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Kinetics of different bioreactor systems with Acidithiobacillus ferrooxidans for ferrous iron oxidation

机译:不同生物反应器系统的动力学与酸性铁氧化物用于铁氧化物的铁氧化物

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摘要

The relative performance of two biofilm-based airlift reactors using different kinds of packing materials and one fixed bed biofilm reactor with a homemade packing material of high specific area (~ 1000 m(2)/m(3)) was addressed. The bioreactors operated under ferrous iron loading rates in the range of 8-120 mol Fe(II)/m(3) h. Acidithiobacillus ferrooxidans cells immobilized in the three bioreactors afforded the reactions for an extended period of 120 days of continuous operation at the dilution rates of 0.2, 0.4, 0.7, 1 and 1.2 h(-1). The maximum ferrous iron oxidation rates achieved in this study at a hydraulic residence time of 1.2 h were about 91, 68 and 51 mol Fe(II)/m(3) h for the fixed bed, airlift1, and airlft2 bioreactors. The performance data from the fixed-bed bioreactor offered a higher potential for ferrous iron oxidation because of fast biofilm development, the formation of a thick biofilm, and lower sensitivity to shear, which enhanced the startup time of the bioreactor and the higher reactor productivity. Proper kinetic models were also presented for both the startup period and the steady-state process.
机译:使用不同种类的填充材料和一个固定床生物膜反应器的两个生物膜的空运反应器的相对性能与高特异性面积的自制填料材料(〜1000μm(2)/ m(3))进行了解决。生物反应器在含铁铁加载率下运行8-120mol Fe(II)/ m(3)小时。在三个生物反应器中固定在三个生物反应器中的酸性辛嘧啶细胞,在稀释率为0.2,0.4,0.7,1和1.2h(-1)的稀释率下连续操作的延长时间为120天。该研究在1.2小时的液压停留时间下实现的最大氧化铁氧化率为固定床,Airlift1和AirlFT2生物反应器的液压停留时间为1.2小时约为91,68和51mol Fe(II)/ m(3)H.由于生物膜开发快,厚度的生物膜形成,厚度较低的剪切浓度,来自固定床生物反应器的性能数据提供了更高的铁氧化潜力。对于启动期和稳态过程,还呈现了适当的动力学模型。

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