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A study of a thin-film algae-bacteria wastewater treatment system.

机译:薄膜藻类细菌废水处理系统的研究。

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摘要

A thin algae-bacteria biofilm system was developed as a potential wastewater treatment process, which would provide reasonable organic stabilization and a simple surface to assist in harvesting the microbial biomass for application on land as an organic fertilizer. The purpose of this study was to evaluate the removal of both organic and nutrient in a laboratory, thin film system using algae-bacteria symbiosis and to examine some of the fundamental biological and biochemical interactions in photosynthetic biofilms.; The laboratory reactor consisted of an inclined acrylic plastic plate, 4 in. wide by 67.5 in. long, on which the algae-bacteria biofilm was grown. The wastewaters were applied to the reactor at flow rates ranging from 2.5 L/d to 20 L/d. Fluorescent lights over the length of the reactor provided continuous luminescence at an intensity of 700 foot-candles at the microbial surfaces. The microbial growths were harvested in 12 to 13 equal segments on a daily basis to maintain a reasonable thickness of biofilm for suitable wastewater treatment. Four pure organic compounds: sodium butyrate, monosodium. glutamate, glucose and sodium benzoate, were examined as sole carbon sources to permit evaluation of their different characteristics with respect to metabolic pathways and cell energy/synthesis relationships. Lawrence municipal wastewaters were examined to determine the treatability characteristics of complex mixtures of organic compounds, as well as to demonstrate the efficiency of this system in processing municipal wastewaters.; The results obtained during this study showed that the overall energy/synthesis relationships observed during the metabolism of soluble, pure organic compounds tended to follow those observed in batch-fed systems rather than those observed in continuously fed, complete mixing systems. It was also noted that the algae metabolism was primarily related to the carbon dioxide released during the energy reactions for bacteria and fungi synthesis. The removal of COD ranged from a low of 53% for sodium butyrate to a high of 79% for glucose. While the COD removal rates were less than those obtained in activated sludge systems, they were close to those obtained in trickling filter systems. The overall growth of biomass varied from 0.54 mg VSS/mg COD removed for sodium butyrate to 0.86 mg VSS/mg COD removal. As more COD was oxidized, more bacteria and more algae were produced. The COD removal rates were essentially the same, 38%, for the septic, raw municipal wastewaters. The suspended solids harvested from the reactor ranged from 1.0 mg VSS/mg COD removed at the 20 L/d flow rate to 2.8 mg VSS/mg COD removed at the 5 L/d flow rate. There was greater algae growth at the lower flow rates and in the municipal wastewaters than in the pure organic compounds.; This initial study of the thin film, algae-bacteria reactor demonstrated the ability of bacteria, fungi, algae, and protozoa to produce a simple wastewater treatment system. It was shown that the thin film bioreactor was quite different from the completely mixed activated algae previously studied. Further research will be needed to determine if the thin film algae-bacteria bioreactor has practical value in treating municipal and industrial wastewaters in developing countries where simple wastewater treatment systems and nutrient recovery are essential.
机译:开发了一种薄藻-细菌生物膜系统作为潜在的废水处理工艺,该工艺将提供合理的有机稳定性和简单的表面,以帮助收集微生物生物量,以有机肥料的形式应用于陆地。这项研究的目的是评估利用藻类细菌共生的实验室薄膜系统中有机物和营养物的去除,并研究光合生物膜中一些基本的生物学和生化相互作用。实验室反应器由一块倾斜的丙烯酸塑料板组成,该板长4英寸,宽67.5英寸,上面生长有藻类细菌生物膜。废水以2.5 L / d至20 L / d的流速施加到反应器中。反应器整个长度上的荧光灯在微生物表面以700英尺烛光的强度提供连续发光。每天以12至13等份的方式收集微生物的生长量,以保持合理的生物膜厚度,以便进行适当的废水处理。四种纯有机化合物:丁酸钠,一钠。谷氨酸,葡萄糖和苯甲酸钠被作为唯一的碳源进行了检查,以评估它们在代谢途径和细胞能量/合成关系方面的不同特征。对劳伦斯市政废水进行了检查,以确定有机化合物的复杂混合物的可处理性,并证明了该系统在处理市政废水中的效率。在这项研究中获得的结果表明,在可溶性纯有机化合物代谢过程中观察到的总体能量/合成关系倾向于遵循在分批进料系统中观察到的能量/合成关系,而不是在连续进料的完全混合系统中观察到的能量/合成关系。还注意到藻类代谢主要与细菌和真菌合成的能量反应过程中释放的二氧化碳有关。 COD的去除范围从丁酸钠的低53%到葡萄糖的79%高不等。虽然COD去除率低于活性污泥系统中的去除率,但与滴滤系统中的去除率接近。生物量的总体生长范围从丁酸钠去除的0.54 mg VSS / mg COD到去除的0.86 mg VSS / mg COD不等。随着更多的COD被氧化,产生了更多的细菌和藻类。对于化粪池,未经处理的城市废水,COD去除率基本相同,为38%。从反应器中收集的悬浮固体的范围为:以20 L / d流速除去的1.0 mg VSS / mg COD到以5 L / d流速除去的2.8 mg VSS / mg COD。与纯有机化合物相比,较低流速和市政废水中藻类的生长更大。这项对薄膜藻细菌反应器的初步研究证明了细菌,真菌,藻类和原生动物产生简单废水处理系统的能力。结果表明,薄膜生物反应器与先前研究的完全混合的活化藻类完全不同。在需要简单的废水处理系统和养分回收的发展中国家,薄膜藻类细菌生物反应器在处理市政和工业废水方面是否具有实用价值,将需要进一步的研究。

著录项

  • 作者

    Kim, Ju-Young.;

  • 作者单位

    University of Kansas.;

  • 授予单位 University of Kansas.;
  • 学科 Engineering Environmental.
  • 学位 Ph.D.
  • 年度 1999
  • 页码 178 p.
  • 总页数 178
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 环境污染及其防治;
  • 关键词

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