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生物质化学工程 ›› 2023, Vol. 57 ›› Issue (5): 35-43.doi: 10.3969/j.issn.1673-5854.2023.05.005

• 研究报告 • 上一篇    下一篇

复合水凝胶SA/AAm-Lgs的制备及其对Fe3+的静/动态吸附

马培林, 宋亚婷, 李旭, 刘志明()   

  1. 东北林业大学 材料科学与工程学院, 黑龙江 哈尔滨 150040
  • 收稿日期:2022-10-26 出版日期:2023-09-30 发布日期:2023-10-07
  • 通讯作者: 刘志明 E-mail:zhimingliuwhy@126.com
  • 作者简介:刘志明, 博士生导师, 研究领域: 生物质材料化学、纤维素气凝胶和纳米纤维素、木质素及其功能性复合材料; E-mail: zhimingliuwhy@126.com
    马培林(1998—), 女, 山西忻州人, 硕士生, 主要从事生物质复合材料研究
  • 基金资助:
    国际横向课题(070-43221007)

Preparation of SA/AAm-Lgs Hydrogel and Its Static/Dynamic Adsorption Properties for Fe3+

Peilin MA, Yating SONG, Xu LI, Zhiming LIU()   

  1. College of Material Science and Engineering, Northeast Forestry University, Harbin 150040, China
  • Received:2022-10-26 Online:2023-09-30 Published:2023-10-07
  • Contact: Zhiming LIU E-mail:zhimingliuwhy@126.com

摘要:

将木质素磺酸钠(Lgs)引入到以海藻酸钠(SA)和丙烯酰胺(AAm)为基体的溶液中, 通过自由基聚合法制备得到多孔三维的复合水凝胶(SA/AAm-Lgs), 使用扫描电子显微镜(SEM)、傅里叶变换红外光谱(FT-IR)和力学性能测试仪等对其结构和性能进行分析, 并将其应用于去除废水中的Fe3+。研究结果表明: 实验成功制备了多孔三维网状结构的复合水凝胶SA/AAm-Lgs。当Lgs用量增加时, 水凝胶的断裂伸长率和抗拉强度相应增加, 溶胀性能也有一定程度提高。SA/AAm-Lgs(含Lgs 7 mg)静态吸附Fe3+的较佳工艺为: 水凝胶用量0.5 g、温度25 ℃、Fe3+初始质量浓度2 g/L, 该条件下水凝胶对Fe3+的吸附量可以达到143 mg/g, 吸附性良好且具有循环使用性能。吸附动力学和吸附等温线模拟结果表明该水凝胶对Fe3+的吸附过程符合准二级动力学和Langmuir模型。此外, 通过固定床工艺对Fe3+进行动态吸附实验证明了SA/AAm-Lgs具有良好的工业价值。对固定床高度、Fe3+进水质量浓度和流速对突破曲线的影响进行探讨, 结果表明: 随着固定床高度的增加, 突破时间延长; 随着Fe3+进水质量浓度增大和流速增加, 突破时间急剧缩短。BDST模型能准确预测不同流速或浓度下的突破时间, 理论突破时间和实际突破时间的平均误差均小于15%。

关键词: 海藻酸钠, 木质素磺酸钠, 三价铁离子, 静态吸附, 动态吸附

Abstract:

Sodium lignin sulfonate(Lgs) was introduced into the solution based on sodium alginate(SA) and acrylamide(AAm) as the matrix, and the porous three-dimensional composite hydrogels(SA/AAm-Lgs) were successfully prepared by free radical polymerization method. The structure and properties of SA/AAm-Lgs were analyzed by scanning electron microscopy(SEM), Fourier transform infrared spectroscopy(FT-IR) and mechanical property tester and it was also applied to remove Fe3+ from wastewater. The results showed that SA/AAm-Lgs with porous three-dimensional network structure were successfully prepared. When the amount of Lgs increased, the elongation at break and the tensile strength of hydrogel increased correspondingly, and the swelling property also increased to a certain extent. The best static adsorption process of SA/AAm-Lgs for Fe3+ was as follows: the amount of Lgs was 7 mg, the temperature was 25 ℃, and the initial mass concentration of Fe3+ was 2 g/L. Under these conditions, the adsorption capacity of SA/AAm-Lgs on Fe3+ could reach 143 mg/g, showing good adsorption and recycling performance. The adsorption kinetics and adsorption isotherm simulation results showed that the adsorption process of Fe3+ by SA/AAm-Lgs conformed to the quasi-second-order kinetics and Langmuir model. In addition, the dynamic adsorption experiments on Fe3+ by fixed bed technology proved that the SA/AAm-Lgs had good industrial value. The effects of fixed bed height, initial mass concentration of Fe3+ and flow rate on the breakthrough curve were discussed. The results showed that with the increase of fixed bed height, the breakthrough time was extended. When the initial mass concentration and flow rate of Fe3+ increased, the breakthrough time was shortened sharply. The BDST model could accurately predict the breakthrough time at different flow rates or concentrations, and the average deviation of theoretical breakthrough time and actual breakthrough time was less than 15%.

Key words: sodium alginate, sodium lignosulfonate, ferric ion, static adsorption, dynamic adsorption

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