College of Environmental Science and Engineering, Guilin University of Technology, Guilin 541004, China; Guangxi Key Laboratory of Environmental Pollution Control Theory and Technology, Guilin University of Technology, Guilin 541004, China.
College of Environmental Science and Engineering, Guilin University of Technology, Guilin 541004, China.
Bioresour Technol. 2021 Sep;336:125333. doi: 10.1016/j.biortech.2021.125333. Epub 2021 May 27.
Biochar derived from co-pyrolysis of sewage sludge and calcium sulfate was used to remove Cd(II) from aqueous solution. The results showed that the Cd(Ⅱ) adsorption better followed Freundlich model, and the maximum adsorption capacities were 109.0 mg/g (288 K), 127.9 mg/g (298 K) and 145.4 mg/g (308 K). The Cd(Ⅱ) removal was a multi-layer adsorption process dominated by chemisorption, which was also a spontaneous and endothermic process. The contribution of physisorption gradually increased as the Cd(Ⅱ) initial concentration. The Cd(Ⅱ) removal process which better followed pseudo-second-order kinetic model, was divided into three stages. The first (0-0.3 h) and second stages (0.3-2 h) were separately controlled by liquid film diffusion/intraparticle diffusion/chemical reaction and liquid film diffusion/chemical reaction, while the third stage (0.3-24 h) was the dynamic equilibrium process. The speciation distribution of Cd on biochar surface was mainly CdCO/CdOOC and CdO/CdSiO, indicating coprecipitation, ion exchange and complexation contributed more to the Cd(Ⅱ) removal.
由污水污泥和硫酸钙共热解得到的生物炭被用于从水溶液中去除 Cd(II)。结果表明,Cd(Ⅱ)吸附更符合 Freundlich 模型,最大吸附容量分别为 109.0 mg/g(288 K)、127.9 mg/g(298 K)和 145.4 mg/g(308 K)。Cd(Ⅱ)的去除是一个由化学吸附主导的多层吸附过程,也是一个自发和吸热的过程。随着 Cd(Ⅱ)初始浓度的增加,物理吸附的贡献逐渐增加。Cd(Ⅱ)去除过程更符合准二级动力学模型,可分为三个阶段。第一阶段(0-0.3 h)和第二阶段(0.3-2 h)分别由液膜扩散/内扩散/化学反应和液膜扩散/化学反应控制,而第三阶段(0.3-24 h)是动态平衡过程。Cd 在生物炭表面的形态分布主要为 CdCO/CdOOC 和 CdO/CdSiO,表明共沉淀、离子交换和络合作用对 Cd(Ⅱ)的去除贡献更大。