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Alternative biological systems for the treatment of vinasse from wine

机译:用于处理葡萄酒中酒糟的替代性生物系统

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This work studied alternative treatment schemes for the vinasse wastewater from winendistilleries aiming at overcoming the problems caused by the high nitrogen and sulfurnconcentrations. A plexiglas laboratory-scale upflow anaerobic sludge blanket (UASB) reactor ofn20 L volume that was operated at 458C and hydraulic retention time 1 d, was included in all thenexamined systems. System 1 was the conventional UASB reactor, system 2 was the UASB reactornsupplemented with iron. System 3 consisted of the UASB reactor supplemented with iron and anCSTR reactor that operated under the following conditions: Diluted Oxygen 1.2mg/L, HydraulicnRetention Time 1 d, pH 6.7 and Temperature 458C. System 3 aimed at converting ammoniumndirectly to dinitrogen gas under anaerobic conditions but it needed to be preceeded by a firstnpartial nitrification step. All systems had high COD efficiencies over 75%. Ferrous iron additionnapart from enhancing the performance of systems 2 and 3, it was able to retain all sulphurncontent of the wastewater as ferrous sulfide stripping the biogas from hydrogen sulfide. Systemn3 also managed to meet its goal, since it achieved an 86% nitrogen reduction. Conclusively,nsystem 3 seems to be a very promising environmental technology for the treatment of distillerynand winery byproducts, as well as industrial wastewater with high sulfur and nitrogen content.
机译:这项工作研究了葡萄酒酿造厂的酒糟废水的替代处理方案,旨在解决氮和硫含量高引起的问题。在随后所有检查的系统中均包括一个容量为20 L的有机玻璃实验室规模的流式厌氧污泥层(UASB)反应器,该反应器在458°C下运行,水力停留时间为1 d。系统1是常规的UASB反应器,系统2是装有铁的UASB反应器。系统3由加有铁的UASB反应器和在以下条件下运行的CSTR反应器组成:稀释氧气1.2mg / L,水力保留时间1 d,pH 6.7和温度458C。系统3旨在在厌氧条件下将氨直接转化为氮气,但首先要进行部分硝化步骤。所有系统的COD效率均超过75%。除了提高系统2和3的性能外,添加亚铁还可以保留废水中所有的硫磺含量,因为亚铁硫化物从硫化氢中去除了沼气。 Systemn3还成功实现了其目标,因为它实现了86%的氮减少。最后,nsystem 3似乎是一种非常有前途的环境技术,用于处理酒糟和酒厂副产品以及高硫和氮含量的工业废水。

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