过氧木质素的碳吸附剂

V. Halysh, I. Deykun, I. Trus, V. Radovenchyk, M. Gomelya
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引用次数: 0

摘要

过渡到非传统类型的植物原料生产纤维素和基于它的材料对世界各地的科学家和工业界来说越来越重要。为此,最有利的办法是利用农工综合体中秸秆或秸秆形式的废物。在非木质纤维素原料的有机溶剂脱木质素过程中,形成了高可溶性木质素含量的废溶液,这是一种非常环保的方法。从生态学的角度来看,创造一种复杂的、几乎没有废物的技术来将木质素加工成目标产品是很重要的。研究了用菜籽秸秆有机溶剂脱木质素后蒸煮废液中沉淀的木质素制备吸附剂,以脱除水中的危险合成染料的可能性。在蒸煮结束时,纤维素产品通过过滤从废溶液中分离出来。废溶液收集在一个单独的容器中,用5体积的水处理,导致木质素冷凝。从蒸煮液中分离浓缩木质素,5500 rpm离心10 min,蒸馏水洗涤,离心脱水,80℃干燥至恒定含水率7-8%。然后用20%的正磷酸溶液或20%的氢氧化钠溶液处理木质素,然后在马弗炉中炭化。木质素碳化后,平均孔径减小至2.191 ~ 4.421 nm,氢氧化钠处理后孔径增大1.8倍,正磷酸处理后孔径增大2.0倍,提高了材料的吸附能力。水溶液的pH值对污染物吸附过程的影响是决定性的。含氧官能团在酸性环境下使吸附材料表面带正电荷,从而与同样带正电荷的染料阳离子形成静电斥力。当pH值增加到微碱性时,官能团发生解离,因此吸附剂表面获得负电荷,这导致与染料产生静电吸引力。从2.0到6.0,阳离子染料的吸收率随pH值的增加而增加,pH值的进一步增加不影响工艺效率。木质素的碳化导致吸附剂孔隙率的增加,因此需要更多的时间才能达到完全的吸附平衡。在前80分钟,观察到亚甲基蓝的最大吸收率,接触180分钟后,达到完全吸附平衡。利用Langmuir方程估计了染料在吸附剂上的吸附等温线,确定了木质素表面的空吸附位是均匀的,染料吸附是单层的。建立了用伪二阶模型描述吸附动力学的模型。开发一种有效的过氧木质素作为碳吸附剂的方法,可以创造资源节约型技术。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Carbon sorbents from peracetic lignin
The transition to non-traditional types of plant raw materials for the production of cellulose and materials based on it is becoming more and more relevant for for scientists and industry around the world. The most expedient for this is the use of waste from the agro-industrial complex in the form of straw or stalks. During the delignification of non-wood lignocellulosic raw materials by the organosolv method, which is quite environmentally friendly, spent solutions with a high soluble lignin content are formed. From an ecological point of view, it is important to create a complex, practically waste-free technology for processing lignin into target products. The paper investigated the possibility of using lignin precipitated from the spent cooking solution after organosolv delignification of rapeseed straw with the following carbonization for obtaining sorbents for the removal of dangerous synthetics dyes from water solution. At the end of cooking, the cellulosic product was separated from the spent solution by filtration. The spent solution was collected in a separate container and treated with 5 volumes of water, resulting in lignin condensation. Condensed lignin was separated from the cooking solution by centrifugation at 5500 rpm for 10 min and washed with distilled water, dehydrated by centrifugation and dried at a temperature of 80 oC until a constant moisture content of 7-8% was reached. Then lignin was treated with a 20 wt.% solution of orthophosphoric acid or 20 wt.% solution of sodium hydroxide, after which it was carbonized in a muffle furnace. Carbonization of lignin leads to a decrease in the average pore size to 2.191-4.421 nm and to an increase in the pore volume by 1.8 times when treated with sodium hydroxide and 2.0 times when treated with orthophosphoric acid, which allows to increase the sorption capacity of the material. The influence of the pH of an aqueous solution on the process of pollutant sorption is decisive. Oxygen-containing functional groups give the surface of sorption materials a positive charge in an acidic environment, which leads to the formation of electrostatic repulsion forces with the dye cation, which also has a positive charge. When the pH is increased to slightly alkaline, dissociation of functional groups occurs, therefore the surface of the sorbent acquires a negative charge, which leads to the emergence of forces of electrostatic attraction with the dye. Absorption of cationic dye increases with increasing pH from 2.0 to 6.0, further increase in pH does not affect the efficiency of the process. Carbonization of lignin leads to an increase in the porosity of the sorbent, so it takes more time to reach full sorption equilibrium. During the first 80 minutes, the maximum absorption rate of methylene blue is observed, after 180 minutes of contact, full sorption equilibrium is reached. Using the Langmuir equation, the sorption isotherm of dye absorption on the obtained sorbents was estimated, and it was established that the vacant adsorption sites on the lignin surface are homogeneous and the dye adsorption is monolayer. It was established that the sorption kinetics is described by a pseudo-second-order model. The development of an effective method of peracetic lignin utilization as carbon sorbent allows to create resource-saving technologies.
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