Pagnanelli Francesca, Beolchini Francesca, Di Biase Antonietta, Vegliò Francesco
Dipartimento di Chimica, Facoltà di SMFN, Università degli Studi La Sapienza, P le A Moro 5, Roma 00185, Italy.
Water Res. 2004 Feb;38(4):1055-61. doi: 10.1016/j.watres.2003.10.031.
Continuous heavy metal biosorption in membrane reactor apparatus using binary metal solutions was here considered. A dynamic model was developed to simulate biosorption performances on the base of metal mass balances in the system considering biosorption as an equilibrium process. The effect of three Langmuir-type competitive models on dynamic simulations of biosorption was then studied by using predictive equilibrium models (whose adjustable parameters were determined only by single metal system biosorption data) and not predictive equilibrium models (adjustable parameters directly by binary biosorption data). Predictive competitive models can give simulation profiles that are different from those obtained using non-predictive models. This detachment is due to the non-ideal competition among metals in solution which cannot be predicted only on the base of biosorption data in single metal systems. The dynamic model for multi-component biosorption here proposed was compared with experimental results reported in the literature and obtained using a biomass in a similar membrane reactor apparatus with ternary metal systems. The simulated profiles (obtained by using predictive equilibrium models) can reproduce qualitatively the specific adsorbent selectivity and the overshoot regions in the permeate concentrations of the metals with the minor affinity.
本文研究了在膜反应器装置中使用二元金属溶液进行连续重金属生物吸附的情况。基于将生物吸附视为平衡过程的系统中金属质量平衡,建立了一个动态模型来模拟生物吸附性能。然后,通过使用预测平衡模型(其可调参数仅由单一金属系统的生物吸附数据确定)和非预测平衡模型(直接由二元生物吸附数据确定可调参数),研究了三种朗缪尔型竞争模型对生物吸附动态模拟的影响。预测竞争模型给出的模拟曲线与使用非预测模型得到的不同。这种差异是由于溶液中金属之间的非理想竞争,仅基于单一金属系统中的生物吸附数据无法预测。本文提出的多组分生物吸附动态模型与文献中报道的、在类似的使用生物质的膜反应器装置中采用三元金属系统所获得的实验结果进行了比较。模拟曲线(通过使用预测平衡模型获得)能够定性地再现特定吸附剂的选择性以及具有较小亲和力的金属在渗透物浓度中的过冲区域。