-oil residual char for adsorption of heavy metals. Use of AC from residual char in water treatment contributes to circular economy.

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