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Research on the characteristic of power consumption in a novel rotating drum bioleaching reactor of different sizes

机译:新型不同尺寸转鼓生物浸出反应器功耗特性研究

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摘要

A novel rotating drum bioreactor (RDB) with the volume of 18 L and 96 L in our previous work has shown the potential for bioleaching processes with high solid concentration. In this paper, a larger RDB with a volume of 703 L was scaled up, and effect of operation condition and baffle parameters on power consumption in the 96 L and 703 L RDBs was investigated. The results showed that the specific power consumption increased with the rotation speed and was insensitive to aeration rate. Meanwhile, the specific power consumption was negatively related to loading coefficient and was positively related to diameter of RDB. It was found that the power consumption increased with the increase of number and width of baffles. The mass transfer performance was most economic, when the 703 L RDB was equipped with 8 baffles with a 0° angle. The mass transfer performance of the 703 L RDB at the same specific power was close to that of a stirred tank bioreactor (STB) commercially used. For the Al_2O_3 slurry system, the specific power consumption in the 703 L RDB was less than 1/3 of that in the traditional STB with the same diameter.
机译:在我们之前的工作中,新型的转鼓式生物反应器(RDB)的体积分别为18 L和96 L,显示了高固体浓度生物浸出工艺的潜力。在本文中,按比例放大了一个容量为703 L的较大RDB,并研究了操作条件和挡板参数对96 L和703 L RDB中功耗的影响。结果表明,比功率消耗随转速的增加而增加,对通气量不敏感。同时,单位功耗与负载系数成负相关,与RDB的直径成正相关。结果发现,随着挡板数量和宽度的增加,功耗也随之增加。当703 L RDB配备8个角度为0°的挡板时,传质性能最为经济。 703 L RDB在相同比功率下的传质性能与商业上使用的搅拌釜生物反应器(STB)接近。对于Al_2O_3浆料系统,在703 L RDB中的单位能耗小于具有相同直径的传统STB的1/3。

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